CN2820271Y - Multistage gas/liquid separator - Google Patents
Multistage gas/liquid separator Download PDFInfo
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- CN2820271Y CN2820271Y CN 200520118471 CN200520118471U CN2820271Y CN 2820271 Y CN2820271 Y CN 2820271Y CN 200520118471 CN200520118471 CN 200520118471 CN 200520118471 U CN200520118471 U CN 200520118471U CN 2820271 Y CN2820271 Y CN 2820271Y
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- pipe
- separator
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Abstract
The utility model relates to a multistage gas and liquid separator which comprises a gas inlet pipe, a gas outlet pipe, a separation pipe and a condensation pipe. The utility model is characterized in that the multistage gas and liquid separator also comprises an oblique pipe and a water sealing pipe; the separation pipe has two stages; the lower end of the gas inlet pipe extends into the upper part of a first-stage separation pipe to be mutually communicated; the lower end of the first-stage separation pipe is communicated with one end of the oblique pipe, and the other end of the oblique pipe is communicated with the water sealing pipe; the upper end of the water sealing pipe is provided with a waste gas inlet hole, and the lower end of the water sealing pipe is provided with a water outlet; the upper part of the first-stage separation pipe is communicated with the upper part of a two-stage separation pipe by the condensation pipe; the lower end of the gas outlet pipe extends into the upper part of the two-stage separation pipe to be mutually communicated; the lower end of the two-stage separation pipe is communicated with the water sealing pipe. The utility model has the advantages of simple structure, convenient operation and high separating efficiency, and is suitable for the separation of various gases and liquids.
Description
Technical field
The utility model relates to a kind of instrument that needs gas-liquid separation, has two-stage or the multi-stage gas-liquid separator of separator tube more than three grades in particular to a kind of.
Background technology
At present, common gas-liquid separator mainly is the gas-liquid separator as Fig. 5, Fig. 6 and structure shown in Figure 7 on the market, all there are some shortcomings in they in varying degrees: gas-liquid separator shown in Figure 5 comprises the container 11 that deionized water is housed, shortcoming is: the structure more complicated, when utilizing this gas-liquid separator to carry out gas-liquid separation, gas liquid mixture carries out in the condensation process through the deionized water plane, need adjust inconvenient operation according to different elements with deionized water plane distance d; Gas-liquid separator shown in Figure 6 comprises cooling circulating water device 12, and shortcoming is: the structure more complicated needs to be equipped with the cooling circulating water device; Gas-liquid separator shown in Figure 7 is a primary separator, and separative efficiency is low, and separating effect is not very desirable.
The utility model content
Technical problem to be solved in the utility model be propose a kind of simple in structure, easy to operate, separative efficiency height, effective multi-stage gas-liquid separator.
Technical scheme provided by the utility model is: a kind of multi-stage gas-liquid separator, comprise air inlet pipe, escape pipe, separator tube, inclined tube, water sealing (sealing water) pipe, condenser pipe, described separator tube is provided with two-stage, the lower end of described air inlet pipe is stretched into one-level separator tube top and is interconnected, the lower end of one-level separator tube is connected with an end of inclined tube, and the other end of inclined tube is connected with water sealing (sealing water) pipe, and the water sealing (sealing water) pipe upper end is provided with exhaust apertures, the water sealing (sealing water) pipe lower end is provided with delivery port, the top of one-level separator tube is connected by condenser pipe with the top of secondary separator tube, and the lower end of escape pipe is stretched into secondary separator tube top and is interconnected, and secondary separator tube lower end is connected with water sealing (sealing water) pipe.
In above-mentioned multi-stage gas-liquid separator, in order to increase the liquid path of flowing through, described one-level separator tube is made as spherical structure.
In above-mentioned multi-stage gas-liquid separator, further separate for promoting gas-liquid, the end that described condenser pipe is connected with the one-level separator tube is lower than the other end.
