CN101270765A - Vacuum system for conveying a high amount of supplemental liquid - Google Patents
Vacuum system for conveying a high amount of supplemental liquid Download PDFInfo
- Publication number
- CN101270765A CN101270765A CNA2007101124406A CN200710112440A CN101270765A CN 101270765 A CN101270765 A CN 101270765A CN A2007101124406 A CNA2007101124406 A CN A2007101124406A CN 200710112440 A CN200710112440 A CN 200710112440A CN 101270765 A CN101270765 A CN 101270765A
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- CN
- China
- Prior art keywords
- pump
- unit
- liquid
- separation machine
- chamber
- 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.)
- Pending
Links
- 239000007788 liquid Substances 0.000 title claims abstract description 42
- 230000000153 supplemental effect Effects 0.000 title description 2
- 239000000203 mixture Substances 0.000 claims abstract description 6
- 238000000926 separation method Methods 0.000 claims description 19
- 230000005484 gravity Effects 0.000 claims description 4
- 239000007789 gas Substances 0.000 description 15
- 230000005540 biological transmission Effects 0.000 description 8
- 238000007789 sealing Methods 0.000 description 7
- 238000000034 method Methods 0.000 description 6
- 238000005086 pumping Methods 0.000 description 6
- 239000012530 fluid Substances 0.000 description 5
- 238000005192 partition Methods 0.000 description 4
- 230000001681 protective effect Effects 0.000 description 4
- 230000002093 peripheral effect Effects 0.000 description 3
- 230000003628 erosive effect Effects 0.000 description 2
- 230000000737 periodic effect Effects 0.000 description 2
- 230000000391 smoking effect Effects 0.000 description 2
- 229910001220 stainless steel Inorganic materials 0.000 description 2
- 229910000906 Bronze Inorganic materials 0.000 description 1
- 229910001060 Gray iron Inorganic materials 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 230000000740 bleeding effect Effects 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- 239000010974 bronze Substances 0.000 description 1
- 238000004891 communication Methods 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- KUNSUQLRTQLHQQ-UHFFFAOYSA-N copper tin Chemical compound [Cu].[Sn] KUNSUQLRTQLHQQ-UHFFFAOYSA-N 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000001419 dependent effect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 238000007667 floating Methods 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- NJPPVKZQTLUDBO-UHFFFAOYSA-N novaluron Chemical compound C1=C(Cl)C(OC(F)(F)C(OC(F)(F)F)F)=CC=C1NC(=O)NC(=O)C1=C(F)C=CC=C1F NJPPVKZQTLUDBO-UHFFFAOYSA-N 0.000 description 1
- 239000010935 stainless steel 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
- F04D—NON-POSITIVE-DISPLACEMENT PUMPS
- F04D31/00—Pumping liquids and elastic fluids at the same time
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
- F04D—NON-POSITIVE-DISPLACEMENT PUMPS
- F04D13/00—Pumping installations or systems
- F04D13/12—Combinations of two or more pumps
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
- F04D—NON-POSITIVE-DISPLACEMENT PUMPS
- F04D25/00—Pumping installations or systems
- F04D25/16—Combinations of two or more pumps ; Producing two or more separate gas flows
- F04D25/163—Combinations of two or more pumps ; Producing two or more separate gas flows driven by a common gearing arrangement
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Structures Of Non-Positive Displacement Pumps (AREA)
- External Artificial Organs (AREA)
- Applications Or Details Of Rotary Compressors (AREA)
Abstract
The invention relates to a pump apparatus for conveying gas-liquid mixture, comprising a first pump (7) for conveying gas having a first pump cavity (28) and a first impeller (33), a second pump (11) for conveying liquid having a second pump cavity (36) and a second impeller (41), and a driving device (2) for driving the pumps (7, 11) having a driving shaft (4) capable of driving rotatably. The driving shaft (4) is connected with two impellers (33, 34).
Description
Technical field
The present invention relates to a kind of vacuum pump-unit when transmitting liquid that is used for.
Background technique
Water-ring pump is widely used in the generation vacuum.This pump transmits gas in mode efficiently.Yet its shortcoming is be restricted aspect the transmission liquid.If exceeding, the ratio of liquor charging body to be passed and the body volume of supplying gas to be passed is about 5% value, gravity phenomenon (gravitational phenomena), noise interference and excessive mechanical tension can take place on the assembly of pump so thereupon, cause blocking, the damage of motor overload or pump.
Use the second independent pump to be used for transmitting liquid and can bring the more space demand, need to consume more energy, and be accompanied by higher operation and installation expense.
