METHOD AND APPARATUS FOR ANALYZING AND CONTROLLING CARBONATE AND SULFIDE IN GREEN LIQUOR SLAKING AND CAUSTICIZING

Abstract: A process and apparatus for measuring carbonate and sulfide concentrations in white and green pulping liquor and in the slaker/causticizing (S, C1) cells and controlling the causticizing reaction and other stages using this information. Specifically the causticizing control logic is based on determining the concentration of sodium carbonate and sodium sulfide (GC/A) in the green liquor, in the white liquor-mud slurry at the slaker or first causticizer (ML3) and in the white liquor being sent to the digester house and using this information to control the entire process. Th e concentration and flow rate of the green liquor may be measured and controlled quite easily. The proposed strategy will control the green liquor flow rate (V41) to the slaker to maintain the desired Na2CO3 concentration in the slaker/causticizer liquor despite variations which occur in the lime. The green liquor concentration is also controlled in a control loop. Weak wash liquor (L40) is added to the green liquor to maintain the concentration of the Na2CO3 in the green liquor. The slaking/causticizing process is controlled by adjusting the flow rate and concentration of the green liquor. This strategy will control the process based on direct measurements of the critical component in the system, sodium carbonate. The green liquor flow rate will be automatically adjusted by a control loop to maintain the desired Na2CO3 concentration in the white liquor. The last measurement is to determine the concentrations of sodium hydroxide, sodium carbonate, and sodium sulfide in the white liquor which is sent to the digester house to be used in the cooking process. It is important to measure the sodium hydroxide and sodium sulfide concentrations in the white liquor (RS3, GC/A) so that the amount of liquor to be charged in the digester(s) may be correctly determined. Changes in sodium sulfide concentration (generated at the recovery boiler) can affect white liquor (AA/EA) concentration.

Description: METHOD AND APPARATUS FOR ANALYZING AND CONTROLLING CARBONATE AND SULFIDE IN GREEN LIQUOR SLAKING AND CAUSTICIZING BACKGROUND OF THE INVENTION Field of the Invention Analyzing green liquor, slaker and causticizing cells, and white liquor chemicals and controlling pulp mill operations from the analysis. Other Art A good diagram of the causticizing process may be found in Pulp and Paper Manufacture, 2nd Ed., Volume I, The Pulping of Wood, 1969, prepared under the direction of the Joint Textbook Committee of the Paper Industry, R. G. MacDonald, editor, and J. N. Franklin, technical editor, the McGraw Hill Book Company, New York, publisher. The diagram is Figure 9-72 on page 535. The process actually starts with the recovery furnace. The black liquor consisting of organic and inorganic chemicals and water is charged to the furnace where the water is evaporated, the organic components are burned and inorganic components are recovered in the form of a molten smelt. The molten smelt containing mostly sodium carbonate and sodium sulfide is continuously decanted from the furnace bed and dissolved in water (weak wash) at the dissolving tank or tanks to form green liquor. A typical green liquor composition is about 60-65% sodium carbonate and 25-28% sodium sulfide by weight (% of solids) expressed as Na.o. A typical solids content of green liquor is around 18% of total liquor weight. The green liquor is pumped from the dissolving tank or tanks to a green liquor clarifier where the dregs settle out. The dregs are impurities, i.e., undissolved solids from the furnace. These are mainly carbon, calcium, magnesium and iron compounds. Following clarification, the green liquor is mixed with reburned lime from the kiln in the slaker. Usually the amount of lime is adjusted to maintain a specified white liquor concentration. Makeup lime in the form of fresh lime (or limestone burned in the kiln) is added to the reburned lime to replace lime losses in the system. Grits (large, unreacted lime particles) are removed from the slaked lime slurry in the classifier section of the slaker. In the slaker the lime or calcium oxide reacts with the water in the green OMPI ∑ SNAT\O liquor to form calcium hydroxide and this in turn reacts with the sodium carbonate in the green liquor to form sodium hydroxide and calcium carbonate, which then flows to the causticizing cells. Causticizing cells are used to allow enough time for the causticizing reaction that starts in the slaker to approach completion. From the caustϊcizers, the slurry is pumped to the white liquor clarifier (or a pressure filter) to separate the white liquor from the lime mud, calcium carbonate. The clarified white liquor is pumped to storage and then to the digester house to pulp wood chips. The mud or calcium carbonate in the bottom of the clarifier is pumped to a mud washer where it is washed with water from the mud filter and the dregs washer. The overflow water from the mud washer is called weak wash and this is used at the dissolving tank or tanks to dissolve the smelt to form raw green liquor. In the usual process then, weak wash is used at the dissolving tank or tanks to dissolve the molten sodium salts exiting from the recovery boiler. The resulting raw green liquor is then clarified to remove the dregs and then pumped to the slaker. Lime feed to the slaker is generally based on the total flow of green liquor and the slaker temperature, the slaker temperature specification being such as to maintain a specified white liquor strength and safe operating conditions. The causticizing reaction is usually controlled by chemical analysis (titration) of the white liquor taken from a causticizing cell or from the white liquor clarifier overflow. Lime feed, green liquor density at the dissolving tank or tanks or a combination of the two is usually changed to maintain a white liquor strength within a mill's specification. The specifica¬ tion is generally expressed as the sodium hydroxide and sodium sulfide concentration in the white liquor, i.e., AA (active alkali) or EA (effective alkali). These expressions are defined and discussed on pp. 358-363 of MacDonald and Franklin, supra. White liquor AA or EA concentration does vary considerably because of changes in lime availability (CaO content), reactivity (rate of hydration), mass flow rate of lime to the slaker or combinations of these. Sodium carbonate concentration changes in the green liquor feed will also affect the resulting white liquor strength. The presence of this number of uncontrolled variables makes it very difficult to control the slaking/ causticizing reaction. Present practice uses a total titratable alkali (TTA) measure¬ ment to control liquor strength and causticizing efficiency. TTA is a measurement of sodium hydroxide, sodium carbonate, and sodium sulfide, and is, therefore, only an indirect, approximate determination of the Na 2 CO 3 concentration in the liquor. Another variable that makes slaker control difficult is the colorimetric titration (ABC test) used to analyze the liquor. The ABC test is found in TAPPI test T624 OS-68 (Parts 9, 10 and 11). It may be modified to fit specific mill conditions. Titration end points are not identified by a crisp color change. Rather, there is a gradual change in color, for example, from orange to red or from green to blue depending on which indicator is used. This "diffuse" end point determination results in much uncertainty in the liquor . concentrations which are the only variables which are measured regularly. There have been attempts to solve these problems. Hultman, et al, U.S. Patents 4,236,960 and 4,311,666 describe a different type of process for controlling the degree of causticizion. Sutinan and Haapoja, "Causti¬ cizing Plant and Lime Kiln Computer Control" describes a Nokia Autolime system. TAPPI test T624 OS-68 describes tests for the analysis of soda and sulfite white and green liquors. Test 12 describes the sodium carbonate (evaluation method) test. SUMMARY OF THE INVENTION A process and apparatus for measuring carbonate and sulfide concentrations in white and green pulping liquor and in the slaker and causticizing cells and controlling the causticizing reaction and other stages using this information. The proposed process control logic reduces or eliminates most of the above-mentioned process control problems. It is based on the idea that a kraft mill slaker is really a carbonate reactor, i.e., carbonate ions in the green liquor are crystallized from solution with hydrated lime, and sodium hydroxide is generated in the process. Specifically the causticizing control logic is based on determining the concentration of sodium carbonate and sodium sulfide in the green liquor, in the white liquor-mud slurry at the slaker or first causticizer and in the white liquor being sent to the digester house and using this information to control the entire process. This logic is much different than present practice. OMPI The reason for measuring the concentration of sodium sulfide in the green liquor is not to control the slaking/caustieizing process, but to indicate inefficiencies in the process and to take steps to control them. An increase in sulfide concentration will tend to decrease the efficiency of the causticizing reaction. Knowledge of the concentration of sodium sulfide entering the slaker will indicate to the operator or process computer the optimum causticizing efficiency that can be expected from his recausticiz- ing plant. The changes in sulfide concentration will also indicate changes in recovery boiler sodium sulfide reduction efficiency and will allow steps to be taken to better control boiler sodium sulfide reduction efficiency. It is desired that as much of the sodium carbonate in the green liquor as possible be converted to sodium hydroxide in the slaker and caustieizers. It is impossible to completely convert all the sodium carbon¬ ate to sodium hydroxide - some sodium carbonate will remain in the white liquor. The ultimate limit as to how much sodium carbonate may be converted to sodium hydroxide is governed by the equilibrium causticizing efficiency. A discussion of the factors governing the equilibrium causticiz¬ ing efficiency may be found on pp. 532-534 of MacDonald and Franklin, supra. It is desirable to maintain the final white liquor at a composition very close to that determined by the equilibrium causticizing efficiency. If this is performed correctly, the benefits will be high efficiency of operation due to efficient conversion of sodium carbonate to sodium hydroxide, and low sodium carbonate "deadload" in the white liquor, which has many benefits throughout digestion, evaporation and recovery. In order to achieve this, it is necessary to closely balance the amounts of lime and green liquor being added to the slaker. An excess of green liquor to lime will result in low conversion efficiency of sodium carbonate to sodium hydroxide. An excess of lime to green liquor will impair the settling and filtering characteristics of the calcium carbonate "mud," which must be removed from the white liquor before it can be used in the digesters. Variations in the a 2 CO 3 concentration in the liquor at the slaker or causticizer are the result of variations in the concentration and flow rate of lime and green liquor. Lime quality and quantity can be variable and difficult to control - changes in mass flow rate, availability (% CaO) and lime reactivity (how fast hydration occurs) affect the Na ^ CO, concentration in the slaker/causticizer liquor, but are extremely difficult to measure and control. However, the concentration and flow rate of the green liquor may be measured and controlled quite easily. The proposed strategy will control the green liquor flow rate to the slaker to maintain the desired Na„CO« concentration in the slaker/causticizer liquor despite variations which occur in the lime. The green liquor concentration is also controlled in a control loop. The advantages of this strategy are as follows: 1. A constant, desired concentration of Na_C0 3 is controlled early in the slaking/causticizing reaction, ensuring safe, efficient operation. 2. The slaking/causticizing process is controlled by adjusting the flow rate and concentration of the green liquor, which is technically quite easy to accomplish. Controlling the concentration, activity, and flow rate of the lime is technically difficult and therefore is allowed to vary within normal limits and the green liquor flow rate is adjusted in response to these variations. This strategy provides much more precise control than do strategies which attempt to adjust lime flow rate in response to changes in liquor flow rate and concentration. 3. This strategy will control the process based on direct measurements of the critical component in the system, sodium carbonate. This provides much more precise control than do strategies based on TTA liquor conductivity, liquor density or other indirect, approximate indications of Na-COq in process liquors. The overall liquor room production rate (amount of white liquor generated per minute) will be controlled by the flow rate of lime to the slaker. As the production rate needs to be increased or decreased in order to maintain an overall mill liquor balance, the flow rate of lime added to the slaker is correspondingly increased or decreased. The green liquor flow rate will be automatically adjusted by a control loop to maintain the desired Na 2 COg concentration in the white liquor. Both chemical inventory (lime and liquor storage levels) and mill production rates can be maintained by this strategy. Chemical inventory and/or production rate may be controlled either manually or automatically. The last measurement is to determine the concentrations of sodium hydroxide, sodium carbonate, and sodium sulfide in the white liquor which is sent to the digester house to be used in the cooking process. It is important to measure the sodium hydroxide and sodium sulfide OMPI concentrations in the white liquor so that the amount of liquor to be charged in the digester(s) may be correctly determined. Changes in sodium sulfide concentration (generated at the recovery boiler) can affect white liquor AA/EA concentration. The apparatus takes a sample from an appropriate line - green liquor, slaker/causticizer liquor, or white liquor to the digester - filters the sample if necessary, takes a measured quantity, reacts that measured quantity with an acid to generate hydrogen sulfide and carbon dioxide and measures the quantities of these gases in a gas chromatograph. The apparatus has four main circuits: the filter circuit, the sampling circuit, the reactor circuit and the gas chromatograph circuit. A mud separation circuit is also utilized if the apparatus is to analyze liquor from the slaker or causticizing cells. A number of operations or modes are performed in each of these circuits during a test cycle. These modes are sequenced differently depending upon the different operation of the mill. The unit must operate consistently over a long period of time and must give reproducible results. For example, the liquor is corrosive and can also plug lines. The inventors have devised an apparatus which eliminates eorrosion and reduces line plugging to a minimum. This required a great deal of lab and mill testing and redesign to accomplish. During the testing, it was found that the liquor being analyzed, the degree of completion of the reaction and the temperature of the reactive gases would cause changes in the results which would lead to an inability to control the process. Again, a great deal of time and laboratory and mill testing was required before the problem was recognized, the sources of the problem discovered and corrective measures taken. The present apparatus and control logic is the result of several man-years of work extending over a several-year period and the present application represents the inventor's understanding as of the date of the application of the problem and the solution. The work is continuing. BRIEF DESCRIPTION OF THE DRAWINGS Figure 1 is a diagram of the principal components of the test unit. Figure 2 is a diagram of the filter circuit for the apparatus. Figure 3 is a diagram of a three-filter circuit unit for the apparatus when operating in a three-component configuration. Figure 4 is a diagram of the mud separation circuit. Figure 5 is a cross-sectional view of the reactor for the apparatus. Figure 6 is a top plan view of the reactor for the apparatus. Figure 7 is an interior side plan view partially in cross section showing the magnetic spin bar driver and the spin bar in the reactor chamber. Figure 8 is a cross-sectional view along line 8-8 of Figure 7. Figure 9 is a plot of a gas chromatograph voltage output over the course of gas analysis resulting from a typical green liquor sample. Figure 10 is a schematic diagram of a data collection circuit. Figure 11 is a diagram of a single loop apparatus in a pulp mill. Figure 12 is a diagram of a double loop apparatus in a pulp mill. Figure 13 is a diagram of a triple loop apparatus in a pulp mill. Figure 14 is a diagram of a cascaded control. DESCRIPTION OF THE PREFERRED EMBODIMENT The apparatus has four main circuits: the filter circuit, the sampling circuit, the reactor circuit and the gas chromatograph circuit. A mud separation circuit is also used if the apparatus is to be utilized to analyze liquor from the slaker or causticizing cells. Each of these circuits has a number of operations or modes which are performed during one test cycle. These modes are sequenced differently depending upon the particular operation of a mill. The parts and modes will be described for each of the circuits. A possible sequence will then be described. It should be noted that most of the operable valves throughout the unit are two-position valves. This is for ease and simplicity of operation. Three-position valves or multiple port