Further improve as the utility model, in above-mentioned separator, the size of sample size and carrier gas flux per sample, described separator tube is provided with multistage, the escape pipe lower end is stretched into afterbody separator tube top and is interconnected, and separator tubes at different levels lower end all is connected with water sealing (sealing water) pipe.
Further improve as the utility model, in above-mentioned separator, described separator tube is provided with three grades, the escape pipe lower end is stretched into three grades of separator tube tops and is interconnected, secondary separator tube upper end is connected with three grades of separator tube upper ends, and secondary separator tube lower end all is connected with water sealing (sealing water) pipe with three grades of separator tube lower ends.
Further, in above-mentioned separator, described air inlet pipe, escape pipe, separator tube, inclined tube, water sealing (sealing water) pipe, condenser pipe is structure as a whole.
Further improve as the utility model, in above-mentioned separator, described air inlet pipe lower end is provided with bent angles that are 90 degree, and gas liquid mixture separates tube wall through the air inlet pipe one-level that clashes, and accelerating not, the solution of complete reaction further reacts.
Further improve as the utility model, in above-mentioned separator, the separator tube tube wall that the part of end, described escape pipe lower end is communicated with it is affixed, and the gas process forms air whirl during this junction, promotes gas-liquid separation.
The utility model has following advantage: the utility model is relatively simple for structure, do not need to be equipped with the cooling circulating water device, easy to operate, the size of sample size and carrier gas flux per sample, separator tube can be made as two-stage or more than three grades, gas-liquid separation efficient height, effective.
Description of drawings
Fig. 1 is the structural representation of the utility model secondary gas-liquid separator.
Fig. 2 is the utility model secondary gas-liquid separator using method schematic diagram.
Fig. 3 is the structural representation of three grades of gas-liquid separators of the utility model.
Fig. 4 is three grades of gas-liquid separator usings method of the utility model schematic diagram.
Fig. 5 is the structural representation of one of prior art gas-liquid separator.
Fig. 6 is two a structural representation of prior art gas-liquid separator.
Fig. 7 is three a structural representation of prior art gas-liquid separator.
Wherein, three grades of separator tube 11-of 1-air inlet pipe 2-one-level separator tube 3-inclined tube 4-water sealing (sealing water) pipe 5-exhaust apertures 6-delivery port 7-secondary separator tube 8-escape pipe 9-condenser pipe 10-deionized water container 12-cooling circulating water device.
The specific embodiment
Below in conjunction with the description of drawings specific embodiment of the present utility model.
Referring to Fig. 1, the utility model secondary gas-liquid separator comprises air inlet pipe 1, escape pipe 8, separator tube, inclined tube 3, water sealing (sealing water) pipe 4, condenser pipe 9.Wherein, separator tube is provided with two-stage, i.e. one-level separator tube 2 and secondary separator tube 7, and in order to increase the liquid path of flowing through, one-level separator tube 2 is made as spherical structure.The lower end of air inlet pipe 1 is stretched into one-level separator tube 2 tops and is interconnected, and air inlet pipe 1 lower end is provided with bent angles that are 90 degree, and gas liquid mixture is through air inlet pipe one-level separator tube 2 walls that clash, and accelerating not, the solution of complete reaction further reacts.The lower end of one-level separator tube 2 is connected with an end of inclined tube 3, the other end of inclined tube 3 is connected with water sealing (sealing water) pipe 4, water sealing (sealing water) pipe 4 upper ends are provided with exhaust apertures 5, water sealing (sealing water) pipe 4 lower ends are provided with delivery port 6, the top of one-level separator tube 2 is connected by condenser pipe 9 with the top of secondary separator tube 7, for promoting gas-liquid further to separate, condenser pipe 9 is set to: an end that is connected with one-level separator tube 2 is lower than the other end.The lower end of escape pipe 8 is stretched into secondary separator tube 7 tops and is interconnected, and secondary separator tube 7 tube walls that the part of end, escape pipe 8 lower end is communicated with it are affixed, and the gas process forms air whirl during this junction, promotes gas-liquid separation.Secondary separator tube 7 lower ends are connected with water sealing (sealing water) pipe 4.Air inlet pipe 1, escape pipe 8, separator tube, inclined tube 3, water sealing (sealing water) pipe 4, condenser pipe 9 is structure as a whole, and whole gas-liquid separator adopts the quartz ampoule of the different size that has shaped to fire and forms.
