US3741007A - Carburetor flow stand - Google Patents

Carburetor flow stand Download PDF

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US3741007A
US3741007A US00280783A US3741007DA US3741007A US 3741007 A US3741007 A US 3741007A US 00280783 A US00280783 A US 00280783A US 3741007D A US3741007D A US 3741007DA US 3741007 A US3741007 A US 3741007A
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air
fuel
carburetor
streams
tracer material
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J Bordeaux
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Carter Automotive Co Inc
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Assigned to CARTER AUTOMOTIVE CORPORATION, INC., 9666 OLIVE BOULEVARD, ST. LOUIS, MISSOURI 63132, A CORP. OF DE. reassignment CARTER AUTOMOTIVE CORPORATION, INC., 9666 OLIVE BOULEVARD, ST. LOUIS, MISSOURI 63132, A CORP. OF DE. ASSIGNMENT OF ASSIGNORS INTEREST. Assignors: ACF INDUSTRIES, INCORPORATED
Assigned to CARTER AUTOMOTIVE COMPANY, INC. reassignment CARTER AUTOMOTIVE COMPANY, INC. ASSIGNMENT OF ASSIGNORS INTEREST. Assignors: ACF INDUSTRIES, INCORPORATED
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    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F02—COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
    • F02M—SUPPLYING COMBUSTION ENGINES IN GENERAL WITH COMBUSTIBLE MIXTURES OR CONSTITUENTS THEREOF
    • F02M19/00—Details, component parts, or accessories of carburettors, not provided for in, or of interest apart from, the apparatus of groups F02M1/00 - F02M17/00
    • F02M19/01—Apparatus for testing, tuning, or synchronising carburettors, e.g. carburettor glow stands
    • G—PHYSICS
    • G01—MEASURING; TESTING
    • G01F—MEASURING VOLUME, VOLUME FLOW, MASS FLOW OR LIQUID LEVEL; METERING BY VOLUME
    • G01F9/00—Measuring volume flow relative to another variable, e.g. of liquid fuel for an engine
    • G01F9/001—Measuring volume flow relative to another variable, e.g. of liquid fuel for an engine with electric, electro-mechanic or electronic means

Definitions

  • a plurality ofinfrared analyzers detects the tracer com [58] Fie'ld 73/116 118 centration in the respective streams. Further detector means detects the quantity of air flowing in the respective stream.
  • Analog divider circuitry is interconnected [56] References cued with the tracer and air detectors and derives from the UNITED STATES PATENTS detected tracer concentration and air quantity air-fuel grultikner 73/118 ratios of the stream mixtures as e 2,734,381 2/1956 Jacobson 73/118 ux 30 Claims, 4 Drawing Figures Primary Examiner-Jerry W. Myracle Attorney-Peter S. Gilster et a1.
  • air-fuel ratios of the air-fuel mixture produced by the carburetor can be determined automatically or mathematically.
  • airfuel ratio (sometimes referred to as fuel-air ratio) is meant the ratio of the quantity (weight) of air flowing through the carburetor per unit time to the quantity (weight) of fuel flowing through the carburetor per unit time during operation of the carburetor.
  • the quantity of air has been measured after the air-fuel mixure leaves the carburetor and after the fuel has been separated from the air by means such as orifice meters, venturi meters, and so-called sonic nozzles. Measurement of the quantity of fuel is carried out in such prior art by metering the fuel as it enters the carburetor, as by means of a positive displacement meter. Examples of the prior art include Converse III et al. U. S. Pat. 3,517,552 and references cited therein.
  • the tracer is one having a high absortion characteristic in the infrared spectrum.
  • carburetor flowtesting apparatus i.e., a carburetor flow stand, and methods for determining air-fuel ratios produced by a multi-throat carburetor under conditions representative of normaloperations thereof; the provision of such apparatus and methods providing highly accurate and rapid determination of fuel-air ratios produced by a carburetor under test; the provision of such apparatus and methods involving downstream measurement of fuel quantity by infrared detection of a tracer in the fuel; and the provision of such apparatus and methods characterized by improved and more accurate downstream measurement of air flow.
  • carburetor flow-testing apparatus comprises means for establishing an air flow through each of a plurality of throats of a carburetor under test and an arrangement for supplying liquid fuel to the carburetor for causing the throats thereof to produce flow of an air-fuel mixture from the carburetor.
  • the fuel contains a tracer material in a predetermined percentage. Provision is made for dividing the air flow into a plurality of streams corresponding to respective throats of the carburetor.
  • the invention further comprises means for evaporating the tracer material from liquid fuel of the mixture and for separating liquid fuel from the mixture to provide an air flow including the tracer material in gaseous (vapor) form.