valves are used in several specific applications. Where so used, the use of these valves is noted. Filter Circuit The purpose of the filter circuit is to remove particulate material from the liquor to prevent both the plugging of the test equipment and the chemical side reactions that would mask the true composition of the liquor. The following description is directed to the filter circuit of Figures 2 and 3. Each of the filter circuits in the three circuit array shown in Figure 3 would have the same parts and operating sequence, so the same reference numerals will be used for the individual elements in these circuits. The circuit has the following components: Major components F - Filter. FS - Filter shock dome. Lines ML - Mill liquor line in the causticizing system between the green liquor clarifier and the slaker, between the slaker and first causticizer, between the first and second causticizers or between the clear white liquor storage tank and the digester, depending on the liquor being sampled. L22 - Sampling line from the filter outlet line L30A to the sampling circuit. L28 - Liquor return line from the filter circuit to the clarifier, slaker or causticizer depending on liquor being sampled. L29 - Liquor supply line from the mill liquor line ML to the filter circuit. L30 - Filter outlet line from the upper part of the filter F to the liquor return line L28. L30A - Filter outlet line from the filter F to the sampling line L22. L30B - Filter outlet line from the filter outlet line L30A to the filter backflush line L31. L30C - Filter outlet line from the filter outlet line L30B to the liquor return line L28. L31 - Filter backflush line from the valve V28 to the filter outlet line L30C. L32 - Filter bypass line from the filter circuit inlet line L29 to the liquor return line L28. L33 - Air inlet line to the top of the filter shock dome FS. L33A - Air inlet line from the air supply to the water backflush line L37. L33B - Air and water inlet line between the water backflush line L37 and the top of the filter shock dome FS. v L34 - Filter inlet and filter backflush outlet line between the valve V28 and the bottom of the filter F. L35 - Inlet line from the filter circuit liquor supply line L29 to the valve V28. L36 - Water supply line. L37 - Water backflush line from the water supply line L36 to the inlet line L33B. Valves Operating valves (solenoid operated) V21 - Valve in the filter outlet line L30A. Two positions: open; closed. V22 - Valve in the sampling line L22. Two positions: open; closed. V24 - Valve in the filter bypass line L32. Two positions: open; closed. V26 - Valve in the air inlet line L33A. Two positions: open; closed. V28 - Filter inlet-backflush three-way T valve at juncture of the filter backflush line L31, the filter inlet line L34 and the inlet line L35. Two positions: position one (backflush) (IB) - open to the filter backflush line L31 and the filter backflush outlet line L34, closed to the inlet line L35; position two (filter) (2F) - open to the filter inlet line L34 and the inlet line L35, closed to the filter backflush line L31. V29 - Valve in the water backflush line L37. Two posi¬ tions: open; closed. Check valves V18 - Check valve in the filter outlet line L30B to prevent flow through the line L30 into the filter F. V23 - Check valve in the filter backflush line L31 to prevent flow through the line L31 into the filter F. Pressure valve (open or partially open, manually operable) V20 - Back pressure valve in the filter outlet line L30B to provide pressure in the filter F and to induce preferential flow into the sampling line L22 when the valve V22 is open. Pressure relief valve (normally closed, automatically openable) V27 - Pressure relief valve on the filter F. Repair valves (normally open, manually operable) VI 9 - Repair valve in the liquor return line L28. V25 - Repair valve in the filter circuit liquor supply line L29. The filter circuit has several operating modes. Bypass mode (no liquor to filter) (Bypass) The first mode is a liquor bypass mode in which the liquor is taken from the mill liquor line, through the bypass line and returned to the slaker or eausticizer without passing through the ilter. Lines involved ML - Mill liquor line. L28 - Liquor return line from the filter circuit. L29 - Liquor supply line from the mill liquor line ML to the filter circuit. L32 - Filter bypass line from the filter circuit inlet line L29 to the filter circuit outlet line L28. Valves involved Operating valves/position V21 - Valve in the filter outlet line L30A/elosed. V22 - Valve in the sampling line L22/closed. V24 - Valve in the ilter bypass line L32/open. V26 - Valve in the air inlet line L33A/closed. V28 - Filter inlet-backflush valve/position one (backflush) (IB) - open to the filter backflush line L31 and the filter backflush outlet line L34, closed to the inlet line L35. V29 - Valve in the water backflush line L37/closed. Check valves VI 8 - Check valve in the filter outlet line L30B to prevent flow through the line L30 into the filter F. V23 - Check valve in the filter backflush line L31 to prevent flow through the line L3I into the filter F. Repair valves V19 - Repair valve in the liquor return line L28. V25 - Repair valve in the filter circuit liquor supply line L29. Flow ML through V25 through L29 through V24 through L32 through V19 through L28. Time The time will vary. Liquor filtering mode (Filter) The second mode is a liquor filtering mode in which the liquor is taken from the mill liquor line, filtered in the filter F and returned to the return line in order to establish steady state filtering of the liquor. Major components involved F - Filter Lines involved ML - Mill liquor line. L28 - Return line from the filter circuit. L29 - . Liquor supply line from the mill liquor line ML to the filter circuit. L30 - Filter outlet line from the upper part of the filter F to the return line L28. L34 - Filter inlet line from the valve V28 to the bottom of the filter F. L35 - Inlet line from the filter circuit liquor supply line L29 to the valve V28. Valves involved Operating valves/position V21 - Valve in the filter outlet line L30A/open. V22 - Valve in the sampling line L22/closed. V24 - Valve in the filter bypass line L32/closed. V26 - Valve in the air inlet line L33 A/closed. V28 - Filter inlet-backflush valve/position two (filter) (2F) - open to the filter inlet line L34 and the inlet line L35, closed to the filter backflush line L31. V29 - Valve in the water backflush line L37/closed. Check valves V18 - Check valve in the filter outlet line L30B to prevent flow through the line L30 into the filter F. V23 - Check valve in the filter backflush line L31 to prevent flow through the line L31 into the filter F. Pressure valve V20 - Back pressure valve in the filter outlet line L30B. Repair valves VI 9 - Repair valve in the filter circuit liquor return line L28. V25 - Repair valve in the filter circuit liquor supply line L29. Flow ML through V25 through L29 through L35 through V28 through L34 through F through V21 through L30 through V20 throughV18 throughV19 throughL28. Note: When first starting up the analyzer, a filter cycle is immediately performed to provide a liquor sample for the first reaction. For all subsequent reactions, the filter cycle is started at a time determined by an action somewhere else in the system. It can be started by a sequencer output which is energized when a new liquor sample is desired. This could be signaled by completion of filling the acid pump AP2 or opening the valve which applies pressure to the reactor Rl. Time 60 seconds - will vary depending on time required to fill lower part of filter with liquor and provide an adequate flow in L30 to provide a consistent liquor sample to the sample line L22. Liquor sampling mode (sample) The-4hird-mode s-arliquorτsampHng mode in which the liquor is taken from the mill liquor line, filtered and sent to the sampling circuit to provide the test sample. The parts, lines, valves and valve positions are the same in this mode as in the second mode, the filter mode, except for the following change. Major components involved F - Filter Lines involved L22 - Sampling line from the ilter outlet line L30A to the sampling circuit. Valves involved Operating valves/position V22 - Valve in the sampling line L22/open. Pressure valves V20 - Back pressure valve in the filter outlet line L30B provides back pressure to cause preferential diver¬ sion of the filtered liquor into the sampling line L22. Flow ML through V25 through L29 through L35 through V28 through L34 through F through V21 through L30A: part through V22 through L22 to sampling circuit, part through V20 through L30B through VI 8 through L30C through VI 9 through L28. Time 60 seconds - will vary depending on time needed to com¬ pletely flush and fill sample circuit with new liquor. Stop sampling mode (Stop) The fourth mode is a stop sampling mode which is a pause to allow the sample valve V22 in the sampling circuit to change position. The parts, lines, valves, valve positions and flows are the same as in the second mode - the filter mode. Time 5 seconds or as needed to ensure closure of valve V22. Liquor backflush mode The fifth mode is a liquor backflush mode, in which the liquor is used to backflush or backwash particulate matter in the filter from the filter to the return line. It takes place in two stages. Stage 1 (Backflush 1) In stage 1 the filter outlet valve V21 is closed and liquor from the mill liquor line ML fills the filter to the middle of the filter shock dome FS. Major components involved F - Filter FS - Filter shock dome. Lines involved ML - Mill liquor line. L29 - Liquor supply line from the mill liquor line ML to the filter circuit. L33 - Air inlet line to the top of the filter shock dome FS. L34 - Filter inlet line from the valve V28 to the bottom of the filter F. L35 - Inlet line from the filter circuit liquor supply line L29 to the valve V28. Valves involved Operating valves/position V21 - Valve in the filter outlet line L30A/closed. V22 - Valve in the sampling line L22/closed. V24 - Valve in the filter bypass line L32/closed. V26 - Valve in the air inlet line L33A/closed. V28 - Filter inlet-backflush valve/position two (filter) (2F) - open to the filter inlet line L34 and the inlet line L35, closed to the filter backflush line L31. V29 - Valve in the water backflush line L37/closed. Repair valves V25 - Repair valve in the filter circuit liquor supply line L29. Flow ML through V25 through L29 through L35 through V28 through L34 into F to middle of FS. Time 10 seconds or as needed to provide sufficient liquor to backwash filter. Stage 2 (Backflush 2) In stage 2 air, admitted at the top of the filter shock dome FS, drives the liquor through the filter element of the filter F, out the inlet to the filter element, through the filter backflush outlet line L34, the backflush Une L31, the filter outlet line L30C, and the filter circuit liquor return line L28. Major components involved F - Filter Lines involved L28 - Liquor return line from the filter circuit. L30C- Filter outlet line from the filter backflush line L31 to the filter circuit liquor return line L28. L31 - Filter backflush line from the valve V28 to the filter outlet Une L30C. L33 - Air inlet line to the top of the filter shock dome FS. L34 - Filter backflush outlet line from the bottom of the filter F to the valve V28. Valves involved Operating valves/position V21 - Valve in the filter outlet line L30A/elosed. V22 - Valve in the sampling line L22/closed. V24 - Valve in the filter bypass line L32/open. V26 - Valve in the air inlet line L33A/open. V28 - Filter inlet-backflush valve/position one (backflush) (IB) - open to the filter backflush line L31 and the filter backflush outlet line L34, closed to the inlet line L35. V29 - Valve in the water backflush line L37/closed. Check valves V18 - Check valve in the filter outlet line L30B to prevent flow through the line L30 into the filter F. V23 - Check valve in the backflush line L31 to prevent flow through the line L31 into the filter F. Repair valves VI 9 - Repair valve in the filter circuit liquor return line L28. Flow Air V26 through L33 into F. Liquor F through L34 through V28 through V23 through L31 through L30C through V19 through L28. Time 15 seconds or as needed to adequately backflush filter. Water backflush mode The sixth mode is a water backflush mode in which water is introduced at the top of the filter shock dome FS and washes particulate matter from the filter element, out the bottom of the filter through the filter backflush outlet Une L34, the backflush line L31, the filter outlet line L30C, and the filter circuit Uquor return line L28. The water backflush mode would normally occur in place of a first mode, a bypass mode, and would follow a fifth mode, the liquor backflush mode. It is used any time the filter is excessively dirty with particulate matter. The Uquor supply would normally be turned off. The parts, lines, valves and valve positions are the same as in stage 2 of the fifth mode, stage 2 of the Uquor backflush mode, with the following additions and changes. Lines involved L33A- Air line to the filter shock dome not used. L33B- Inlet line from the water backflush line L37 to the top of the filter shock dome FS. L36 - Water supply line. L37 - Water backflush line from the water supply line L36 to the inlet line L33B. Valves involved Operating valves/position V26 - Valve in the air inlet Une L33A/closed. V29 - Valve in the water backflush line L37/open. Flow Water: L36 through V29 through L37 through L33B through F through L34 through V28 through V23 through L31 through L30C through V19 through L28. Time 60 seconds or as needed to provide a complete washing of the filter element. Mud separation circuit - slaker/causticizer white liquor It is often desirable for control appUcations to obtain liquor samples directly from the slaker or causticizer for analysis. This liquor contains 8-10% by weight suspended calcium carbonate mud solids, which must be removed prior to analysis. The level of soUds loading present in this liquor is too high to be introduced immediately to the filter circuit since severe plugging of the filter element would result. The purpose of the mud separation unit is to remove the bulk of the soUds from the Uquor and yield a "clear" liquor containing 1% or less suspended mud solids. This "clear" Uquor is filterable and becomes the Uquor supply to the filter circuit. It should be noted that the mud separation unit in no way interferes with subsequent operation of the analyzer system. The filter, sample, reactor, and gas chromatograph circuits operate exactly as they do when no mud separation circuit is utiUzed. The mud separation circuit merely ensures that an acceptable liquor sample is provided to the filter circuit. The best method of mud separation has been found to involve the use of a continuous settUng cone. This device receives unclarified liquor from the slaker or causticizer, separates the mud from the liquor, returns the mud to the slaker or causticizer, and supplies a continuous "clear" liquor supply to the filter circuit. The advantages of this apparatus and method are simplicity, reliabiUty, ease of operation and a fresh, uninterrupted supply of Uquor to the filter circuit so that operation of the filter circuit is not disturbed. The settling cone itself is a nonmechanical thickener of a type commonly used for continuous liquid-solid separations in low volume appli¬ cations. The details of the construction and operation of these units are well known and will not be given in detail here, but may be found in Perry, J. H. (Ed.) Chemical Engineers Handbook, 3rd Ed., McGraw-Hill Book Co., Inc. New York, 1950, pp. 940-941. The mud separation unit should be designed for a capacity that wiU deliver a desirable flow of "clear" liquor (approximately 2-3 Uters/minute) to the filter circuit. The following description is of the mud separation circuit shown in Figure 4. The circuit consists of the following components: Major components Tl - — Continuous settling ~ cone. T2 - Clear liquor tank. SP1 - Unclarified liquor supply pump from unclarified Uquor supply line L39 to unclarified liquor supply line L40. SP2 - Clear liquor supply pump in filter circuit liquor supply line L29. Bl - Bustle pipe and launder ring apparatus from settling cone Tl to clear liquor supply line L43. OMPI « « >-.o Lines L29 - Liquor supply line to the filter circuit. L39 - Unclarified liquor supply line from slaker (or causti¬ cizer) to unclarified Uquor supply pump SP1. L40 - Unclarified liquor supply line from unclarified liquor supply pump SP1 to junction of settUng cone inlet line L41 and settling eone bypass line L42. L41 - SettUng cone inlet Une from unclarified liquor supply Une L40 to settUng cone Tl. L42 - SettUng cone bypass line from unclarified liquor supply line L40 to slaker (or causticizer) return Une L50. L43 - Clear liquor supply line from bustle pipe/launder ring apparatus Bl to junction of clear Uquor tank inlet line L44 and clear liquor tank bypass line L46. L44 - Clear liquor tank inlet line from clear liquor supply line L43 to clear Uquor tank T2. L45 - Clear liquor tank overflow line from clear liquor tank T2 to clear liquor bypass/overflow Une L48. L46 - Clear liquor tank bypass line from clear liquor supply Une L43 to clear Uquor bypass/overflow Une L48. L47 - Clear liquor tank outlet line from clear liquor tank T2 to junction of filter circuit Uquor supply Une L29 and clear liquor tank drain line L51. L48 - Clear liquor tank bypass/overflow line from junction of clear Uquor tank bypass Une L46 and clear liquor tank overflow line L45 to slaker (causticizer) return line L50. L49 - SettUng cone mud discharge line from sett ng cone Tl to slaker (causticizer) return line L50. L50 - Slaker (causticizer) return line returning flows from clear Uquor tank bypass/overflow Une L48, mud discharge line L49, and settling cone bypass line L42 to the slaker (or causticizer). L51 - Clear liquor tank drain