FLOCCULATING APPARATUS

Abstract: This invention relates to a flocculating apparatus which performs control so that the amount of addition of a flocculant can be optimized, and can minimize the water content of a dehydrated cake. The apparatus includes chemical charging devices (6), (7), (8) for adding variable amounts of the flocculant to a solution to be subjected to flocculation, a thermal migration detector (12) for detecting a minute property change in the solution to which the flocculant is to be added, the solution to which the flocculant has been edded or a solution provided in such a manner as to come into contact with the filtrate of the solution to which the flocculant has been added, and a controller (16) for controlling the chemical charging quantity by the chemical charging device (8) so that the detection value of the thermal migration detector (12) becomes least, minimal or a value within the a desired range.

Description: Field of the Invention: This invention relates to an apparatus for flocculating treatment. Particularly, this invention relates to an apparatus for flocculating treatment aimed at controlling to optimize the amount of a flocculant to be injected (added) to a liquid under treatment. More particularly, this invention relates to an apparatus for flocculating treatment suitable for controlling the amount of an organic flocculant (hereinafter referred to occasionally as "polymer") to be added to a liquid under treatment. Background of the Invention: Heretofore, various methods have been proposed for the control of a flocculant to be added in the dehydration of sludge. It has been proposed, for example, to control the amount of a flocculant to be added by indirectly measuring the residual polymer content of the liquid as with the aid of a viscosimeter in view of the fact that the viscosity of the liquid varies with the residual polymer content and then using the result of this measurement as the criterion for the control. The measurement of shear stress in a sample is used in the apparatus of EP-A-0 170 071 in computing and controlling the quantity of polymer to be added to a sewage sludge. The physical properties of the liquid include specific heat, electric conductivity, etc. besides the viscosity. They bring about various effects on the operation of addition of the flocculant. When the amount of addition of the flocculant is controlled by using as a sole criterion the viscosity which is only one of the physical properties, therefore, the actual amount of addition deviates from the proper level possibly to the extent of entailing ineffective flocculation, excessive addition of the flocculant, and unduly high cost of the flocculant. Disclosure of the Invention: An object of this invention is to solve the problems of the prior art described above and provide an apparatus for the flocculating treatment which allows the amount of addition of a flocculant to be controlled accurately and consequently optimized. Another object of this invention is to provide a flocculating treatment which prevents possible deviation in the amount of added flocculant and accomplishes the flocculating treatment inexpensively and efficiently. These objects are accomplished by an apparatus for the flocculating treatment by the addition of a flocculant to a liquid subjected to the flocculating treatment, which apparatus comprises a device for flocculant addition capable of adjusting the amount of addition of the flocculant, a liquid to which the flocculant is to be added, a heat transfer detector disposed so as to contact the liquid containing the added flocculant or the filtrate from the liquid containing the added flocculant, and a control device for controlling the amount of the flocculant supplied by the device for flocculant addition in accordance with the value of detection displayed on the heat transfer detector. EP-A-0 150 111 describes a method for detecting coagulation in a liquid or semi-solid material by measuring heat transfer from an electrically conducting wire placed in the sample. The present invention resides in controlling the amount of addition of a flocculant to a sludge by detecting changes in the physical constants of the sludge due to changes in the properties of the sludge as changes in heat transfer and adopting the detected changes in heat transfer as the criterion for the control. The inventors made several studies for many years concerning the properties of a liquid resulting from a flocculating treatment, to acquire the knowledge that the water content of the cake resulting from the dehydration, the detected value from the heat transfer detector in the liquid produced by the flocculating treatment (or the liquid undergoing the flocculating treatment) and the concentration of added flocculant in the sludge are closely related to each other as illustrated in Figs. 5 and 6 and the water content of the dehydrated cake is minimized by controlling the amount of addition of the