Summary of the invention
Therefore, the object of the present invention is to provide a kind of vacuum pump-unit when transmitting liquid that is used for.
Above-mentioned purpose realizes by the described characteristic of claim 1.Key of the present invention is to form vacuum pump and the single-phase combination that is used for the pump of fluid transfer.Pump-unit of the present invention is compact especially, compares with the water-ring pump of sizable transmission liquid, has improved 30% efficient, and described pump-unit is without any need for additional control unit, and prevents that described vacuum pump from transshipping too much owing to transmitting liquid.
Other beneficial effect of the present invention is provided in the dependent claims.Characteristic of the present invention and details provide by describing two mode of executions with reference to the accompanying drawings.
Description of drawings
Fig. 1 is the perspective view according to the pump-unit of a mode of execution;
Fig. 2 is the front view according to the pump-unit of Fig. 1;
Fig. 3 is the side view according to the pump-unit of Fig. 1;
Fig. 4 is the plan view according to the pump-unit of Fig. 1;
Fig. 5 is the longitdinal cross-section diagram according to the pump chamber that passes through pump-unit of Fig. 1;
Fig. 6 is the schematic representation according to sequence of flow in the pump-unit operating process of Fig. 1; And
Fig. 7 is the schematic representation according to sequence of flow in second embodiment's the pump-unit operating process.
Embodiment
With reference to Fig. 1 to Fig. 5 an embodiment of the invention are described below.The structure of described pump-unit at first, is described.Pump-unit 1 comprises the transmission device that is configured to motor 2, and motor 2 has along live axle 4, motor housing 5 and the pedestal 6 of spin axis 3 location.In addition, pump-unit 1 comprises that being used for vacuum first pump, 7, the first pumps 7 has the first suction connected element 8, the first outlet connected element 9 and first pump case 10.First pump 7 is configured to water-ring pump especially.In addition, pump-unit 1 comprises second pump 11 that is used to transmit liquid with the second suction connected element 12, the second outlet connected element 13 and second pump case 14.Second pump 11 is configured as side channel pump (sidechannel pump) and is (self-priming) of self-priming.Yet second pump 11 also can be used as the pump configuration of other any suitable transmission liquid.At last, pump-unit 1 comprises first supply tube 15 with first liquor separation machine 16, has first discharge pipe 17, second supply tube 19 that are used for farther transmission gas of second seperator 18 and is used for second discharge pipe 20 of farther transmission liquid.
The center that first pump chamber 28 departs from live axle 4.Live axle 4 is conducted through first pump chamber 28, and live axle 4 seals with first pump case 10 on the one hand, on the other hand with 29 sealings of first cover plate.First impeller 33 is positioned on the live axle 4 in first pump chamber 28.First impeller 33 is positioned on the live axle 4 in the mode of " suspending (floating) " especially.In the side of first pump case 10 facing to motor 2, live axle 4 is by sealed 34 sealing in path of shell 10, and Sealing 34 is configured to the movable annular Sealing.
The diameter of live axle 4 reduces slightly in the zone of first cover plate 29.
The second suction connected element 12 and the second outlet connected element 13 and pump chamber 36 fluid communication.Partition walls 37 has second connection mouth 42.First connection mouth 32, second connection mouth 42 and connecting tube 43 form through-flow between first pump chamber 28 and second pump chamber, 36 perimeters and are connected 47.Connecting tube 43 is configured to for example cast runner.
The operation of pump-unit 1 will be described with reference to Fig. 6 hereinafter.Although the flow sequence in pump-unit 1 operating process is schematically illustrated in Fig. 6, has still provided respectively with in the pump-unit 1 and respectively constructed the drawing reference numeral that element is associated, so that described order is more readily understood.
By main supply tube 45, gas-liquid mixture is passed through the pumping action suction from process chamber 48.Pressure p
sIn main supply tube 45, take advantage.Liquid by the pumping action suction is owing to the reason of gravity concentrates on the bottom of the first liquor separation machine 16, so gas-liquid mixture to small part is separated into two kinds of components of liquids and gases.The gas that can contain liquid residue then by first pump 7 via first supply tube 15 under pumping action, be pumped into first pump chamber 28 through first connected element 8 of bleeding.The rotation of first impeller 33 that motor 2 drives by live axle 4 forces operating liquid in first pump chamber 28 of first pump 7 under action of centrifugal force, away from running shaft 3, arrives the peripheral border of first pump chamber 28.Thereby the operating liquid of first pump 7 forms liquid ring at the exterior domain of first pump chamber 28.Because first pump chamber 28 is with respect to the exocentric structure of live axle 4, so caused such chamber, promptly, it seals with gastight manner, and fix limit, fix limit by first impeller 33 on the other hand by liquid ring on the one hand, and its volume periodically changes in the process of running shaft 3 rotations at impeller 33.Periodic variation interrelates with the periodic relief of pressure on this volume.Thereby have first outlet 31 in the zone that chamber has minimum volume and has a pressure maximum,, have pressure p by this outlet
D>p
sGas leave from first pump 7.