line from clear liquor tank outlet line L47 to return Une L50. L52 - Water flush line from mill water supply to unclari¬ fied Uquor supply line L39. Operating and repair valves (manually operable) V30 - SettUng cone inlet valve in settling cone inlet line L41. Two positions: open, closed. V31 - Settling cone bypass valve in settling cone bypass Une L42. Two positions: open, closed. V32 - Clear liquor tank bypass valve in clear liquor tank bypass line L46. Two positions: open, closed. V33 - Clear liquor tank inlet valve in clear liquor tank inlet line L44. Two positions: open, closed. V34 - Clear liquor tank outlet valve in filter circuit liquor supply line L29. Two positions: open, closed. V35 - Clear liquor tank drain valve in clear liquor tank drain line L51. Two positions: open, closed. V36 - Water flush valve in water flush line L52. Two . positions: open, closed. V37 - Unclarified liquor supply valve in unclarified liquor supply line L39. Two positions: open, closed. The mud separation unit has five modes of operation, these being the normal operating mode, the clear liquor tank bypass mode, the settling cone bypass mode, the circuit shutdown/water flush mode, and the circuit shutdown/standby mode. Normal operating mode The first mode is the normal operating mode. The circuit will normally remain in this mode. The circuit will be removed from this mode only as necessitated by the need for repairs to the mud separation or filter circuits, or upon shutdown of the slaking/causticizing process. Major parts involved Tl - Continuous settling cone. T2 - Clear liquor tank. SP1 - Unclarified liquor supply pump/on. SP2 - Clear liquor supply pump/on. Bl - Bustle pipe/launder ring apparatus. Lines involved L29 - Liquor supply line to filter circuit. L39 - Unclarified liquor supply line. L 0 - Unclarified liquor supply line. L41 - Settling cone inlet Une. L43 - Clear liquor supply line. L44 - Clear quor tank inlet line. L45 - Clear Uquor tank overflow Une. L48 - Clear Uquor tank bypass/overflow line. L49 - Settling cone mud discharge Une. L50 - Slaker (causticizer) return Une. Operating valves/position V30 - SettUng cone inlet valve/open. V31 - Settling cone bypass valve/closed. V32 - Clear liquor tank bypass valve/closed (or throttled). May be throttled partially open when circuit is in operation in order to direct some clear liquor to the return line L50 to ensure that L50 does not become plugged. V33 - Clear Uquor tank inlet valve/open. V34 - Clear liquor tank outlet valve/open. V35 - Clear liquor tank drain valve/closed. V36 - Water flush valve/closed. V3 - Unclarified liquor supply valve/open. Flow Unclarified liquor From slaker (or causticizer) through V37 through L39 through SP1 through L40 through V30 through L41 into Tl. Clear liquor From Tl through Bl through L43 through V33 through L44 into T2 through L47 through V3 through SP2 through L29. Mud From Tl through L49 through L50 to slaker (or causticizer). Time The time wiU vary. The circuit wiU normally be in this mode, being removed from this mode only for maintenance of this circuit or the filter circuit or upon shutdown of the slaking and causticizing process. Clear Uquor tank bypass mode The second mode is the clear Uquor tank bypass mode. This mode is utilized when it is necessary to stop the flow of clear liquor to the clear liquor tank. This may be necessitated by the need for repairs to this part of the circuit, or by the need for repairs to the filter circuit which require that the flow of clear Uquor to the filter circuit be stopped. Major components involved Tl - Continuous settling cone. T2 - Clear liquor tank. SP1 - Unclarified liquor supply pump/on. SP2 - Clear liquor supply pump/off. Bl - Bustle pipe/launder ring apparatus. Lines involved L39 - Unclarified liquor supply line. L40 - Unclarified liquor supply line. L41 - Settling cone inlet line. L43 - Clear liquor supply line. L46 - Clear liquor tank bypass line. L47 - Clear liquor tank outlet line. L48 - Clear liquor tank bypass/overflow line. L49 - Settling cone mud discharge line. L50 - Slaker (or causticizer) return line. L51 - Clear Uquor tank drain line. Operating valves/position V30 - Settling cone inlet valve/open. V31 - Settling cone bypass valve/closed. V32 - Clear liquor tank bypass valve/open. V33 - Clear liquor tank inlet valve/closed. V34 - Clear liquor tank outlet valve/closed V35 - Clear liquor tank drain valve/open. V36 - Water flush valve/closed. V37 - Unclarified liquor supply valve/open. Flows Unclarified liquor From slaker or causticizer through V37 through L39 through SP1 through L40 through V30 through L41 into Tl. Clear Uquor From Tl through Bl through L43 through V32 through L46 through L48 through L50 to slaker or causticizer. From T2 through L47 through L35 through L51 through LδO ^ into slaker or causticizer. Mud From Tl through L49 through L50 to slaker or causticizer. Time Varies as required to repair maintenance problem necessi- tating clear Uquor tank bypass. SettUng Cone Bypass Mode The third mode is the settUng cone bypass mode. This mode is utiUzed when it is necessary to stop operation of the settUng cone in order to repair this part of the circuit. The flow of clear liquor will be interrupted in this mode and there wiU be no sample flow to the filter circuit and analyzer. Major components involved SP1 - Unclarified liquor supply pump/on. SP2 - Clear liquor supply pump/off. Lines involved L39 - Unclarified liquor supply line. L40 - Unclarified liquor supply line. L42 - Settling tank bypass Une. L47 - Clear liquor tank outlet line. L50 - Slaker or causticizer return line. L51 - Clear liquor tank drain line. Operating valves/position V30 - SettUng tank inlet valve/closed. V31 - Settling tank bypass valve/open. V32 - Clear liquor tank bypass valve/closed. V33 - Clear liquor tank inlet valve/open. V34 - Clear liquor supply valve/open. V35 - Clear liquor tank drain valve/open. V36 - Water flush valve/open. V37 - Unclarified liquor supply valve/open. / JRE _ Flows Unclarified liquor From slaker or causticizer through V37 through L39 through SP1 through L40 through V31 through L42 through L50 to slaker or causticizer. Time Varies as needed to complete maintenance repairs necessi¬ tating bypass of settling cone. Circuit Shutdown/Water Flush Mode The fourth mode is the circuit shutdown/water flush mode. This mode is used when it is necessary to entirely shut down the circuit for maintenance or in response to a shutdown of the slaking/causticizing process. The flow of unclarified Uquor to the system is stopped and all Unes and major parts are flushed with water to ensure that they are clean and unplugged. Major components involved Tl - Settling cone. T2 - Clear liquor tank. SP1 - Unclarified liquor supply pump/on. SP2 - Clear liquor supply pump/on. Bl - Bustle pipe/launder ring. Lines involved L40 - Unclarified liquor supply line. L41 - Settling tank inlet line. L42 - SettUng tank bypass line. L43 - Clear liquor supply line. L44 - Clear liquor tank inlet line. L45 - Clear liquor tank overflow line. L46 - Clear liquor tank bypass line. L47 - Clear Uquor tank outlet line. L48 - Clear liquor tank bypass/overflow line. L49 - Settling cone mud discharge line. L50 - Return line to slaker or causticizer. L51 - Clear liquor tank drain line. L52 - Water flush line. Operating valves/position V30 - Settling cone inlet valve/open. V31 - SettUng cone bypass valve/open. V32 - Clear Uquor tank bypass valve/open. V33 - Clear liquor tank inlet valve/open. V34 - Clear Uquor tank outlet valve/open. V35 - Clear Uquor tank drain valve/open. V36 - Water flush valve/open. V37 - Unclarified liquor supply valve/closed. Flow Water Through L52 through V36 through L39 through SP1 through L40 through: V31 through L42 through L50 into slaker or causticizer. V30 through L41 into Tl. From Tl through L49 through L50 into slaker or causticizer. From Tl through Bl through L43 through: V32 through L46 through L48 through L50 into slaker or causticizer. V33 through L44 into T2 through L47 through: V34 through SP2 through L29. V35 through L51 through L50 into slaker or causticizer. Time 15 minutes or as needed to completely flush circuit with water. Note This operation, as described, wiU completely flush the entire circuit with water. Selected valves may be closed as desired to direct wash water only through selected Unes and parts of the circuit. It is not always necessary or desirable to flush the entire circuit. Circuit Shutdown/Standby Mode The fifth mode is the circuit shutdown/standby mode. This mode is used after the circuit has been flushed with water. The circuit is in a "standby" condition and will remain in this condition until restarted. - tTO O PI Major components involved All components are in "standby." All tanks are drained and all pumps are off. Lines All Unes have been flushed and drained and remain in a standby mode. Operating valves/position V30 - Settling tank inlet valve/open. V31 - Settling tank bypass valve/closed. V32 - Clear liquor tank bypass valve/closed. V33 - Clear Uquor tank inlet valve/open. V34 - Clear Uquor supply valve/open. V35 - Clear liquor tank drain valve/closed. V36 - Water flush valve/closed. V37 - Unclarified liquor supply valve/closed. Flow No flow in circuit once tanks and lines empty and drain. To restart the circuit and return to the first or normal operating mode, the unclarified liquor supply valve V29 is opened and pumps SP1 and SP2 are turned on. The circuit wiU then resume normal operation. The circuit should be started and be running at least 30 minutes prior to starting the rest of the analyzer system in order to ensure that all tanks have been filled and the circuit has reached equilibrium. Sampling circuit The purpose of the sampling circuit is to obtain a measured liquor sample and a measured amount of acid, to hold them separately until the reactor can receive them, and to transport them to the reactor. It has two main sections, a sample valve and an associated sample loop shown in the upper central part of Figure 1, and an acid section shown in the right hand side of Figure 1. The sample loop obtains a 10 cc sample of the filtered Uquor and the acid pump obtains a 50 cc sample of 10% sulfuric acid by volume (approximately 2.2 N). The acid pump strokes to deliver a full 50 cc of acid but only 40 cc goes to reactor. The rest is left in the sample loop SL2 and is washed out when fresh liquor displaces the acid in the liquor sampling mode. It has the following components: -fUREAc OMPI o Major components SL2 - Sample loop for obtaining a 10 cc filtered liquor sample. It is connected to the ports P5 and P6 of the sample valve V14. API - The air piston for operating the piston in the positive displacement acid pump AP2. Two posi¬ tions: position one (acid in or fϊU) (IF); position two (acid out or transfer) (2T). AP2 - Positive displacement acid pump for obtaining a 50 cc sample of 10% sulfuric acid. Two positions: position one (acid fill and standby) (IF); position two (acid out or transfer) (2T). Lines L9 - Antϊflocculant line from the antif locculant supply to the acid supply line L20. L14 - Air line from the air supply line L27 to the valve . Vll. L15 - Air line from the valve Vll to the port PI of the sample valve V14 for supplying air to move the sample valve VI to position one (sampling) (IS). LI 6 - Air line from the valve Vll to the port P2 of the sample valve VI 4 for supplying air to move the sample valve VI 4 to position two (transferring) (2T). L17 - Sample line from the port P4 of the sample valve VI 4 to the port R9 of the reactor HI. L19 - Acid Une from the acid line L21 to the port P3 of the sample valve V14. L20 - Acid supply line from the acid supply to the acid Une L21. L21 - Acid line from the juncture of acid Unes L19 and L20 to the acid pump AP2. L22 - Sample line from the filter system to the port P8 of the sample valve VI 4. L23 - Sample line from the port P7 of the sample valve V14 to the sewer. L24 - Air line from the valve VI 7 to the inner side of the piston in API to move the piston outwardly to position one (acid fill) (IF). L25 - Air line from the valve V17 to the outer side of the piston in API to move the piston inwardly to posi¬ tion two (acid transfer) (2T). L26 - Air line from the air supply line L27 to the valve V17. L27 - Air supply line. Valves Operating valves Vll - Solenoid operated air valve connecting the air line LI 4 to either the air line LI 5 or the air Une LI 6 to position the sample valve V14. Two positions: position one (sampling) (IS) - the air line L14 con¬ nected to the air line L15; position two (transferring) (2T) - the air line L14 connected to the air line LI 6. V14 - Air operated sample valve has two operational ports. PI - Connected to the air line LI 5 to allow air to move the valve to position one (sampling), and P2 - Connected to the air line LI 6 to allow air to move the valve to position two (transferring). And six sample ports: P3 - Connected to the acid line LI 9, P4 - Connected to the sample line L17, P5 - Inlet to the sample loop SL2, P6 - " Outlet from the sample loop SL2, P7 - Connected to the sewer line L23, P8 - Connected to the sample line L22. It has two positions: Position one (sampling) (IS) - receiving the sample from the fUter circuit into the sample loop SL2. Connects ports P5, P6, P7 and P8. Position two (transferring) (2T) - sending the sample from the sample loop SL 2 to the reactor Rl. Connects ports P3, P4, P5 and P6 and sends acid charge from AP2 through sample loop SL2 to reactor Rl. V17 - Solenoid operated air valve connecting air line L26 to either the air Une L24 or the air Une L25. Two positions: position one (acid fill) (IF): the air line L26 connected to the air Une L25; position two (acid transfer) (2T): the air line L26 connected to the air Une L24. Check valves V12 - Check valve in the sample line L17 prevents material or gas from returning through the Une L17 from the reactor Rl to the sampling circuit. V15 - Check valve in the acid line L19 prevents backflow of acid from LI 9 through L20 into AP2 during the acid pump fiU mode. VI 6 - Cheek valve in the acid supply line L20 prevents backflow of acid through the acid supply line L20 during the acid transfer mode. Pressure regulation valves AR2 - Pressure regulation valve in the air line L26. AR3 - Pressure regulation valve in the air line L14. The sample valve and its associated sample loop receives and holds a measured Uquor sample. The acid system receives and holds a measured amount of acid separate from the liquor sample. These are held until the reactor can accept the sample and the acid. The circuit then transports the sample, followed by the acid, to the reactor Rl. During this latter step, the acid passes through the sample loop SL2. This accomplishes two objectives: (1) the sample is transported to the reactor assembly by the acid and (2) the sample loop is cleaned by the acid during the injection. After the transfer some acid remains in the loop and will dissolve any residue that may remain in the loop. Cleaning the sample loop before each liquor analysis is important because the liquor being handled tends to crystallize out on any surfaces with which it comes in contact. During the next sample reception, the sample is circulated through the sample loop SL2 and out of the system through Une L23. This requires 60 to 100 seconds to ensure that aU of the acid and any residue that may be present is removed from the sample loop, and that the new sample is a representative sample of the Uquor currently being utilized by the process. The sampling circuit has several operating modes. In many of these modes the valving arrangement is the same. An initial acid flush cycle (Modes 1-4) is performed at start-up to ensure that the sample system is clean and filled with acid before sample analysis begins. At start-up, there may 'or may not be a sample in the sample loop depending upon the status of the sample system at shutdown. Standby mode (Standby 1) The first mode is a standby mode in which there is acid or liquor in the sample loop SL2, depending on the status of the sample circuit at shutdown. Major components involved SL2 - Sample loop/filled with 10 cc of acid or liquor. API - Air operated piston for operating the piston in the acid pump/position one (acid fill) (IF). AP2 - Acid pump/position one (acid fill) (IF). Lines involved L14 - Air line from the air supply line L27 to the valve Vll. L15 - Air line from the valve Vll to the port PI of the sample valve VI 4. L24 - Air line from the valve V17 to the inner side of the piston in API. L26 - Air line from the air supply line L27 to the valve V17. L27 - Air supply line. Valves involved Operating valves/position Vll - Solenoid operated air valve/position one (sampling) (IS): connecting the air lines L14 and L15. V14 - Air operated sample valve/position one (sampling) (IS): connecting the ports P5, P6, P7 and P8. SfcEA , OMPI τ V17 - Solenoid operated air valve/position one (acid fill) (IF): connecting the air Unes L26 and L24. Check valves VI 5 - Check valve in the acid Une LI 9 holds acid in the Une L19. VI 6 - Cheek valve in the acid supply line L20 holds acid in the acid Unes L20 and L21. Pressure regulation valves AR2 - Pressure regulation valve in the air Une L26. AR3 - Pressure regulation valve in the air line L14. Flow Air L27 through AR3 through L14 through Vll through L15 through PI into V14. L27 through AR2 through L26 through V17 through L24 into API. Liquor No flow. Sample valve repositioning mode (Reposition 1) The second mode is a sample valve repositioning mode. The sample valve is moved from the sample receiving position to the sample transferring position. Major components involved SL2 - Sample loop/10 cc of acid present. API - Air operated piston for operating the piston in the acid pump/position one (acid fill) (IF). AP2 - Positive displacement acid pump/position one (acid fiU) (IF). Lines involved L14 - Air line from the air supply line L27 to the valve Vll. L16 - Air line from the valve Vll to the port P2 of the