AN APPARATUS ANALYSING COMBUSTION GAS

Abstract: A known apparatus for analysing the carbon monoxide content in combustion gases, based on the supply of a gas and air mixture in a known ratio to a combustion chamber in which combustion is catalyzed by means of a platinum wire, the resistance of which is measured as an expression of the heat generation and thus the CO content, is supplemented with an oxygen meter of the same type, to whose combustion chamber combustion gas is supplied. The output signal of the O2 measuring bridge (22) is corrected for the contribution caused by the CO content by passing a signal from the input of the CO meter (17) to a correcting element (25) inserted between the output of the O2 meter (20) and its indicator (23). Correction can also be made for the hydrogen and hydrocarbon content in the combustion gas to improved the accuracy of the O2 measurement.

Description: An apparatus analysing combustion gas The invention relates to an apparatus of the ype de¬ fined in the introductory portion of claim 1. Most of the combustibles in combustion gases, which may be exhaust gases from internal combustion engines or flue gases from heating plants, are comprised of carbon mo¬ noxide CO and hydroge-n H„ which are present in virtually constant quantitative proportions. The same applies to unburned hydrocarbons (CH) with an accuracy acceptable in practice. The rest of the gas, apart from oxygen 0„, is either inacti e as is the case with nitrogen N •, carbon dioxide CO- and water vapour H_0 , or is not pre¬ sent in any great amounts. The measurement result produced by the kno n apparatus of the present type can thus be taken as an expression of the CO content in the combustion gas, and as a matter of fact the apparatus is used in practice for measuring the CO content, e.g. in case of carburetter adjustment. In the combustion the following processes take place: 2C0 + 0, 2C0„ + 68 kcal 2H 2 + 2H 2 0 -. 58 kcal (CH) O _ >pC0 2 + q H 2 0 + x kcal The amount of heat generated per unit of time deter¬ mines the resistance of the catylyzing platinum wire and is taken as an expression of the reaction rate of the CO/0- mixture hich at a fixed temperature and pressure and steady state gas mixture is V = k 1 • -'.CO) -CO,), where the concentrations of the reacting gases are stated b brackets, and k, is a catalyst dependent constant. If (0-.) is kept constant by accurate dosage of the air volume flow supplied, the reaction rate and thus the reaction heat produced by the catalytic combustion ill depent on (CO) alone, i.e. the reaction heat is a measure of (CO). This is obtained by suitable selec¬ tion of the flow rate of the gas mixture and of the other variables in the combustipn system. Nozzles through which the gases are drawn by a pump can be used for the dosage of the volume flows. An air 10 inlet nozzle of th_e same size as the gas inlet nozzle gives the 0 2 amount 1/2 * 213. = 10.53. so that an 0 2 content in the combustion gas of not more than about 2?_ cannot cause an error exceeding 100 15 21 at very small CO concentrations of about 0.5?_. The increasing fuel prices have resulted in an ever greater desire for the best possible utilization of the fuel and thus the greatest possible reduction of the 20 content of combustibles in the combustion gas. When a carburetter is adjusted to a lean mixture, i.e. to a petrol/air weight ratio below 1:13, e.g. 1:15, the consumption of petrol falls, while the tractive force will decrease significantly only when the mixture is 25 made even leaner. The leaner mixture supplied to the engine, the lower the CO content in the exhaust gas; but the oxygen content in the gas will simultaneously increase because of the increasing excess of air which is supplied to the engine. A leaner mixture also causes a greater Zy generation of heat in the engine, and hen the oxygen content in the exhaust gas exceeds 3 to 5 % by volume, there is a great risk of engine breakdown due to burn- -ing of the valves Thus, in connection with adjustment of carburetters there is a great need for a measuring facility of not only the content of combustibles, in particular CO, in the exhaust gas, but also of the 0-. content to prevent this from getting so great that the exhaust val es of the engine ill be endangered. The object of the inven¬ tion is to provide an apparatus of the present type which is capable of meeting this need within reason¬ able economic limits. This object is achieved by the construction of the appa¬ ratus defined in the characterizing portion of claim 1. It will be seen from the above expression of the heat generation in the combustion chamber that the genera¬ tion of heat depends upon both the CO