Referring to Fig. 3, three grades of gas-liquid separators of the utility model, be on the basis of two-stage gas-liquid separator, to design moulding, be with the difference of two-stage gas-liquid separator: separator tube is provided with three grades, escape pipe 8 lower ends are stretched into three grades of separator tube 10 tops and are interconnected, secondary separator tube 7 upper ends are connected with three grades of separator tube 10 upper ends, and an end of condenser pipe 9 is connected with the bottom of secondary separator tube 7, and secondary separator tube 7 lower ends all are connected with water sealing (sealing water) pipe 4 with three grades of separator tube 10 lower ends.
In the utility model multi-stage gas-liquid separator, the size of sample size and carrier gas flux per sample, separator tube can be provided with multistage, and escape pipe 8 lower ends are stretched into afterbody separator tube top and are interconnected, and separator tubes at different levels are arranged side by side, and its lower end all is connected with water sealing (sealing water) pipe 4.
The course of work of the utility model multiple-stage separator is as follows:
Referring to Fig. 2, the mixture that forms gas and liquid through gas generating unit enters the multi-stage gas-liquid separator, mixture is through air inlet pipe 1 one-level separator tube 2 walls that clash, liquid flows down along tube wall, gas rises and carries out the one-level separation, and the solution of complete reaction further reacts because fierce bump is accelerated not simultaneously.Liquid flows down through inclined tube 3 and enters water sealing (sealing water) pipe 4, form water seal, can get rid of the interference of ambient atmos, simultaneously detected gas, inclined tube 3 makes the gas of complete reaction not to discharge from exhaust apertures 5 continuously than minute bubbles, and avoiding forming discharging suddenly than air pocket influences test result.The exhaust system device is arranged above whole instrument, and like this, the waste gas of discharging from exhaust apertures is discharged under the effect of exhaust system smoothly, avoids the laboratory is polluted.The gas that rises enters secondary separator tube 7 through oblique condenser pipe 9, through long condenser pipe 9 condensations, portion of water progress condensation in the gas, in secondary separator tube 7, gas clashes into escape pipe 8 and forms air whirl, carrying out the second time separates, dry gas just can enter gas analyzing apparatus by escape pipe 8 outlets of multi-stage gas-liquid separator, waste liquid enters the waste collection bottle through waste liquid delivery port 6, this is the two-stage gas-liquid separator course of work, it is mainly used in, and the sample feeding amount is smaller, and carrier gas flux is smaller, carries out the instrument of gas-liquid separation easily.
In the time will comparing a large amount of samples and big carrier gas flux, can select three grades of gas-liquid separators for use, referring to Fig. 4, gas does not directly enter gas-detecting device in the secondary separation, further separate but enter three grades of separator tubes 10, the course of work and secondary gas-liquid separator are basic identical, and it has than the better separating effect of two-stage.
Claims (8)
1, a kind of multi-stage gas-liquid separator, comprise air inlet pipe (1), escape pipe (8), separator tube, condenser pipe (9), it is characterized in that: this multi-stage gas-liquid separator also comprises inclined tube (3), water sealing (sealing water) pipe (4), described separator tube is provided with two-stage, the lower end of described air inlet pipe (1) is stretched into one-level separator tube (2) top and is interconnected, the lower end of one-level separator tube (2) is connected with an end of inclined tube (3), and the other end of inclined tube (3) is connected with water sealing (sealing water) pipe (4), and water sealing (sealing water) pipe (4) upper end is provided with exhaust apertures (5), water sealing (sealing water) pipe (4) lower end is provided with delivery port (6), the top of one-level separator tube (2) is connected by condenser pipe (9) with the top of secondary separator tube (7), and the lower end of escape pipe (8) is stretched into secondary separator tube (7) top and is interconnected, and secondary separator tube (7) lower end is connected with water sealing (sealing water) pipe.