sample valve V14. L24 - Air line from the valve V17 to the inner side of the piston in API. L26 - Air line from the air supply line L27 to the valve V17. L27 - Air supply line. Valves involved Operating valves/position Vll - Solenoid operated air valve/position two (trans- f erring) (2T): connecting the air lines L14 and I 6. V14 - Air operated sample valve/position two (transfer¬ ring) (2T): connecting the ports P3, P4, P5 and P6. VI 7 - Solenoid operated air valve/position one (acid fill) (IF): connecting the air Unes L26 and L25. Check valves V15 - Check valve in the acid line L19 holds acid in the Une L19. VI 6 - Check valve in the acid supply line L20 holds acid in the acid lines L20 and L21. Pressure regulation valves AR2 - Pressure regulation valve in the air line L26. AR3 - Pressure regulation valve in the air line L14. Flow Air L27 through AR3 through L14 through Vll through L16 through P2 into VI 4. L27 through AR2 through L26 through V17 through L24 into API. Time 5 seconds or as needed to ensure V14 has completed switching. Acid transferring mode (Transfer 1) The third mode is a transfer mode in which the acid pump forces the 50 cc of acid in the acid pump AP2 through the sample loop SL2 and into the reactor. An initial flushing of the system with acid is performed to ensure that the system is cleaned and filled with acid before sample analysis commences. Major components involved SL2 - Sample loop. API - Air operated piston for operating the piston in the acid pump/position two (acid transfer) (2T). AP2 - Positive displacement acid pump/position two (acid transfer) (2T). Lines involved L14 - Air line from the air supply Une L27 to the valve Vll. LI 6 - Air line from the valve Vll to the port P2 of the sample valve VI 4. L17 - Sample Une from the port P4 of the sample valve V14 to the port R9 of the reactor Rl. LI 9 - Acid line from the acid line L21 to the port P3 of the sample valve V14. L21 - Acid Une from the acid pump AP2 to the acid line L19. L25 - Air line from the valve V17 to the outer side of the piston in API. L26 - Air line from the air supply line L27 to the valve V17. L27 - Air supply line. Valves involved Operating valves/position Vll - Solenoid operated air valve/position two (trans¬ ferring) (2T): connecting the air Unes L14 and L16. V14 - Air operated sample valve/position two (transf¬ erring) (2T): connecting the ports P3, P4, P5 and P6. V17 - Solenoid operated air valve/position two (acid trans¬ fer) (2T): connecting the air Unes L26 and L24. Check valves V12 - Check valve in the sample line L17 prevents the Uquor and acid from returning to the sample circuit once it has entered the reactor. V15 - Check valve in the acid line L19 allows acid to flow from AP2 through L21 through LI 9 into V14.. VI 6 - Check valve in the acid line L20 prevents acid from returning to the acid supply system when AP2 transfers the acid. Pressure regulation valves AR2 - Pressure regulation valve in the air line L26. AR3 - Pressure regulation valve in the air line L14. Flow Air L27 through AR3 through L14 through Vll through L16 through P2 into V14. L27 through AR2 through L26 through V17 through L25 into API to move piston upwardly. Liquid AP2 through L21 through V15 through L19 through P3 through P5 through SL2 through P6 through P4 through VI 2 through L17 into Rl. Time 30 seconds or as needed to ensure AP2 has completed its stroke. Sample valve repositioning mode 2 (Reposition 2) The fourth mode is a second sample valve repositioning mode to move the sample valve from position two (transferring) to position one (sampling), and to move the acid pump from position two (acid transfer) to position one (acid fiU) to fiU the acid pump with acid and antiflocculant. It is necessary to add antiflocculant to the reaction mixture to prevent flocculation and deposition of sulfur in the reactor. It is best to add a known amount of antiflocculant to each reaction by mixing antiflocculant solution with acid when the acid pump refills. By proper choice of antiflocculant storage concentration and proper sizing of antiflocculant lines L9 and acid supply line L20, the proportions of acid and antiflocculant drawn into the acid pump AP2 will be such as to ensure a desirable concentration of antiflocculant in the reaction mixture. Sufficient turbulence exists in L20, L21 and AP2 during the acid fill step to ensure adequate dissolution of antiflocculant in the acid. Major components involved SL2 - Sample loop/approximately 10 cc acid. API - Air operated piston for operating the piston in the acid pump/position one (acid fill) (IF). API - Positive displacement acid pump/position one (acid fiU) (IF). Lines involved L9 - Antiflocculant supply line from antiflocculant storage to acid supply line L20. L14 - Air valve from the air supply line to the valve Vll. L15 - Air Une from the valve Vll to the port PI of the sample valve V14. L20 - Acid supply line from the acid supply to the line L21. L21 - Acid line from the acid supply line L20 to the acid pump AP2. L24 - Air line from the valve V17 to the inner side of the piston in API. L26 - Air lines from the air supply line L27 to the valve V17. L27 - Air supply line. Valves involved Operating valves/position Vll - Solenoid operated air valve/position one (sampling) (IS). V14 - Air operated sample valve/position one (sampling) (IS): connecting the ports P5, P6, P7 and P8. V17 - Solenoid operated air valve/position one (acid fill) (IF): connecting the air Unes L26 and L25. Check valves V15 - Check valve in the acid line L19 prevents backflow of acid from L19 through L21 into AP2. V16 - Check valve in the acid supply line L20 allows acid to flow from L20 through L21 into AP2. Pressure regulation valves AR2 - Pressure regulation valve in the air line L26. AR3 - Pressure regulation valve in the air line L14. Flow Air L27 through AR3 through L14 through Vll through L15 through PI into V14. L27 through AR2 through L26 through V17 through L24 into API. Acid L20 through V16 through L21 into AP2. Antiflocculant L9 through L20 through V16 through L21 into AP2. Time 5 seconds Note: Time not really important - a great excess of time (approximately 12 minutes for the system described) is available for the pump to fill and valve to switch. Standby mode (Standby 2) The fifth mode is a second standby mode (Standby 2) in which the sample valve waits to receive a sample from the filter circuit. It is identical to the first mode (Standby 1) and will not be given in detail again. Its time is 12 minutes, but may change depending on the operation of a particular system. Sample collecting mode (Sample) The sixth mode is a sample collecting mode in which a sample is collected from the filter circuit. Major components involved SL2 - Sample loop/initially filled with 10 cc acid from last sample transfer mode. API - Air operated piston for operating the piston in the acid pump/position one (acid fill) (IF). AP2 - Positive displacement acid pump/position one (acid fiU) (IF). Lines involved L14 - Air line from the air supply line L27 to the valve Vll. L15 - Air supply line from the valve Vll to the port PI of the sample valve V14. L22 - Liquor sample line from the filter system to the port P8 of the sample valve V14. L23 - Sample line from the port P7 of the sample valve VI 4 to the sewer. L24 - Air line from the valve V17 to the inner side of the piston in API. L26 - Air Une from the air supply line L27 to the valve V17. L27 - Air supply Une. Valves involved Operating valves/position Vll - Solenoid operated air valve/position one (sampUng) (IS): connecting the air Unes L14 and L15. V14 - Air operated sample valve/position one (sampUng) (IS): connecting the ports P5, P6, P7 and P8. V17 - Solenoid operated air valve/position one (acid fill) (IF): connecting the air Unes L26 and L25. Check valves VI 5 - Check valve in the acid Une LI 9 holds the acid in the Une L19. V16 - Check valve in the acid supply line L20 holds the acid in the Unes L20 and L21. Pressure regulation valves AR2 - Pressure regulation valve in the air line L26. AR3 - Pressure regulation valve in the air line L14. Flow Air L27 through AR3 through L14 through Vll through L15 through PI into V14. L27 through AR2 through L26 through V17 through L24 into API. Liquor L22 through P8 through P5 through SL2 through P6 through P7 through L23. Time 60 seeonds or as needed to ensure complete flushing and filling of sample loop with a fresh liquor sample. Standby mode (Standby 3) The seventh mode is a third standby mode (Standby 3) in which the sample circuit waits for the reactor circuit to receive the sample. It is identical to the first and fifth modes (Standby 1 and Standby 2) and wiU not be given in detail. The sample loop is filled with Uquor rather than acid at this stage. Sample valve repositioning mode (Reposition 3) The eighth mode is a third sample valve repositioning mode (Reposition 3) in which the sample valve V14 is moved from position one (sampling) to position two (transferring). It is identical to the second mode (Reposition 1) and will not be given in detail. Its time is the same as Reposition 1. Acid transferring mode (Transfer 2) The ninth mode is a second transfer mode (Transfer 2) in which the acid pump forces the 50 cc of acid through the sample loop and into the reactor. This carries the sample into the reactor also. Acid remains in the sample loop to clean the sample loop of any material that may have coated on the tubing during the seventh mode (Standby 3). This acid and the residue wiU be removed from the system during the next sample collecting mode. It is identical in operation to the third mode (Transfer 1) and will not be given in detail. Sample valve repositioning mode (Reposition 4) The tenth mode is a fourth repositioning mode (Reposition 4) in which the sample valve V14 is moved from position two (transferring) to position one (sampling) and the acid pump AP2 is filled with acid and antiflocculant. It is identical to the fourth mode (Reposition 2) and its time is the same. Reactor circuit The reactor is shown in Figures 5 and 6 and the reactor circuit is shown in the bottom left hand section of Figure 1. As may be seen in Figure 5, the reactor Rl has a reactor compartment R2 which is defined by a cover member R3, sidewalls R4 and a base R5. The cover member R3 has four ports: R6 for the vent gas from the reactor to the sewer Une, R7 for the wash water to the reactor, R8 both for the reactor gas from the reactor to the gas chromatograph and for gas under pressure to pressurize the reaction chamber, and R9 for the sample and acid to the reactor. The base R5 defines the bottom R10 of the chamber R2. The bottom R10 is sloped toward the central outlet valve V13 so that the reaction chamber R2 may be washed and drained easily after each reaction. The magnetic spin bar R13 provides turbulence and mixing of the reaction mixture. The base R5 rests on a pressure chamber Rll and pressure within the chamber Rll is maintained by the rubber diaphragm R12 between the base R5 and the pressure chamber Rll. Air enters the pressure chamber Rll through air Une LI and the air pressure holds the valve VI 3 in its upper closed position to maintain Uquid within the reaction chamber R2. When the air pressure is bled from the Une LI, the valve V13 drops into its lower position allowing the reaction chamber R2 to be drained. The liquid goes into outlet Une L18 to be sewered or otherwise treated. The reactor circuit has the foUowiπg components: Major components Rl - Reactor Ml - Magnetic spin bar driver for reactor mixer. Lines LI - Air line from the valve V10 to the reactor outlet pressure chamber Rll. L2 - Line to the gas chromatograph GC. L2A - Line between the reactor gas Une L6 and the gas chromatograph GC. L2B - Line between the reactor pressurization line L1Q and the Une L2A. L3 - Air line between the air supply line L27 and the line Lll. L4 - Water supply line between the water supply and the port R7 of the reactor Rl. L5 - Vent line from the port R6 of the reactor Rl to the sewer. L6 - Reaction gas line from the line L13 to the Une L2A. L7 - Air line between air line L14 and the spin bar driver Ml, L8 - Reactor pressurization Une between the reactor pressurization Une L10 and the reactor line L13. L10 - Reactor pressurization line between air supply line L27 and Unes L8 and L2B. Lll - Connecting line between the air line L3 and the gauge line L12, and the reactor gas Une L6, the air pressure line L8 and the reactor line L13. LI 2 - Gauge line between the air Une L3 and the connect¬ ing Une Lll, and the gauge protector Gl and the pressure gauge G2. L13 - Reactor line between the port R8 of the reactor Rl and the juncture of the reactor gas Une L6, the reactor pressurization line L8 and the connecting Une Lll. LI 4 - Air line between the air supply line L27 and the valve VI 0. L17 - Sample line between the sample valve V14 and the port R9 of the reactor Rl. L18 - Outlet line from the valve V13 of the reactor Rl. Valves Operating valves (solenoid operated) V3 - Valve in the air Une L3. Two position: open; closed. V4 - Valve in the water line L4. Two positions: open; closed. V5 - Valve in the vent line L5. Two positions: open; closed. V6 - Valve in the reaction gas line L6. Two positions: open; closed. V8 - Valve in the reactor pressurization line L8. Two positions: open; closed. V10 - Valve between the air line L14 and the air line LI. Two positions: open; closed. Operating valves (air operated) VI 3 - Outlet valve in the reactor Rl between the reaction chamber R2 and the outlet line L18. It is operated by air pressure from the line LI. Two positions: closed when the air is on; open when the air is off. Check valves V12 - Check valve in the sample line L17 preventing either the sample, the reaction gas or air from flowing back through the sample line L17. Pressure regulation valves AR1 - Pressure regulation valve in the air line LI. AR3 - Pressure regulation valve in the air line L14. AR4 - Pressure regulation valve in the air line L3. AR5 - Pressure regulation valve in the reactor pressuriza¬ tion line L10. O PI Repair valves (normaUy open, manually operable) V7 - Repair valve in the air Une L7. Ports R6 - Port in the reactor Rl for the vent Une L5. R7 - Port in the reactor Rl for the water line L4. R8 - Port in the reactor Rl for the reactor Une L13. R9 - Port in the reactor Rl for the sample line L17. The operating sequence of the reactor is as f oUows: (1) The reactor is cleaned: (a) The reactor is drained. (b) The reactor is filled with water. (c) The reactor is again drained. (d) The reactor is again filled with water. (e) The reactor is again drained. (f) The reactor is again filled with water. (g) The reactor is again drained. (2) The reactor is vented for 5 seconds, then resealed. (3) The acid and sample are placed in the reactor and the reaction starts. (4) After approximately 11 minutes, the reactor is placed under pressure using a precise air pressure regulator. This is important if a direct relationship between gas chromato¬ graph output and Uquor concentration is to be obtained. The final reactor pressure should be about 2 psi above the highest total reactor pressure resulting from the sum of aU the partial pressures or the expected components or 26 psi above the ambient pressure. This is to compensate for the" dependence of reactor pressure on Uquor concentration which would provide an incorrect reading if there was no compensation. (5) The reaction is allowed to go to completion. (6) The reaction gas is transferred to the gas chromatograph. The time of transfer must be long enough to obtain a representative sample of gas in the sample loop SLl of the gas chromatograph. This usually requires 40-50 seconds. The cycle takes approximately 19 minutes, but will vary according to the characteristics of each individual system. Standby mode (Standby) The first mode of the reactor circuit is a standby mode in which the reactor is waiting to receive the sample. It usually occurs only at start¬ up. The reactor contains whatever was present in it at shutdown. This can 5 be the old reaction mixture, wash water, etc. Major components involved Rl - Reactor Lines involved LI - Air line from the valve V10 to the valve V13. 10 L14 - Air line from the air supply line L27 to the valve V10. L27 - Air supply line. Valves involved Operating valves/position 15 V3 - Valve in the air line L3/closed. V4 - Valve in the water line L4/closed. V5 - Valve in the vent line L5/closed. V6 - Valve in the reaction gas line L6/closed. V8 - Valve in the air pressure line L8/closed. 20 V10 - Valve between the air lines L14 and Ll/open. VI 3 - Outlet valve in the reactor Rl /closed. Pressure regulation valves AR1 - Pressure regulation valve in the air line LI. AR3 - Pressure regulation valve in the air line L14. 25 Flow Air — - L27 through AR3 through L14 through VI 0 through LI through AR1 into Rll to hold VI 3 closed. Vent mode (Vent) 30 The second mode is a vent mode. The reactor is vented when the sample valve V14 is repositioned from position one (sampUng) to position two (transferring). This allows the pressure in the reaction chamber to reach atmospheric pressure prior to sample injection. The gas in the reactor contains, at most, minor amounts of carbon dioxide and hydrogen sulfide. 