After first pump 7, before gas further transmitted by gas discharge pipe 46, remaining treatment fluid or the operating liquid in the pump was separated from the gas in gas in the second liquor separation machine 18.The liquid that separates in the second liquor separation machine 18 is introduced second discharge pipe 20 by connected element 26, and further transmits with the liquid from 11 dischargings of second pump.
The liquid that separates in the first liquor separation machine 16 by under the pumping action of second supply tube 19, enters second pump chamber 36 via the second suction connected element 12 by second pump 11.First impeller, the 33 the same driven shafts 4 of second impeller 41 of second pump 11 and first pump 7 drive.Therefore first pump 7 and second pump 11 have common live axle 4.Therefore, be configured as first pump 7 of water-ring pump and be configured to be very compact and to save the space as the combination of second pump 11 of side channel pump.After second pump 11, the liquid that is transmitted is introduced second discharge pipe 20 by the second outlet connected element 13, and transmits by second discharge pipe 20.
In the first liquor separation machine 16, gas-liquid mixture is separated into the gentle body portion of liquid part, prevented, because the moment flow of liquid volume of smoking by the pumping action of water-ring pump exceeds 5% the maximum permissible value of being about in the gas volume that is transmitted by water-ring pump.Guaranteed like this no matter how many amounts of liquor charging body to be passed is, always water-ring pump is not operated there to be cavitation erosion (cavitation-free) mode.This just means the damage of the assembly that can be avoided pump and the overload of motor 2.Simultaneously, pump-unit 1 is compared with water-ring pump sizable, that transmit liquid, and efficient has improved 30%.
In second discharge pipe 20, have the pressure p identical with first discharge pipe 17
DAlthough may be in the second liquor separation machine 18 and pump 7 and 11 on the pressure side on cause disturbing the pressure compensation phenomenon, in principle, in second discharge pipe 20, exist and be different from pressure p in first discharge pipe 17
DPressure be possible.
Liquid from liquid ring in first pump chamber 28 can flow into second pump chamber 36 by connecting 47.This has eliminated the risk of the dry operation of side channel pump.
Because the difference of pressure is very little between two pump chambers 28,36, so do not need axle is carried out complexity and very effective sealing between two pump chambers 28,36.Therefore, narrow clearance seal is just enough.Because the cause of the transmission characteristic of side channel pump does not need special controlling mechanism to operate second pump 11 that transmits liquid, so compare with for example centrifugal pump, the combination of water-ring pump and side channel pump is especially useful.
Another embodiment of described pump-unit 1 describes with reference to figure 7 hereinafter.Different be basic with first embodiment, provide two supply tubes that separate 15,19 to replace being used for smoking the main supply tube 45 of gas-liquid mixture by pumping action, and the first liquor separation machine 16 that separates from the gas that is transmitted of the liquid that is used for being transmitted.First supply tube 15 is mainly used in transmission gas, is configured to guarantee to keep vacuum in treatment chamber 48 as first pump 7 of water-ring pump.Be configured to utilize second supply tube 19 in treatment chamber 48, to transmit liquid as second pump 11 of self-priming pump (especially as side channel pump).Through-flow between first pump 7 and second pump 11 is connected 47 and prevented that side channel pump from having only dry operation under the situation of small amount of liquid, thereby prevented the damage to sealing.
Claims (8)
1. pump-unit is used to transmit gas-liquid mixture, comprising:
A. first pump (7) is used to transmit gas and comprises:
I. first pump chamber (28), and
Ii. first impeller (33),
B. second pump (11) is used to transmit liquid and comprises:
I. second pump chamber (36), and
Ii. second impeller (41), and
C. drive unit comprises the live axle (4) of rotatable driving being used to drive described pump (7,11),
D. described live axle (4) links to each other with two impellers (33,34).
2. pump-unit according to claim 1 is characterized in that, described first pump (7) is configured to water-ring pump.