concentration and the 0„ concentration. The said correcting signal hich is supplied to the 0_ meter and depends upon the CO content measured by the residual combustion gas meter, eliminates at any rate essentially the effect exerted on the 0_ measurement by the variation of the CO con¬ tent . As stated abo e, however, the 0- content in the exhaust gas causes some inaccuracy in the measurement of the ' CO content. This inaccuracy can be essentially eliminated by the construction of the apparatus defined in claim 2 Claims 3 and 4 define embodiments of the apparatus hich are expedient in practice. Where a more accurate measurement of the 0 ? content is desired, regard must also be had to the contribut ons to the reaction heat hich are due to the corr-bustion of hydrogen H and hydrocarbons (CH) in t e combustion gas. At no load operation, the reaction heat in the 0-, measuring chamber is usually composed of the fol¬ lowing approximate contributions: CO : 82- 52?. H 2 : 12- 18?. ( C H ) : 6- 30?ά and at full load operation CO : 86- 933S H 2 : 10- 35S ( CH ) : 6- 4?ά Claims 5-7 define means for providing a correcting sig¬ nal which depends upon the content of hydrogen and for correcting the 0„ measurement and/or the CO measurement on the basis of this signal, and claims 8-10 define means for providing a correcting signal which depends upon the hydrocarbon content and for correcting the 0 ? measure¬ ment and/or the CO measurement and optionally the H_ measurement on the basis of this signal. The foregoing description is particularly concerned with the use of the apparatus for the control of exhaust gases from internal combustion engines; however, in a modified version the apparatus can also be used for the control of flue gases from heating * plants, e.g. oil burners. The invention will be explained more fully below with reference to the drawing, in which fig. 1 is a graph which shows an example of the content o CO and 0_ in the exhaust gas from an automobile engine as a function of the air/petrol ratio in the fuel mixture supplied, RAD ORIGINA ■ HL fig. 2 is a diagram of an embodiment of the apparatus of the invention, fig. 3 is a diagram of the electric circuitry incorpo¬ rated in the apparatus, fig. 4 is a diagram of another, more accurately measu¬ ring embodiment of the a paratus of the invention, and fig. 5 is a diagram of the electric circuitry incorpo¬ rated in that apparatus. In the diagrams conduits for the transport of air and gas are sho n by double lines, hile electric connecting leads are shown by single lines. In fig. 1 the weight ratio (in per- cent) of air to pe¬ trol of the fuel mixture is plotted along the abscissa and the content in per cent of carbon monoxide CO and oxygen 0„ in the exhaust gas along the ordinate. The curves shown apply to a specific engine and a specific fuel, but are typical. It will be seen that after a reduction of the CO content to about 0.2 - 0.3?. by volume corresponding to a mix proportion of about 14.6 • 15.0, no considerable additional reduction is obtained by making the mixture leaner, whereas the content of oxygen increases evenly from this mixture range, accom¬ panied by a corresponding increased heat load on the engine, particularly the exhaust valves. Generally, as has been mentioned previously an oxygen content in the exhaust gas above 3 to 5?ό by vol. should not be tole¬ rated. The part of the apparatus of fig. 2 hich serves to mea¬ sure the CO content in exhaust gases is generally known OMPI and has a pump 10, which draws the exhaust gases and atmospheric air through filters 11 and 12, respectively, and dosing nozzles 13 and 14, respectively, and through a measuring cell 16 in the form of a combustion cham- ber. A mixing chamber (not shown) may optionally be inserted between that chamber and the nozzles. The mix¬ ture of exhaust gases, air and combustion products is discharged to the atmosphere from the pump 10. The mea- suring cell 16 contains a platinum wire 15 which cata- lyzes combustion of the CO of the exhaust gases by means of the 0„ content of the air. This combustion can be initiated at a relatively low temperature, such as about 400 C, provided by passing an electric current through the platinum wire. The same platinum wire is incorporated in a measuring bridge 17 which applies a signal to a pointer instrument 18, said signal being indicative of the resistance of the wire and thus of its temperature, which in turn is indicative of the generation of heat per unit of time dependent upon the carbon monoxide concentration (CO). In other words, the pointer instrument 18 can be calibrated directly in vol. ?. CO. To measure the 0_ content the apparatus additionally comprises a nozzle 19 and a