35 Major components involved Rl - Reactor Lines involved LI - Air Une from the valve V10 to the chamber Rll of the reactor Rl. L5 - Vent line from the port R6 of the reactor Rl to the atmosphere. L14 - Air line between the air supply line L27 and the valve V10. L27 - Air supply line. Valves involved Operating valves/position V3 - Valve in the air Une L3/closed. V4 - Valve in the water Une L4/closed. V5 - Valve in the vent line L5/open. V6 - Valve in the reaction gas line L6/closed. V8 - Valve in the pressure Une L8/closed. V10 - Valve between the air lines L14 and Ll/open to hold the outlet valve VI 3 of the reactor Rl closed. VI 3 - Outlet valve from the reactor Rl/closed. Pressure regulation valves AR1 - Pressure regulation valve in the air line LI. AR3 - Pressure regulation valve in the air line L14. Flow Air Rl through R6 through V5 through L5 to vent line to sewer. L27 through AR3 through L14 through V10 through LI through AR1 into Rll to hold V13 closed. Time 5 seconds as needed for air in reactor to reach equiUbrϊum with atmospheric pressure. In the vent mode prior to the introduction of the sample, the vent mode must end prior to introduction of sample into reactor to ensure no loss of reaction gas products. Drain mode (Drain) The third mode is a reactor drain mode. During the washing cycle the reactor is drained either of reaction products or of wash water. Major components involved Rl - Reactor Lines involved LI - Air line from the valve V10 to the outlet valve V13 of the reactor Rl. L3 - Air line from the air supply line L27 to the connecting line Lll. Lll - Connecting Une from the air line L3 to the reactor Une LI 3. LI 3 - Reactor line from the connecting line Lll to the port R8 of the reactor Rl. L18 - Outlet line from the reactor Rl. L27 - Air supply line. Valves involved Operating valves/position V3 - Valve in the air line L3/open. V4 - Valve in the water line L4/closed. V5 - Valve in the vent line L5/closed. V6 - Valve in the reaction gas line L6/closed. V8 - Valve in the air pressure line L8/closed. V10 - Valve between the air lines L14 and Ll/elosed to bleed air from the line LI to open the valve V13. VI 3 - Outlet valve of the reactor Rl/open to drain the reactor through the outlet line L18. Check valves V12 - Check valve in the sample line L17 prevents air from escaping through the sample Une L17. Pressure regulation valves AR4 - Pressure regulation valve in the air line L3. Flow Air No flow in line LI. L27 through AR4 through L3 through V3 through Lll through LI 3 through R8 into Rl. Liquid Rl through VI 3 through L18. Time 10 seconds or as needed to completely drain reactor. Fill mode (FiU) The fourth mode is the reactor fiU mode. During the wash cycle, the reactor is filled with wash water. Major components involved Rl - Reactor Lines involved LI - Air line from the valve V10 to the chamber Rll of the reactor Rl. L4 - Water Une between the water supply and the port R7 of the reactor Rl. L5 - Vent Une from the port R6 of the reactor Rl to the atmosphere. L14 - Air line from the air supply line L27 to the valve V10. L27 - Air supply Une. Valve involved Operating valves/position V3 - Valve in the air line L3/closed. V4 - Valve in the water line L4/open. V5 - Valve in the vent line L5/open. V6 - Valve in the reaction gas line L6/closed. V8 - Valve in the air pressure line L8/closed. V10 - Valve between the air lines L14 and Ll/open. VI 3 - Outlet valve of the reactor Rl/elosed. Check valves V12 - Check valve in the sample line L17 prevents air from entering the sample circuit. Pressure regulation valves AR1 - Pressure regulation valve in the air line LI. AR3 - Pressure regulation valve in the air Une LI 4. Flow Air Rl through R6 through V5 through L5 to vent line to sewer. L27 through AR3 through L14 through V10 through LI through AR1 into Rll to hold VI 3 closed. OMPI Water L4 through V4 through R7 into Rl. Time 20 seconds or as needed to sufficiently fill reactor with water. Sample transferring mode (Transfer) The sixth mode is the sample transferring mode. The sample is received from the sampling circuit. Major components involved Rl - Reactor. Lines involved LI - Air line from the valve V10 to the outlet valve 13 of the reactor Rl. L14 - Air line from the air supply line L27 to the valve V10. L17 - Sample line from the sample circuit to the port R9 . of the reactor Rl. L27 - Air supply line. Valves involved Operating valves/position V3 - Valve in the air line L3/closed. V4 - Valve in the water line L4/elosed. V5 - Valve in the vent line L5/closed. V6 - Valve in the reaction gas line L6/closed. V8 - Valve in the air pressure line L8/closed. V10 - Valve between the air lines L14 and Ll/open. V13 - Outlet valve from the reactor Rl/elosed. Check valves V12 - Check valve in the sample line L17 prevents the sample or reaction gases from returning through line L17. Pressure regulation valves AR1 - Pressure regulation valve in the air line LI. AR3 - Pressure regulation valve in the air line L14. Flow Air L27 through AR3 through L14 through V10 through LI through AR1 into Rll to hold V13 closed. Liquor SL2 through V14 through L17 through V12 through R9 into Rl. Acid AP2 through L21 through V15 through L19 through V14 through SL2 through L17 through V12 through R9 into Rl. Time 30 seconds or as needed to ensure complete transfer of acid and sample. Reaction mode (Reaction) The seventh mode is the reaction mode. The reaction between the acid and the sample takes place in the reaction chamber. There are two stages in the reaction mode, reaction 1 and reaction 2. Reaction 2 is the continuation of reaction 1 after pressure has been appUed to the reaction chamber and is identical to reaction 1. Major components involved Rl - Reactor Lines involved LI - Air line from the valve V10 to the outlet valve V13 of the reactor Rl. L14 - Air line from the air supply line L27 to the valve V10. L27 - Air supply line. Valves involved Operating valves/position V3 - Valve in the air line L3/closed. V4 - Valve in the water Une L4/closed. V5 - Valve in the vent line L5/closed. V6 - Valve in the reaction gas Une L6/closed. V8 - Valve in the air pressure Une L8/closed. V10 - Valve between air lines L14 and Ll/open. VI 3 - Outlet valve in the reactor Rl/closed. Check valves V12 - Check valve in the sample line L17 prevents the reaction gas from entering the sample circuit through the sample line LI 7. Pressure regulation valves AR1 - Pressure regulation valve in line LI. AR3 - Pressure regulation valve in air line L14. Flow Air L27 through AR3 through L14 through V10 through LI through AR1 into Rll to hold VI 3 closed. Time The total time of the reaction is about 15 minutes. It is divided into the two parts before and after pressure is applied. Pressurization mode (Pressure) The eighth mode is a pressurization mode. Eleven minutes after the reaction begins, air pressure is appUed through a precise regulator to the reaction chamber to maintain a constant final reactor pressure. It was decided to pressurize 11 minutes into the reaction, because at this time: 1) the reaction is essentially complete and no further pressure rise is anticipated; 2) four minutes of reaction time remain, which allows the air which has been added in the pressurization step to become well mixed with the reaction gases to yield a homogeneous reaction gas sample at the end of the reaction. The time of pressurization may be changed as needed in response to the characteristics of individual reactor systems. The pressurization step was added in response to observations made during the development of the system. In order to make vaUd comparisons among samples, it is necessary to have a constant final gas pressure. If this is not done, then the experience of our experiments will be repeated. In these experiments, the final gas pressure inside the reactor was aUowed to remain at whatever pressure existed due to the release of carbon dioxide and hydrogen sulfide from the reaction. This pressure varied according to the amounts of sodium carbonate and sodium sulfide in the liquor sample. It was observed that, although an increase in sodium carbonate concentration in the Uquor did cause an increase in the carbon dioxide peak area generated by the gas chromatograph, the relationship was not directly proportional. Furthermore, the carbon dioxide peak area was influenced by the amount of Na 2 S in the Uquor, which resulted in erroneous sodium carbonate measurements due to changes in the sodium sulfide concentration in the Uquor. The measurement of sodium sulfide in the Uquor was affected in the same manner. After this was reaUzed, it was decided to adjust the pressure so that there would be the same total moles of gas in the system for each measurement. This can be done by maintaining the reaction gas in the reactor at a constant pressure at the completion of the reaction. The addition of air will act as a diluent, and the total moles of gas wUl remain fixed among a number of samples. It has been found that the total pressure of air, carbon dioxide and hydrogen sulfide, under the conditions existing in the reactor, wiU not exceed 24 psi. By adding additional air to obtain a 26 psi pressure, it is possible to obtain gas samples each containing a constant total number of moles of gas. The air has substantiaUy no carbon dioxide or hydrogen sulfide and does not affect the readings for carbon dioxide or hydrogen sulfide generated in the reaction. The peak areas for carbon dioxide and hydrogen sulfide will then be directly proportional to the concentrations of sodium carbonate and sodium sulfide, respectively, in the liquor. Furthermore, sodium carbonate measurements wiU not be affected by the sodium sulfide concentration in the liquor, nor will the sodium sulfide measurements be affected by the sodium carbonate concentration. The measurements of sodium carbonate and sodium sulfide are then used to control the process. Major components involved Rl - Reactor Lines involved LI - Air line between the valve VI 0 and the outlet valve VI 3 of the reactor Rl. L8 - Reactor pressurization line between the reactor pressurization Une L10 and the reactor Une L13. L10 - Reactor pressurization Une between the reactor pressurization line L8 and the air supply Une L27. Lll - Connecting line between the reactor pressurization line L8 and the pressure gauge line L12. L12 - Pressure gauge line from the connecting line Lll to the gauge protector Gl and the air pressure gauge G2. L13 - Reactor line between the reactor pressurization Une L8 and the port R8 of the reactor Rl. L14 - Air line between the air supply line L27 and the valve VI 0. L27 - Air supply line. Valves involved Operating valves/position V3 - Valve in the air line L3/closed. V4 - Valve in the water line L4/closed. V5 - Valve in the vent line L5/closed. Vδ - Valve in the reaction gas line L6/closed. V8 - Valve in the reactor pressurization line L8/open. V10 - Valve between the air Unes L14 and Ll/open. VI 3 - Outlet valve in the reactor Rl/closed. Check valves V12 - Check valve in the sample line L17 prevents reac¬ tion gases from entering the sample circuit through the sample line. " Pressure regulation valves AR1 - Pressure regulation valve in the air line LI. AR3 - Pressure regulation valve in the air line L14. AR5 - Pressure regulation valve having a precision of + .02 psi in the reactor pressurization line L10. Flow Air L27 through AR2 through L14 through V10 through LI through AR1 into Rll to hold VI 3 closed. L27 through AR5 through L10 through V8 through L8 through LI 3 through R8 into Rl. Reaction gas transfer mode (Gas to G.C.) The ninth mode is the reaction gas transfer mode. The reaction gas is transferred to the gas chromatograph (G.C). This requires enough OMP time to aUow a representative sample to be received in the sample loop SLl of the gas chromatograph. Major components involved Rl - Reactor Lines involved LI - Air Une between the valve V10 and the reactor outlet valve V13. L2A - Line between the reaction gas Une 6 and the gas chromatograph. L6 - Reaction gas Une between the reactor Une L13 and the gas chromatograph Une L2A. L13 - Reactor Une between the port R8 of the reactor Rl and the reaction gas Une L6. L14 - Air line between the air supply line L27 and the valve V10. L27 - Air supply Une. Valves involved Operating valves/position V3 - Valve in the air Une L3/closed. V4 - Valve in the water Une L4/elosed. V5 - Valve in the vent line L5/closed. V6 - Valve in the reaction gas line L6/open. V8 - Valve in the air pressure line L8/closed. V10 - Valve between the air lines L14 and Ll/open. VI 3 - Outlet valve in the Reactor Rl/closed. Check valves V12 - Check valve in the sample line L17 prevents reac¬ tion gas from entering the sample circuit through the sample line LI 7. Pressure regulation valves AR1 - Pressure regulation valve in the air line LI. AR3 - Pressure regulation valve in the air line LI 4. Flow Air L27 through AR3 through L14 through V10 through LI through AR1 into Rll to hold VI 3 closed. Reaction gas Rl through R8 through L13 through V6 through L6 through L2A to gas chromatograph. Time 40 seconds or as needed to ensure that the gas chromato¬ graph has received a representative reaction gas sample. Stop transfer mode (Stop) The tenth mode is the stop transfer mode. The reaction gas valve Vδ is closed. Time is aUowed for the pressure in the gas chromatograph system to equalize. Major components involved Rl - Reactor Lines involved LI - Air line between the valve VI 0 and the reactor outlet valve VI 3. L14 - Air line between the air supply line L27 and the valve V10. L27 - Air supply line. Valves involved Operating valves/position V3 - Valve in the air line L3/closed. V4 - Valve in the water line L4/closed. V5 - Valve in the vent line L5/closed. V6 - Valve in the reaction gas line L6/closed. V8 - Valve in the air pressure line L8/closed. V10 - Valve between the air lines L14 and Ll/open. VI 3 - Outlet valve in the Reactor Rl/closed. Check valves V12 - Check valve in the sample line L17 prevents reac- tion gas from entering the sampUng system through the sample Une. Pressure regulation valves AR1 - Pressure regulation valve in air line LI. AR3 - Pressure regulation valve in air line L14. Flow Air L27 through AR3 through L14 through V10 through LI through AR1 into Rll to hold V13 closed. Time 5 seconds or as needed for the pressure in the gas chroma¬ tograph sample chamber to equilibrate. Magnetic spin bar driver The Uquor within the reactor chamber R2 is stirred by the mixing rod R13 within the reactor and resting on the drain valve V13 in the bottom of the reactor. This rod is magnetically coupled with and rotated by the magnetic spin bar driver M2 in chamber Ml. The magnetic spin bar driver is shown in Figures 7 and 8. A powerful horseshoe magnet M3 faces upwardly toward the spin bar R13. The horseshoe magnet M3 is mounted on a rotating plate M4. Any type of mounting may be used. It may be adhered to the plate M4 with epoxy or other type of adhesive. It is shown mounted in an arcuate depression in the upper face of the plate M4. The plate M4 rests on a base M5. Both the rotating plate M4 and the base M5 are shown as being circular in cross section. The base M5 has an upper flat horizontal supporting surface M6 around its periphery. A circular recessed section M7 is within the periphery. The recessed section M7 also has a flat horizontal surface below surface M6 and a vertical side waU that extends from its surface to the supporting surface M6. A circular further recessed section M8 is within section M7. The surface of recessed section M8 is also flat and below the surface of section M7. The section M8 also-has-a vertical side waU that extends from its surface to the surface of section M7. The periphery of the base M5, the periphery of the section M7 and the periphery of the section M8 are concentric. The section M8 holds a nylon and glass ball bearing M9. The plate M4 has a cylindrical shaft M10 that fits and rotates within bearing M9. A motor section Mil of the plate M4 fits and rotates within the recessed section M7 of the base M5. There is a clearance between the motor section Mil and the surfaces of the recessed section M7. The motor section Mil is circular and concentric with both the cylindrical shaft M10 and the outer circular periphery M12 of the plate M5. The periphery M13 of the motor section Mil is broken by equaUy spaced radial slots or indentations M14. OMPI An air Une Ml 5 extends through the base M5 below the recessed section M8. Two secondary air passages M16 extend from air line M15 angularly upwardly to the surface of the recessed section M7. The outlets of the secondary air passage Ml 6 are aligned with the radial slots Ml 4 to aUow air to impinge against the side walls of the radial slots M14 and rotate the plate M4. The outlets of the secondary air passages Ml 6 are shown as 180° apart and on opposite sides of air line Ml 5. The outlets may be paraUel to a tangent to the periphery of recessed section M7 or be angled toward the periphery. The outlets may be, as shown, near the periphery of recessed section M7. Air from air line L7 passes through line Ml 5 and passages Ml 6 to impinge against the walls of the radial slots M14 to rotate the plate M4. The escaping air from the secondary air passages Ml 6 also acts as a bearing for the plate M5 between the surface M17 of the plate M4 and the supporting surface M6 of the base M5. The air eventually escapes along the surface M6 and out through the gap between the base and the revolving plate. The rotation of plate M4 rotates the magnet M3. The rotating magnet M3 rotates the spin bar R13. The magnetic spin bar drive has the following components and operation: Major components involved Ml - Magnetic spin bar mixer chamber. M2 - Magnetic spin bar mixer driver. Lines involved L7 - Air line from the air line L14 to the chamber Ml. L14 - Air line from the air supply line L27 to the air line L7. L27 - Air supply line. Valves involved Pressure regulation valves AR3 - Pressure regulation valve in the air line L14. Repair valves V7 - Repair valve in the air pressure Une L7. Flow L27 through AR3 through L14 through V7 through L7 into Ml to operate M2. It wiU be appreciated that the magnetic spin bar drive may also be turned off and on depending on whether the reactor chamber is f Uled or empty by changing the valve V7 to a solenoid operated on/off valve and operating it on the same cycle as valve VI 0 which controls the outlet valve VI 3 of the reactor. Valves V7 and V10 would open and close together. Gas Chromatograph System In the reactor the green Uquor or white Uquor is reacted with acid to form carbon dioxide and hydrogen sulfide gases. The concentration of these gases is measured in the gas chromatograph. The chromatograph outputs a continuous analog