CN203220843U - Separating device for separating gas insoluble in water from water vapor - Google Patents
Separating device for separating gas insoluble in water from water vapor Download PDFInfo
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- CN203220843U CN203220843U CN 201320199072 CN201320199072U CN203220843U CN 203220843 U CN203220843 U CN 203220843U CN 201320199072 CN201320199072 CN 201320199072 CN 201320199072 U CN201320199072 U CN 201320199072U CN 203220843 U CN203220843 U CN 203220843U
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Abstract
The utility model relates to a separating device for separating gas insoluble in water from water vapor. The separating unit comprises a separation barrel with an air inlet, an air outlet and a liquid outlet, a condensing device and a liquid collecting device, particularly, a first gas collecting device communicated with the air outlet of the separation barrel and a second gas collecting device communicated with the side wall of the liquid collecting device, wherein the first gas collecting device comprises a first air collecting pipe one end part of which is communicated with the air outlet of the separation barrel and a first gas collector communicated with the other end part of the first air collecting pipe; the second gas collecting device comprises a second air collecting pipe one end part of which is communicated with the side wall of the liquid collecting device and a second gas collector communicated with the other end part of the second air collecting pipe. The separating device provided by the utility model has the advantages of separating gases different in density from water vapor, and being high in reliability.
Description
Technical field
The utility model relates to a kind of separator, is specifically related to a kind of separator that water-fast gas is separated with water vapour.
Background technology
In chemical field, water-fast gas separated with water vapour right and wrong usually see, for example, the Chinese patent publication number is CN201618437U, it discloses a kind of cellar for storing things formula moisture trap, side at water tank is equipped with cold water storage cistern, and how installation is to the condenser pipe that is arranged in parallel in it, and the condenser pipe below is provided with water tank, cold water storage cistern is provided with air inlet and gas outlet, high-temperature gas is in air inlet enters cold water storage cistern, through the cooling of condenser pipe, behind the water vapour condensation by contact pipe, form the liquid pearl, splash in the ponding casing, water-fast gas is discharged from the gas outlet, thereby realizes gas-water separation.Yet, above-mentioned moisture trap is for the bigger gas of density, as argon gas (Ar), then under the gravity effect, mobile towards the cold water storage cistern bottom, and the gas outlet generally all is the top at cold water storage cistern, therefore, the bigger gas of corresponding density, then can't discharge from the gas outlet, not only cause the waste of resource, and can't reach effect and the purpose of separation.
Summary of the invention
Technical problem to be solved in the utility model is to overcome the deficiencies in the prior art, and a kind of improved separator for separating of water-fast gas and water vapour is provided.
For solving the problems of the technologies described above, the utility model is taked following technical scheme:
A kind of separator for separating of water-fast gas and water vapour, it comprises having air inlet, the cylinder of gas outlet and leakage fluid dram, be arranged on the condensing unit in the cylinder, be arranged on the fluid collection device of leakage fluid dram below, particularly, separator also comprises first gas collector that is connected with the gas outlet of cylinder and second gas collector that is connected with the sidewall of fluid collection device, wherein first gas collector comprises first discharge that an end is connected with the gas outlet of cylinder and first gas collector that is connected with first discharge the other end, and first gas collector is used for the less gas of collection density; Second gas collector comprises second discharge that an end is connected with the sidewall of fluid collection device and second gas collector that is connected with second discharge the other end, and second gas collector is used for the bigger gas of collection density.
Preferably, fluid collection device is funnel-form, the collecting tank that it comprises the frustum that the cross section diminishes gradually from top to bottom and bickers and be arranged on the below of bickering, and second discharge is connected with the conical surface of frustum.
Further, preferably, the end face that second discharge is communicated with the frustum conical surface is outward-dipping from top to bottom.Wherein the cone-apex angle of frustum be 90 ° for most preferably.More be conducive to collection and the discharging of liquid.
Implement and preferred aspect according to one of the utility model is concrete, also be provided with on the frustum and be positioned at the baffle plate that its part that is positioned at frustum is blocked in second discharge top.Prevent that effectively the liquid pearl from flowing to second gas collector from second discharge.
According to another concrete enforcement and preferred aspect of the utility model, condensing unit comprises U-shaped heat exchanger tube and the supply system of condensed water is provided that wherein the two ends of U-shaped heat exchanger tube are connected with outlet pipe with the water inlet pipe of supply system respectively.
Preferably, U-shaped heat exchanger tube is resistant to elevated temperatures stainless steel, and it high temperature corrosion can not take place under water vapor, so can not bring the problems such as obstruction of extra pollution and condensate line to collection gas.
Preferably, the gas outlet is arranged on the top of cylinder, and air inlet is arranged on the bottom side of cylinder; Leakage fluid dram is arranged on the bottom of cylinder and is connected with fluid collection device.
In addition, the less gas of density is hydrogen, helium or carbon monoxide.The gas that density is bigger is argon gas.
Because the enforcement of above technical scheme, the utility model compared with prior art has following advantage:
The utility model with the gas outlet of cylinder be connected with first gas collector, the sidewall of fluid collection device is connected with second gas collector, by condensing unit water vapour is liquefied again, water-fast density is less and collected by first gas collector and second gas collector respectively than atmospheric, liquid integument fluid collection device after the liquefaction is collected, therefore, can be used for separating of different densities gas and water vapour, and have higher reliability.
Description of drawings
The utility model is described in more detail below in conjunction with accompanying drawing and specific embodiment.
Fig. 1 looks schematic diagram for the master according to separator of the present utility model;
Wherein: 1, cylinder; 10, air inlet; 11, gas outlet; 12, leakage fluid dram; 2, condensing unit; 20, U-shaped heat exchanger tube; 3, fluid collection device; 30, frustum; 31, bicker; 32, baffle plate; 33, collecting tank; 4, first gas collector; 40, first discharge; 41, first gas collector; 5, second gas collector; 50, second discharge; 51, second gas collector; 6, water inlet pipe; 7, outlet pipe.
The specific embodiment
As shown in Figure 1, for separating of the separator of water-fast gas and water vapour, it comprise have air inlet 10, the cylinder 1 of gas outlet 11 and leakage fluid dram 12; Be arranged on the condensing unit 2 in the cylinder 1; Be arranged on the fluid collection device 3 of leakage fluid dram below; First gas collector 4 that is connected with the gas outlet 11 of cylinder 1; Second gas collector 5 that is connected with the sidewall of fluid collection device 3.
Above-mentioned gas outlet 11 is arranged on the top of cylinder 1, and air inlet 10 is arranged on the bottom side of cylinder 1; Leakage fluid dram 12 is arranged on the bottom of cylinder 1 and is connected with fluid collection device 3.Condensing unit 2 comprises U-shaped heat exchanger tube 20 and the supply system of condensed water is provided that wherein the two ends of U-shaped heat exchanger tube 20 are connected with outlet pipe 7 with the water inlet pipe 6 of supply system respectively.Fluid collection device 3 is funnel-form, specifically comprises the frustum 30 that the cross section diminishes gradually from top to bottom and bickers 31 and the collecting tank 33 that is arranged on 31 belows of bickering.First gas collector 4 comprises first discharge 40 that an end is connected with the gas outlet 11 of cylinder 1 and first gas collector, 41, the first gas collectors 4 that are connected with first discharge, 40 the other end are used for the less gas of collection density.Second gas collector 5 comprises second discharge 50 that an end is connected with the sidewall (frustum 30) of fluid collection device 3 and second gas collector, 51, the second gas collectors 5 that are connected with second discharge, 50 the other end are used for the bigger gas of collection density.
In this example, in order to reach optimal separating efficiency, it is capable that cylinder 1 is cylinder, and the cone-apex angle of frustum 30 is 90 °, is convenient to the discharging of liquid.Meanwhile, also be provided with on the frustum 30 and be positioned at the baffle plate 32 that its part that is positioned at frustum 30 is blocked in second discharge, 50 tops, again the end face that second discharge 50 is communicated with frustum 30 conical surfaces be arranged to outward-dipping from top to bottom, more effectively prevent the liquid pearl from second discharge 50 discharged to second gathering system 51.