flocculant so as to minimize the numerical value detected by the use, for example, of a hot-wire flow meter hereinafter termed "a hot wire current meter". Figs. 5 and 6 are graphs showing the relation between the amount of addition of a flocculant (cationic polymer) to a sewage-mixed raw sludge as a raw water, the value of detection a (potential difference) indicated on a hot-wire flow meter, and the water content of dehydrated cake. As shown in Fig. 5, the value of detection indicated by the hot-wire current meter is in the minimum zone and the water content of the dehydrated cake is minimum when the amount of addition of the flocculant is about from 150 to 200 ppm. Fig. 6 is a diagram showing a similar relation obtained from a different mixed raw sludge from the sludge of Fig. 5. It is seen that the value of detection indicated by the hot-wire current meter and the water content of the dehydrated cake are both minimum when the amount of addition of a flocculant was approximately in the neighbourhood of 150 ppm. When this test was repeated on various kinds of raw water, the results clearly showed relations similar to those shown in Figs. 5 and 6. It has been further demonstrated that relations similar to those mentioned above exist concerning such characteristic properties as ease of cake separation and amount of filtrate besides the water content of the cake. The present invention has been completed on the basis of this knowledge. Since it effects the control of the amount of addition of a flocculant based on the value of detection obtained with a heat transfer detector, it is capable of adjusting the amount of addition of the flocculant so as to minimize the water content of the dehydrated cake. Brief Description of the Drawings: Fig. 1, Fig. 2, and Fig. 3 are each a system diagram of an apparatus embodying the present invention. Fig. 4 is a block diagram of a hot-wire current meter. Fig. 5 and Fig. 6 are graphs showing test results. Fig. 7A and Fig. 7B are graphs meant to aid in the explanation of the method of control. Fig. 8 is a system diagram of another apparatus embodying the present invention. Fig. 9 is a partial structural diagram. Fig. 10 is a system diagram of yet another apparatus embodying the present invention. Fig. 11 is a partial structural diagram of the XI part of Fig. 10. Fig. 12 and Fig. 13 are each a system diagram of still another apparatus embodying the present invention. Best Mode of embodying the Invention: Now, the present invention will be described below with reference to working examples as illustrated in the accompanying drawings. Fig. 1 is a system diagram of an apparatus for the flocculating treatment in one working example of this invention. The raw water from a raw sludge pit 1 is forwarded through a pipe 3 provided with a pump 2 and introduced into a flocculation tank 4. The flocculation tank 4 is provided with a stirrer 5 and is supplied with a cationic organic flocculant from a flocculant injecting device which comprises a flocculant storage tank 6, a flocculant injection pipe 7, and a flocculant injection pump 8. The liquid resulting from the flocculating treatment in the flocculation tank 4 is transferred to a dehydrator 9 as solid-liquid separating means. The dehydrated cake produced in the dehydrator 9 is forwarded to the step of cake disposal using an incinerator, for example, while the filtrate is forwarded to a filtrate storage tank 10. The filtrate storage tank 10 is provided with a thermometer 11, a heat transfer detector 12, and an electric conduction meter 13. The detection signals issued from these measuring instruments 11, 12, and 13 are introduced into an operation controller 16. The operation controller 16 is supplying a control signal to the flocculant injection pump 8. The pump 8 is subjected to inverter control, for example. As the heat transfer detector contemplated by this invention, a hot-wire type or hot-film type current meter or a heat conductivity meter which is generally used for the detection of heat transfer can be adopted. Otherwise, a device which is provided with a self-heating source capable of energizing a heater and effecting required heating or a device which is provided with a heating source such as the combination of a heater with a thermometer and, therefore, is allowed to effect indirect heating with the heater may be adopted. Now, the present invention will be described below with reference to an embodiment employing a hot-wire current meter. The hot-wire current meter, as universally known, is designed to keep a flow of a fixed electric current to a hot wire serving as a heating member; this hot wire is inserted in a fluid. A change in the flow rate of this fluid produces a proportionate change in the degree with which the fluid deprives the hot wire of heat. As a result, the temperature of the hot wire is changed and the resistance thereof is also changed. The hot-wire current meter detects this change in resistance in the