CN103706211A - Cyclone natural gas washing tank - Google Patents
Cyclone natural gas washing tank Download PDFInfo
- Publication number
- CN103706211A CN103706211A CN201310689816.5A CN201310689816A CN103706211A CN 103706211 A CN103706211 A CN 103706211A CN 201310689816 A CN201310689816 A CN 201310689816A CN 103706211 A CN103706211 A CN 103706211A
- Authority
- CN
- China
- Prior art keywords
- tank body
- baffle plate
- tank
- baffling box
- natural 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.)
- Granted
Links
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 title claims abstract description 66
- 239000003345 natural gas Substances 0.000 title claims abstract description 33
- 238000005406 washing Methods 0.000 title claims abstract description 21
- 229910001220 stainless steel Inorganic materials 0.000 claims abstract description 20
- 239000010935 stainless steel Substances 0.000 claims abstract description 17
- 239000004744 fabric Substances 0.000 claims description 16
- 239000004810 polytetrafluoroethylene Substances 0.000 claims description 8
- 229920001343 polytetrafluoroethylene Polymers 0.000 claims description 8
- 239000011159 matrix material Substances 0.000 claims description 3
- 239000007789 gas Substances 0.000 abstract description 19
- 238000000926 separation method Methods 0.000 abstract description 9
- 238000000746 purification Methods 0.000 abstract description 6
- 239000007788 liquid Substances 0.000 abstract description 4
- 239000002245 particle Substances 0.000 description 9
- 239000007787 solid Substances 0.000 description 7
- 230000000694 effects Effects 0.000 description 6
- 238000004140 cleaning Methods 0.000 description 4
- 239000000463 material Substances 0.000 description 3
- 238000005260 corrosion Methods 0.000 description 2
- 230000007797 corrosion Effects 0.000 description 2
- 238000005201 scrubbing Methods 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000005119 centrifugation Methods 0.000 description 1
- 239000004047 hole gas Substances 0.000 description 1
- 239000003595 mist Substances 0.000 description 1
Images
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- Cyclones (AREA)
Abstract
The invention discloses a cyclone natural gas washing tank comprising a tank body, a gas inlet pipe and a gas outlet pipe connected with the tank body, and a baffling box positioned in the tank body and connected with the tank body, wherein the pipe orifice of the gas inlet pipe is enwrapped in the baffling box; the surface of the baffling box, opposite to the gas inlet pipe, is an inclined plane; a vent hole is formed in the baffling box; a first baffle plate positioned in the tank body is arranged above the baffling box; a second baffle plate positioned in the tank body is arranged below the baffling box; a separation pipe is arranged between the first baffle plate and the second baffle plate; a gas outlet hole is formed in the bottom of the separation pipe; a rotational flow plate is arranged between the separation pipe and the tank body and forms a spiral gas passage between the outer cylindrical surface of the separation pipe and the inner wall of the tank body; a gas outlet hole is formed in the center of the first baffle plate; a liquid drop hole is formed in the second baffle plate; a stainless steel silk screen demister positioned in the tank body is arranged above the first baffle plate; a liquid collecting tank positioned in the tank body is arranged below the baffling box. The cyclone natural gas washing tank disclosed by the invention is high in purification efficiency.
Description
Technical field
The invention belongs to gas purifying equipment technical field, be specifically related to a kind of natural gas washing tank.
Background technology
Gas purification is common industrial operation, and along with the development of gas industry, the purification of natural gas has also obtained development rapidly.In practice, gas cleaning plant is of a great variety, and wherein, gas scrubbing tank is more common a kind of.Existing natural gas adopts washing tank to carry out washing, purifying conventionally, and gas scrubbing tank generally comprises surge tank and washing tank two parts, natural gas to be washed is introduced into surge tank, after surge tank internal gas pressure is stable, at the bottom of entering the tank of the washing tank that cleaning solution is housed by pipeline from surge tank, gas passes through cleaning solution from bottom to top, discharges, thereby complete washing process from gas outlet.Existing washing tank is provided with downward 45 ° of angular cuts (as shown in Figure 1) in its air inlet pipe end, play certain break-in effect to a certain extent to entering airflow direction.Yet, adopt 45 ° of downward angular cut structures of air inlet pipe end, can only change the flow direction of small part of gas, the clean-up effect of natural gas is poor.
Summary of the invention
The object of the present invention is to provide a kind of natural gas washing tank.