measuring cell 20 through which a dosed volume flow of exhaust gases are drawn by the pump 10 from the filter 11. The measuring cell 20 is of the same type as the measuring cell 16 described in the foregoing, and its platinum wire 21 is incor¬ porated in a measuring bridge 22 which supplies an output signal to a pointer instrument. As will appear from the previously gi en expression of the reaction rate the reaction heat in the measuring cell 20 depends not only upon the 0_ content, but also upon the CO content. The circuit sho n in fig. 3 serves primarily to eliminate the effect of the (CO) on the output sig¬ nal from the measuring bridge 21 and, conversely, also to correct the output signal from the measuring bridge 16 for the error caused by the fact that the mixture • supplied to the measuring cell 16 not only contains oxygen introduced ith the atmosphere through the nozzle 14, but also the oxygen present in the exhaust gases. The circuit comprises two correcting elements or units 24 and 25 and t o signal processing units or opera¬ tion amplifiers 26 and 27. The first correcting ele¬ ment 24 in series ith a rectifier 28 is inserted bet een the CO measuring bridge 17 and its pointer instrument 18. In addition to being supplied to the instrument 18, the output signal x from the unit 24 is also applied to the input of the unit 26 w ich pro¬ vides an output signal K, -x ~ '.. ere k, and αare adjus¬ ting factors. This output signal is supplied to an input of the unit 25 hich in series ith a rectifier 29 is inserted bet een the output of the 0_ measuring bridge 22, from hich it receives a signal y', and the pointer instrument 23 of the 0-, measuring bridge 22. The unit 25 is adapted to multiply its t o input sig¬ nals by each _ovther to provide an output signal — -A y = y'-k-i-x . which is supplied to the pointer instru¬ ment 23 and is freed of the part -of the signal y 1 hich is due to the (CO) in the exhaust gases so that the instrument 23 can be calibrated directly in vol. ?ό 0_,. The output signal y is also supplied to the fourth unit 27, which provides an output signal -k -y here k_ is an adjusting factor. This output signal is supplied to an input of the first unit 24 adapted to add it to OMPI the signal x' applied to it from the CO measuring bridge 17. The output signal x = x' - _y thus generated is supplied to the pointer instrument 18, freed of the effect the 0-, content in the exhaust gases has on the output signal x' from the CO measuring bridge 17. T ie apparatus shown in fig. 4 contains the same ele¬ ments 10-16 and 19-21 as that of fig. 2 and further two measuring cells 30 and 32 with a platinum wire 31 and 33, respectively, and three dosage nozzles 34, 35 and 36, as well as a regulating valve 37. The nozzle 34 is connected in series with the measuring cells 16 and 30, and this series connection forms one of three branches which are connected in parallel with each other between the nozzles 13 and 14 at one side and the pump 10 at the other. The second branch is formed by a series connection of the measuring cell 32 and the nozzle 35, and the third branch is formed by the regulating valve 37. The nozzle 19, the measuring cell 20, and the nozzle 36 form an independent series con¬ nection between the filter 11 and the pump 10. Circuit-wise the two series-connected .measuring cells 16 and 30 are disposed between the nozzle -34 and the pump and therefore operate at a relatively lo pressure, which may e.g. be about 0.5 atmosphere or about 5 - 10 N/cm , while the nozzle 35 is disposed between the pump and the measuring cell 32 which thus operates at a relative¬ ly high pressure, which may e.g. be about 0.8 atmosphere or about 8 * 10 N/cm . Also the nozzle 36 is disposed between the punp and the measuring cell 20 to which it is connected; the pressure in this easuring cell may e.g. be about 0.7 atmosphere or about 7 • 10 N/cm . The series connection of the measuring cells 16 and 30 serves to isolate the part of the reaction heat which is due to the hydrogen content in the exhaust gases. It appears from the kinetic theory of matter that the average speed of the molecules is inversely proportional to the square root of the molecular weight. For CO and H„ having the molecular weights of 28 and 2, respectively, e have The thermal conductivity of a gas mixture is due to the fact that energy-rich molecules by their thermal move¬ ments diffuse out between less energy-rich molecules, it being presupposed that the mixing does not simul¬ taneously take place by macroscopic turbulence. From the kinectic theory of matter we have: V = = N m - 2 M v 2 3 where p = pressure V = volume = number of molecules m = mass of a molecule v = average speed of the molecules and = molecular eight The above equation gives i.e. the average speed of the molecules is inversely proportional to the square root of the molecular weight For CO and H- ha ing the molecular eights of 28 and 2, respecti ely, e have: -^ - Emrtζj Since according to Graham's law the diffusion rate is proportional to the average speed H„ will diffuse 3.74 times as far as CO in the same period of time. However , the fas H ? molecules have more collisions than the CO molecules in the same period of time so the random migration of the H_ molecules is therefore actually somewhat shorter than would be expected from the kinetic theory of mat¬ ter alone. Similarly, for (CH) we have (CH) being here conceivably composed of: 11 _>._ CH 4 13 6 or -O C 2 H 4 56 18. C 3 H 8 9 5. C 2 H 2 6 8 C .0 C 3 H 6 which gives an average molecular weight of 36.2. It is now endeavoured to measure the reaction heat of a catalytic combustion at such a low pressure as will make the dependence of the reaction rate upon the supply of matter emerge. Suppose that a boundary layer is dis¬ posed just above the catalyst surface, the molecule movements parallel with the surface will predominantly be produced by the macroscopic translation energy of the ensemble, while the movement in the normal direction of the surface may be expected to be caused mainly by the thermal molecule diffusion. Therefore, in ' principle it must be possible to measure the diffu¬ sion rate of a gas that reacts on the catalyst sur¬ face by connecting the two reaction chambers in se¬ ries and comparing their reaction heat. For a gas which when burned gives an enthalpy change Δ H J/mol, the reaction heat will in this case be pro¬ portional to Δ H/V I. and also depend upon the tempera- ture of the catalyst, upon the binding energy bet een gas molecule and catalyst, upon the migration capacity of the gas molecules and upon their ability to stay on the catalyst surface until they have reacted. It may reasonably be expected that a relatively large part o f the fast H„ molecules react in the front reaction chamber as opposed to the more slowly diffusing CO and (CH) molecules. Thus, relatively much H ? is spent in the front chamber, and this is shown in the subsequent chamber by a relative minor reaction heat owing to the great H„ consumption of the front chamber. As appears from the tables 1-4 below, in which limits for normally occurring concentrations of H ? , CO and (CH) are used, it may be expected that the- difference between the reaction heat of the two reaction chambers is predorniπaπirlry—to- be- ascribed to H-, and CO reactions TABLE 1 f- . g/mole > H kj/molι A H O PI TABLE 2: No load operation Cone . Δ H O c vol. % ' \jTW share H 2 0.5 - 4 85 - 684 33.3 - - 46.0 CO 3 - 10 160 - 535 62.8 - - 35.9 (CH) 0.03-0.8 10.2- 27'1 3.9 - - 18.1 TABLE 3: Full load operation, low r.p.m, Cone. ϋ. % rel c vol V H share TABLE 4: Full load operation, high r.p.m Cone . c• ΛH % rel. c vol. ?ό M share Other occuring reactions are 2 H. 2 H 2 0 2 NO 2 CO 7- N. 2 CC and the secondary reaction 2 NO 5 H. .> 2 , H. 2 H 2 0 hich are both catalysed by Pt. Since these reactions - ** ; " only take place atλ^.1' here 2 is the equivalent air/ fuel ratio, they have no practical importance in connection with 0„ measurements. The reaction proceeds very slowly, and the reaction proceeds only at extremely active Pt Thus, an approximate determination of the C0/H„ ratio of the gas may be performed, and as the total reaction heat is known as well, figures for the concentration of CO and H_ ca . n be obtained which, however, are vitiated by errors, caused e.g. by the presence of (CH). As mentioned in the opening paragraphs, an accurate 0_ measurement requires not only knowledge of the CO and H„ concentrations, but also of the (CH) concentration, which should preferably be measured without any phase displace¬ ment in terms of time ith respect to the other measure¬ ments. Also, it . ould be advantageous to use, as far as possible, the same principle - catalytic combustion - for this measurement as for the others. The next task is then to determine such changes in the state of the gas as will no make the characteristics of (CH) emerge. The equilibrium constants for the CO and H„ reactions are ' CO [° 2 ] 2 [co] 2 . o 2 ] CD "~ ~~ fi OMPI and for the ( CH ) r eact i ons : K CH ___l;I-- Φ K] • [" ■ 2 ' where the exponential sums are stated in the subsequent brackets. It will be seen that in case of equilibrium a sufficient increase in pressure makes the two first- mentioned reactions go to the right while the (CH) reactions mainly go to the left as C.