Source: https://patents.google.com/patent/US3165693A/en
Timestamp: 2019-07-20 03:24:53
Document Index: 70811107

Matched Legal Cases: ['art 46', 'art 48', 'art 48', 'art 46', 'art 46', 'art 48', 'art 48']

US3165693A - Continuously operable apparatus and method for counting particles in successive portions of a flowing fluid stream - Google Patents
Continuously operable apparatus and method for counting particles in successive portions of a flowing fluid stream Download PDF
US3165693A
US3165693A US175172A US17517262A US3165693A US 3165693 A US3165693 A US 3165693A US 175172 A US175172 A US 175172A US 17517262 A US17517262 A US 17517262A US 3165693 A US3165693 A US 3165693A
US175172A
1961-05-15 Priority to US116907A priority Critical patent/US3165692A/en
1962-02-23 Application filed by Technicon Instruments Corp filed Critical Technicon Instruments Corp
1962-02-23 Priority to US175172A priority patent/US3165693A/en
1962-05-12 Priority claimed from FR897385A external-priority patent/FR1325237A/en
1965-01-12 Publication of US3165693A publication Critical patent/US3165693A/en
Jan. 12, 1965 J. lsREELl ETAL 3,165,693
coNTzmuousLY OPERABLE APPARATUS AND METHOD FOR couNTING PARTICLES IN SUCCESSIVE PORTIONS OF A FLOWING FLUID STREAM Filed Feb. 23. 1962 E l LEE m @Mmmm m T D ,w @ma w A. e ww M P. UH aw M O/ M MMM n M m ucuzw aro@ A wm .n TM mil w nm: m l mim@ m u l 2 2 m B, m r n n m n @awww/v. mw m ,w: a 9/ m w s p. MA m.. 2ML ,o M 7 .H o M .l A IIL A A BULB AIB FRE L18 (//D United States PatentI 3,165,693 CoNnNUoUsLY OPERABLE APPARATUS AND METHOD Fon CoUNTING PARTrcLEs iN'sUC- CESSIVE PORTINS OF A FLOWNG FLUIDV STREAM .lack Isreeli, Tuckahoe, and Theodore Pleasant Valley, N.Y., assignors to Techuicon Instrui ments Corporation, Chauncey, N.Y., a r4corporation-.of i
New York v Filed Feb. 23, 1962, Ser. No.,175,172
13 Claims. (Cl, S24-'71.)
suspended, effected a particle count by causing a mercury siphon to displace a small predetermined volume of the suspension from a large beaker and measuring the number of particles in the displaced suspension. Due to the necessity of providing separate beakers of liquid, the count determinations could not be accomplished in a continuous fashion and the counts were determined in-batch fashion wherein individual beakers of the liquid were intermittently supplied -to the counter manually for the count determinations.
The primary object of the present invention is to provide a method and apparatus for continuously determining the numberof particles suspended in a liquid medium.
Another object is to provide an apparatus of the aboveindicated type whose operation is based on the'electrical4 conductivity difference between the particles and the liquid suspension medium and which is so constructed that clogging is prevented in the constricted ow path for the liquid.
Another object is to provide apparatus, which includes a particle counter cell for determining the number of particles in a liquid, with simple and inexpensive means for Yproviding a predetermined level of liquid'in the cell an'd for automatically controlling the level of the liquid inthe cell. Y l g A further object is the provision of a cel-l which is especially well adapted for use in automatic and continuous particle counters.-
The above and vother objects, features and advantages of the invention will be more fully understood from the following description of the presently preferred embodiment of the invention considered in connection with the accompanying illustrative drawings.
FIG. l is a more or less diagrammatic view illustrating cell 16, and an electrical measuring circuit generally in-V dicated by the reference numeral 18. The liquid samples Whose particle contents are to be determined are provided in open top receptacles 270 which are arranged in a circular row on a rotary support plate 22 which is intermittently rotated to position the open top of each sample receptacle below the inlet end of an inlet aspirating tube 26. The inlet tube is pivoted into and out of each receptacle asrit isV moved into position by the rotation of the support plate 22 and a portion of the sample from each ICC receptacle is aspirated from its respective receptacle by the action of pump 14 and flows as a stream through supply tube 26 and pump tube 28 where it joins a stream of an inert gas, for example air, which is supplied through pump tube 30, and a vstream of a diluent, for example distilled Water, which is supplied through pump tube 32'. The separate streams join each other at fitting 34 and are mixed in the horizontalmixing helical coil 36 toform a segmented stream consisting of a series of liquid segments L consisting ofsample liquidand diluent separated from each other by an intervening'segment G of air, and this segmented stream is transmitted to the T-connection`38 by the action of the pump. I i As seen in FIG. 3, the air segments G are separated from' the segmented stream byaspiration at T-connection 3S via tube240 and pump tube 42, respectively, as shown by FIG. l and the sample diluted stream, in consolidated form, ows to the cell 16 via tube 44. The gas segments aid in keeping 'the interna-l walls of the various tubes of the apparatus clean and also subdivide each sample into aseries Vof liquid segments which assists in the mixing of the sample with the diluent in the mixing coil 36. Moreover, since the intake tube 24 is removed from the receptacle 20 to permit the succeeding receptacle to be moved intoV aspirating position, the continuously operating pump 14 Vdraws air into the inlet tube 26 so that each sample is separated from the 'other by an'intervening segment of air and because of the continuous operationof the pump each sample is also separated from each other by an intervening segment of diluent.
Referring now to FIG. 2, the cell 16 is preferably made' of heat-resistant glass sold under the trademark Pyrex, and is of tubular construction. VThe cell comprises a chamber part 46 and an aspirator part 48 which is positioned in the chamber part in fluid tight relation therewith due to the resilient sealing ring 50. The ringis positioned in a groove 52 provided on the outer upper surface of part 48 and abuts against a shoulder 54 provided on the inner upper surface 'of part 46. Y
The lower portion of part 46 is shaped to form a chamber 56 which'receives the liquid whose particle content is to be determined. This lower portion is also provided with a downwardly inclined inlet arm 58 having an outlet end 60 positioned 'above a wall 62 so that the incoming liquid, which is` in the form of drops, falls onto the wall and not directly into the -liquid in chamber 56 to prevent Y any disturbance of the liquid. Tube 44 from the T-connection 38 is connected to the inlet end 64 of arm 58 for transmitting the consolidated liquid stream to the particle counter cell. Since the liquid is electrically conductive, the manner of introducing the liquid into the chamber 56 of the cell in vthe form of separate individual drops which do not fall directly into the liquid, minimizes electrical'V disturbance of the measuring circuit which might otherwisel occur because of possible induced currents in the conductive liquid.` The air segments between the samples also reduce the effects of induced currents.
The lower portion of the chamber part-i6 is provided' with a horizontally extending arm 66 to which is con-` nected a hollow resiliently compressible bulb 68 which isf in communica-tion with chamber 56 and is used to controlthe level 'of liquid in the chamber as will be more understood hereinafter. The bottom of the chamber is provided withv 'an' opening 70 through which excess liquid hows fromthe chamber in the form ofindividual drops and Valso through which passes any foreign matter that may be present in the liquid. p
The aspirator part 48 of the cell has its lower portion shaped to form a chamber 72 which is positioned in chamber 56. The wall 74 which separates the chambers is provided with an aperture 76 of relatively small size to form a constricted ow path for the liquid from chamber 56 to chamber 72. The upper portions of the aspirator part is provided with a horizontally extending outlet arm 78 to which a suction tube 80 is connected. 'I'he suction tube is connected to aspirating pump tube 82 and it will be understood that the suction tube as Well as bulb 68 are suiiciently stil to resist deformation or collapse under the suction effect of the pump tube 82.
A grounded electrode 84 extends through aspirator part 48 and its lower end is adjacent one side ofaperture 76 in chamber 72. The inner wall of chamber 56 is coated with an electrically conductive material 86 and another electrode 88 has one of its ends in contact with the coating 86 and is positioned in the liquid in chamber 56 adjacent the other side of aperture 76. The opposite end of electrode 88 is connected to the previously mentioned measuring circuit 18.
As explained in our co-pending application Serial No. 116,907, filed May l5 1961, and as indicated above, aperture 76 provides a constricted flow path for the liquid from chamber S6 to chamber 72. The conductivity of this flow path changes as an individual particle is carried with the liquid through the aperture because the particle displaces the liquid medium within the aperture and thereby changes the electrical resistance of the aperture` contents. This Produces a voltage pulse .of short duration which has a magnitude proportional to the particle size and this voltage pulse is .transmitted to the measuring circuit 18 and is utilized in operating a recorder 92 which records the number of particles in the sample.
The size of the aperture is selected so that only particles' of a given size range can pass through the aperture and in'this manner the apparatus is able to select and count those particles only which constitute a particular constituent of the liquid, for example white or red corpuscles in whole blood. A diluent is added to the liquid in sucient quantities to dilute the liquid and thereby reduce the probability of two or more particles passing simultaneously through the aperture 76, since it will be readily apparent that this would still result in a single voltage pulse even though two particles are present in the aperture. The conductivity of the diluent can be selected so that the resulting liquid has a conductivity which is different from the particles suspended therein.
Operation of pump 14 results in the flow` of liquid from chamber 56 through aperture 76 intochamber 72 and form said chamber the'liquid is transmitted from the cell by suction through tubes 80 and pump tube 82, respectively. The suction effect provided by the pump prevents clogging whichmay otherwise occur in the relatively small aperture 76, especially. in the case of relatively large particles. The suction prevents this clogging and aids in dislodging any particle which may be entrapped in the aperture.
As indicated above bulbv 68 is provided for adjusting the level of the liquid in chamber 56 at thev commencement of the operation of the particle counter. In actual practice, the liquid level in chamber 56 is predetermined before placing the particle counter in operation for counting blood cells or other particles in such a manner as to avoid the waste of blood or other liquid under test. More particularly, water, for example, is the liquid which is utilized for this purpose. In the initial stage of the operation for predetermining the level of liquid in chamber 56, when the pump 14 is operated air which enters through opening '70 is aspirated through chamber 72 until the liquid, presently water, which is admitted into chamber 56 through tube 44 rises to a point just above .the aperture 76 so that liquid will then pass through said aperture from chamber 56 and into chamber '72. It is to ybe noted that more liquid enters chamber 56 through tubes 28 and 32 than is withdrawn from said chamber through chamber 72 and outlet 78 by pump tube 82. This difference in liquid quantities is discharged from chamber 56 through opening 70. It is desirable to provide a liquid level in chamber 56, for the normal operation of the apparatus, which is higher than the liquid level which obtains as a result of the operation just described. One kof the reasons 4for providing this higher liquid level is to guard against the possibility of clogging of the aperture 76 by particles which might iloat and collect at the upper surface of the liquid and which, if the liquid level is closely adjacent to the aperture 76, might enter said aperture. For the purpose of raising the level of the liquid in chamber 56 to provide the desired operating level, illustrated by FIG. 2, sufciently above the aperture 76 to minimize the possibility of clogging the aperture, bulb 68 may -be manipulated in a manner which will now be described,.it being understood that the apparatus is still being operated with the introduction of water into chamber 56. After the level of liquid in chamber 56 rises to the level immediately above aperture 76, bulb 68 is compressed While liquid continues to flow into chamber S6 through tube 44, and the compression of said bulb is thereafter gradually released resulting in a reduction of pressure in chamber 56 to a value below that of the atmospheric pressure at the outlet 70 so that. as. lliquid continues to ow into l chamber 56 no liquid ows through outlet 7i) with the result that the liquid rises in said chamber. By proper manual manipulation of bulb 68, namely by partial compression and gradual release of compression while the liquid flows through chamber 56 through tube 44, the level of the liquid in said chamber is conveniently and quickly predetermined. The apparatus is now in condition for examining Vthe liquid in the receptacles 20 to determine the number of particles. which they contain and the inlet end of the inlet tube 24 is inserted in one of the receptacles to begin the operation of the apparatus. It is to be noted that except for opening 70, the particle counter cell 16 is `closed so that the atmospheric pressure applied at the opening 70 is operative to maintain the level of theliquid in chamber 56.