form of a change in voltage and determines the flow rate of the fluid. The present invention utilizes the operating principle of this hot-wire current meter and sets conditions for a constant flow rate of the fluid and, thereby, determines a change in the flow rate by detecting the transfer of feeble heat removed from the hot wire in the form of a change in resistance (voltage) and then perceiving this change in resistance in the form of a change in physical property. The filtrate storage tank 10, therefore, is provided with a stirrer 14 and, for the purpose of enabling the stirrer 14 to be rotated constantly at a fixed speed in the course of measurement and, at the same time, uniformizing the conditions of stirring, further provided with an overflow pipe 15 adapted to maintain a fixed level in the tank. Fig. 4 is a schematic structural diagram of the hot-wire current meter 12 which is used in the present working example. This hot-wire current meter 12 is provided with a hot wire (resistor) 12a, a constant-current generator 12b, and a voltmeter 12c. The hot wire 12a is kept in contact with the liquid being circulated at a fixed flow rate as indicated by an arrow mark S inside the filtrate storage tank 10. While this liquid has fixed physical properties, the hot wire 12a in which a constant current is flowing offers a fixed resistance and consequently a constant voltage because the amount of heat removed from the hot wire 12a is fixed. When a change occurs in the physical properties of the liquid, the resistance is varied because the amount of heat removed from the hot wire 12a is varied. To be specific, the change in resistance occurs because there arises transfer of heat from the hot wire into the liquid. Since the electric current flowing in the hot wire 12a is constant, the change in resistance can be detected as a change in voltage. This change in voltage represents the detected value of the physical property in the liquid. The change in the physical property of the hot wire 12a may be detected in the form of a change in resistance or in voltage. The working example has been described as using a constant-current hot-wire current meter. Optionally, this invention may be embodied with a constant-temperature type hot-wire current meter. As clearly noted from the description made thus far, the use of the hot-wire current meter in the way contemplated by this invention permits detection of even a feeble change in physical property by simply giving a fixed flow rate. In the apparatus of Fig. 1 which is constructed as described above, the raw water in the flocculation tank 4 is subjected to a flocculating treatment caused by addition of a flocculant. The amount of addition of this flocculant in this case is so controlled as to minimize the value of the detection made in the filtrate storage tank 10 and indicated by the hot-wire current meter. The method for controlling the amount of addition of the flocculant will be described below with reference to Fig. 7A and Fig. 7B. Fig. 7A and Fig. 7B are typical diagrams intended to aid in the explanation. While they show changes, Δn, in the amount of addition of a flocculant with great exaggeration, the actual changes may be properly selected to suit the kind of polymer, for example. With reference to Fig. 7A, it is assumed that the amount of addition of a flocculant at a given time t₁ is n₁ the amount of addition of the flocculant at the next time t₂ is n₂ (n₂ is a feeble amount, Δn, larger than n₁). When the values of detection, a₁ and a₂, of the hot-wire current meter obtained respectively for the amounts, n₁ and n₂, of addition are compared and a₂ is found to be smaller than a₁, the amount of addition at the subsequent time t₃ is changed to n₃ (n₃ is Δn larger than n₂). This procedure is repeated. As a result, the amount of addition is gradually approximated to the amount of addition, N, that minimizes the value of detection of the hot-wire current meter. With reference to fig. 7B, the value of detection of the hot-wire current meter grows from a₁ to a₂ as the amount of addition is increased from n₁ to n₂. In this case, the amount of addition at the subsequent time t₃ is decreased from n₂ to n₃ (n₃ is Δn smaller than n₂). Then, at the further subsequent time t₄, the amount of addition is changed to n₄ (n₄ is Δn smaller than n₃). By repeating this procedure, required approximation to the amount of addition, N, that minimizes the value of detection of the hot-wire current meter can be attained. With reference to Fig. 7A and Fig. 7B, the repeated change in the amount of addition by a fixed increment Δn may possibly result in a passage beyond the optimum amount of addition N. If this passage takes place, the amount of addition is decreased by ½Δn at a time, for example. when the repeated decrease in the amount of addition results in a passage beyond the optimum amount N, then the amount of addition is reversively returned by ¼Δn. By gradually decreasing the width