In addition, in this example, U-shaped heat exchanger tube 20 is stainless steel, and it high temperature corrosion can not take place under water vapor, so can not bring the problems such as obstruction of extra pollution and condensate line to collection gas; Simultaneously in first discharge 40 and second discharge 50, be respectively equipped with desiccant layer, prevent from also being mixed with in the water-fast gas a spot of water vapour, and then, water-fast gas and water vapour separated more up hill and dale.
The concrete enforcement of separator in this example is as follows:
In U-shaped heat exchanger tube 20, add the condensed water that flows, water-fast gas (for example hydrogen, helium or carbon monoxide and argon gas) and water vapor mixture body are in air inlet 10 guiding cylinders 1, after mist touches U-shaped heat exchanger tube 20, water vapour liquefaction wherein forms the globule, drip to fluid collection device 3 or directly splash into fluid collection device 3 from U-shaped heat exchanger tube 20 along the inwall of cylinder 1, from 31 discharges of bickering, receive to collecting tank 33 then; The gas outlet 11 of gas (for example hydrogen, helium or carbon monoxide) the self-separation tube 1 that water insoluble density is less is collected by first gas collector 4, the gas that water insoluble density is bigger (for example argon gas), under the effect of gravity, leakage fluid dram 12 to separator 1 moves, when frustum 30 places that move to fluid collection device 3, part is collected by second gas collector 5 earlier, some continues to flow downward, bounce-back upwards after running into liquid level, flow to frustum 30 places again, and collected by second gas collector 5 again.In first discharge 40 and second discharge 50, be respectively equipped with simultaneously desiccant layer (CaCl for example
2), prevent from also being mixed with in the water-fast gas a spot of water vapour, and then, water-fast gas and water vapour more effectively separated.
In sum, the utility model is connected the gas outlet of cylinder with first gas collector, the sidewall of fluid collection device is connected with second gas collector, by condensing unit water vapour is liquefied again, water-fast density is less and collected by first gas collector and second gas collector respectively than atmospheric, liquid integument fluid collection device after the liquefaction is collected, the U-shaped heat exchanger tube that while the utility model adopts is stainless steel, high temperature corrosion can not take place in it under water vapor, so can not bring the problems such as obstruction of extra pollution and condensate line to collection gas, therefore, can be used for separating of different densities gas and water vapour, and have higher security and reliability.
More than the utility model has been done detailed description; its purpose is to allow the personage that is familiar with this art can understand content of the present utility model and is implemented; can not limit protection domain of the present utility model with this; all equivalences of doing according to spiritual essence of the present utility model change or modify, and all should be encompassed in the protection domain of the present utility model.
Claims (10)
1. separator for separating of water-fast gas and water vapour, it comprises having air inlet (10), the cylinder (1) of gas outlet (11) and leakage fluid dram (12), be arranged on the condensing unit (2) in the described cylinder (1), be arranged on the fluid collection device (3) of described leakage fluid dram (12) below, it is characterized in that: described separator also comprises first gas collector (4) that is connected with the gas outlet (10) of described cylinder (1) and second gas collector (5) that is connected with the sidewall of described fluid collection device (3), described first gas collector (4) comprises first discharge (40) that an end is connected with the gas outlet (10) of described cylinder (1) and first gas collector (41) that is connected with described first discharge (40) the other end, described first gas collector (4) is used for the less gas of collection density, described second gas collector (5) comprises second discharge (50) that an end is connected with the sidewall of described fluid collection device (3) and second gas collector (51) that is connected with described second discharge (50) the other end, and described second gas collector (5) is used for the bigger gas of collection density.
2. the separator for separating of water-fast gas and water vapour according to claim 1, it is characterized in that: described fluid collection device (3) is funnel-form, the collecting tank (33) that it comprises the frustum (30) that the cross section diminishes gradually from top to bottom and bickers (31) and be arranged on described bickering (31) below, described second discharge (50) is connected with described frustum (30).
3. the separator for separating of water-fast gas and water vapour according to claim 2 is characterized in that: the end face of the end that is connected with described frustum (30) frustum of described second discharge (50) is outward-dipping inclined-plane from top to bottom.