3. according to the described pump-unit of above-mentioned each claim, it is characterized in that described second pump (11) is a self-priming pump.
4. according to the described pump-unit of above-mentioned each claim, it is characterized in that described second pump (11) is configured to side channel pump.
5. pump-unit according to claim 1 is characterized in that, at least one liquor separation machine (16) is set for and separates the liquid that transmits from the gas that transmits.
6. pump-unit according to claim 5 is characterized in that, at least one liquor separation machine (16) is positioned at the suction side of described pump (7,11).
7. according to claim 5 or 6 described pump-units, it is characterized in that, be provided with the second liquor separation machine (18) at outlet side.
8. according to each described pump-unit in the claim 5 to 7, it is characterized in that at least one liquor separation machine (16,18) is configured to the gravity separation machine.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE102007013872A DE102007013872A1 (en) | 2007-03-20 | 2007-03-20 | Vacuum system for high additional liquid quantities |
DE102007013872.7 | 2007-03-20 |
Publications (1)
Publication Number | Publication Date |
---|---|
CN101270765A true CN101270765A (en) | 2008-09-24 |
Family
ID=39713084
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CNA2007101124406A Pending CN101270765A (en) | 2007-03-20 | 2007-06-26 | Vacuum system for conveying a high amount of supplemental liquid |
Country Status (4)
Country | Link |
---|---|
US (1) | US20080232954A1 (en) |
CN (1) | CN101270765A (en) |
DE (1) | DE102007013872A1 (en) |
IT (1) | ITMI20071529A1 (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103026072A (en) * | 2010-06-17 | 2013-04-03 | 弗里德科股份公司 | Conveying device |
CN104619989A (en) * | 2012-09-03 | 2015-05-13 | 施特林工业咨询公司 | Side-channel pump, and method for operating a side-channel pump |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US8821113B2 (en) * | 2010-12-21 | 2014-09-02 | Hamilton Sundstrand Corporation | Air cycle machine seal land |
DE102015200843A1 (en) * | 2015-01-20 | 2016-07-21 | Speck Pumpen Vakuumtechnik Gmbh | pump unit |
DE102022001696A1 (en) | 2022-05-13 | 2023-11-16 | Truma Gerätetechnik GmbH & Co. KG | Two-stage pump |
Family Cites Families (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3213794A (en) * | 1962-02-02 | 1965-10-26 | Nash Engineering Co | Centrifugal pump with gas separation means |
US3558236A (en) * | 1968-09-10 | 1971-01-26 | Delavan Manufacturing Co | Self-purging regenerative turbine pump |
US4914921A (en) * | 1988-08-16 | 1990-04-10 | Cbi Research Corporation | Refrigeration method and apparatus using aqueous liquid sealed compressor |
US4946349A (en) * | 1989-07-19 | 1990-08-07 | National Space Development Agency Of Japan | Water ring vacuum pump |
WO1995004224A1 (en) * | 1993-08-03 | 1995-02-09 | United Technologies Corporation | Centrifugal fuel pump with starting stage |
NL9401455A (en) * | 1994-09-07 | 1996-04-01 | Andre S J Van Coillie En Johan | Self-priming centrifugal pump-vacuum pump combination for, among other things, liquid fuels such as petrol, gasoil, kerozene, etc. with improved deaerator and integrated evaporation recovery option. |
-
2007
- 2007-03-20 DE DE102007013872A patent/DE102007013872A1/en not_active Withdrawn
- 2007-05-30 US US11/755,157 patent/US20080232954A1/en not_active Abandoned
- 2007-06-26 CN CNA2007101124406A patent/CN101270765A/en active Pending
- 2007-07-27 IT IT001529A patent/ITMI20071529A1/en unknown
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103026072A (en) * | 2010-06-17 | 2013-04-03 | 弗里德科股份公司 | Conveying device |
CN103026072B (en) * | 2010-06-17 | 2016-08-03 | 弗里德科股份公司 | Conveying equipment |
CN106122045A (en) * | 2010-06-17 | 2016-11-16 | 弗里德科股份公司 | Conveying equipment |
CN104619989A (en) * | 2012-09-03 | 2015-05-13 | 施特林工业咨询公司 | Side-channel pump, and method for operating a side-channel pump |
Also Published As
Publication number | Publication date |
---|---|
ITMI20071529A1 (en) | 2008-09-21 |
DE102007013872A1 (en) | 2008-09-25 |
US20080232954A1 (en) | 2008-09-25 |
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Application publication date: 20080924 |