of decrement in the manner just mentioned, the amount of addition can be eventually brought to coincidence with the maximum amount of addition N. Even after the optimum amount of addition N is reached, it may still be necessary to vary the amount of addition within a prescribed range, due to variations in the properties of the raw water. It is, therefore, desirable to add the optimum amount of addition N and to follow rapidly any possible changes, in the optimum amount of addition N. In the apparatus illustrated in Fig. 1, the values of detection of the thermometer 11 and the electric conductivity meter 13 are also introduced into the operation controller 16. This is because the value of detection of the hot-wire current meter is affected by a possible change in the attributes of the raw water (such as temperature and soluble salt concentration) and, therefore, the portions of contribution made by the changes in temperature and electric conductivity to the change in the value of detection of the hot-wire current meter must be withdrawn (compensated) to allow sole comparison of changes in the value of detection of the hot-wire current meter exclusively with respect to changes in the amount of addition. Fig. 2 is a system diagram of an apparatus for flocculating treatment as another embodiment of the present invention. In this embodiment, a first and a second flocculation tank 41, 42 are installed. To the first flocculation tank 41, a cationic polymer from its storage tank 61 is added via a flocculant injection pipe 71 and a flocculant injection pump 81. To the second flocculationtank 42, an anionic polymer from its storage tank 62 is supplied via a flocculant injection pipe 72 and a flocculant injection pump 82. To the flocculation tanks 41, 42, filtering devices 101, 102 as solid-liquid separating means are respectively connected via discharge pipes 91, 92 adapted to release liquids from the tanks. The filtrates emanating from these filtering devices are stored respectively in filtrate storage tanks 111, 112. The filtrate storage tanks 111, 112 are each provided with the thermometer 11, the hot-wire current meter 12, and the electric conductivity meter 13. The detection signals from these measuring instruments are introduced into the operation controller 16. The flocculant injection pump 81 is controlled in accordance with the data of detection from the filtrate storage tank 111 and the flocculant injection pump 82 is controlled in accordance with the data of detection from the filtrate storage tank 112. This method of control is identical with that which has been described with reference to the apparatus of Fig. 1. Also in the apparatus of Fig. 2, the flocculant injection pumps 81, 82 may be controlled based on the value of detection of the hot-wire current meter, the temperature, and the electric conductivity obtained of the filtrate from the dehydrator 9. In the apparatus of Fig. 2, the detection with the hot-wire current meter is effected on both the liquids in the two flocculation tanks 41, 42. Optionally, the detection with the hot-wire current meter may be effected only on the liquid in the first flocculation tank 41 and the control mentioned above may he effected only with respect to the amount of addition of the cationic polymer. In this case, the amount of addition of the anionic polymer may be proportionated to the controlled amount of addition of the cationic polymer. (Since the sludge is negatively charged, the control is obtained nearly perfectly by using as the main target of control the amount of addition of the cation polymer which is added first). Fig. 3 is a system diagram of an apparatus for flocculating treatment as still another embodiment of this invention. In this embodiment, an inorganic flocculant is added to the first flocculation tank 41 and an amphoteric polymer is added to the second flocculation tank 42. The detection with the hot-wire current meter is effected on the filtrate from the second flocclation tank 42 and the amounts of addition of the polymers are controlled in accordance with the aforementioned procedure using the results of the detection. In this case, the outcome of the detection with the electric conductivity meter disposed in the filtrate storage tank 112 is used for the purpose of compensating for the effect of the addition of the inorganic flocculant. Again in the present embodiment, the detection with the hot-wire current meter may be effected on the filtrate from the dehydrator 9 and the control of the amount of addition may be effected on the basis of the outcome of the detection in the same manner as in the embodiment of Fig. 1. In the present embodiment, the detection with the hot-wire current meter is not effected on the liquid held in the first flocculation tank 41. This is because no clear discrimination may be made as to the question whether changes in the value of detection with the hot-wire current meter with respect to the liquid held inside the second flocculation tank 42 are ascribable to the influence of the inorganic flocculant or to that of the polymer if the filtrate from the first flocculation tank 41 is additionally subjected to detection and control. In the embodiment of Fig. 3, the first flocculation tank 41 is provided with a pH meter 30 and the amount of addition of the inorganic flocculant is controlled based on the pH data produced by the pH meter so as to be approximated to the optimum amount of addition. In consequence of this control, the otherwise possible excessive addition of the inorganic flocculant is precluded, the effect of the inorganic flocculant on the value of detection of the hot-wire current meter is alleviated to a great extent, and the accuracy of the control of the amounts of addition of the polymers is enhanced. Particularly when the amphoteric polymer is used as in the present embodiment, the control by means of the pH meter 30 proves to be desirable in the sense of curbing the elution of cation or anion. In the apparatuses of Figs. 1 to 3, the flocculated sludge may be even pelletized within the tank by controlling the amount of addition and the revolution number of the stirrer in the flocculation tank. In the present invention, the hot-wire current meter alone may be used and the thermometer and other measuring instruments may be omitted. Further, the embodiment of Fig. 1, similarly to the apparatuses of Figs. 2 and 3, may be operated so as to effect the detection with the hot-wire current meter on the liquid held outcome of the detection. Though the present embodiment is depicted as adding the flocculant to the in the flocculation tank and carry out the control of the amount of addition based on the flocculation tank, the present invention may be alternatively embodied in an apparatus of flocculating treatment of the type allowing the flocculant to be injected into a pipe passing the liquid subjected to the flocculating treatment (the feed pipe for the raw water, for example). Fig. 8 is a system diagram of an apparatus for the flocculating treatment conforming to this type of embodiment. The raw water from a raw water storage tank is forwarded via a pipe 201 provided with a raw water pump (not shown) to a centrifugal dehydrator (which may be a belt press dehydrator or a screw press dehydrator; the type of dehydrator irrelevant) 203. To an inlet halfway along the length of the raw water pump-incorporating pipe 201, a cationic organic flocculant from a flocculant injection device provided with a flocculant injection pipe 202 and a flocculant injection pump 207 is supplied. The solid residue emanating from the dehydrator 203 is discharged through a concentrated sludge outlet 204, to be disposed of separately. The relatively clean liquid separated by the dehydrator is forwarded via a separated clear liquid outlet 205 to a separated liquid storage tank 208. Part of the separated liquid collecting in the separated liquid storage tank 208 is quantitatively forwarded by a pump 209 to a sampling tank 215. This sampling tank 215 is provided with a heat transfer meter (hot-wire current meter) 210. The heat transfer meter of this kind is susceptible conspicuously of the influence of the flow speed of the liquid or susceptible of the influence of the pulsation of the transfer pump 209. To eliminate these influences, the present embodiment is adapted to give to the heat transfer meter a relatively large fixed flow by the use of a stirring device 214 so as to render a possible change in flow volume negligible. When the separated water is caused to flow into the sampling tank by virtue of the difference of height of water level, the pump 209 is omitted as illustrated in Fig. 9 (which is a system diagram illustrating another structure for the IX part shown in Fig. 8) . Conversely, when the pump 209 is of the type capable of discharging a given fluid continuously at a constant flow rate, the stirring device 14 may be omitted. In the sampling tank 215, the condition (physical property) of the separated water is determined with the heat transfer meter 210. The signal of detection from the heat transfer meter 210 is forwarded to a signal amplifier-converter 211, there to be converted into the form fit for the operation in the operation controller. An operation controller 212, in response to the signal from the converter 211, issues a stated operation signal to the drive device for the flocculant injection pump 207 and consequently effects the control of the amount of addition of the flocculant from the flocculant injection pump 207 through the flocculant injection pipe 202. Preferably, the drive device for the flocculant injection pump 107 is of the type capable of continuously varying the amount of discharge of the pump (amount of addition of the flocculant) as with an inverter. In Figs. 8 and 9, the reference numerals 213a, 213b each denote an outlet pipe for the treated liquid. Fig. 10 is a system diagram of an apparatus embodying the present invention by the combined use of an organic flocculant (amphoteric polymer) and an inorganic flocculant. In the present embodiment, the inorganic flocculant is injected into the raw water pipe 201 and the organic flocculant is subsequently injected into the pipe 201 by a flocculant injection pump 250. Between the points of addition of the inorganic flocculant and the organic flocculant, a sensor 251 such as, for example, a pH meter or an electric conductivity meter. On the basis of the signal of detection from this sensor 251, a controller 252 effects the control of the injection of the inorganic flocculant. The remainder of the construction of this embodiment is identical to the construction of the embodiment of Fig. 8. Thus, like component parts are denoted by like reference numerals. Also in this embodiment, the injection pump 207 for the organic flocculant is controlled based on the detection signal from the heat transfer meter 210. The apparatus of Fig. 10 may be provided, as illustrated in Fig. 11 (illustrating another construction for the XI part shown in Fig. 10), with a sensor 255 for measuring the pH value or electric conductivity of the separated water. The control of the addition of the flocculant, accordingly, may be effected on the basis of the detection signal from this sensor 255. Optionally, this embodiment may be further provided with a thermometer. It is also permissible to have the separated water storage tank and the sampling tank integrally formed as illustrated in Fig. 11. Though the embodiments cited thus far invariably cause the filtrate to flow continuously into the filtrate storage tank. The present invention may otherwise cause the filtrate to be received portionwise in a stated amount into the filtrate storage tank and the detection with the hot-wire current meter may be effected on the separate portions of the filtrate. The batchwise determination involved in this case can be attained by having a level gauge provided for the filtrate storage tank and operating this level gauge in allowing a new batch of the filtrate to flow continuously into the tank completely evacuated of the previous batch of the filtrate until it reaches the stated level and subsequently setting the hot-wire current meter to service. The present invention may omit the thermometer and rely solely on the hot-wire current meter. It is also allowed to effect the control of the amount of addition by using the ease of cake separation or the amount of filtrate as the criterion of control instead of the water content of the dehydrated cake. It may use two or more of these characteristic properties as criteria for the control of the amount of addition of a flocculant. In the embodiments cited above, the filtrate resulting from the dehydration of the flocculant-added liquid is held in contact with the hot-wire current meter. This arrangement is effective in preventing the SS component and the floc from adhering to the hot-wire current meter, stabilizing the operation of the apparatus, and facilitating the maintenance of the apparatus. Optionally, the present invention allows a modification such that the hot-wire current meter directly contacts the liquid before the addition of a flocculant or the liquid before the flocculating treatment as illustrated in Fig. 12 and Fig. 13. The apparatuses of Fig. 12 and Fig. 13 are each provided with a storage tank 10A for admitting the liquid before the addition of a flocculant (Fig. 12) or the liquid before the flocculating treatment (Fig. 13) in the place of the filtrate storage tank 10. The remainders of the construction of the apparatuses of Fig. 12 and Fig. 13 are identical with the construction of the apparatus of Fig. 1. Thus, like component parts are denoted by like reference numerals. The expression "filtrate from the flocculant-added liquid" as used in the present invention means the filtrate resulting from the filtration of the liquid in the flocculation tank and the dehydrated filtrate resulting from the dehydration of the filtrate just mentioned with the dehydrator. In the data of control illustrated in Fig. 7, the control is carried out so as to minimize the amount of addition of a flocculant. Optionally, the control may be performed so that the amount of addition of a flocculant will fall in a target range. Economic Utility of the Invention: As described above, the apparatus of this invention for the flocculating treatment, owing to the use of a heat transfer meter, is capable of easily detecting a feeble change in the physical property of a given liquid in the form of a change in resistance (voltage) and consequently effecting accurate control of the amount of addition of a flocculant and ensuring desired optimization of the amount of addition of the flocculant. Thus, the otherwise possible deviation of the amount of addition of the flocculant is avoided and the required flocculating treatment is effectively and inexpensively carried out.