signal corresponding to the flow rate of gas through the detector of the chromatograph. By integrating this signal for the proper time intervals (corresponding to the time of appearance of carbon dioxide and hydrogen sulfide at the detector), the concentrations of carbon dioxide and hydrogen sulfide in the reaction gas are measured. CaUbration of the reactor/gas chromatograph system using liquors of known concentration aUows the carbon dioxide and hydrogen sulfide measurements to be converted directly to a determination of sodium carbonate and sodium sulfide in the Uquor sample. The analysis process takes about four minutes for both carbon dioxide and hydrogen sulfide. It may be necessary to analyze only for carbon dioxide in the green Uquor and causticizer white liquor samples. This would reduce the analysis time for these samples to one and one-half minutes. The gas ehromatograph may be used to successively analyze the reaction gases from a number of reactors. For one slaking/causticizing Une, three Uquor samples should be analyzed, resulting in a three-reactor analyzer system. For this reason the valve VI is a four position valve having four inlets from the reactors or other outside sources and one outlet to the gas chromatograph. It cycles through the four positions until is is at the proper position to receive reaction gas from the selected reactor. It requires approximately five seconds to move from one position to the next. Another five seconds is allowed to electronically cheek the position of the valve. The inner details of a gas chromatograph wiU not be given. It is a standard piece of equipment and its details, other than aUowing time for it to cycle through its procedure and the results of its analysis are not important here. There are a number of valves in the gas chromatograph that aUow the sample loop to be filled, the gas sample to be carried to the analysis column, and the sample loop and analysis column to be purged and backflushed. This discussion will not include the standard heUu flush and backflush that occurs within the gas chromatograph itself since these are normal functions of the instrument. We wiU merely note that these valves and operations exist in any gas chromatograph and wiU give only a general overview of the process and the apparatus. The only procedures that will be described in detail are the external procedures. The chromatrograph circuit has few parts. These are: Components Major components GC - Gas chromatograph/two positions: position one (standby) is used in three different modes - mode 1A (bypass); mode IB (gas transfer); mode 1C (purge) - position two (analyze). SLl - Sample loop for the gas chromatograph. Lines L2 - Line to the gas chromatograph L2A - Line from the reaction gas line L6 to the gas chromatograph GC. L2B - Line from the calibration gas line L7 to the gas chromatograph line L2A. L2C - Line from the air pressure line L10 to the gas chromatrograph line L2B. L6 - Reaction gas line from the reactor Rl to the gas chromatograph Une L2A. L7 - Calibration gas line from the CaUbration gas supply to the gas chromatograph Une L2B. L10 - Air pressure line from the air supply line L27 to the gas chromatograph line L2C. L14 - Air line from air supply line L27 to air line L53. L27 - Air supply line. L53 - Air line from air line L14 to valve VI to operate the valve. fCJRE OMPl _ Valves Operating valves VI - Valve in the gas chromatograph Une L2A. Four positions to bring sample into gas chromatograph: position one (reactor one); position two (reactor two); position three (reactor three); position four (spare). V2 - Valve in the high pressure air Une L2C. Two positions: open; closed. V6 - Valve in the reaction gas Une L6. Two positions: open; closed. V7 - Valve in the CaUbration gas Une L7. Two positions: open; closed. Pressure regulation valves AR3 - Pressure regulation valve in air Une L14. AR5 - Pressure regulation valve in high pressure air line L10. In the sequence of operations, the gas chromatograph takes a gas sample into the sample loop SLl, analyzes the gas sample, purges the sample from the system and backflushes the system. It then waits for a new sample to be suppUed. Standby mode (Standby) The first mode is a standby mode. The gas chromatograph is waiting for a sample from the reactor circuit. Major components involved GC - Gas chromatograph/position one (standby) Valves involved Operating valves/position VI - Valve in gas chromatograph Une L2A/position four (closed). This is exemplary. The valve may be in any position at start-up. It will depend upon the valve position when the system was shut down. V2 - Valve in high pressure air line L2C/closed. V6 - Valve in the reaction gas Une L6/elosed. V7 - Valve in the calibration gas Une L7/closed. Flow No flow of reaction gases. Reposition mode (Reposition) The second mode is a reposition mode (Reposition). The valve VI is repositioned around its four positions until it is Uned up with the right reactor. It moves in the same direction, either clockwise or counter¬ clockwise, requiring five seconds to move. An additional five seconds is alloted for the system to check the position of the valve. If its location is not right, it wiU move again and be checked again. This will continue until it is in the right position. The other valves and the gas chromatograph remain as they are. Standby mode (Standby 2) The third mode is a new Standby mode (Standby 2) in which aU the valves remain in their positions until the reactor circuit is ready to transfer a gas sample. Reaction gas transfer mode (Gas to G.C.) The fourth mode is a reaction gas transfer mode. The gas chromatograph is internally valved so that the reaction gas goes through the sample loop and then to the vent to sewer. The time of this transfer is long enough for a representative sample to be received. The initial gas entering the sample loop SLl will usually not be representative of the bulk of gas in the reactor. The lines from the reactor to the gas chromatograph are initially filled with air from the previous air purge mode. Air must be flushed from these lines and the sample loop to ensure a representative sample of reaction gas is obtained. It requires a period of time to obtain a steady state sample in the sample loop. Consequently the time will vary depending on the several factors influencing the gas transfer to the sample loop. These factors may include the arrangement and dimensions of the tubing between the reactor and the sample loop, the sample purge condi- tions, and the conditions of pressure, gas composition, etc. existing in the reactor itself at the time of gas transfer. The time is usually between 40 and 60 seconds. Major components involved GC - Gas chromatograph/mode 1A (gas transfer). SLl - Sample loop for the gas chromatograph. Lines involved L2A - Gas chromatograph Une from the reaction gas Une L6 to the sample loop SLl. L6 - Reaction gas line from the reactor to the line L2A. L13 - Reactor Une from the port R8 of the reactor Rl to the line L6. Valves involved Operating valves/position VI - Valve in gas chromatograph Une L2A/position one (reactor circuit one). V2 - Valve in high pressure air Une L2C/closed. V6 - Valve in reaction gas line L6/open. V7 - Valve in the calibration gas Une L7/closed. Flow Reacton gas Rl through Rδ through L13 through V6 through L6 through L2A through VI through SLl to sewer. Time 40 seconds or as needed to obtain a representative sample of reaction gas in the sample loop. The time of 40 seconds is representative. The length of time is the time required to obtain a representative sample of reaction gas in the sample loop SLl. Stop sample mode (Stop) The fifth mode is a stop sampling mode in which the reaction gas he gas chromatograph is stopped and the gas pressure in the sample loop Uowed to equalize with atmospheric pressure. Major components involved GC - Gas chromatograph/mode IB (gas transfer). SLl - Sample loop of the gas chromatograph. Valves involved Operating valves/position VI - Valve in gas chromatograph line L2A/position one (reactor circuit one). V2 - Valve in high pressure air line L2A/closed. V6 - Valve in reaction gas line L6/closed. V7 - Valve in calibration gas line L7/closed. Flow No flow Time 5 seconds or as needed for conditions in sample loop to equilibrate. Analysis mode (Analyze) The sixth mode is an analysis mode in which the sample is analyzed in the gas chromatograph. There is no change in the external circuit. The change is in the internal system of the gas chromatograph. It switches from position two (gas transfer) to position three (analyze). Major components involved GC - Gas chromatograph/position two (analyze). SLl - Sample loop of the gas chromatograph. Valves involved Operating valves/position VI - Valve in gas chromatograph line L2A/position one (reactor circuit one). V2 - Valve in high pressure air line L2A/closed. V6 - Valve in the reaction gas line L6/closed. V7 - Valve in the calibration gas line L7/closed. Flow Helium through sample loop carries reactor gas through column past detector out vent. Time 4 minutes depending on elutriation time of carbon dioxide and hydrogen sulfide through column. The time may be more or less than 4 minutes depending on the length of the column, column packing characteristics, helium flow rate, etc. The time wiU be one and one-half minutes if the analysis is only of carbon dioxide. Again, the time may be more or less than one and one-half minutes because of other factors. Sample purge mode (Purge) The seventh mode is a gas purge mode in which high pressure air is used to purge the sample from the sample loop and the Unes between the sample loop and reactor. J JXE OMPI Major components involved GC - Gas chromatograph/mode 1C (purge). SLl - Sample loop for gas chromatograph. Lines involved L2 - Gas chromatograph line from high pressure air Une L10 to the sample loop SLl. Includes Unes L2A, L2B and L2C. L10 - High pressure Une between air supply Une L27 and the gas chromatograph Une L2. L27 - Air supply line. Valves involved Operating valves/position VI - Valve in the gas chromatograph Une L2A/position one (reactor circuit one). V2 - Valve in the high pressure air Une L2C/open. V6 - Valve in the reaction gas Une L6/closed. V7 - Valve in the CaUbration gas line L7/elosed. Pressure regulation valves AR5 - Pressure regulation valve in the high pressure air Une L10. Flow Air L27 through AR5 through L10 through V2 through L2 through SLl to vent to sewer. Time 1 minute 5 seconds or as needed to adequately purge lines and loop. During the time that the Uquor sample in reactor 1 is completing its reaction, the valve VI would move to postions 2 and 3, and the gas chromatograph would be analyzing the gas samples from the second and third reactors. Data coUection and analysis The gas chromatograph output circuitry generates voltage "peaks" which correspond to the appearance of each gas component at the detector of the gas chromatograph. The time interval (from the start of the analysis) during which each component (air, carbon dioxide and hydrogen sulfide) wiU pass through the detector is a characteristic of each component gas. This time interval during which each component appears at the detector is very reproducible and is easily estabUshed for each gas. The gas chromatograph output circuitry generates a continuous 0-1 volt analog signal which is proportional to the flow of gas through the detector. During the time interval each component passes through the detector, a voltage "peak" is generated in response to the appearance of the component. Figure 9 is a plot of G.C. voltage output over the course of a gas analysis resulting from a typical green Uquor sample. Each component of the gas sample is identified, and the time interval during which it appears is noted. The voltage "peaks" for each component are easily observed from the figure. The integrated voltage for each component (which is equal to the area under each peak) is proportional to the amount of the component in the gas sample. Furthermore, the carbon dioxide and hydrogen sulfide integrated voltages are proportional to the sodium carbonate and sodium sulfide concentrations in the liquor. The integrated peak areas for CO and H 2 S are therefore a measure of the Na 2 CO 3 and Na 2 S concentrations in the liquor sample. The data coUection circuit enables the carbonate/sulfide analyzer to convert the voltage peaks generated by the gas chromatograph into values which correspond to the concentrations of Na 2 CO 3 and Na 2 S in the liquor. The data coUection circuit consists of the following major components: GC - Gas chromatograph output circuitry VCO - Voltage-to-frequency converter M - Microcomputer A schematic of the data collection circuit is shown in Figure 10. The associated wiring and components needed to Unk the major components are known and are therefore not iUustrated. In order to calculate the concentration of Na 2 C0 3 and Na 2 S in the liquor sample, the CO 2 and H 2 S voltage peaks must be integrated. There are many methods which may be utilized to accomplish the integra¬ tion. The preferred method of peak integration is to utilize a voltage-to- frequency converter (VCO) to convert the 0-1 volt G.C. output signal to a 0-10,000 HZ frequency signal. The continuous series of electronic pulses thus generated is utilized as input to a digital microcomputer. The time intervals corresponding to the appearance of the CO 2 and H 2 S peaks are programmed into the microcomputer software. During the discrete time intervals corresponding to the peak for each component, the microcomputer counts the total number of pulses generated by the VCO for the peak period. The number of pulses thus counted is a measure of the peak area. The peak area measurements thus obtained for COo and H S are proportional to the concentrations of Na 2 C0 3 and Na 2 S, respectively, in the Uquor sample. The microcomputer, furthermore, aUows for calibration of the analyzer by providing the abiUty to convert the pulse count measurements to direct determinations of Na 2 C0 3 and Na 2 S in the Uquor. The pulse count is directly proportional to the concentration of chemical in the Uquor. By analyzing several Uquors of known concentrations, and measuring the pulse counts generated from these known liquors, one can easily estabUsh the correct conversion factors to convert the pulse counts to concentration measurements. These conversion factors are then stored in the micro¬ computer software. The conversion factors are appUed to the pulse counts for aU subsequent liquor samples to provide direct determinations of Na«COo and Na„S in the liquor. The liquor concentrations may be given as printed data or converted to analog signals for use as input to control devices. Methods of generating such outputs are varied and are weU known. Reactor temperature measurement system The measurement of sodium carbonate and sodium sulfide gener¬ ated by the carbonate/sulfide analyzer have been observed to be affected by the temperature at which the reaction occurs. The reaction temperature is primarily governed by the temperature inside the analyzer cabinet. The measurements generated by the analyzer vary in direct proportion with the cabinet temperature. As the cabinet temperature increases, the resultant measurements of sodium carbonate and sodium sulfide correspondingly increase. There must be compensation for this phenomena if accurate measurements are to be obtained for aU samples despite reactor tempera¬ ture variations. It has been determined that the best method of eUminating measurement errors due to reactor temperature variations is to apply a correction factor to each measurement based on the cabinet termperature during the reaction. In order to determine the proper factor for each measurement, the cabinet temperature is measured at the completion of OMPI each reaction. The proper correction factors, based on the cabinet temperature, are then automatically computed for each sample and applied to the "raw" or "uncorrected" values generated by the gas chromatograph. This strategy has been found to be an effective method of eUminating errors caused by reaction temperature variations. It has been found that for each 1°C deviation from a reference temperature the G.C. measured area for Na 2 CO 3 increases or decreases 0.4% and the G.C. measured area for Na 2 S increases or decreases 0.7%. The correction for Na 2 CO 3 is: CA = MA *1 + 0.004 (To - T)* and for Na 2 S is: CA = MA il + 0.007 (To - T)* CA = corrected area MA = G.C. measured area To = reference temperature T = actual temperature of gas from reactor As an example if the reference temperature is 30°C and the actual temperature is 27°C, then for Na 2 CO 3 CA = MA l + 0.004 (30 - 27)έ = 0.988 MA and for Na 2 S CA = MA il + 0.007 (30 - 27)* = 0.979 MA The temperature measurement system uses a resistance tempera¬ ture detector (RTD) mounted inside the cabinet, and a relay which closes to allow the detector to be sampled by the analyzer data coUection system. The relay closes to aUow sampUng of the detector immediately upon completion of the transfer of reactor gases to the gas chromatograph sample chamber. It remains closed for 20 seconds or as needed to obtain an accurate temperature measurement. The RTD signal is converted to a temperature measurement in the data coUection software. A resistance temperature detector has been found to be the best suited temperature measuring device. The detector element exhibits an electrical resistance which varies directly with temperature. This resis¬ tance is easily measured electronically and is easily converted to a temperature reading since the calibration of these elements is weU docu- mented. Other devices, such as thermocouples or thermistors, which exhibit electrical properties that vary as a function of temperature could also be utiUzed in this application. Materials of construction AU materials have been selected to ensure maximum service- abiUty and resistance to the effects of heat, pressure, and the corrosive properties of the Uquid and gas streams. We have found the foUowing materials to be the best for the specific applications Usted below: The reactor's top and base is constructed of P.V.C. (polyvinyl chloride). The fixture at top of pump is P.V.C. The mounting board for aU solenoids, etc. is P.V.C. The magnetic spin bar driver is P.V.C. The reactor cylinder and the acid pump cyUnder are glass. AU tubing that is in direct contact with acid or the gases is teflon, aU other tubing is nylon. AU fittings that are in direct contact with acid or the gases are nylon. The reactor gas to gas chromatograph and the vent solenoids are teflon. AU check valves are teflon. The sample loop is nylon. The acid pump piston is teflon coated 316 S.S. (stainless steel). The fittings that come into indirect contact with gases or those that are flushed with air or water are 316 S.S. AU fittings, tubing, valves, columns, etc. within the gas chromatograph are 316 S.S. The gas isolation valve mounted on front of gas chromatograph is 316 S.S. The air, water, pressurization and purge solenoids are 304 S.S. AU fittings on the air and water Unes that are on inlet sides of solenoid or regulators are brass. AU regulators are aluminum. The liquor/acid sample valve is Hastalloy C. Operation In an overaU system these circuits would operate together. The precise operation wUl depend upon the miU configuration. A typical operation for one reactor circuit is shown in the foUowing table. In this table, the operating valves, the valve positions - open (O), closed (C) or position (1, 2) -, the change of position (*), and the time are given. For an analyzer utiUzing multiple reactor circuits, the time of start-up of each circuit would be offset so as to result in no overlap of gas chromatograph operation. Otherwise the logic and sequencing for each circuit wiU in general be identical, although minor modifications could be made to each individual reactor circuit in response to differences in liquor strength or other characteristics without adversely affecting the overaU system operation. Table I Time Filter Sample Reactor Gas Chrom. 