  • Infrared analyzers function as means for detecting the partial pressure of the gaseous tracer material in said air flow in each of the streams while a pressure sensing means is responsive to air pressure in the streams.
  • a plurality of analog dividers compare the partial pressure of the gaseous tracer material and air the pressure in corresponding ones of the streams and derive from the compared pressures air-fuel ratios corresponding to the throats.
  • Meters provide a readout of the air-fuel ratios thus derived.
  • the invention thus involves establishing an air flow through the throats of the carburetor, supplying fuel including the tracer material in a predetermined percentage to the carburetor to produce the flow of airfuel mixture from it, dividing the flow into a plurality of streams corresponding to the throats detecting the concentration of the tracer material and the quantity of air flowing in the respective streams, and finally deriving from the detected tracer concentration and the detected air quantity the air-fuel ratios produced by the throats.
  • FIG. 1 is a schematic diagram, in partly blockdiagram form, of a flow-testing apparatus constructed according to the present disclosure
  • FIG. 2 is a similar schematic diagram of the presently disclosed flow-testing apparatus.
  • FIGS. 3 and 4 represent in cross section two infrared radiation detection arrangements useful in the apparatus of FIGS. 1 and 2.
  • carburetor flow-testing apparatus of the present invention includes a carburetor flow stand indicated generally at 11 on which is adapted to be mounted a carburetor, as depicted at 13, for flow-testing (or so-called flowing) of the carburetor under conditions representative of normal operation thereof. While carburetor 13 is shown in outline form only, it will be understood that it contains the usual fuel bowl and float mechanism, together with an automatic choke, idle and high-speed fuel systems, as well as a conventional throttle valve.
  • Liquid fuel including a tracer material as described hereinbelow, is supplied to carburetor 13 from a fuel tank 15 containing a volume of fuel 16 by a fuel line 17 connected to the carburetor.
  • Fuel line 17 includes a valve 19 for controlling the supply of fuel, which is maintained by a pump 21 and pressure regulator valve 23 at a predetermined pressure indicated by'a pressure gauge 21.
  • Fuel is withdrawn from fuel tank 15 by pump 21, and discharged into a pipe loop 27 which recirculates the fuel to the tank 15.
  • Pipe loop 27 preferably includes a number of so-called drops which supply the fuel to other carburetors, Fuel line 17 may be considered one of such drops.
  • Recirculation of the fuel to tank 15 is preferably of a flow rate adequate to insure agitation of the fuel 16 in the tank and thereby to insure uniform mixing of the tracer with the fuel.
  • a conventional stirrer in tank 15 may instead be employed, if desired.
  • Tank 15 includes a floating cover or head 29 for minimizing vapor space over the fuel which might otherwise upset the relative balance of the tracer and fuel from evaporation.
  • a monitor or detector 31 for detecting the quantity of the tracer in the fuel.
  • This detector may, for example, comprise a infrared absorption analyzer which, in conjunction with certain electronic monitor circuitry 33, provides a signal on a lead 35 which varies as a function of the percentage of the tracer in the fuel. It will be noted that the signal on lead 35 could be used to drive a meter or other indicator device, thereby to visually indicate the percentage of tracer in fuel 16, or could'be used to regulate automatically the addition of fuel or tracer to tank 15, thereby to maintain a concentration of tracer in fuel 16 at a predetermined level.
  • the fuel 16 in tank 15 may be gasoline, it is preferred to use a fuel which is much less volatile, such as Stoddards solvent (having a flash point of about 100 F.), in order to reduce significantly the possibility of fire or explosion during operation of the flow stand.
  • Stoddards solvent having a flash point of about 100 F.
  • a suction line 37 is provided for causing air to be drawn through carburetor 13.
  • suction line 37 conventionally communicates with a local vacuum source represented in the drawings by a vacuum pump 39 and is interconnected with a suitable plenum chamber 41 of the test stand by means of a plurality of suction branches 43.
  • Each suction branch 43 includes a so-called sonic nozzle 45 in series with a control valve 47. Air is thus drawn through carburetor 13, through a separator-evaporator 49 and thence through a pair of conduits 50a and 50b into plenum chamber 41, and fnally through one or more of the sonic nozzles 45, depending upon the positions of control valves 47.
  • the test stand provides a ducting arrangement interconnecting the downstream side of the carburetor with the vacuum source and by means of which air is drawn by the vacuum source through the carburetor.
  • Sonic nozzles 45 are each of the type described in detail in the aforementioned Converse et al. U.S. Pat. N 0. 3,517,552 and referred to therein as a critical flow venturi meter.
  • a critical flow venturi meter Such a nozzle is characterized by operation such that the pressure upstream of the nozzle is directly proportional to the volumetric flow rate of the air flowing through the nozzle so long as the pressure drop across the nozzle exceeds a predetermined magnitude, occurring at sonic velocities.
  • the pressure in plenum chamber 41 is a direct function of the air volume flowing per unit of time through nozzles 45 and thus through carburetor 13. This pressure in plenum chamber 41 is detected by a conventional pressure detector or transducer 51.
  • Detector 51 is interconnected with suitable circuitry 52 or conversion means for converting the pressure variations sensed by transducer 51 so as to drive a meter or gauge 53.
  • Gauge 53 may be calibrated'directly in air volume or weight units to provide a convenient reading thereof during operation of the flow stand.
  • carburetor 13 may be assured to be a multithroat type, such as a so-called four-barrel carburetor having two sides, each with a main and an auxiliary throat or venturi. In such a carburetor, each side contributes to the air-fuel mixture produced by the carburetor. In testing such a fourbarrel carburetor, it ordinarily may be sufficient (as assumed herein) to be able to determine the air-fuel ratio of the air-fuel mixture produced by each side of the carburetor.
  • evaporator-separator 49 (hereinafter referred to simply as an evaporator) is constructed so that it has two symmetrically identical halves 55a and 55b for dividing the air-fuel mixture from carburetor 13 into two halves or streams corresponding to the throats of each side of the carburetor.
  • side 55a of evaporator 49 receives the air-flow mixture from the main and auxiliary throats of one side of the carburetor and side 55b receives the air-fuel mixture flowing from the other side of carburetor 13.
  • Each side of evaporator 49 represented in the drawings as a chamber in cross-section, the two sides of chambers 55a and 55b being defined by a partition 56, includes suitable baffles as indicated at 57 for causing evaporation of the tracer material from the liquid fuel flowing from carburetor 13 as well as separation of the liquid fuel from this mixture.
  • an air flow is provided from each side of the evaporator which is substantially free of liquid fuel but which includes the tracer material in gaseous form.
  • the partial pressure of the tracer material in this flow from each side of evaporator 49 varies as a function of the air-fuel ratio of the air-fuel mixture produced by the throats of the corresponding side of carburetor 13.
  • a drain provision 58 including a valve connected with drain lines at the bottom of the evaporator permits draining of the separated fuel.
  • individual infrared gas analyzers 59a and 59b are employed to detect the partial pressure of the tracer material in the air stream from evaporator 49. l.e., pressure detectors 61a and 61b effectively detect the pressure of and thereby the quantity of the air of the gas mixture flowing through the respective conduits 50a and 50b.
  • Pressure detectors 61a and 61b may simply be responsive to absolute air pressure or instead they may be responsive to the partial pressure of oxygen in the air. In either case, they may be said to detect or be responsive to the partial or absolute pressure associated with the air in the respective air streams flowing from the evaporator.
  • detectors 61a and 61b each generate a signal proportional to the mass flow rate of air flowing through sample lines 67a and 67b, respectively, and thus serve as meansfor detecting the quantity of air flowing per unit of time from the respective sides of the evaporator.
  • Respective circuits63a and 63b are analog dividers functioning as means for comparing the partial pressure of the tracer material, as detected by the respective analyzers 59a and 5% with the partial pressure associated with the air, as detected by pressure detectors 61a and 61b, in respective ones of the two streams flowing from evaporator 49.
  • Each of the means 63a and 63b derives from the compared pressures an air-fuel ratio produced by. the throats of each of the two sides of the carburetor. These air-fuel ratios are indicated by meters 65a and 65b or other analog readout means.
  • the tracer material infuel 16 is preferably a compound selected from one of the halogenated hydrocarbons and preferably one of the compounds such as dichlorodifluoromethane,- dichlorotetrachloromethane,
  • Evaporator 49 causes substantially complete evaporation of this tracer material from the liquid fuel (such as Stoddards solvent) separating the liquid fuel from the air-flow mixture such that the air flowing from each of the two halves 55a and 55b of evaporator 49 includes this tracer material in gaseous form.
  • sampling probes 68a and 68b extending into conduits 50a and 50b, respectively, and thence through sampling lines or conduits 67a and 67b.
  • sampling lines or conduits are interconnected with a valve 69 having a normal position in which conduit 67a communicates with stunner" conduit fib and conduit 67b communicates with a further conduit 71b, and a reversed position in which conduit 67a communicates with conduit 71b and conduit 67b communicates with conduit 71a.
  • valve 69 having a normal position in which conduit 67a communicates with stunner" conduit fib and conduit 67b communicates with a further conduit 71b, and a reversed position in which conduit 67a communicates with conduit 71b and conduit 67b communicates with conduit 71a.
  • Conduits 71a and 71b supply the withdrawn air including the gaseous tracer to respective sample cells 73a and 73b of infrared analyzers 59a and 59b.
  • Conduits 75a and 75b interconnected with vacuum line 37 or a conduit 77 and with sample cells 71a and 71b, respectively, draw the air and tracer material through the sample cells.
  • a suitable restriction (not 1 shown) which is sufficiently small that the velocity of air drawn through the restriction from conduits 50a and 50b is of sonic magnitude. Accordingly, air flow rates are constant through the sample cells 73a and 73b and do not vary substantially with any variations in'the vacuum (i.e., absolute pressure) maintained by vacuum source 39.
  • pressure sensors6la and 67b are prefera bly located in close proximity (as illustrated) to sample cells 73a and 73b, respectively, so that the pressure sensed by them is that associated with'the air passing through the sample cells;
  • Infrared analyzers 59b and 59b constitute radiation absorption analyzer means which generically may be regarded as a type of spectrum analyzer and which may each be of a commercially available type responsive to the tracer material. Or they may be of construction de- 59a and 59b includes a source of infrared radiation which is periodic in character, an arrangement for directing'the periodic radition through the respective sample cell 73a, 73b and through a reference or comparison cell, and means responsive to changes in the pressure of a gas caused by differential absorption in the sample and reference cells.
  • the latter pressureresponsive means provides an electrical signal via re-- spective leads 7% and 79b to analog divider circuits 63a and 63b, respectively ⁇ Signals varying as a function of the air pressure are provided to circuits 63a and 63b from pressure detectors 61a and 61b by respective leads 81a and 81b.
  • Analog divider circuits 63a and 63b are of a type known to those skilled in the art. As each analog divider circuit 63a, 63b receives the tracer partial pressure signal on line 79a, 79b and air flow signal on line 81a, 81b, the circuit calculates an air-fuel ratio, providing a signal representative of this ratio on a respective output lead 83a, 83b for operation of meters 65a and 65b. t i
  • Analog divider circuits 63a and 63b are each interconnected with lead 35. Any variations in the concentration of tracer material in fuel 16 are signalled by monitor circuitry 33 and the resultant signal on lead 35 causes circuits 63a and 63b to compensate for this variation by correcting accordingly the fuel-air ratio output signal provided on output leads 83a and 83b.
  • the outputs of analog dividers 63a and 63b are connected to meters 65a and 65b through a reversing switch 85 having a normal position interconnecting output lead 83a with meter 65a and output lead 83b with meter 65b.
  • Switch 85 has also a reverse position interconnectingoutput lead 83a with meter 65b and output lead 83b with meter 65a.
  • output signal from analog dividers 63a and 63b may also be supplied to suitable recorders 99 (not shown) or to digital voltmeters (not shown). Representative leads for these purposes are indicated at 87a, 87b and 89a, 89b.
  • analog dividers 63a and 63b may include provision for multiplying the respective tracer and air quantity input signals by suitable scale constants. In this way dividers 63a and 63b may provide additional output signals respresentative of the rates of air flow and fuel flow through the carburetor and which are displayed by suitable additional meters (not shown).
  • pressure detectors 61a and 61b may, as noted, be of the type directly responsive to absolute, or total,
  • gas pressure in lines 71a and 71b may instead advantageously comprise so-called polarographic oxygen partial pressure sensors of the type disclosed in an article by G. A. Rost in Aerospace Medicine, vol. 41, no. 8, August, 1970.
  • Such sensors are responsive solely to the partial pressure of oxygen in a gas mixture. Since the ratio of oxygen in atmospheric air does not vary substantially, detection of the oxygen partial pressure by the sensors provides an extremely accurate measurement of the quantity of air in the fuel-air mixture flowing from the evaporator 49.
  • a small polarizing voltage is applied across electrodes of a polarographic sensor of this type, the sensor produces a current which is proportional to the partial pressure of oxygen.
  • the system of FIG. I quickly and accurately provides determination of the air-fuel ratios produced by a four-barrel or other multi-throat carburetor under conditions representative of normal operation of the carburetor.
  • the carburetor 11 is placed on flow stand 11 and fuel line 17 is connected to fill the fuel bowl of the carburetor.
  • the throttle is set to a desired opening as explained previously and vacuum source 39 and plenum 41 establish an air flow through one or more throats of the carburetor, as appropriate.
  • Evaporator 49 evaporates the tracer material from the air-fuel mixture in each stream and separates liquid fuel from the air-fuel mixture in each stream to provide an air flow including the tracer material in gaseous form. A portion of the flow in each stream is withdrawn from conduits 50a and 50b for sampling by analyzers 59a and 59b.
  • the anaylzers detect the partial pressure and thus the concentration of the gaseous tracer material for each of the two streams, providing signals which are functions of this concentration to analog dividers 63a and 63b.
  • the partial pressure of air flowing in the two streams is detected by pressure detectors 61a and 61b (which may be polarographic oxygen sensors, as noted) and thus signals representative of the air quantity in the two streams are also provided to the analog dividers.
  • Analog dividers 63a and 63b effectively compare the partial pressures of the tracer material and of the air for the corresponding flow steams and derive the air-fuel ratios for the respective streams, each air-flow ratio being displayed by the appropriate one of meters 65a and 65b.-The system responds very quickly, e.g., in the order of a few seconds, and thus it may quickly be ascertained that the carburetor is satisfactory or must be rejected, or necessary adjustments made. Since there may be several throttle settings and possibly several adjustments, the ability of the system to indicate quickly and accurately the air-fuel ratios for each side (or each throat) is highly advantageous, greatly reducing the amount of time required for testing each manufactured carburetor.
  • carburetor flow testing apparatus of the invention which has improved speed of response. That is, the apparatus provides extremely rapid, substantially dynamic determination of the air-fuel ratios produced by a carburetor under test.
  • the apparatus includes a test stand 1 1' which may be similar to test stand 11 shown in FIG. I or may be of a type as disclosed in the before-mentioned copending application of Jean Bordeaux but including in any case an evaporator-separator or, simply, evaporator 49' (sometimes referred to as a vaporizer).
  • a carburetor 13 is shown mounted to test stand 11', fuel including a tracer material in a predetermined percentagebeing supplied to the carburetor via a fuel line 17 of a suitable fuel distribution system like that represented in FIG. 1.
  • evaporator 49 Associated with evaporator 49 is an air pressure detector or transducer 51 responsive to the air pressure in evaporator 49.
  • This pressure like the pressure in plenum chamber 41 of FIG. 1, is a direct function of the volume of air flowing per unit of time through carburetor 13.
  • This pressure relationship results from sonic nozzles 45 through which vacuum source 39 withdraws air from the evaporator 49', which functions, of course, to evaporate or vaporize tracer material and separate liquid fuel from the air-fuel mixture thereby to provide an air flow including the tracer material in gaseous form.
  • a transducer 51 is interconnected with pressure conversion circuitry 52 which drives meter 53 to provide display of the air flow in weight or volumetric units, as in cubic feet per minute.
  • a sample tube or conduit 67 withdraws from evaporator 49 a portion of the air flow (including the gas eous tracer) for analysis by a radiation analyzer cell 73, preferably the sample cell of an infrared analyzer.
  • the sampled gas is drawn through the analysis or sample cell by virtue of a conduit 77 interconnecting cell 73 in the vacuum line 37.
  • sample conduit 67 provides relatively little restriction so as to cause relatively rapid flow of sampled gas from the air-flow through sample cell 73'. Accordingly, the sample cell fills quickly, permitting the air (i.e., gas mixture) therein to be analyzed almost immediately following any change in the operation of carburetor 11. Air is thus withdrawn from evaporator 49 through sample line 67' at a much greater rate than in the apparatus of FIG. 1. Accordingly, the pressure detected by transducer 51 will be reduced and so will not accurately reflect the volume of air flowing through the carburetor. It is necessary, therefore, to correct the air measurement.
  • a polarographic oxygen partial pressure analyzer 61 of the type discussed previously communicates with sample line 67' at a point closely adjacent sample cell 73'.
  • circuitry 93 for supplying polarizing voltage for'sensor 61' and amplifying the sensors output signal.
  • the oxygen detector circuit 93 provides signals to pressure compensation circuitry 95 and to an analog divider 63 like that shown in FIG. 1 which signals vary as a function of the oxygen partial pressure sensed by sensor 61'.
  • the compensation circuit provides a pressure compensation signal to pressure conversion circuit 52 for causing the air quantity (volumetric) indication provided by meter 53 to be increased as a function of any increase in the oxygen partial pressure.
  • the short term rate of response of oxygen sensor 61 need not be very fast.
  • variations in the partial pressure (i.e., concentration) of the tracer material in the air flow passing through detector cell 73' resulting from variations in the air-fuel ratio produced by the carburetor, will be quickly detected by cell 73' and converted by'the tracer detector circuitry 91 associated with cell -73 and supplied as a signal to analog divider 63.
