CN208406511U - A kind of gas and water separator - Google Patents
A kind of gas and water separator Download PDFInfo
- Publication number
- CN208406511U CN208406511U CN201820996699.5U CN201820996699U CN208406511U CN 208406511 U CN208406511 U CN 208406511U CN 201820996699 U CN201820996699 U CN 201820996699U CN 208406511 U CN208406511 U CN 208406511U
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- China
- Prior art keywords
- air
- water
- tank body
- inlet tube
- flow
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- 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 - Fee Related
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- Drying Of Gases (AREA)
- Separating Particles In Gases By Inertia (AREA)
Abstract
The utility model relates to a kind of gas and water separators, the air water input pipe being arranged diagonally downward is flowed to along air water, the air water input pipe enters before tank body and is divided into two-way output in branch is forked, it is the water flow input pipe being connected in tank body lower section side wall all the way, another way is the airflow inlet tube being connected in tank body upper section side wall；The tank body is erected for cylindrical straight and is set, and the top of the tank is provided with air-flow efferent duct, and bottom is provided with scum pipe, and side wall is provided with water flow efferent duct, and the nozzle height of the water flow efferent duct is not higher than the entrance height of airflow inlet tube；Cooling jacket is provided on the airflow inlet tube, the horizontally disposed stainless steel cloth demister having for the not cooled collet of air-flow mist that is completely cooling and being formed to be become to droplet of the tank interior, the stainless steel cloth demister are located between airflow inlet tube outlet and air-flow efferent duct；Present apparatus structure is simple, dehydration efficiency is high.
Description
Technical field
The utility model relates to gas-water separation technology field, in particular to a kind of gas and water separator.
Background technique
Since moisture content is very big on the influence of the performance of low concentration gas internal combustion engine, when conveying low-concentration methane gas
Low-concentration methane gas need to be carried out dehydrating.Currently, most of low concentration gas power station is dehydrated using whirlwind or using weight
Power dehydration or first progress gravity dehydration carry out whirlwind dehydration again, however due to using water mists defeated when low-concentration methane gas conveying
It send, the water content of low-concentration methane gas will increase, and use existing dewatering de-water ratio 85% hereinafter, water removal effect
It is bad, therefore also the low-concentration methane gas containing a large amount of moisture content can be such that generating set operation troubles rate improves, generating efficiency drop
It is low.
Utility model content
The utility model is directed to prior art problem, provides the gas and water separator that a kind of structure is simple, dehydration efficiency is high.
In order to achieve the above object, the technical solution adopted in the utility model are as follows: a kind of gas and water separator is flowed to along air water
The air water input pipe being arranged diagonally downward, the air water input pipe enter before tank body and are divided into two-way output in branch is forked, are all the way
It is connected to the water flow input pipe in tank body lower section side wall, another way is the airflow inlet tube being connected in tank body upper section side wall；The tank
Body is erected for cylindrical straight and is set, and the top of the tank is provided with air-flow efferent duct, and bottom is provided with scum pipe, and side wall is provided with water
Efferent duct is flowed, the nozzle height of the water flow efferent duct is not higher than the entrance height of airflow inlet tube；On the airflow inlet tube
It is provided with cooling jacket, the tank interior is horizontally disposed the mist formed for the not cooled collet of air-flow is completely cooling
Foam becomes the stainless steel cloth demister of droplet, and the stainless steel cloth demister is located at airflow inlet tube outlet and air-flow output
Between pipe.
The liquidometer detachably installed is additionally provided on the tank body.
The bottom of the tank body is equipped with supporting leg.
The cooling jacket uses chilled brine as coolant.
The utility model is compared with prior art: present apparatus structure is simple, and dehydration efficiency is high, and inverted gas and water body is through air water
After input pipe enters, air-flow enters airflow inlet tube, and water flow enters water flow input pipe, is cooled down by being arranged on airflow inlet tube
Condensate moisture in the air-flow for flowing through airflow inlet tube can be fallen at droplet and enter water flow input pipe by collet, and air-flow enters
After tank body, completely not cooling mist is become into droplet through stainless steel cloth demister and is dropped in tank base, gas is through air-flow
Efferent duct excludes；Water flows through after water flow input pipe enters tank interior, excludes through water flow efferent duct；Impurity in water flow is through gravity
It can be excluded through scum pipe after precipitating.
Detailed description of the invention
Fig. 1 is the structural schematic diagram of the utility model gas and water separator.
Specific embodiment
Below with reference to Fig. 1, the utility model is described in further detail.