During operation of the apparatus, the rate of flow of incoming liquid into chamber 56 is'somewhat greater than the rate of flow of the outgoing liquid from charnber 72. However, the level of the liquid in chamber 56 remains substantially at the position shown above the aperture 76 because of the atmospheric pressure applied to the closed system through openingV 78 and the excess liquid due to the difference in the flow rates Hows in the form of drops from chamber 56 through outlet 70. This constant dripping of excess liquid from chamber 56 helps in removing any particlesfrom the` chamber which might otherwise tend to clog aperture 76.
The power supply 94 of the measuring ,circuit comprises ahigh lvoltage direct current supplywith a high resistance in series with the voltage source so that the currentsl in the circuit are substantially constant. Accordingly, as the conductivity of the constricted ow path of the liquid changes due to the passage of the particles through the aperture 76, the voltage changes in proportion to the change in resistance of the ow path. This resulting'voltage pulse is amplified by the amplifier 96 and the amplified voltage is ltransmitted to threshold circuit g8. The threshold circuit transmits only'those voltage pulses which are above a predetermined mag-j nitude corresponding to a particle of a particular size. The transmitted voltage pulsesV are received by a count rate circuit 100 which provides a voltage that is proportional to'the rate of flow of the particles through the aperture 76. Since this rate of flow is approximately proportional to the quantity of particles present in a predetermined volume of liquid, the voltage provided by circuit ltiildsameasureof the number of particlesin the sample. This voltage is supplied to one side of a nulltype balancing circuit 102 and the difference in voltage between the measuring side of the circuit and the constant voltage side of the circuit is applied to the motor of the recorder 92 which operates a stylus to produce,
stemming 104 which is indicauye ef a'numterpof par' It will be notedfthat the recording ticles in the sample. consists of peaks .106 separated fromeach-fother in the direction of movement of the chart paper indicated by.4v
Y each: other by a seg-'mentof diluent and during ,the passage of diluent through the cell 16,'no peaks occur. InA
thismanner, eachsample can easily be distinguishedfrom the other onvithe chart paper of `the recorderfand a continuous recording of' the number of particles in each sample 'is continuously=provided.
It is Withinthe scope ofthe'inventionito utilize the apparatus vfor continually monitoring a continuous stream of liquid to determine th'e'number of particles present in thestream. 'Thiscan easily be'accomplished by counecting'the intake tube26 tQ-an oltake from a conduitV infwhich Aa str eam is owing andcontinuouslyV` transmitting a portion of said stream .throughiube 26. Of4
course, ,when the apparatus is to monitor `|a stream, a sample supply device `1 2 is not used.
'Thesample supply device may-be of the type shown inr 'l the U.S. application of Jack Isreeli, Serial No. 666,403, filed 'June 18, 1957, and assigned to the` assignee of the present application, now- Patent No. 3,038,340.
The various circuits comprising the measuring means 18 have not been described jin detail .since they, are Well known circuits and their details do non-:per se,- orm a part of .this invention. The proportioning pump 14 is preferably of the type shown in U.S. Patent` No. 2,935,028, issued May 3, 1960. Brieiiy'described, the pump comprises `a series of compressing rollers 110 whosel ends are connected to sprocket chains 112 whichmove-the rollers longitudinally of the flexibly resilient pump tubes. During this movement, the pump ltubes are compressed along their lengths by the rollers against a platen .114 for the pumping operation. Since the pum'p tubes are closed by their engagement with-the rollers, it will be observed that the tubes connected to the particle counter cell 16 are not exposed to the atmosphere.
While the invention has .wide application for industrial uses for the counting of minute particles distributed in various fluids, it is considered to have important clinical uses especially for counting blood cells in blood specimens whereby to eliminate thetedious methods which ,involve the counting'oi` blood cells by a technician with .the required aid of a microscope. Also, it Willbe understood that by reason of thefact that the invention provides for andV makes possible the examination Aof a'series of specimens or samples one after another flowing in a stream through the apparatus, the present apparatus and method greatly reduce the time required for making blood counts besides eliminating the tedious Work referred to and greatly reducing the chances of error.
This application relates in subject matter to our above mentioned co-pending application, Serial No. 116,907,
tiled May l5, 1961. Itis within the scope of the present invention to employ anti-clogging devices described in our co-pending application in the apparatus described in the present application.
While we have shown and described the preferred embodiment of our invention, it will be understood that the invention may be embodied otherwise than as herein specifically illustrated or described, and that certain changes in the form and arrangement of parts and in the specic manner of practicing the invention may be made Without departing from the underlying idea or principles of this invention within the scope of the appended claims.
l. Particle counting apparatus for continuously determining the number of particles in a liquid having a different electrical conductivity than said particles, said apparatus comprising:
.tus comprising:v 1 Y v (a) a cell having first andsecond chambers separated (a) `a cell` havingl iirst and second-"chambers: separated from each otherby a Wall having an aperture thereVv in forming a Vconstricted flow path forkthe' liquid" from said iirst chamber to said second'chamber, 1;
vv(b)n said first chamber having ya liquid inlet and said second chamber having a liquid outlet,r Y
Y (0)'means .connected to said inlet; for'tr'an'smitting a stream of liquid to said first chamber,
'(d) means connected tosa'id outlet; for causing .ioW'w of the liquid through said constricted ow path.
vto said outlet, v Y
(e) means formeasuring the electrical'conductivity of said Vtiovv path-during .theow of the liquid therethroughas a measurement of the number of particles in said liquid, and Y q (f) means in communication with said rstjchamber Afor ,varyingvthe pressure therein and thereby controlling the level of liquid insaid iirstchamber. l2. Particle counting apparatus forvcontinuously deter- 'the number of particlesin a Aliquid havinga diierent electrical conductivitythansaid particles, said appara from each other by a rWall having anaperture therein forming` a constricted flow path for the liquid vfrom said iirst chamber to said second chamber,
g (b) said iirst chamber having aliquid` inlet andsaid second vchamber vhaving a liquid outlet,
`(c) meansjconnected to said inletfor ltransmitting a stream of liquid'to said rst chamber,
(d)'means connected to said outletfor'causing iiow f for varying the Vpressure therein fand thereby controlling the level 'of liquid Vin Vsaid iirstV chamber,
(g) said liquid level controlling means comprising a hollow resiliently compressible member adapted to be compressed `and`y released from ,compression to vary the pressure in said-,first chamber." 1'
, 3. Particle counting apparatus for continuously determining thenumber of particles in a liquid having a difierent electrical conductivity than said'particles, lsaid apparatus comprising: Y t
(a) a cell having first and second chambers separated from each other by a Wall having an aperture therein forming a constricted owpath for the liquid from said first chamber to said secondchamber,
( b) said lirst chamber having ya liquid inlet and Vsaid second chamber having a liquid outlet, (c) .means connected to said inlet for transmitting a stream of liquid to said rst'chamber, l (d) means connected to said outlet for causing ow of the liquid through said constricted iiovvV path to Y said outlet, (e) means for measuring the electrical conductivity of said iiow path during the ow of the liquid therethrough as a measurement of the number of particles" 4. Particle counting apparatus for continuously determining the number of particles in ya liquid having a different electrical conductivity than said particles, said apr paratus comprising:
(a) a cell` having first and second chambers-separated .from each. other `by a wall having an aperture therein forming a constricted fiow` path for the liquid lfrom said first chamber to said second chamber, l
` (b) said first chamber having a liquid inletand said second ychamber having a liquid outlet,
(c) means connected to said inlet for transmitting a stream of liquid to said first chamber,
(d) suction means connected to said outlet for causing ow of the liquid through saidconstricted iiow'rpath to said outlet, v i i f (e) meansfor measuring thefelectrical conductivity v of said fiow path during the fiow of the liquid therethrough as ameasurement of the number of particles in said liquid, 'and f ,i
(f)"meansv in communication with saidviirst chamber for varying the pressure therein and thereby controlling the level of liquid in saidfi'rst chamber.:
5. lParticle counting apparatus for V'continuously determining the number of particles in a liquid having a different electrical conductivity than said particles,'saidrap paratus comprising: l
(a) a cell having first and second chambers separated from each other by a Wall having anaperture ltherein forming'a constricted iiow` path `forfthe liquid v.from
said first chamber Vto said second chamber, (b) said rst chamber having a liquid inlet and 'said second chamber having a liquid outlet,
(c) means connected to said inlet for transmitting a stream of liquid to said first chamber, Y i (d) suction means `connected to said outletfor causing flow of the liquid through said constricted fiow path to said'outlet, i f t Y i f (e) meansr for measuring 'the Velectrical, conductivity of said fiow path during the ow vof the liquid ltherethrough as a measurement of the number of particles in said liquid, and A (f) means in communication with said first chamber for varying the pressure therein and thereby controlling the level of liquid in -said first chamber,
(g) saidy liquidlevel controlling means comprising a hollow resiliently compressible Vmember adapted 'to be -compressed and released 'from' compression to vary the pressure in said first chamber,
(h) said first chamber having an opening exposed to the atmosphere for maintaining liquid in said first chamber Yby atmospheric pressure exerted on the liquid at said opening. 4
6. A particle counter cell forl determining the number of particles in a liquid, comprising:
(a) first and second chambers separated from each other by a wall having an aperture therein forming a constricted fioW path for the liquid from said first chamber to said second chamber,
(b) said first chamber having an inlet for the liquid,
(c) said second chamber having an outlet for the ilow of the liquid from said cell ,af-ter passing through said aperture,
(d) an electrode in said rst chamber at one side of said aperture and another electrode in said 'second chamber at the other sideof said aperture for sensing changes in conductivity of the liquid as it and a particle therein iiow through said aperture, and
(e) means in communication with said first chamber for varying'the pressure therein and therebycontrolling the level of liquid insaid first chamber.
7. A particle counter cell for determining lthe number of particles in azliquid comprising:
(a) first and second chambers separated from each other by a wall having an'aperture therein forming a constricted4 ow path for the liquid fromeaid iirst .chamber to said second chamber, .-f
(b) said first'chamber having an inlet furthe liquid and a Wallin the pathV of fiow of the incoming liquid to Ipeventthe latter from falling` directly on the liquid in said chamber,
' (c) said second chamber having. an outletfor the ow of the liquid from said cell yafter passing through said' aperture, and 1 (d) an electrode in said first chamber lat one side of v said aperture and another electrodeinl said second chamber at the other side of said -aperture for sensing changes in conductivity offthe `liquid as it and a particle therein fiow through said aperture.
8. A particle countercell for determining the number of particles in a liquid, comprising:
(a) first and` second chambers separated from each other by 'a wall having anapertureftherein forming s a constricted fiow path for the liquidffrom said first chamber to said second chamber,
(b) said first chamber having an inlet for the liquid, (c) said second chamber having an outlet for the oW ofthe liquid from said cell after passing through said aperture, l j 1 l (d) `an electrode in `said first chamber at one side of said aperture and another electrode in said second chamber at the other side of said aperture for sensing changes in conductivity ofthe liquid as: it and Y a particle therein flow through said aperture, and
(e) means in communication with said rst chamber for varying the pressure therein and thereby controlling the level of liquid in said first chamber,
(f) said liquid llevel controlling means comprising a n hollow resiliently compressible member adapted to be compressed and released fromA compression to vary the pressure in said first chamber.
I 9. A particle counter cell for determining the number of particles in a liquid, comprising:
(a) first and second 'chambers separated from each other by a`r wallhaving an aperture therein forming a constricted ow path for the liquid from said first chamber to said second chamber,
(c) said second chamber having an outlet for the flow of the liquid from said cell after passing through said aperture,
(d) an electrode in said first chamber at one side of said aperture and another electrode in said second chamber at the other side of said aperture for sensing changes in conductivity of the liquid as it and a particle therein fiow through said aperture, and
(e) means in communication with saidfirst chamber for varying the pressure therein and thereby controlling the level of liquid in said first chamber,
(f) said liquid level vcontrollingmeans comprising a -hollow resiliently compressible member adapted to be compressed and released from compression to vary the pressure in said first chamber,
(g) said riirst chamberfhaving an opening exposed to the atmosphere for maintaining liquid in said first chamber by atmospheric pressure exerted on the liquid at said opening.
l0. A particle counter cell for determining the number of particles in a liquid, comprising: n
(a) first and second chambers separated from each other by a wallhaving an aperture therein forming a constricted flow path for the liquid from said first chamber to said second chamber,
(c) said second chamber having an outletfor the dow of the liquid from said cell after passing through said aperture,
(d) means for measuring the electrical conductivity of said fiow path during the flow ofthe'liquid'th'erethrough as a measurement of the number of particles in said liquid, said measuring means comprising:
(e) a layer of electrically conducting material onthe inner surface of said first chamber,
(f) an electrode positioned in said rst chamber in contact with said surface,
(g) another electrode positioned in said second chamber, and means in communication with said first chamber for varying the pressure therein and thereby controlling the level of liquid in said rst chamber.