-H-. alone consti¬ tutes more than half of the hydrocarbons. There is no equilibrium in a reaction chamber, but owing to the use of a catalyst and the presence of a high temperature it may be assumed that at least a certain equilibrium is provided directly at the catalyst sur¬ face if only the concen rations, i.e. the pressure, are sufficient. All reactions will produce a greater reaction heat in a chamber with a greater pressure for the mere reason that no more molecules react, but a greater reaction heat incr.ease is to be expected for CO and H- than for (CH) because of the concentration dependence of the reaction rates. ..hen the pressure is doubled, the difference in the reaction heat q between a high pressure chamber and a low pressure chamber will be proportional to where q and p are the exponential sum in the counter and denominator, respectively, of the equilibrium constant. Hence Δq r (C0) is proportional to 283 Φ = 640 Δq p (H 2 ) is proportional to 242 Φ = 545 2. A . .(CH) is proportional to 2043 applying to C-H n Φ = 1500, and Δς_(C0) _ 640 = 0.43 Δq r (C 3 H 3 ) TIM In comparison, measurements performed have given OMPI Δ q ( CO ) 1 .18 r = = 0 . 47 , Δ q r ( C 3 H 8 ) 2 . 51 which must be said to tally sufficiently well with the theory. The circuit shown in fig. 5 has 'four measuring bridges 40-43 to measure the resistances 'of the platinum wires of the four measuring cells 16, 30, 32 and 20 and to provide signals X., X_, X, and X., respectively, representing these resistances and thus the reaction heat in the measuring cells. The output signal X, from the bridge 40 is applied to an operation amplifier 44 supplied with another three signals which are indicative of the hydrogen, hydrocarbon and oxygen content, respectively, of the combustion gas. The operation amplifier 44 processes the signals supplied so as to provide an output signal representing the CO content corrected for the three factors mentioned. This output signal is passed through a rectifier 45 to a pointer instrument 46 calibrated in vol.?. CO. The output signal X_ from the bridge 41 is supplied to an operation amplifier 47 which also receives a signal k, . x, from a potentiometer 48 connected to the output of the bridge 40, to generate an output signal k, . x, - x„, which is supplied to a computing, unit 49 together with a version of the signal X, modified by a circuit 50. The computing unit 49 provides an output signal - x. which is supplied to a multiplier 51 that multiplies the signal by k„. The signal . —*—— BAD - x, thus produced is supplied to an operation amplifier 52 to hich are supplied additional signals indicative of the CH, 0 and CO content, respectively. The operation amplifier- 52 is designed to process and combine the signals supplied so as to provide an output signal which represents the hydrogen content and is corrected for errors caused by CH, 0 and CO. The CO and H signals provided are supplied to their respective potentiometers 53 and 54 to provide signals k,(C0) and k.(H), respectively, which are supplied to an operation amplifier 55 that provides an output signal I- -,(CO + k. (H) J k,. This signal together with the output signal X, from the measuring bridge 42 are applied to an operation amplifier 56, which provides an output signal x, - k-,(C0) + k. (H)J ^ to be supplied to another operation amplifier 57, to which are also supplied signals indicative of the CO, H and 0 content; the operation amplifier 57 is designed to process and combine the signals supplied so as to provide an output signal which is indicative of the CH content in the combustion gas and is corrected for false contributions. The output signal X. from the measuring bridge 43 is supplied to a multiplier 58 hich multiplies it by k- , and the signal k. . x. thus produced is applied to a computing unit 59. This unit also receives a signal 2 2 (CO) + (H) + (CH) provided by an addition circuit 60 by addition of the three output signals from two computing units 61 and 62 and an operation amplifier 63 to hich are supplied the signals CO, H and CH, re¬ spectively. The computing unit 59 provides an output sig,na1 O PI ( C0 ) 2 + ( H ) ( CH ) which represents the oxygen content and is corrected for errors caused by the content of CO, H and CH. This signal is passed through a rectifier 64 to a pointer instrument 65 calibrated in vol.?ό 0„. The practical details of the apparatus of the invention can be designed in other ways than those shown in the drawing and described in the foregoing. Thus, e.g. the hydrocarbon content might optionally be measured by two series-connected catalyst/combustion chambers analogously with the procedure described for hydrogen. BA °OR I GI »NA O PI