For achieving the above object, technical scheme of the present invention is:
A kind of cyclone type natural gas washing tank, comprise tank body, the air inlet pipe being connected with tank body and escape pipe, it is characterized in that: also comprise and be positioned at the baffling box that tank body is connected with tank body, in baffling box is enclosed in the air inlet pipe mouth of pipe, the face of the baffling box relative with air inlet pipe is inclined plane, baffling box offers steam vent, baffling box top is provided with the first baffle plate that is positioned at tank body, baffling box below is provided with the second baffle that is positioned at tank body, between the first baffle plate and second baffle, be provided with separator tube, separator tube bottom is provided with venthole
, between separator tube and tank body, being provided with spiral board, spiral board forms spiral air passage between the external cylindrical surface of separator tube and the inwall of tank body, and the first baffle plate center is provided with venthole
, second baffle is provided with drop hole, and the first baffle plate top is provided with the stainless steel cloth demister that is positioned at tank body, and baffling box below is provided with the collecting tank that is positioned at tank body.
Further, on the metallic matrix of stainless steel cloth demister, be compounded with PTFE thin layer.
Compared with prior art, beneficial effect of the present invention is:
1, inner tank wall arranges baffling box, the face of the baffling box relative with air inlet pipe is inclined plane, the natural gas that arrives baffling box inclined plane is completely changed and flows to by baffling box, natural gas is discharged and is entered tank body along inner tank wall tangential direction from the steam vent of baffling box and does gyration, solid particle in natural gas and larger free liquid drop under the effect of centrifugal force clashes into inner tank wall, and drop on spiral board and finally fall into collecting tank along inwall, the centrifugation clean-up effect of natural gas is improved greatly.
2, the first baffle plate and the second baffle in tank body, and be provided with separator tube between two plates, between separator tube and tank body, be provided with spiral board, spiral board forms spiral air passage between the external cylindrical surface of separator tube and the inwall of tank body, when natural gas rotates in spiral air passage under the effect of centrifugal force, part solid particle and droplet are fallen into collecting tank from drop hole, have reached the object of gas-liquid separation.
3, stainless steel cloth demister is set in body, natural gas enters after washing tank, free drop and solid particle that particle is large fall into washing tank collecting tank, natural gas rises to fine and close stainless steel cloth, less solid particle is blocked, small drop is built up in stainless steel cloth demister and is finally fallen into collecting tank, and the natural gas after purification is discharged from escape pipe, and Compressed Gas is effectively purified.
4, on the base material of stainless steel cloth demister, be compounded with PTFE thin layer, low friction and antistick characteristic due to PTFE film, can reduce the frictional resistance between droplet and demister, greatly improves washing tank purification efficiency.
Accompanying drawing explanation
Fig. 1 is the structural representation of the air inlet pipe of existing washing tank;
Fig. 2 is structural representation of the present invention;
Fig. 3 is the sectional view at A-A place in the present invention;
Wherein Reference numeral is: 1-tank body, 2-air inlet pipe, 3-escape pipe, 4-baffling box, 41-inclined plane, 42-steam vent, 5-stainless steel cloth demister, 6-collecting tank, the 7-the first baffle plate, 8-second baffle, 9-separator tube, 10-venthole
, 11-spiral board, 12-venthole
, 13-drop hole.
The specific embodiment
Below in conjunction with accompanying drawing, the present invention will be further described:
As shown in the figure, a kind of cyclone type natural gas washing tank, comprises tank body 1, the air inlet pipe 2 being connected with tank body 1 and escape pipe 3.In tank body 1, be connected with baffling box 4, in baffling box 4 is enclosed in the mouth of pipe of air inlet pipe 2.Wherein, air inlet pipe 2 one end are stretched in tank body 1 and are connected and fixed with tank body 1, and baffling box 4 is connected with tank body 1 inwall, and in the mouth of pipe of air inlet pipe 2 is enclosed in; Also can be by air inlet pipe 2 suits and baffling box 4, baffling box 4 is positioned at tank body 1 and is connected with tank body 1.Above-mentioned connected mode can directly adopt and be welded to connect, and also can adopt and be threaded.The face of the baffling box 4 relative with air inlet pipe 2 is inclined plane 41, makes the length of baffling box 4 two sides different, and baffling box 4 is provided with exhaust outlet 42, and wherein exhaust outlet 42 is arranged on the side that baffling box 4 length are longer.Baffling box 4 tops are provided with the first plate washer 7 that is positioned at tank body 1, and baffling box 4 belows are provided with the second plate washer 8, the first plate washer 7 centers that are positioned at tank body 1 and are provided with venthole
12, second baffle 8 is provided with drop hole 13.Between the first plate washer 7 and the second plate washer 8, be provided with separator tube 9, separator tube 9 bottoms are provided with venthole
10.Between separator tube 9 and tank body 1, be provided with spiral board 11, spiral board 11 forms spiral air passage between the external cylindrical surface of separator tube 9 and the inwall of tank body 1.The first plate washer 7 tops are provided with stainless steel cloth demister 5, the second plate washer 8 belows that are positioned at tank body 1 and are provided with the collecting tank 6 that is positioned at tank body 1.