A kind of gas and water separator flows to the air water input pipe 10 being arranged diagonally downward, the air water input pipe along air water
It is divided into two-way output in branch is forked before 10 entrance tank bodies 20, is the water flow input pipe 11 being connected in 20 lower section side wall of tank body all the way,
Another way is the airflow inlet tube 12 being connected in 20 upper section side wall of tank body；The tank body 20 is erected for cylindrical straight and is set, the tank
Air-flow efferent duct 21 is provided at the top of body 20, bottom is provided with scum pipe 22, and side wall is provided with water flow efferent duct 23, the water flow
The nozzle height of efferent duct 23 is not higher than the entrance height of airflow inlet tube 12；Cooling folder is provided on the airflow inlet tube 12
Set 13, the mist that 20 inner horizontal of tank body is provided with for forming the not cooled complete cooling of collet 13 of air-flow become
The stainless steel cloth demister 24 of droplet, the stainless steel cloth demister 24 are located at the outlet of airflow inlet tube 12 and air-flow output
Between pipe 21.
The liquidometer 25 detachably installed is additionally provided on the tank body 20；Cleaning liquidometer easy to disassemble in this way.
The bottom of the tank body 20 is equipped with supporting leg 26.
The cooling jacket 13 uses chilled brine as coolant.
Present apparatus structure is simple, and dehydration efficiency is high, and for inverted gas and water body after the entrance of air water input pipe 10, air-flow enters gas
Input pipe 12 is flowed, water flow enters water flow input pipe 11, by the way that cooling jacket 13 is arranged on airflow inlet tube 12, can will flow through
Condensate moisture in the air-flow of airflow inlet tube 12 falls at droplet enters water flow input pipe 11, after air-flow enters tank body 20, warp
Completely not cooling mist is become droplet and is dropped in 20 bottom of tank body by stainless steel cloth demister 24, and gas is through air-flow efferent duct
21 exclude；After water flows through the entrance tank interior of water flow input pipe 11, excluded through water flow efferent duct 23；Impurity in water flow is through gravity
It can be excluded through scum pipe 22 after precipitating.
Embodiment described above is only that preferred embodiments of the present invention are described, not practical to this
Novel range is defined, and under the premise of not departing from the spirit of the design of the utility model, those of ordinary skill in the art are to this
The various changes and improvements that the technical solution of utility model is made should all fall into the guarantor that claims of the utility model determine
It protects in range.
Claims (4)
1. a kind of gas and water separator, it is characterised in that: flow to the air water input pipe being arranged diagonally downward, the air water along air water
Input pipe enters before tank body and is divided into two-way output in branch is forked, is the water flow input pipe being connected in tank body lower section side wall all the way, separately
It is the airflow inlet tube being connected in tank body upper section side wall all the way；The tank body is erected for cylindrical straight and is set, and the top of the tank is set
It is equipped with air-flow efferent duct, bottom is provided with scum pipe, and side wall is provided with water flow efferent duct, the nozzle height of the water flow efferent duct
Not higher than the entrance height of airflow inlet tube；Cooling jacket is provided on the airflow inlet tube, the tank interior level is set
It is equipped with the stainless steel cloth demister for the not cooled collet of air-flow mist that is completely cooling and being formed to be become to droplet, it is described
Stainless steel cloth demister is located between airflow inlet tube outlet and air-flow efferent duct.
2. a kind of gas and water separator as described in claim 1, it is characterised in that: be additionally provided with detachable peace on the tank body
The liquidometer of dress.
3. a kind of gas and water separator as described in claim 1, it is characterised in that: the bottom of the tank body is equipped with supporting leg.
4. a kind of gas and water separator as described in claim 1, it is characterised in that: the cooling jacket use chilled brine as
Coolant.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820996699.5U CN208406511U (en) | 2018-06-26 | 2018-06-26 | A kind of gas and water separator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820996699.5U CN208406511U (en) | 2018-06-26 | 2018-06-26 | A kind of gas and water separator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN208406511U true CN208406511U (en) | 2019-01-22 |
Family
ID=65106889
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201820996699.5U Expired - Fee Related CN208406511U (en) | 2018-06-26 | 2018-06-26 | A kind of gas and water separator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN208406511U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110332405A (en) * | 2019-07-15 | 2019-10-15 | 南京凯祥管道工程有限公司 | A kind of steam, condensation heat tracing technique and steam tracing system |
-
2018
- 2018-06-26 CN CN201820996699.5U patent/CN208406511U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110332405A (en) * | 2019-07-15 | 2019-10-15 | 南京凯祥管道工程有限公司 | A kind of steam, condensation heat tracing technique and steam tracing system |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20190122 Termination date: 20190626 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |