US3822968A - Pulsating fluid pumping system - Google Patents
Pulsating fluid pumping system Download PDFInfo
- Publication number
- US3822968A US3822968A US00233457A US23345772A US3822968A US 3822968 A US3822968 A US 3822968A US 00233457 A US00233457 A US 00233457A US 23345772 A US23345772 A US 23345772A US 3822968 A US3822968 A US 3822968A
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- US
- United States
- Prior art keywords
- aerator
- fluid
- liquid
- pumped
- gas
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
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- 238000005086 pumping Methods 0.000 title claims abstract description 20
- 239000012530 fluid Substances 0.000 title abstract description 53
- 238000005276 aerator Methods 0.000 claims description 22
- 239000007788 liquid Substances 0.000 claims description 20
- 238000006073 displacement reaction Methods 0.000 claims description 6
- 229920006395 saturated elastomer Polymers 0.000 claims description 2
- 239000007789 gas Substances 0.000 description 12
- 235000015097 nutrients Nutrition 0.000 description 12
- 230000000694 effects Effects 0.000 description 9
- 238000009434 installation Methods 0.000 description 9
- 238000005187 foaming Methods 0.000 description 6
- 230000015572 biosynthetic process Effects 0.000 description 4
- 239000002184 metal Substances 0.000 description 3
- 229910052751 metal Inorganic materials 0.000 description 3
- 230000036461 convulsion Effects 0.000 description 2
- 230000007717 exclusion Effects 0.000 description 2
- 239000013060 biological fluid Substances 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 239000006260 foam Substances 0.000 description 1
- 230000008014 freezing Effects 0.000 description 1
- 238000007710 freezing Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000155 melt Substances 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 239000003643 water by type Substances 0.000 description 1
Images
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
- F04B—POSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS
- F04B43/00—Machines, pumps, or pumping installations having flexible working members
- F04B43/08—Machines, pumps, or pumping installations having flexible working members having tubular flexible members
- F04B43/10—Pumps having fluid drive
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
- C12M29/00—Means for introduction, extraction or recirculation of materials, e.g. pumps
- C12M29/12—Pulsatile flow
Definitions
- the present invention relates to pumping systems, and more specifically to pulsatory pumping systems for fluids, mainly for biological nutrient media in installations to maintain life activity of biological cells and tissues.
- a positivedisplacement trickling pump consisting of two vessels located at different levels, one of the vessels, the upper one, supplying the fluid through a dropper, and the other, the lower one, receiving the pumped fluid.
- pumping systems with such pumps have large overall dimensions determined by the mutual disposition of the chamber with the biological tissues or cells, and the supplying and the receiving vessels.
- the positive-displacement jerk pump consists of two coaxially disposed tubular cham' bers, the lower end of the inner tubular chamber communicating with the outer chamber, and the upper end of this same chamber extending beyond the outer chamber and being connected with the consumer of the pumped fluid, while the outer tubular chamber has at its bottom inlet holes and at its top communicates with a pulsatory source of compressed air.
- Such a pump must be submerged to a considerable depth into the J fluid metal to be pumped.
- metal is pressurized into the inner chamber wherefrom under a pressure pulseit flows to the consumer.
- One more disadvantage is the slow rate of fluid suction into the outer chamber, as the intensity of suction is only defined by the depth of the pump submersion into the fluid. Increased depth of pump submersion involves enlarged overall dimensions of the pump and of the installation as a whole, and besides, causes formation of stagnant pockets within the fluid volume. The latter circumstance results in the melt freezing. Formation of stagnant zones is always undesirable, especially 'in installations for maintaining life activity of biological tissues.
- An object of the invention is to rule out foaming of the medium in the zone of suction.
- Another object is to raise the efficiency of the system.
- Further objects of the invention are to improve the suction intensity of the pump and to exclude formation of stagnation pockets in the fluid being pumped.
- part of the pump housing with the fluid ejection hole is submerged into the fluid being pumped so that through this hole the inner space of the pump chamber permanently communicates with the fluid to be pumped.