1l. A method of continuously determining the number of particles in a liquid having a different electrical conductivity than said particle, said method comprising:
(a) providing a particle counter cell having a first chamber provided with an outlet opening and a.
second chamber separated from said first chamber by a Wall having an aperture therein forming a constricted flow path for the liquid from said first chamber to said second chamber,
(b) transmitting liquid to said first chamber at oneV fiow rate to provide liquid therein at a level which is above said aperture so that liquid flows into said second chamber through said aperture, and transmitting liquid from said second chamber at a rate of ow which is less than said one ow rate, whereby Y the excess liquid due to said difference in flow rates iiows from said first chamber through said outlet opening,
(c) varying the pressure on the liquid in said iirst chamber during the ow of the liquids to raise the level of the liquid in said first chamber to a position above said first mentioned level, and thereafter (d) electrically measuring the changes in conductivity in said constricted flow path.
l2. A method of continuously determining the number of particles in a liquid having a different electrical conductivity than said particles, said method comprising:
(a) providing a particle counter cell having a first chamber provided with an outlet opening exposed to atmosphere and a second chamber separated from said first chamber by a Wall having an aperture therein forming a constricted iiow path for the liquid from said first chamber to said second chamber,
(b) transmitting liquid to said first chamber at one flow rate to provide liquid therein at a level which is above said aperture so that liquid ows into said second chamber through said aperture, and transmitting liquid from said second chamber at a rate of ow which is less than said one iiow rate, whereby the excess liquid due to said difference in ow'rates flows from said first chamber through said outlet opening,
chamber during the iiow of the liquids to a Value below atmospheric pressureV so that atmospheric pressure on said liquid in said iirst chamber at said outlet opening prevents flow of the excess liquid from 5 said first chamber and the level of liquid therein rises to a position above said first mentioned level, and thereafter (d) electrically measuring the changes in conductivity in said constricted fioW path.
13. A method of continuously determining the number of particles in a liquid having a difierent yelectrical conductivity than said particles, said method comprising:
(a) providing a particle counter cell having a first chamber provided with an outlet opening exposed to atmosphere and a second chamber separated from said first chamber by a wall having an aperture therein forming a constricted ow path for the liquid from said first chamber to said second chamber, said first chamber having a compressible member connected thereto in fiuid flow communication therewith, i
(b) transmitting liquid to said first chamber at one flow rate to provide liquid therein at a level which is above said aperture so that liquid flows into said second chamber through said aperture, and transmitting liquid from said Vsecond chamber at a rate of iiow which is less than said one flow rate, whereby the excess liquid due to said difference in iiow rates flows from said rst chamber through said outlet opening,
(c) compressing said member while liquid is flowing into said first chamber and thereafter gradually releasing said compressed member to reduce the pressure on the liquid in said firstl chamber to a value below atmospheric pressure so that atmospheric pressure on said liquid in said first chamber at said outlet opening prevents flow of the excess liquid from said first chamber and the level of liquid therein rises to a position above said first mentioned level, and thereafter (d) electrically measuring the changes in conductivity in said constricted flow path.