00:00 Bypass Standby 1 Standby Standby V21 C Vll IS V3 C VI 4 V22 C V14 IS V4 C V2 C V24 O V17 IF V5 C V6 C V26 C AP2 IF V6 C V7 C V28 IB (00:05) V8 C GC 1 V29 C V10 O (20:35) ( 00:40) V13 C 00:05 00:05 00:05 Reposition 1 Vent Vll 2T * V3 C V14 2T * V4 C V17 IF V5 O * AP2 IF V6 C 00:10 00:05 V8 C Transfer V10 O Vll 2T V13 C V14 2T (00:35) V17 2T * AP2 2T * 00:40 00:40 00:30 00:35 Filter Reposition 2 Standby V21 O * Vll IS * V3 C V22 C V14 IS * V4 C V24 C * V17 IF * V5 C * V26 C AP2 IF * V6 C 00:45 V28 2F * 00:05 V8 C V29 C Standby 2 V10 O (01:00) Vll IS V13 C V14 IS (02:15) V17 IF AP2 IF 01:40 01:00 00:5. Sample Sample V21 O Vll IS V22 O V14 IS V24 C V17 IF V26 C AP2 IF V28 2F (01:00) V29 C 02:40 01:00 01:00 1 Stop Standby 3 V21 O Vll IS V22 C V14 IS V24 C V17 IF V26 C AP2 IF V28 2F (01:55) V29 C Time Filter Sample Reactor Gas Chrom. 02:45 00:05 Backflush 1 V21 C * V22 C V24 C V26 C V28 2F V29 C 02:55 00:10 02:15 Backflush 2 Drain V21 C V3 O * V22 C V4 C V24 O * V5 C V26 O * V6 C V28 IB * V8 C V29 C V10 C * (00:15) V13 O * 03:05 00:10 Fill 03:10 00:15 V3 C * Bypass V4 O * V21 C V5 O * V22 C V6 C V24 O V8 C V26 C * V10 O * V28 IB V13 C * 03:25 V29 C 00:20 (13:00) Drain V3 O * V4 C * V5 C * V6 C V8 C V10 C * V13 O * 03:35 00:10 FiU V3 C * V4 O * V5 O * V6 C V8 C V10 O * V13 C * 03:55 00:20 Drain V3 O * V4 C * V5 C * V6 C V8 C V10 C * V13 O * ~^ " Time Filter Sample Reactor Gas Chrom. 04:05 00:10 Fill V3 C * V4 O * V5 O * V6 C V8 C V10 O * V13 C * 04:25 00:20 Drain V3 O * V4 C * V5 C * Vδ C V8 C V10 C * V13 O * 04:35 01:55 00:10 Repositio: n 3 Vent Vll 2T * V3 C * V14 2T * V4 C V17 IF V5 O * AP2 IF Vδ C (00:05) V8 C V10 O * V13 C * 04:40 00:05 00:05 Transfer Transfer Vll 2T V3 C V14 2T V4 C V17 2T * V5 C * AP2 2T * V6 C (00:30) V8 C V10 O V13 C 05:10 00:30 00:30 Reposition 4 Reaction 1 Vll IS * V3 C V14 IS * V4 C V17 IF * V5 C AP2 IF * V6 C 05:15 00:05 V8 C Standby 2 V10 O Vll IS V13 C 16:10 V14 IS 11:00 Filter V17 IF Pressure V21 O * AP2 IF V3 C V22 C (11:55) V4 C V24 C * V5 C V26 C V6 C V28 2F * V8 O * Time Filter Sample Reactor Gas Chrom. 16:20 00:10 Reaction 2 17:10 01:00 11:55 V3 C Sample Sample V4 C V21 O Vll IS V5 C V22 O * V14 IS Vδ C V24 C V17 IF V8 C V26 C AP2 IF V10 O V28 2F (01:00) V13 C V29 C (04:25) 18:10 01:00 01:00 Stop Standby 3 V21 O Vll IS V22 C * V14 IS V24 C V16 IF V26 C AP2 IF V28 2F (05:10) V29 C 18:15 00:05 Backflush 1 V21 C * V22 C V24 C V26 C V28 2F V29 C 18:25 00:10 Backflush 2 V21 C V22 C V24 O * V26 O * V28 IB * V29 C 18:40 00:15 Bypass 20:35 V21 C 20:35 V22 C Reposition V24 O VI 1 * V26 C * V2 C V28 IB V6 C V29 C V7 C (16:15) GC 1 20:40 00:05 Standby VI 1 V2 C V6 C V7 C GC 1 Time Filter Sample Reactor Gas Chrom. 20:45 04:25 00:05 Gas to G.C. Gas to G.C. V3 C VI 1 V4 C V2 C V5 C V6 O * Vδ O * V7 C V8 C GC 1 VIO O (00:40) V13 C 21:25 00:40 00:40 Stop Stop V3 C VI 1 V4 C V2 C V5 C Vδ C * Vδ C * V7 C V8 C GC 1 V10 O (00:05) V13 C 21:30 00:05 00:05 Drain Analyze V3 O * VI 1 V4 C V2 C V5 C V6 C V6 C V7 C V8 C GC 2 V10 C * (04:00) V13 O * 21:40 00:10 Fill V3 C * V4 O * V5 O * V6 C V8 C V10 O * V13 C * 22:00 00:20 Drain V3 O * V4 C * V5 C * V6 C V8 C V10 C * V13 O * Time Filter Sample Reactor Gas Chrom. 22:10 00:10 FiU V3 C * V4 O V5 O * V6 C V8 C VIO O V13 C # 22:30 00:20 Drain V3 O V4 C * V5 C V6 C V8 C VIO C * V13 O * 22:40 00:10 FiU V3 C * V4 O * V5 O * V6 c V8 c V10 O * V13 c * 23:00 00:20 Dram * V14 2T * V17 IF AP2 IF (00:05) * OMPI Time Filter Sample Reactor Gas Chrom. 23:15 00:05 00:05 Transfer Transfer Vll 2T V3 C V14 2T V4 C V17 2T * V5 C * AP2 2T * V6 C (00:30) V8 C V10 O V13 c 23:45 00:30 00:30 Reposition 4 Reaction 1 Vll IS * V3 C V14 IS * V4 c V17 IF * . V5 c AP2 IF * V6 c 23:50 00:05 V8 c Standby 2 V10 O 25:30 Vll IS V13 c 04:00 V14 IS (11:00) Purge V17 IF VI 1 AP2 IF V2 O * (11:55) V6 C V7 C GC 1 * 26:35 01:05 Standby 34:45 16:15 11:00 1 V2 C * Filter Pressure Continues Continues Continues Continues Use Figures 11, 12 and 13 are schematic diagrams showing the use of the apparatus in the causticizing system. Control loop 1 seen in Figure 11 discloses the use of the analyzer in controUing the sodium carbonate concentration in the green liquor to the slaker. In this diagram green liquor from the green liquor clarifier GLC flows through the miU liquor line MLl and is pumped by the green liquor pump GLP to the slaker S. Lime is added to the green liquor at the slaker S. There is an additional Une in this diagram. That is Une L40 which carries a portion of the weak wash into the mill liquor line MLl. The line L28/29 designates two lines, L29 which carries the Uquor from the miU Uquor line MLl to the reactor system RSI and L28 which returns the Uquor from the reactor system RSI to the miU liquor line MLl. Each of the reactor systems - RSI, RS2 and RS3 - includes a filter circuit, a sample circuit and a reactor circuit. These circuits are shown in Figures 1-3. The Une L2 carries the reaction gas from the reactor system RSI to the gas chromatograph/analyzer GC/A in which the gas is analyzed for carbon dioxide (resulting from sodium carbonate in the liquor) and hydrogen sulfide (resulting from sodium sulfide) as described above. The analyzer, using the carbon dioxide analysis, outputs a signal through the control Une CL1 to the controUer which operates the valve V40 to increase or decrease, the amount of weak wash flowing through line L40 into MLl in order to maintain a constant sodium carbonate concentration in the green Uquor going to the slaker. The hydrogen sulfide analysis has several uses. It is an indication of the reduction efficiency in the recovery boiler. The sodium sulfide concentration can be given to the recovery boiler operator to confirm to him that the reduction efficiency is good or to aUow him to make corrections to improve the reduction efficiency. It is also an indication of the potential efficiency in the causticizing operation. As the concentration of sodium carbonate or sodium sulfide in the green Uquor increases, the efficiency of the causticizing operation decreases. This wttl give the operator information about the causticizing reaction that the green Uquor is about to undergo and aUow the causticizing operator to take corrective action. The second control loop of this system is shown in Figure 12. This loop controls the balance of green Uquor and Ume, and in fact controls the entire slaking operation. A "clear" liquor sample is taken from the calcium carbonate mud separator at either the slaker or first causticizer. This "clear" Uquid is then filtered to remove aU the remaining calcium carbonate mud. The sodium carbonate-and^odmnr-sulfide-concentration in this filtered Uquor is then measured in the GC/A from the reaction gas from the second reactor system, RS2. The control loop logic wiU contain a set point for the desired sodium carbonate concentration in the Uquor. This set point NagCO, concentration wiU, as proven by miU experience, result in the best combina¬ tion of high conversion efficiency of to NaOH, low Na«CO 3 "deadload," and acceptable mud settling characteristics. The loop wiU then control the slaker operation via mass flow of sodium carbonate to the slaker so as to maintain and control this concentration of Na 2 CO 3 t e Uquor leaving the slaker. There are two ways of contro ing the sodium carbonate concentration in the slaker or first causticizer. One is the usual method of controUing the amount of Ume being added to the slaker. The other, and the method the inventors consider to be significantly better, is shown in Figure 12. In this method the amount of sodium carbonate in the green liquor is controUed by loop 1 as is described above. The amount of this green liquor added to the slaker is controUed by loop 2. The amount of sodium carbonate and sodium sulfide in the white liquor from the first causticizer or slaker is determined by the GC/A from the reaction gases from RS2. A signal, based on the sodium carbonate, is then sent through control Une CL2 to the controUer which operates the valve V41 to increase or decrease the amount of green liquor flowing through MLl into the slaker S. The measurement of the chemical concentrations in the white liquor is taken from the line between the clear white liquor storage tank and the digester or digesters. The concentrations of sodium sulfide and sodium carbonate in the white liquor are determined directly by analysis by the GC/A of the reaction gases from the third reaction system, RS3. The amount of sodium hydroxide in the white liquor, however, must be deter- mined indirectly. There are three pieces of information which must be combined to yield the sodium hydroxide concentration in the white Uquor. 1. The sodium carbonate concentration in the white liquor; 2. The sodium carbonate concentration in the green liquor; 3. The sodium hydroxide concentration in the green liquor. Measurements 1 and 2 are used to determine the amount of carbonate in the green liquor which, in the slaking/causticizing operation, has been converted to sodium hydroxide in the white Uquor. The difference between the amount of NanCO entering the system with the green liquor and the amount of Na 2 CO 3 leaving with the white liquor is the concentration of NaOH which has been produced in the white liquor due to the causticizing reaction. AU chemical concentrations are expressed on a sodium oxide (Na„O) basis. Some sodium hydroxide also enters the system with the green liquor. This sodium hydroxide passes unchanged through the system to the white liquor and must be accounted for. This source of NaOH in the system is relatively stable - a periodic (every eight hour) determination of NaOH in the green liquor may be manually performed by an operator and entered into the analyzer software. The determination of the NaOH in the green Uquor may be performed directly in titration of a green Uquor sample. It may alter¬ natively be determined indirectly by titrating the NaOH in the white Uquor. The amount of NaOH in the white Uquor which cannot be accounted for by the amount of NaOH generated in reeaustieizing is the amount of NaOH which has entered with the green Uquor. It is recommended that the NaOH in the green Uquor be determined by the indirect method, which has the advantage of reducing errors caused by time lags in the process. The amount of NaOH associated with the green Uquor is then stored in the microprocessor memory until updated by another titration. This value is used to update each subsequent white liquor sodium hydroxide determination. The analyzer wiU solve the foUowing equation for each succeed¬ ing sample to determine the sodium hydroxide concentration in the white Uquor: NaOH (white liquor) = Na 2 CO 3 (green Uquor) - Na 2 CO 3 (white Uquor) + NaOH (green Uquor) The carbonate analysis is updated with each sample every 19 minutes. The determination of sodium hydroxide in the green Uquor is updated by manual titration of a green or white Uquor sample when necessary, usually every eight hours. An updated, complete clarified white liquor analysis (determination of sodium hydroxide, sodium sulfide, and sodium carbonate) is provided to the digester operator or digester process computer every 12 to 19 minutes. The system software must also take into consideration the time delays in the slaking, causticizing and clarification operations in order to correctly determine the current NaOH concentration in the white liquor. This wiU determine the amount of chemicals to be added to the digester in order to control the pulping process. Cascaded Control Opportunities In many appUcations it wiU be sufficient and desirable to utiUze carbonate/sulfide analyzer measurements as the primary input to process control devices. However, in some appUcations it may be advantageous to control the process directly with a measurement device providing a more immediate but less accurate (in terms of sodium carbonate concentration) response to process changes. If these devices are utilized, measurements from the earbonate/sulfide analyzer should be used as set point control signals for the primary controllers. This "cascaded" type control system will greatly improve the accuracy of the primary control measurement devices and improve control of the process. Several measurement devices such as conductivity probes, density gauges, etc. provide rapid response to process changes. However, these devices provide only indirect measurements of the sodium carbonate concentration - they respond to the concentration of all chemicals in the process stream. The ratio of sodium carbonate to total chemicals in the process stream wiU vary with time, resulting in improper determinations of sodium carbonate concentration and less precise control of the process than could be obtained if sodium carbonate was measured directly. However, the changes which influence the calibration of these devices in measuring sodium carbonate concentration occur slowly - certainly greater than the 15-20 minute sampUng period generated by the earbonate/sulfide analyzer. The direct measurements of sodium carbonate generated by the earbonate/sulfide analyzer may be used as a set point control input to each primary control device. This practice will have the effect of adjusting the calibration of the primary device (conductivity probe, density gauge, etc.) every 15-20 minutes so that it is an accurate indicator of Na„COo concentration despite the previously mentioned variations in the ratio of Na 2 CO 3 /total chemicals. A cascaded control strategy of this type wiU have the advantage of having both an accurate method of determining sodium carbonate concentrations in the process and the ability to respond immedi- ately to changes in the process. This is iUustrated in Figure 14. The main items are the αTs oTvTI^tan DT, the green liquor clarifier GLC, the green liquor pump GLP, the slaker S and the first causticizer Cl. Mill Uquor Une MLl carries green liquor from dissolving tank DT to the green liquor clarifier GLC, and miU Uquor line ML2 carries green liquor from the green liquor clarifier GLC to the slaker S. The principal weak wash line L42 carries weak wash to lines L40 and L41. The weak wash in Une L41 is used to dissolve the smelt in the dissolving tank DT. The amount of weak wash going to the dissolving tank DT through Une L41 is controUed by valve V41. The amount of weak wash is determined by the density of the green liquor from the dissolving tank DT. This is monitored in miU Une MLl by the density meter DM1. The signal from the density meter DM1 is carried through control line CL1 to the valve controUer CN1. The valve V41 is controUed by CN1 with a signal which passes through control Une CL2. This is a standard local control loop in which a local direct measurement is used to monitor the proeess conditions. Figure 14 also iUustrates the use of local conditions to monitor and control the amount of weak wash entering ML2 to maintain the carbonate level in the green Uquor. However, in this instance the gas chromatograph/analyzer is used to determine the set points for this loeal control. The valve V40 is used to control the flow of weak wash in Une L40, which is the amount of weak wash which wiU enter the miU Uquor Une ML2. This is monitored locaUy be a density meter DM2 which sends a signal through control Une CL3 to the control unit CN2. CN2 operates the control valve V40 to increase or decrease the flow of weak wash to maintain the density in ML2 at a specified level. However, the density of the liquor is not a direct indication of sodium carbonate in the liquor. A sample of the density-controUed Uquor from ML2 is taken and analyzed for sodium carbonate concentration by reactor system RSI and the gas chromatograph/analyzer unit GC/A. This direct determination of sodium carbonate is utilized to send a set point signal through control line CLS to CN2 in order to adjust the density set point so that the density more accurately reflects the sodium carbonate concentration in the liquor.