- the housing of the positivedisplacement pump consists of a chamber having elastic walls enclosed with a clearance in a chamber having rigid walls, wherein said clearance should communicate with a pulsatory pressure source.
- Such a pumping system provides for intense ejection of the portion of fluid (which is determined by the pump displacement) and similarly intense suction of a new portion with a minor stirring effect on the fluid in the zone of suction-compression.
- Exclusion of foaming is due to the'high rate of passage of the fluid portion through the layer of fluid medium, and intense suction is secured by the vacuum built up in the working chamber of the pump.
- FIGURE is a schematic view of the pumping arrangement in accordance with the present invention.
- the installation comprises an auxiliary chamber 1 wherein placed are the biological tissue or cells 2, this chamber communicating through a piping 3 with a storage vessel 4 of the biological nutrient fluid.
- Vessel 4 communicates with an aerator 5 which in turn communicates with chamber 1.
- Pipes 6 and 7 serve, respectively, for delivering and I removing a gas medium required to aerate the nutrient fluid.
- the nutrient medium is circulated by means of a positive-displacement pump 8.
- the latter consists of two chambers located with a clearance one inside the other: an outer chamber 9 and an inner working chamber 10 with elastic walls 11. Chamber 10 in its upper part terminates in a narrowing pipe 12 having rigid walls.
- a hole 13 for the fluid ejection is provided at the end of pipe 12 so that hole 13 of pipe 12 is below the level of the nutrient fluid 14.
- the space of the clearance between the outer chamber 9 and the inner chamber 10 communicates by means of an air pipeline 15 with a pulsatory pressure source, Le. a pneumatic generator 16.
- the installation operates as follows.
- the pulse feeding and stopping cycles are continuously repeated so as to attain a pulsatory supply of the portions of fluid 14 into chamber 1, thus simulating natural life conditions of the biological tissue.
- a pulsatory system for pumping liquids comprising: a positive-displacement pump having two chambers divided by an elastic resilient wall, one of said chambers having an opening for the intake and ejection of liquid, the other one of said chambers communicating with a pulsatory pressure source, said opening for the intake and ejection of liquid being submerged into the liquid to be pumped and allowing a predetermined layer of the liquid to be pumped between said opening and a gas medium said liquid to be pumped is located in a storage vessel; an aerator filled with gas and located over said opening so that each batch of liquid to be pumped and ejected due to a pressure pulse on said elastic wall from said opening through said layer of the liquid being pumped, moves onto the walls of said aerator, spills out over said walls of said aerator while saturated with gas, and spills down outside from said aerator gas supply means for supplying said gas to said aerator; gas removal means for removing gas from said aerator; an auxiliary chamber communicating with said
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- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Health & Medical Sciences (AREA)
- Organic Chemistry (AREA)
- Life Sciences & Earth Sciences (AREA)
- Wood Science & Technology (AREA)
- General Engineering & Computer Science (AREA)
- Bioinformatics & Cheminformatics (AREA)
- Zoology (AREA)
- Biomedical Technology (AREA)
- Biotechnology (AREA)
- Microbiology (AREA)
- Mechanical Engineering (AREA)
- Biochemistry (AREA)
- General Health & Medical Sciences (AREA)
- Genetics & Genomics (AREA)
- Sustainable Development (AREA)
- Jet Pumps And Other Pumps (AREA)
Abstract
The pumping system can be utilized wherever pulsatory fluid pumping is expedient or possible. The system is distinguished by the fact that the positivedisplacement pump employed therein is submerged into the fluid being pumped so, that the hole for fluid ejection is located below the level of this fluid, and the inner space of the pump working chamber permanently communicates with the fluid to be pumped.