2, multi-stage gas-liquid separator as claimed in claim 1 is characterized in that: described one-level separator tube (2) is a spherical structure.
3, multi-stage gas-liquid separator as claimed in claim 1 is characterized in that: described condenser pipe (9) is lower than the other end with the end that one-level separator tube (2) is connected.
4, multi-stage gas-liquid separator as claimed in claim 1 is characterized in that: described separator tube is provided with more than three grades, and escape pipe (8) lower end is stretched into afterbody separator tube top and is interconnected, and separator tubes at different levels lower end all is connected with water sealing (sealing water) pipe (4).
5, multi-stage gas-liquid separator as claimed in claim 1, it is characterized in that: described separator tube is provided with three grades, escape pipe (8) lower end is stretched into three grades of separator tube (10) tops and is interconnected, secondary separator tube (7) upper end is connected with three grades of separator tubes (10) upper end, and secondary separator tube (7) lower end all is connected with water sealing (sealing water) pipe (4) with three grades of separator tubes (10) lower end.
6, as each described multi-stage gas-liquid separator of claim 1 to 5, it is characterized in that: described air inlet pipe (1), escape pipe (8), separator tube, inclined tube (3), water sealing (sealing water) pipe (4), condenser pipe (9) is structure as a whole.
7, as each described multi-stage gas-liquid separator of claim 1 to 5, it is characterized in that: described air inlet pipe (1) lower end is provided with one and is 90 bent angles of spending.
8, as each described multi-stage gas-liquid separator of claim 1 to 5, it is characterized in that: the separator tube tube wall that the part of described escape pipe (8) end, lower end is communicated with it is affixed.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200520118471 CN2820271Y (en) | 2005-09-09 | 2005-09-09 | Multistage gas/liquid separator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200520118471 CN2820271Y (en) | 2005-09-09 | 2005-09-09 | Multistage gas/liquid separator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2820271Y true CN2820271Y (en) | 2006-09-27 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 200520118471 Expired - Lifetime CN2820271Y (en) | 2005-09-09 | 2005-09-09 | Multistage gas/liquid separator |
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| CN (1) | CN2820271Y (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103055789A (en) * | 2012-12-26 | 2013-04-24 | 淮安万邦香料工业有限公司 | Reaction vessel negative pressure distilled water separating apparatus |
| CN106110770A (en) * | 2016-08-18 | 2016-11-16 | 江苏德林环保技术有限公司 | A kind of integral type gas-liquid separator |
| CN111013331A (en) * | 2019-11-19 | 2020-04-17 | 鲁西化工集团股份有限公司煤化工二分公司 | Vapor-liquid separation system and process for low-temperature methanol washing of gas inlet medium and application |
-
2005
- 2005-09-09 CN CN 200520118471 patent/CN2820271Y/en not_active Expired - Lifetime
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103055789A (en) * | 2012-12-26 | 2013-04-24 | 淮安万邦香料工业有限公司 | Reaction vessel negative pressure distilled water separating apparatus |
| CN106110770A (en) * | 2016-08-18 | 2016-11-16 | 江苏德林环保技术有限公司 | A kind of integral type gas-liquid separator |
| CN106110770B (en) * | 2016-08-18 | 2018-06-26 | 江苏德林环保技术有限公司 | A kind of integral type gas-liquid separator |
| CN111013331A (en) * | 2019-11-19 | 2020-04-17 | 鲁西化工集团股份有限公司煤化工二分公司 | Vapor-liquid separation system and process for low-temperature methanol washing of gas inlet medium and application |
| CN111013331B (en) * | 2019-11-19 | 2022-03-04 | 鲁西化工集团股份有限公司煤化工二分公司 | Vapor-liquid separation system and process for low-temperature methanol washing of gas inlet medium and application |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CX01 | Expiry of patent term |
Expiration termination date: 20150909 Granted publication date: 20060927 |
|
| EXPY | Termination of patent right or utility model |