Claims: CLAIMS 1. A process comprising clarifying pulp miU green liquor, transporting said clarified green Uquor to a slaker, adding weak wash to said clarified green Uquor while said clarified green Uquor is being transported to said slaker, mixing said weak wash with said clarified green Uquor before said slaker to provide a green Uquor of controUed sodium carbonate concentration, determining the concentration of sodium carbonate in said controlled green Uquor after said mixing and before said slaker, and adjusting the volume of said weak wash being added to said clarified green Uquor in response to changes in the concentration of sodium carbonate in said controUed green Uquor to maintain the concentration of sodium carbonate in said controUed green liquor substantially constant, adding lime to said controUed green liquor in said slaker to react sodium carbonate in said green liquor with calcium hydroxide generated from said lime to form a reaction mixture of green liquor, lime and their reaction products, transporting said reaction mixture from said slaker, determining the concentration of sodium carbonate in said reaction mixture, adjusting the flow of controlled green liquor into said slaker in response to a change in sodium carbonate concentration in said reaction mixture. 2. The process of claim 1 in which each of said steps of determining the concentration of sodium carbonate comprises taking a sample from the appropriate liquor stream, and determining the concentration of sodium carbonate in said sample. 3. The process of claim 2 further comprising removing the suspended solids from each said sample prior to making said determination of sodium carbonate concentration. 4. The process of claim 1 further comprising transporting said reaction mixture through a pluraUty of seriaUy connected causticizing vessels to aUow the reaction to continue. 5. The process of claim 4 in which each of said steps of determining the concentration of sodium carbonate comprises taking a sample from the appropriate Uquor stream, and determining the concentration of sodium carbonate in said sample. 6. The process of claim 5 further comprising removing suspended soUds from each said sample prior to making said determination of sodium carbonate concentration. 7. A process comprising burning pulp miU digestion spent liquors in a furnace to generate an inorganic smelt, dissolving said smelt to generate a pulp miU green Uquor comprising sodium carbonate, sodium sulfide, soluble impurities and insoluble impurities, clarifying said pulp miU green liquor to remove said insoluble impurities, transporting said clarified green liquor to a slaker, adding Ume to said green Uquor in said slaker to react sodium carbonate in said green liquor with calcium hydroxide generated from said Ume to form a reaction mixture of green Uquor, Ume and their reaction products, transporting said reaction mixture from said slaker through a plurality of seriaUy connected causticizing vessels to aUow said reaction to continue, thereafter separating said reaction mixture into a clarified white Uquor and a calcium carbonate mud, returning said clarified white Uquor to said pulp digestion process, transporting said calcium carbonate mud to a washing tank, washing said calcium carbonate mud with water to form a weak wash liquor, using part of said weak wash liquor to dissolve said smelt, adding a part of said weak wash Uquor to said clarified green liquor while said clarified green Uquor is being transported to said slaker, mixing said weak wash liquor and said clarified green Uquor before said slaker to provide a green Uquor of controUed sodium carbonate concentration, determining the concentration of sodium carbonate in said controUed green Uquor after said mixing and before said slaker, adjusting the volume of said weak wash liquor being added to said clarified green Uquor in response to changes in the concentration of sodium carbonate in said controUed green Uquor to maintain the concentra¬ tion of sodium carbonate in said controUed green Uquor substantiaUy constant, determining the concentration of sodium carbonate in the reac¬ tion mixture, adjusting the flow of controUed green Uquor into said slaker in response to changes in sodium carbonate concentration in said reaction mixture. 8. The process of claim 7 in which each of said steps of determining the concentration of sodium carbonate comprises taking a sample from the appropriate liquor stream, and determining the concentration of sodium carbonate in said sample. 9. The process of claim 8 further comprising removing the suspended solids from each said sample prior to making said determination of sodium carbonate concentration. 10. A process comprising clarifying pulp mill green liquor, transporting said clarified green liquor to a slaker, adding water to said clarified green Uquor while said clarified green Uquor is being transported to said slaker, mixing said water with said clarified green Uquor before said slaker to provide a green Uquor of controUed sodium carbonate concentration, determining the concentration of sodium carbonate in said controUed green liquor after said mixing and before said slaker, and adjusting the volume of said water being added to said clarified green liquor in response to changes in the concentration of sodium carbonate in said controUed green Uquor to maintain the concentration of sodium carbonate in said controUed green Uquor substantiaUy constant, adding Ume to said controUed green liquor in said slaker to react sodium carbonate in said green Uquor with calcium hydroxide generated from said Ume to form a reaction mixture of green Uquor, Ume and their reaction products, transporting said reaction mixture from said slaker, determining the concentration of sodium carbonate in said reaction mixture, adjusting the flow of controlled green Uquor into said slaker in response to a change in sodium carbonate concentration in said reaction mixture. 11. The process of claim 10 in which each of said steps of determining the concentration of sodium carbonate comprises taking a sample from the appropriate Uquor stream, and determining the concentration of sodium carbonate in said sample. 12. The process of claim 11 further comprising removing the suspended soUds from each said sample prior to making said determination of sodium carbonate concentration. 13. The process of claim 10 further comprising transporting said reaction mixture through a plurality of seriaUy connected causticizing vessels to aUow the reaction to continue. 14. The process of claim 13 in which each of said steps of determining the concentration of sodium carbonate comprises taking a sample from the appropriate Uquor stream, and determining the concentration of sodium carbonate in said sample. 15. The process of claim 14 further comprising removing suspended soUds from each said sample prior to making said determination of sodium carbonate concentration. 16. A process comprising clarifying pulp mill green Uquor, transporting said clarified green liquor to a slaker, adding Ume to said green Uquor in said slaker to react sodium carbonate in said green liquor with calcium hydroxide generated from said lime to form a reaction mixture of green Uquor, Ume and their reaction products, transporting said reaction mixture from said slaker, determining the concentration of sodium carbonate in said reaction mixture, adjusting the volume of said clarified green Uquor being added to said slaker in response to changes in the concentration of sodium carbonate in said reaction mixture. 17. The process of claim 16 in which said step of determining the concentration of sodium carbonate comprises taking a sample from said reaction mixture, and determining the concentration of sodium carbonate in said sample. 18. The process of claim 17 further comprising removing the suspended solids from said sample prior to making said determinations of sodium carbonate concentration. 19 A process of claim 16 further comprising transporting said reaction mixture through a plurality of serially connected causticizing vessels to aUow said reaction to continue. 20. The process of claim 19 in which said step of determining the concentration of sodium carbonate comprises taking a sample from said reaction mixture, and determining the concentration of sodium carbonate in said sample. 21. The process of claim 20 further comprising removing the suspended solids from said sample prior to making said determination of sodium carbonate concentration. 22. Apparatus comprising a pulp mill green Uquor clarifier, a slaker, first means for transporting clarified green Uquor from said green liquor clarifier to said slaker, second means for adding liquid to said first means, the length of said first means between said second means and said slaker aUowing said green Uquor and said liquid to mix and form a controUed green liquor, third means between said second means and said slaker for determining the sodium carbonate concentration in said controUed green liquor in said first means, fourth means responsive to said third means for adjusting flow of Uquid in said second means, fifth means for adding lime to said slaker, sixth means for transporting a reaction mixture of green Uquor, lime and reaction products from said slaker, seventh means for determining the sodium carbonate concentra¬ tion in said reaction mixture, eighth means responsive to said seventh means for adjusting flow in said first means. 23. The apparatus of claim 22 in which each of said third means and said seventh means comprises means for sampUng the appropriate liquor, and an additional means for determining the sodium carbonate con¬ centration in said sample. 24. The apparatus of claim 23 further comprising each of said sample taking means comprises a means for removing suspended solids from said sample. 25. The apparatus of claim 22 further comprising a pluraUty of seriaUy connected causticizing vessels for aUowing said reaction between green liquor and said lime to continue, said sixth means transporting said reaction mixture from said slaker through said causticizing vessels. 26. The apparatus of claim 25 in which each of said means for determining said sodium carbonate content comprises means for sampling the appropriate liquor, and means for determining the sodium carbonate concentration of said sample. 27. The apparatus of claim 26 further comprising said sampling means has means for removing suspended solids from said sample. 28. Apparatus comprising a slaker for reacting clarified green Uquor with Ume, first means for transporting said clarified green Uquor to said slaker, second means for adding said Ume to said slaker, third means for transporting a reaction mixture of green Uquor, lime and reaction products from said slaker, fourth means for determining the sodium carbonate concen¬ tration in said reaction mixture, fifth means responsive to said fourth means for adjusting the flow of green liquor in said first means. 29. The apparatus of claim 28 in which said means for determining said sodium carbonate content comprises means for sampling said reaction mixture, and means for determining the sodium carbonate concentration of said sample. 30. The apparatus of claim 29 further comprising means for removing suspended solids from said sample. 31. The apparatus of claim 30 further comprising a pluraUty of seriaUy connected causticizing vessels for aUowing said reaction between said green liquor and said lime to continue, said third means transporting said reaction mixture from said slaker through said causticizing vessels. 32. The apparatus of claim 31 in which said means for determining said sodium carbonate content comprises means for sampling said reaction mixture, and means for determining the sodium carbonate concentration of said sample. 33. The apparatus of claim 32 further comprising said sampling means has means for removing suspended solids from said sample. 34. Apparatus comprising first means for clarifying pulp miU green Uquor, second means for reacting said clarified green Uquor with Ume, third means for transporting said clarified green Uquor from said first means to said second means, fourth means for adding Uquid to said third means, the length of said third means between said fourth and said second means aUowing said green Uquor and said Uquid to mix and form a controUed green Uquor, fifth means for determining the sodium carbonate concentration in said controUed green Uquor in said third means at a point between said fourth means and said second means, sixth means responsive to said fifth means for adjusting the flow of Uquid in said fourth means, seventh means for adding Ume to said slaker, eighth means for transporting a reaction mixture of green Uquor, lime and reaction products from said slaker, ninth means for determining the sodium carbonate concentration in said reaction mixture, tenth means responsive to said ninth means for adjusting flow in said first means. 35. The apparatus of claim 34 in which each of said fifth and ninth means comprises means for sampUng the appropriate Uquor, and an additional means for determining the sodium carbonate concentration in said sample. 36. Apparatus comprising a recovery furnace for burning pulp miU digestion waste liquors to form inorganic smelt, a smelt dissolving tank for forming from said smelt, particulate matter and a green Uquor comprising sodium carbonate and sodium sulfide, first means for transporting said smelt from said recovery furnace to said smelt dissolving tank, a green Uquor clarification tank, second means for transporting said green Uquor from said smelt dissolving tank to said green Uquor clarification tank, a slaker for reacting said clarified green Uquor with lime to form a reaction mixture of green Uquor, Ume and reaction products, third means for transporting said clarified green Uquor from said green liquor clarification tank to said slaker, fourth means for adding said Ume to said slaker, causticizing vessels for aUowing said reaction between said green liquor and said Ume to continue, fifth means for transporting said reaction mixture from said slaker through said causticizing vessels, sixth means for separating said reaction mixture into a clarified white Uquor and a calcium carbonate mud, seventh means for transporting said reaction mixture from said causticizing vessels to said separating means, eighth means for transporting said clarified white Uquor to a digester, ninth means for washing chemical from said calcium carbonate mud to form a weak wash effluent, tenth means for transporting said calcium carbonate mud from said separating means to said ninth means, eleventh means for transporting said weak wash effluent from said ninth means to said smelt dissolving tank, twelth means for transporting a portion of said weak wash effluent to said third means, thirteenth means for determining the sodium carbonate concen¬ tration in a mixture of said clarified green Uquor and said weak wash at a point prior to said slaker, fourteenth means responsive to said thirteenth means for adjust¬ ing the flow of weak wash in said twelfth means, fifteenth means for determining the sodium carbonate concentration in said reaction mixture, sixteenth means responsive to said fifteenth means for adjusting flow in said third means. 37. The apparatus of claim 36 in which each of said means for determining said sodium carbonate content comprises means for sampUng the appropriate liquor, and means for determining the sodium carbonate concentration of said sample. 38. Apparatus comprising a first means for burning pulp miU digestion waste Uquors to form an inorganic smelt, second means for dissolving said smelt to form particulate matter and a green Uquor comprising sodium carbonate and sodium sul ide, third means for transporting said smelt from said first means to said second means, fourth means for clarifying said green Uquor, fifth means for transporting said green Uquor from said second means to said fourth means, sixth means for reacting said clarified green Uquor with Ume to form a reaction mixture of green Uquor, Ume and reaction products, seventh means for transporting said clarified green Uquor from said fourth means to said sixth means, eighth means for adding said Ume to said sixth means, ninth means for aUowing said reaction between said green Uquor and said Ume to continue, tenth means for transporting said reaction mixture from said sixth means to said ninth means, eleventh means for separating said reaction mixture into a clarified white Uquor and a calcium carbonate mud, twelfth means for transporting said reaction mixture from said ninth means to said eleventh means, thirteenth means for transporting said clarified white liquor to a pulp mill digester, fourteenth means for washing chemicals froms said calcium carbonate mud to form a weak wash effluent, fifteenth means for transporting said calcium carbonate mud from said eleventh means to said fourteenth means, sixteenth means for transporting said weak wash effluent from said fourteenth means to said second means, seventeenth means for transporting a portion of said weak wash effluent from said seventeenth means to said fifth means, eighteenth means for determining the concentration of sodium carbonate in the mixture of said clarified green Uquor and said weak wash in said fifth means, nineteenth means responsive to said eighteenth means for adjust¬ ing the flow through said seventeenth means, twentieth means for determining the sodium carbonate concen¬ tration in said reaction mixture, twenty-first means responsive to said twentieth means for adjusting flow in said seventh means. 39. The apparatus of claim 38 in which . each of said means for determining said sodium carbonate content comprises means for sampling said appropriate liquor, and means for determining the sodium carbonate concentration of said sample.

Inventors: MCCALL THOMAS FRANKLIN, SPEAKS JERRY ROBERT, WARRICK RONALD PAUL, MCCALL, THOMAS, FRANKLIN, SPEAKS, JERRY, ROBERT, WARRICK, RONALD, PAUL
Applicants: WEYERHAEUSER CO, WEYERHAEUSER COMPANY
Application year: 1984
Main classification: D21C11
IPC codes: D21C11