Description
United States Patent 1191 Makarov et al. 1 Jul 9 1974 ['5 PULSATING FLUID PUMPING SYSTEM 2,496,711 2/1950 Goddard 417/394 X 2,854,003 9/1958 K'rsch 128/233 [76] Inventors it A f?{,, zg j 3,550,162 12/1970 Hi1ffman at al.. 417/394 x i roralon 3,689,204 9/1972 Prisk 4I7/479X Grigorievich Maximov, mikroraion i hi i i fig g i ,xi gj 'g s Primary ExaminerWilliam L. Freeh 24 an of Puschino M Osk ovsk i Assistant Examiner-Richard E. Gluck Oblasti U SS R Attorney, Agent, or FirmEric H. Waters [22] Filed: Mar. 10, 1972 [57] S RACT [211 App]. N0.: 233,457 i H v The pumpmg system can be utllized wherever pulsa- I tory fluid pumping is expedient or possible. {2?} i258! :3':' '.'"::'::::'"i'narasyiwnilififi s is dssssssssshss by we fsss shss s [58] Field 128/253 232 pos1t1ve-d1splacement pump employed therein 1s i submerged into the fluid being pumped so, that the 417/479 239/339 hole for fluid ejection is located below the level of this fluid, and the inner space of the pump working [56] References Clted chamber permanently communicates w1th the flu1d to UNITED STATES PATENTS be pumped 5I5,898 3/l894 Brainard 23 /23 X 1,736,643 11/1927 Beck 417/92 X 1 Claim, 1 Drawing Figure PULSATING PRESSURE SOURCE.
PATENTEUJUL w 3,822,968
PULSATING PRESSURE SOURCE.
l PULSATING FLUID PUMPING SYSTEM The advantage of this pumping system consists in that it has a simple design and small size, requires a small amount of costly biological fluid compared with existing apparatus of this kind, and prevents the appearance of stagnation zones in the fluid being pumped and the foaming of the fluid as a result of energetic ejection. The latter is an advantage in itself. Exclusion of foaming widens the field of application of these systems. Such systems are to be mainly employed in biological laboratory units where foaming and formation of stagnation zones are not allowable.
The present invention relates to pumping systems, and more specifically to pulsatory pumping systems for fluids, mainly for biological nutrient media in installations to maintain life activity of biological cells and tissues.
Widely known are laboratory pumping units for maintaining life activity of biological tissues and cells. In these units fluid is circulated by a positivedisplacement trickling pump consisting of two vessels located at different levels, one of the vessels, the upper one, supplying the fluid through a dropper, and the other, the lower one, receiving the pumped fluid.
The disadvantage of such pumpingsystems consists in the difficulty to maintain constant pressure in the upper vessel.
To keep pressure at the required level additional devices are used which provide for permanent replenishment of fluid, or regulate pressure in the upper vessel according to a prescribed law. This significantly complicates the unit in production and operation.
Besides that, pumping systems with such pumps have large overall dimensions determined by the mutual disposition of the chamber with the biological tissues or cells, and the supplying and the receiving vessels.
What is more, such a system requires a large amount of extremely hard-to-get nutrient fluid to fill it.-
Since units of this type feature certain operating cycles connected with the need to empty the upper vessel, such units require a separate pump for returning the fluid from the lower vessel to the upper one, which further raises the complexity and cost of the unit.
Also known are systems for jerk pumping of molten metals. In these systems the positive-displacement jerk pump consists of two coaxially disposed tubular cham' bers, the lower end of the inner tubular chamber communicating with the outer chamber, and the upper end of this same chamber extending beyond the outer chamber and being connected with the consumer of the pumped fluid, while the outer tubular chamber has at its bottom inlet holes and at its top communicates with a pulsatory source of compressed air. Such a pump must be submerged to a considerable depth into the J fluid metal to be pumped. As pressure is fed to the outer chamber, metal is pressurized into the inner chamber wherefrom under a pressure pulseit flows to the consumer.
(Such systems are known, for example, from a USSR Authors Certificate No. 250,391, cl. 31b2, 39
The disadvantage of these pumping systems consists in that the pumped medium therein is liable to foam in the zone of suction. Therefore these systems cannot be used in installations wherein foaming is completely inadmissible. For example, these pumping systems cannot be utilized in installations for maintaining the life activity of biological tissues.