  • Divider 63 operates as explained with regard to FIG. 1 to effectivelycompare the signals representative of the oxygen and tracer partial pressures and to derive from this comparison an air-fuel ratio which is displayed by meter 65'.
  • infrared analysis apparatus useful for determining air-fuel ratios is illustrated which minimizes interference by vapor-form fuel.
  • the problem of interference may be understood by noting that a fuel such as Stoddards solvent useful for carburetor flowing is a complex mixture of a large number of hydrocarbons. Each compound of this mixture has its own distinctive infrared absorption spectrum. Moreover, other solvents containing high proportions of aromatic compounds may be added to Stoddards solvent to adjust its viscosity.
  • additive solvents may be compounds which have many sharp infrared absorption bands in a region of the infrared spectrum in which analysis of the tracer material is desirably carried out.
  • the resulting infrared absorption of variable blends of solvents or additives with Stoddards solvent is a complex grouping of sharp bands and general background absorption.
  • the absorption bands of such solvent mixture vapors overlap and thus interfere with the absorption bands of the tracer material, such as the fluorocarbon Freon 113," to an extent dependent upon the solvent mixture composition, pressure, and temperature.
  • Such interference degrades the precision of analysis with the result that accuracy in the determination of air-fuel ratios, and stability and repeatability of results are reduced.
  • Apparatus 101 includes adetector'102. Associated with the detector is a source of periodic infrared radiation, here illustrated as an infrared radiation element 103, energized for this purpose by a pulsed voltage soucre 105 or the like providing pulses at a frequency of 5 Hz, for example.
  • a source of periodic infrared radiation here illustrated as an infrared radiation element 103, energized for this purpose by a pulsed voltage soucre 105 or the like providing pulses at a frequency of 5 Hz, for example.
  • Element 103 radiates a single beam of pulsed infrared radiation of predetermined wavelength (i.e., a band or predetermined continuum of infrared energy) which is directed through a front optical window 107, through a sample cell or chamber 109, through an inner optical window 111, and thence through a reference cell or chamber 113.
  • the optical length of sample cell 109 is much shorter than that of reference cell 1 13. Gas to be sampled is admitted to sample cell 109 by air inlet conduit and discharged therefrom by an outlet conduit 117.
  • detector 102 includes a so-called back chamber 119 closed by a lid 121 and including suitable provision such as recesses 123'and 125 in which are positioned respective diaphragm assemblies 127 and 129.
  • a port 131 provides pressure communication between one side of diaphragm assembly 127 and sample cell 109 and a similar port 133 provides communication between one side of diaphragm assembly 129 and reference cell 113.
  • Pressure in back chamber 119 acts on the other side of each of the diaphragm assemblies which are preferably of a construction similar to that used in other types of infrared analyzers.
  • Assemblies 127 and 129 each include a thin gold leaf diaphragm which is movable, with respect to a fixed electrode spaced a small distance, e.g., 0.003 in., from the diaphragm to provide, in effect, a variable capacitor whose capacitance varies with changes in pressure causing movement of the diaphragm.
  • Suitable feedthrough terminals 135 and 137 provide respective interconnections with one of the electrodes of each diaphragm assembly, the body of detector 102 (which may be of brass) providing the other. Terminals 135 and 137 are interconnected with conventional electronic circuitry for converting the capacitance variations into a signal which varies as a function of the concentration of a gas being sampled by sample cell 109 by amplification, filtering, demodulating and conditioning.
  • both reference chamber or cell 113 and back chamber 119 are filled with a sensitizing gas having fuel (e.g., Stoddards solvent) vapor components of the type which would cause absorption interference with the tracer vapor to be detected.
  • fuel e.g., Stoddards solvent
  • inlet conduit 115 is connected for sampling the air flow from evaporator 49 of FIG. 1 or 49 and thus is connected in the same manner as sample conduits 67a, 67b or 67' of FIGS. 1 and 2.
  • Conduit 117 is connected to a vacuum source and thus the gas mixture, i.e., air flow from the evaporator,
  • sample cell 109 including the gaseous or vapor tracer material is drawn through sample cell 109.
  • Such expansion cycles are repeated at the Hz radiation pulse rate, the diaphragm deflection amplitude being directly dependent upon the amount of radiant energy absorbed by the sensitizing or so-called charge gas in reference cell 113.
  • Maximum deflection occurs in the absence of tracer vapor in sample cell 109.