References Cited bythe Examiner UNITED STATES PATENTS 10/53 Coulter 324-,71 l/ 5 9 Coulter et al. 324-71 (c) reducing the pressure on the liquid in said first
1. PARTICLE COUNTING APPARATUS FOR CONTINUOUSLY DETERMINATING THE NUMBER OF PARTICLES IN A LIQUID HAVING A DIFFERENT ELECTRICAL CONDUCTIVITY THAN SAID PARTICLES, SAID APPARATUS COMPRISING: (A) A CELL HAVING FIRST AND SECOND CHAMBERS SEPARATED FROM EACH OTHER BY A WALL HAVING AN APERTURE THEREIN FORMING A CONSTRICTED FLOW PATH FOR THE LIQUID FROM SAID FIRST CHAMBER TO SAID SECOND CHAMBER, (B) SAID FIRST CHAMBER HAVING A LIQUID INLET AND SAID SECOND CHAMBER HAVING A LIQUID OUTLET, (C) MEANS CONNECTED TO SAID INLET FOR TRANSMITTING A STREAM OF LIQUID TO SAID FIRST CHAMBER,
US175172A 1961-05-15 1962-02-23 Continuously operable apparatus and method for counting particles in successive portions of a flowing fluid stream Expired - Lifetime US3165693A (en)
US116907A US3165692A (en) 1961-05-15 1961-05-15 Continuously operable apparatus and method for counting particles in successive portions of a flowing fluid stream
US175172A US3165693A (en) 1961-05-15 1962-02-23 Continuously operable apparatus and method for counting particles in successive portions of a flowing fluid stream
GB1713762A GB986978A (en) 1961-05-15 1962-05-04 Particle counter
CH571462A CH415114A (en) 1961-05-15 1962-05-11 Method and apparatus for continuously counting electrical means of liquid particles suspended in a
FR897385A FR1325237A (en) 1961-05-15 1962-05-12 Particle Counter
DET22107A DE1214905B (en) 1961-05-15 1962-05-12 Electric counting apparatus suspended in a liquid particles
BE617692A BE617692A (en) 1961-05-15 1962-05-15 Particle Counter
US3165693A true US3165693A (en) 1965-01-12
ID=26814745
US116907A Expired - Lifetime US3165692A (en) 1961-05-15 1961-05-15 Continuously operable apparatus and method for counting particles in successive portions of a flowing fluid stream
US175172A Expired - Lifetime US3165693A (en) 1961-05-15 1962-02-23 Continuously operable apparatus and method for counting particles in successive portions of a flowing fluid stream
US (2) US3165692A (en)
BE (1) BE617692A (en)
CH (1) CH415114A (en)
DE (1) DE1214905B (en)
GB (1) GB986978A (en)
US3340470A (en) * 1964-09-23 1967-09-05 Coulter Electronics Flow-through sample apparatus for use with electrical particle study device
US3529239A (en) * 1968-09-27 1970-09-15 Coulter Electronics Electrode arrangement for a particle measuring apparatus
US3539919A (en) * 1968-04-25 1970-11-10 Coulter Electronics Method for making glass aperture tube and product produced thereby
DE1912056C3 (en) * 1968-04-05 1973-07-05 Contraves Ag Device for counting and / or analyzing particles suspended in a liquid
CH481431A (en) * 1968-04-05 1969-11-15 Contraves Ag particle
US2181866A (en) * 1937-05-26 1939-12-05 B D Eisendrath Tanning Co Hydrogen ion meter
US2325695A (en) * 1941-08-22 1943-08-03 Universal Oil Prod Co Fluid meter
1961-05-15 US US116907A patent/US3165692A/en not_active Expired - Lifetime
1962-02-23 US US175172A patent/US3165693A/en not_active Expired - Lifetime
1962-05-04 GB GB1713762A patent/GB986978A/en not_active Expired
1962-05-11 CH CH571462A patent/CH415114A/en unknown
1962-05-12 DE DET22107A patent/DE1214905B/en active Pending
1962-05-15 BE BE617692A patent/BE617692A/en unknown
BE617692A1 (en)
DE1214905B (en) 1966-04-21
BE617692A (en) 1962-11-16
CH415114A (en) 1966-06-15
US3165692A (en) 1965-01-12
GB986978A (en) 1965-03-24
Licht et al. 1950 Mechanism of solute transfer in spray towers
Taylor et al. 1968 The coalescence of disturbance waves in annular two phase flow
US20020020215A1 (en) 2002-02-21 Apparatus and method to obtain representative samples of oil well production
US4231324A (en) 1980-11-04 Milk quantity meter
SE7610110L (en) 1978-03-14 Sample ensured Ning to automated analyzers