Another disadvantage of these systems is their low volumetric efficiency, since at each pressurization stroke considerable volumes of the pumped fluid are wastefully thrown out through the suction hole of the pump outer tubular chamber.
One more disadvantage is the slow rate of fluid suction into the outer chamber, as the intensity of suction is only defined by the depth of the pump submersion into the fluid. Increased depth of pump submersion involves enlarged overall dimensions of the pump and of the installation as a whole, and besides, causes formation of stagnant pockets within the fluid volume. The latter circumstance results in the melt freezing. Formation of stagnant zones is always undesirable, especially 'in installations for maintaining life activity of biological tissues.
An object of the invention is to rule out foaming of the medium in the zone of suction.
Another object is to raise the efficiency of the system.
Further objects of the invention are to improve the suction intensity of the pump and to exclude formation of stagnation pockets in the fluid being pumped.
With these objects in view, in a positive-displacement pumping system serving for pulsatory fluid pumping, according to the invention, part of the pump housing with the fluid ejection hole is submerged into the fluid being pumped so that through this hole the inner space of the pump chamber permanently communicates with the fluid to be pumped.
More particularly, the housing of the positivedisplacement pump consists of a chamber having elastic walls enclosed with a clearance in a chamber having rigid walls, wherein said clearance should communicate with a pulsatory pressure source.
Such a pumping system provides for intense ejection of the portion of fluid (which is determined by the pump displacement) and similarly intense suction of a new portion with a minor stirring effect on the fluid in the zone of suction-compression.
Exclusion of foaming is due to the'high rate of passage of the fluid portion through the layer of fluid medium, and intense suction is secured by the vacuum built up in the working chamber of the pump.
Following is a detailed description of the invention in a preferred embodiment thereof, namely as applied to an installation for maintaining life activity of biological cells and tissues, with references to the appended drawing which shows the installation to maintain the life activity of biological tissues and cells according to the invention.
BRIEF DESCRIPTION OF THE DRAWING The FIGURE is a schematic view of the pumping arrangement in accordance with the present invention.
The installation comprises an auxiliary chamber 1 wherein placed are the biological tissue or cells 2, this chamber communicating through a piping 3 with a storage vessel 4 of the biological nutrient fluid.
Vessel 4 communicates with an aerator 5 which in turn communicates with chamber 1.
Pipes 6 and 7 serve, respectively, for delivering and I removing a gas medium required to aerate the nutrient fluid. The nutrient medium is circulated by means of a positive-displacement pump 8. The latter consists of two chambers located with a clearance one inside the other: an outer chamber 9 and an inner working chamber 10 with elastic walls 11. Chamber 10 in its upper part terminates in a narrowing pipe 12 having rigid walls.
Provided at the end of pipe 12 is a hole 13 for the fluid ejection. The pump is mounted in vessel 4 so that hole 13 of pipe 12 is below the level of the nutrient fluid 14.
Through hole 13 the inner space of the working chamber 10 permanently communicates with the nutrient fluid 14 to be pumped.
The space of the clearance between the outer chamber 9 and the inner chamber 10 communicates by means of an air pipeline 15 with a pulsatory pressure source, Le. a pneumatic generator 16.
The installation operates as follows.
As an air pulse is fed from the pulsating pressure source 16 through the air pipeline 15 to the clearance between chambers 9 and 10, the elastic walls 11 of chamber 10 are strained.
This causes ejection of a portion of fluid from chamber 10 through hole 13 of pipe 12, this portion of fluid is then thrown onto the wall of aerator 5, wherein circulating gas serves to aerate the nutrient fluid. Circulation of gas is achieved due to delivery of the gas along pipe 6 and its removal through pipe 7. This portion of fluid spills down the wall of aerator 5 into chamber 1 wherein the biological tissue or cells are located.
After the air pulse is stopped the resilient walls 11 of chamber 10 under the effect of elastic forces return to their initial position, fluid 14 being intensely sucked from vessel 4 into chamber 10.