Claims: P a t e n t C l a i m s: 1. An apparatus for analysing combustion gases contain¬ ing combustibles of an essentially known composition, said apparatus comprising a residual combustion gas meter having means to supply a dosed volume flow of a mixture of combustion gas and air' in ' a specific ratio to a combustion chamber, which contains a combustion catalyzing element, preferably a platinum metal wire to generate catalytic combustion of part of the mixture, and having means to measure the electrical resistance of the element as an expression of the content of combustible components, c h a r a c t e r i z e d by further comprising an 0~ meter ith means to supply a dosed volume flow of the combustion gas to a combustion chamber with a combustion catalyzing element and with means to measure the resistance of said wire, and comprising means to supply to the 0-. meter a correcting signal dependent upon the output signal of the residual c'o bustion gas meter. 2. An apparatus according to claim 1, c h a r a c t e r ¬ i z e d by further comprising means to supply to the residual combustion gas meter a correcting signal dependent upon the output signal of the 0-. meter. 3. An apparatus according to claim 1 or 2, in which the means to measure the resistance of the catalyst element are formed by measuring bridges, c h a r a c t e r i z e d in that the output signal from the measuring bridge of the 0„ meter is supplied to a correcting element, hich also receives the correcting signal from the residual combustion gas meter and is designed to combine these signals to pro ide an output signal which depends essential ly only upon the 0- content in the gas. O PI 4. An apparatus according to claims 2 and 3, c h a r a c t e r i z e d in that the output signal from the measuring bridge of the residual combustion gas meter is supplied to a correcting element, which also receives the correcting signal from the 0„ meter and is designed to combine these signals to provide an output signal which depends essentially only upon the content of combustible components in the gas. 5. An apparatus according to any of the preceding claims, c h a r a c t e r i z e d by further comprising means to provide a correcting signal depending upon the hydrogen content in the combustion gas, and means to supply said hydrogen signal to the correcting element of the 0 2 meter and/or the residual combustion gas meter. 6. An apparatus according to claim 5, c h a r a c t e r i z e d in that the means to provide the hydrogen signal comprise a combustion chamber which is connected in series with the combustion chamber of the residual combustion gas meter and comprises a catalyst element, means to provide a signal dependent upon the electrical resistance of said catalyst element, and means to combine said signal with the signal indicative of the electrical resistance of the catalyst element of the residual combustion gas meter, to provide a " result- ing signal indicative of the hydrogen content. 7. An apparatus according to claim 6, c h a r a c t e r i z e d in that the said resulting signal is supplied to a correcting element, which also receives the output signals from the residual combustion gas meter and the 0_ meter, to provide a corrected hydrogen signal. An apparatus according to any of the preceding claims c h a r a c t e r i z e d by further comprising means to generate a correcting signal depending upon the hydro¬ carbon content in the combustion gas, and means to supply said hydrocarbon signal to the correcting element of the 0_ meter and/or the residual combustion gas meter and. optionally to the correcting element which corrects the hydrogen signal. » 9. An apparatus according to claim 8, c h a r a c te r i z e d in that the means to generate the hydrocarbon signal comprise a combustion chamber equipped with a catalyst element, said combustion chamber receiving a dosed volume flow of an air and exhaust gas mixture and working at a higher pressure than the residual combustion gas measuring chamber, and means to provide a signal depending upon the resistance of the catalyst element, and means to combine said signal with the output signal of the residual combustion g.as meter and the hydrogen signal so as to provide a resulting signal indicative of the hydrocarbon content. 10. An apparatus according to claim 9, c h a r a c t e r i z e d in that the resulting signal indicative of the hydrocarbon content is supplied to a correcting element, hich also receives the output signals from the residual combustion gas meter and the 0„ meter as ell as the corrected hydrogen signal, ' to provide a corrected hydrocarbon signal. jRE t C_vϊ?I

Inventors: JOHANNSEN OLAF
Applicants: JOHANNSEN OLAF
Application year: 1982
Main classification: G01N27
IPC codes: G01N27, G01N33