  • concentration of the tracer e.g., the fluorocarbon Freon 1 13
  • the deflection amplitude and thus the capacitance variation of diaphragm assembly 127 is increased considerably while the capacitance variation of diaphragm assembly 129 is decreased only slightly.
  • diaphragm assembly 127 detects pressure changes in sample cell 109 resulting from absorption of radiation by the tracer vapor
  • fuel vapors present in cell 109 also induce pressure changes by absorption of the radiation in a sense tending to interfere with the detect ing of pressure changes resulting from tracer absorption.
  • Diaphragm assembly 129 detects pressure changes in reference cell 113 resulting from absorption of the radiation by the concentration of fuel or solvent vapors therein. However, the back chamber arrangement substantially cancels the detected pressure changes in the sample cell resulting from the interfering vapor-form fuel with the detected pressure changes in the reference cell.
  • sample cell 109 and its diaphragm assembly 129 constitute a first radiation detector means responsive to the partial pressure of the tracer material in the air flow from the flow stand evaporator which is sampled.
  • reference cell 113 and its associated diaphragm assembly 129 constitute second radiation detector means responsive to a predetermined fuel vapor concentration, the second detector means being operatively associated by means of back chamber 119 with the first detector means for causing cancellation of the interference by the vapor-form fuel in the sampled air flow.
  • the flow-testing apparatus when detector 102 is used for determination of air-fuel ratios, includes a suitable pressure sensor responsive to the partial pressure of air in the air flow from the evaporator as well as analog divider means responsive to signals from this sensor and from the radiation analyzer electronics for effectively comparing the air and tracer partial pressures to derive the air-fuel mixture produced by the carburetor under test.
  • FIG. 4 illustrates a modified version 102 of the detector shown in FIG. 3, and providing what may be termed a flow-through radiation analyzer embodiment 101'.
  • the flow-testing apparatus when detector 102 is used for determination of air-fuel ratios, includes suitable pressure sensor responsive to the partial pressure of air in the air flow from the evaporator as well as analog divider means responsive to signals from this sensor and from the radiation analyzer electronics for effectively comparing the air and tracer partial pressures to derive the air-fuel mixture produced by the carburetor under test.
  • Detector 102' in addition to minimizing fuel vapor interference, is adapted to provide extremely rapid, substantially dynamic determination of air-fuel ratios produced by a carburetor under test.
  • Detector 102' is shown to include a sample cell 109' which is constituted, in effect, by a portion 137 of a conduit which may be assumed to constitute the downstream end or an extension of an evaporator of the type shown in FIGS. 1 and 2.
  • the evaporator operates as described previously to evaporate the tracer material from the air-fuel mixture flowing from the carburetor and to separate liquid fuel from the mixture to provide an air flow including the tracer material in gaseous, i.e., vapor form, and including also any fuel which may have evaporated.
  • Conduit 137 is shown to include a suitable front window 107 permitting the beam of periodic infrared radiation from source 103 to pass through the sample cell 109', then through a suitable inner window 111' separating the sample cell 109 from a reference chamber or cell 113, and finally through the reference cell.
  • the detector is shown to include a modified port or passage 131 providing communication between cell 109' and diaphragm assembly 127.
  • a polarographic oxygen partial pressure sensor of the type described with regard to FIG. 2 and which is interconnected with suitable amplification circuitry for providing a signal representative of the partial pressure of the air of the air flow.
  • the diaphragm assemblies 127 and 129 of detector 102 are, of course, connected to the conventional analyzer circuitry to provide a signal representative of the partial pressure of tracer in the air flow.
  • analog divider means divides one signal by the other to provide a third signal representative of the air-fuel ratio produced by the carburetor under test.
  • Carburetor flow-testing apparatus for determining air-fuel ratios produced by a multithroat carburetor under conditions representative of normal operation thereof, comprising:
  • first detector means for detecting the concentration of tracer flowing in respective ones of said streams
  • second detector means for detecting the quantity of air flowing in respective ones of said streams
  • means interconnected with said first and second detector means, for deriving from the detector tracer concentration and the detected quantity of air flowing in the respective streams air-fuel ratios of the air-fuel mixture flowing 'in said streams and thereby the air-fuel ratios produced by said throats.
  • said first detector means comprises radiation analyzer means responsive to said tracer material.
  • said radiation analyzer means comprises at least one infrared analyzer, said tracer material having a high infrared absorption characteristic, and further comprising means for causing sampling by said infrared analyzer of a gas mixture, including said tracer material, from each of said streams.
  • Apparatus as set forth in claim 4, comprising a plurality of pressure detectors each associated with a respective one of said infrared analyzers and each responsive to the partial pressure of air in the gas mixture sampled by the respective infrared analyzer.