The pulse feeding and stopping cycles are continuously repeated so as to attain a pulsatory supply of the portions of fluid 14 into chamber 1, thus simulating natural life conditions of the biological tissue.
As the nutrient fluid l4 accumulates in chamber 1, the levels of fluid in vessel 4 and chamber 1 are equalized, so that a current of the nutrient fluid through chamber 1 is realized, and hence, an exchange occurs of this fluid around the biological tissue (cells) 2.
Owing to the fact that the nutrient fluid 14 passes through aerator 5 in small portions and spills down its walls, maximum saturation is achieved of the nutrient fluid with the gases required for the life activity of the biological tissues located in chamber 1.
What we claim is:
1. A pulsatory system for pumping liquids comprising: a positive-displacement pump having two chambers divided by an elastic resilient wall, one of said chambers having an opening for the intake and ejection of liquid, the other one of said chambers communicating with a pulsatory pressure source, said opening for the intake and ejection of liquid being submerged into the liquid to be pumped and allowing a predetermined layer of the liquid to be pumped between said opening and a gas medium said liquid to be pumped is located in a storage vessel; an aerator filled with gas and located over said opening so that each batch of liquid to be pumped and ejected due to a pressure pulse on said elastic wall from said opening through said layer of the liquid being pumped, moves onto the walls of said aerator, spills out over said walls of said aerator while saturated with gas, and spills down outside from said aerator gas supply means for supplying said gas to said aerator; gas removal means for removing gas from said aerator; an auxiliary chamber communicating with said aerator and receiving said batch of liquid from said aerator; and piping connected to said auxiliary chamber and communicating with said storage vessel for circulating liquid from said aerator to said storage vessel through said auxiliary chamber and said piping.
Claims (1)
1. A pulsatory system for pumping liquids comprising: a positive-displacement pump having two chambers divided by an elastic resilient wall, one of said chambers having an opening for the intake and ejection of liquid, the other one of said chambers communicating with a pulsatory pressure source, said opening for the intake and ejection of liquid being submerged into the liquid to be pumped and allowing a predetermined layer of the liquid to be pumped between said opening and a gas medium said liquid to be pumped is located in a storage vessel; an aerator filled with gas and located over said opening so that each batch of liquid to be pumped and ejected due to a pressure pulse on said elastic wall from said opening through said layer of the liquid being pumped, moves onto the walls of said aerator, spills out over said walls of said aerator while saturated with gas, and spills down outside from said aerator gas supply means for supplying said gas to said aerator; gas removal means for removing gas from said aerator; an auxiliary chamber communicating with said aerator and receiving said batch of liquid from said aerator; and piping connected to said auxiliary chamber and communicating with said storage vessel for circulating liquid from said aerator to said storage vessel through said auxiliary chamber and said piping.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US00233457A US3822968A (en) | 1972-03-10 | 1972-03-10 | Pulsating fluid pumping system |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US00233457A US3822968A (en) | 1972-03-10 | 1972-03-10 | Pulsating fluid pumping system |
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US3822968A true US3822968A (en) | 1974-07-09 |
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US00233457A Expired - Lifetime US3822968A (en) | 1972-03-10 | 1972-03-10 | Pulsating fluid pumping system |
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4240409A (en) * | 1979-02-21 | 1980-12-23 | Thermo Electron Corporation | Apparatus for assisting circulation of blood |
WO2013006681A3 (en) * | 2011-07-06 | 2013-04-04 | Joule Unlimited Technologies, Inc. | Bioreactors circulation apparatus, system and method |
-
1972
- 1972-03-10 US US00233457A patent/US3822968A/en not_active Expired - Lifetime
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4240409A (en) * | 1979-02-21 | 1980-12-23 | Thermo Electron Corporation | Apparatus for assisting circulation of blood |
WO2013006681A3 (en) * | 2011-07-06 | 2013-04-04 | Joule Unlimited Technologies, Inc. | Bioreactors circulation apparatus, system and method |
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