Claims: A method for controlling the addition of a flocculant to a liquid wherein the quantity of flocculant to be added is controlled by a control device and heat transfer is detected in the liquid to which the flocculant is to be added, the liquid to which the flocculant has been added or the filtrate from the liquid to which the flocculant has been added and whereby the result of said heat transfer measurement controls the amount of flocculant added by the control device. An apparatus for carrying out the method of claim 1 comprising a flocculant adding device (6, 7, 8; 61, 71, 81,; 62, 72, 82) capable of adjusting the amount of addition of the flocculant, a heat transfer detecting meter (12; 210) so disposed as to contact the liquid to which the flocculant is to be added, the liquid to which the flocculant has been added, or the filtrate from the liquid to which the flocculant has been added, and a control device for controlling the amount of addition of a flocculant in the flocculant adding device based on the outcome of the detection with the heat transfer detecting meter. An apparatus as claimed in claim 2 comprising guiding means (3) for receiving a liquid subjected to a flocculating treatment, guiding the received liquid to at least one part (4) at which the flocculant is added, and further guiding the liquid having incorporated therein the flocculant from the part mentioned above to solid-liquid separating means (9), adding means (6, 7, 8) for adding the flocculant to the liquid in a variable amount at the part for the addition of the flocculant (4), a heat transfer detecting meter (12) disposed so as to contact the liquid separated by the solid-liquid separating means, and control means for controlling the amount of addition of the flocculant through the adding means so that the value of detection of the heat transfer detecting meter is minimized or is kept within a target range. An apparatus as claimed in claim 3, wherein the part for the addition of the flocculant is a flocculation tank (4; 41, 42) provided with stirring means (5). An apparatus as claimed in claim 3, wherein the solid-liquid separating means is a dehydrator (9). An apparatus as claimed in claim 3, wherein the solid-liquid separating means is a filtrating device (101, 102). An apparatus as claimed in claim 3, wherein a plurality of parts are provided for the addition of the flocculant (61, 71, 81; 62, 72, 82). An apparatus as claimed in claim 7, wherein the first of the plurality of parts (61) is used for the addition of a cationic flocculant and the subsequent one of the parts (62) for the addition of an anionic polymer flocculant. An apparatus as claimed in claim 7, wherein the first of the plurality of parts (61) is used for the addition of an inorganic flocculant and the subsequent one of the parts (62) for the addition of a polymer flocculant. An apparatus as claimed in claim 3, wherein at least one of the plurality of parts for the addition of the flocculant comprises a pipe for allowing flow of the liquid under treatment and a feed pipe connected to the pipe and adapted to supply the flocculant to the pipe. An apparatus as claimed in claim 10, wherein the solid-liquid separating means is a centrifugal dehydrator (203). An apparatus as claimed in claim 3, which further comprises at least either of detecting means, i.e. a thermometer (11) and an electric conductivity meter (13), disposed so as to contact the liquid separated by the solid-liquid separating means so that the control means is enabled to effect required compensation of the value of detection of the heat transfer meter on the basis of the value of detection of the detecting means. An apparatus as claimed in claim 4, wherein part of the liquid in the flocculation tank is filtered and the filtrate is caused to contact the heat transfer meter, and the remaining part of the liquid in the flocculation tank is delivered to the downstream side of the guiding means. An apparatus as claimed in claim 3, wherein the heat transfer meter is a hot-wire current meter or a hot-film type current meter. An apparatus as claimed in claim 3, wherein the adding means is provided with a tank for the liquid of the flocculant (6, 61, 62) and a pump (8, 81, 82) and a pipe for forwarding the liquid in the tank to the aforementioned part (7, 71, 72). An apparatus as claimed in claim 9, wherein the amount of addition of the polymer flocculant alone is controlled by the control means. An apparatus as claimed in claim 16, wherein the amount of addition of the inorganic flocculant is controlled on the basis of the pH value or the electric conductivity of the liquid to which the inorganic flocculant has been added.

Inventors: SHIGEMI HIROTAKE C O KURITA WA, TOTOKI TOSHIO C O KURITA WATER, YASUKAWA YOSHIO C O KURITA WAT, SHIGEMI, HIROTAKE, C/O KURITA WATER INDUSTRIES LTD, TOTOKI, TOSHIO, C/O KURITA WATER INDUSTRIES LTD., YASUKAWA, YOSHIO, C/O KURITA WATER INDUSTRIES LTD.
Applicants: KURITA WATER IND LTD, KURITA WATER INDUSTRIES LTD.
Application year: 1990
Main classification: B01D21
IPC codes: B01D37, C02F11, C02F1, B01D21