  • said means for deriving air-fuel'ratios comprises at least one analog divider responsive to signals from said first and second detector means, said analog divider providing an output signal representative of air-fuel ratio, and readout means responsive to said output signal.
  • Apparatus as set forth in claim 1 further comprising means for evaporating tracer material from liquid fuel of said mixture in each stream and for separating liquid fuel from said mixture in each stream to provide an air flow including said tracer material in gaseous form.
  • Apparatus as set forth in claim 1 comprising means for monitoring the percentage of tracer material in said fuel and providing a signal representative of said percentage, said means for deriving air-fuel ratios being responsive to said signal for correcting the derived airfuel ratios according to variations in said percentage.
  • Carburetor flow-testing apparatus for determining air-fuel ratios produced by a multi-throat carburetor under conditions representative of normal operation thereof, comprising:
  • Apparatus as set forth in claim 9 wherein said means for establishing an air flow is constituted by ducting means interconnecting the downstream side of the carburetor with a vacuum source.
  • said ducting means includes a chamber constituting said means for evaporating tracer material andv separating liquid, said means for dividing said flow into streamscomprising means for dividing said chamber into a plurality of compartments, each of said streams flowing into one of said compartments.
  • each of said compartments includes a plurality of baffles.
  • Apparatus as set forth in claim 11 further comprising plenum means interconnected between said chamber and the vacuum source, and means for maintaining in said plenum a pressure which is a function of the volume of air flowing per unit of time from said carburetor.
  • Apparatus as setforth in claim 13 further comprising a pressure transducer associated with said plenum and responsive to the pressure therein and means operative in response to a signal from said transducer for indicating the quantity of air flowing through said carburetor.
  • said means for detecting the partial pressure of the tracer material comprising a plurality of radiation analyzers, each including a sample cell, said apparatus including conduit means for causing sampling of at least a portion of the air flow in each of said streams by a respective one of said sample cells.
  • radiation analyzers are constituted by infrared analyzers, said tracer material having a relatively high infrared absorption characteristic at a location in the infrared spectrum where said fuel has a relatively low infrared absorption characteristic.
  • Apparatus as set forth in claim 15 wherein said means for detecting the partial pressure of air flowing in each of said streams comprises a plurality of pressure detectors each associated with one of said sample cells and each responsive to the partial pressure of the air flowing through the respective cell.
  • each of said radiation analyzers provides a first signal which is a function of the partial pressure of the tracer material in a respective one of the streams and each of said pressure detectors provides a second signal which is a function of the partial pressure of the air in a respective one of the streams, said means for comparing partial pressures being operative in response to said first and second signals.
  • said means for comparing partial pressures comprises a plurality of analog divider means each interconnected with a respective one of said radiation analyzers and with a respective one of said pressure detectors, each divider means providing an output signal representative of the air-fuel ratio in one of said streams.
  • Apparatus as set forth in claim 15 further comprising means for cross-checking operation of said radiation analyzers.
  • said cross-checking means comprises a valve interconnected with said conduit means for causing sampling of the flow in different ones of said air streams by any one of said sample cells.
  • said detecting the partial pressure of tracer material includes the step of generating a first signal which is a function of the partial pressure of the tracer material
  • said detecting the'partial pressure of air includes the step of generating a second signal which is a function of the partial pressure of air, said deriving air-fuel ratios comprising dividing said second signal by said first signal to provide a third signal representative of air-fuel ratio.

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  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Fluid Mechanics (AREA)
  • General Physics & Mathematics (AREA)
  • Investigating Or Analysing Materials By Optical Means (AREA)
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US00280783A 1972-08-15 1972-08-15 Carburetor flow stand Expired - Lifetime US3741007A (en)

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US28078372A 1972-08-15 1972-08-15

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6237575B1 (en) * 1999-04-08 2001-05-29 Engelhard Corporation Dynamic infrared sensor for automotive pre-vaporized fueling control
US6491206B2 (en) 2000-11-27 2002-12-10 Sauer-Danfoss, Inc. Method of making closed cavity pistons

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6237575B1 (en) * 1999-04-08 2001-05-29 Engelhard Corporation Dynamic infrared sensor for automotive pre-vaporized fueling control
US6491206B2 (en) 2000-11-27 2002-12-10 Sauer-Danfoss, Inc. Method of making closed cavity pistons

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FR2196462A1 (cs) 1974-03-15
FR2196462B3 (cs) 1976-05-21
DE2328664A1 (de) 1974-02-28
JPS4951420A (cs) 1974-05-18
JPS5241412B2 (cs) 1977-10-18

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