4. according to claim 2 or 3 described separators for separating of water-fast gas and water vapour, it is characterized in that: the cone-apex angle of described frustum (30) is 90 °.
5. according to claim 2 or 3 described separators for separating of water-fast gas and water vapour, it is characterized in that: also be provided with on the described frustum (30) and be positioned at the baffle plate (32) that its part that is positioned at described frustum (30) is blocked in described second discharge (50) top.
6. the separator for separating of water-fast gas and water vapour according to claim 1, it is characterized in that: described condensing unit (2) comprises U-shaped heat exchanger tube (20) and the supply system of condensed water is provided that the two ends of described U-shaped heat exchanger tube (20) are connected with outlet pipe (7) with the water inlet pipe (6) of supply system respectively.
7. the separator for separating of water-fast gas and water vapour according to claim 6, it is characterized in that: described U-shaped heat exchanger tube (20) is stainless steel.
8. the separator for separating of water-fast gas and water vapour according to claim 1, it is characterized in that: described gas outlet (11) are arranged on the top of described cylinder (1), and described air inlet (10) is arranged on the bottom side of described cylinder (1); Described leakage fluid dram (12) is arranged on the bottom of described cylinder (1) and is connected with described fluid collection device (3).
9. the separator for separating of water-fast gas and water vapour according to claim 1, it is characterized in that: the less gas of described density is hydrogen, helium or carbon monoxide.
10. according to claim 1 or 9 described separators for separating of water-fast gas and water vapour, it is characterized in that: the gas that described density is bigger is argon gas.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201320199072 CN203220843U (en) | 2013-04-19 | 2013-04-19 | Separating device for separating gas insoluble in water from water vapor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201320199072 CN203220843U (en) | 2013-04-19 | 2013-04-19 | Separating device for separating gas insoluble in water from water vapor |
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| Publication Number | Publication Date |
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| CN203220843U true CN203220843U (en) | 2013-10-02 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201320199072 Expired - Lifetime CN203220843U (en) | 2013-04-19 | 2013-04-19 | Separating device for separating gas insoluble in water from water vapor |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105289034A (en) * | 2015-12-09 | 2016-02-03 | 三合五(北京)环保能源科技有限公司 | Gas-liquid chromatography separation device |
| CN105343973A (en) * | 2015-12-09 | 2016-02-24 | 三合五(北京)环保能源科技有限公司 | Hydrogen therapeutic equipment |
| CN107115755A (en) * | 2017-06-30 | 2017-09-01 | 吉林市吉研高科技纤维有限责任公司 | A kind of new shredded tobacco for water pipes separator |
-
2013
- 2013-04-19 CN CN 201320199072 patent/CN203220843U/en not_active Expired - Lifetime
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105289034A (en) * | 2015-12-09 | 2016-02-03 | 三合五(北京)环保能源科技有限公司 | Gas-liquid chromatography separation device |
| CN105343973A (en) * | 2015-12-09 | 2016-02-24 | 三合五(北京)环保能源科技有限公司 | Hydrogen therapeutic equipment |
| CN107115755A (en) * | 2017-06-30 | 2017-09-01 | 吉林市吉研高科技纤维有限责任公司 | A kind of new shredded tobacco for water pipes separator |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C56 | Change in the name or address of the patentee | ||
| CP01 | Change in the name or title of a patent holder |
Address after: 215004, No. 1788, West Ring Road, Suzhou, Jiangsu, Suzhou Patentee after: SUZHOU NUCLEAR POWER RESEARCH INSTITUTE Co.,Ltd. Patentee after: CHINA GENERAL NUCLEAR POWER Corp. Address before: 215004, No. 1788, West Ring Road, Suzhou, Jiangsu, Suzhou Patentee before: SUZHOU NUCLEAR POWER RESEARCH INSTITUTE Co.,Ltd. Patentee before: CHINA GUANGDONG NUCLEAR POWER GROUP Co.,Ltd. |
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| CX01 | Expiry of patent term |
Granted publication date: 20131002 |
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| CX01 | Expiry of patent term |