On the metallic matrix of stainless steel cloth demister 5, be compounded with PTFE thin layer, PTFE is a kind of material with corrosion-resistant, low friction, antistick characteristic, stainless steel wire is wrapped in PTFE as base material completely, stainless steel wire surface forms the wear-resisting resistance to PTFE thin layer drawing of one deck, can keep not viscosity, self-cleaning and the corrosion resistance on whole silk screen surface, the droplet simultaneously with superelevation catches performance, and the filter efficiency of whole demister is greatly improved.Wherein the stainless steel cloth in stainless steel cloth demister 5 is made as two-layerly, and the aperture of stainless steel cloth is irregularly shaped.
When the present invention works, natural gas enters baffling box from air inlet pipe, and the natural gas entering in baffling box is completely changed and flows to by the inclined plane of baffling box, and natural gas is carried out to one-level separation; From the steam vent of baffling box, discharge and enter tank body along inner tank wall tangential direction afterwards and do gyration, by centrifugal action, natural gas is carried out to the second-order separation; Natural gas enters after washing tank, the free drop that particle is large and solid particle fall on spiral board and finally fall into collecting tank, and natural gas enters by the spiral air passage forming between spiral board, separator tube and tank body, and while rotating in gas passage road under the effect of centrifugal force, part solid particle and droplet are fallen into collecting tank from drop hole, and natural gas carries out three grades of separation by collision, eddy flow; Natural gas out passes through venthole in spiral air passage
, venthole
rise to fine and close stainless steel cloth demister, less solid particle is blocked, and collecting tank is built up in stainless steel cloth demister and finally fallen into small drop, and stainless steel wire demister carries out level Four separation by catching mist, adhesion, cohesion to natural gas; Natural gas after purification is discharged from escape pipe, and natural gas is effectively purified.
Claims (2)
1. a cyclone type natural gas washing tank, comprise tank body (1), the air inlet pipe (2) being connected with tank body (1) and escape pipe (3), it is characterized in that: also comprise and be positioned at the baffling box (4) that tank body (1) is connected with tank body (1), in baffling box (3) is enclosed in air inlet pipe (2) mouth of pipe, the face of the baffling box (3) relative with air inlet pipe (2) is inclined plane (41), baffling box (3) offers steam vent (42), baffling box (4) top is provided with the first baffle plate (7) that is positioned at tank body (1), baffling box (4) below is provided with the second baffle (8) that is positioned at tank body (1), between the first baffle plate (7) and second baffle (8), be provided with separator tube (9), separator tube (9) bottom is provided with venthole
(10), between separator tube (9) and tank body (1), be provided with spiral board (11), spiral board (11) forms spiral air passage between the external cylindrical surface of separator tube (9) and the inwall of tank body (1), and the first baffle plate (7) center is provided with venthole
(12), second baffle (8) is provided with drop hole (13), and the first baffle plate (7) top is provided with the stainless steel cloth demister (5) that is positioned at tank body (1), and baffling box (4) below is provided with the collecting tank (6) that is positioned at tank body (1).
2. cyclone type natural gas washing tank as claimed in claim, is characterized in that: on the metallic matrix of stainless steel cloth demister (5), be compounded with PTFE thin layer.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201310689816.5A CN103706211B (en) | 2013-12-17 | 2013-12-17 | Cyclone type natural gas washing tank |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201310689816.5A CN103706211B (en) | 2013-12-17 | 2013-12-17 | Cyclone type natural gas washing tank |
Publications (2)
Publication Number | Publication Date |
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CN103706211A true CN103706211A (en) | 2014-04-09 |
CN103706211B CN103706211B (en) | 2015-11-18 |
Family
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Application Number | Title | Priority Date | Filing Date |
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CN201310689816.5A Expired - Fee Related CN103706211B (en) | 2013-12-17 | 2013-12-17 | Cyclone type natural gas washing tank |
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CN (1) | CN103706211B (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105038888A (en) * | 2015-08-15 | 2015-11-11 | 重庆联合机器制造有限公司 | Natural gas second-stage gas-liquid separator |
CN106440575A (en) * | 2016-11-09 | 2017-02-22 | 珠海格力电器股份有限公司 | Gas-liquid separator and air conditioning system |
CN107353956A (en) * | 2017-08-04 | 2017-11-17 | 华东理工大学 | A kind of compact natural gas suitable for offshore platform pre-processes purification method and device |
Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4668256A (en) * | 1984-11-23 | 1987-05-26 | Domnick Hunter Filters Limited | Liquid/gas separation |
CN101869780A (en) * | 2009-04-27 | 2010-10-27 | 上海金属丝网制品有限公司 | High-efficiency foam destroyer adopting metal base composite PTFE (Polytetrafluoroethylene) |
CN201988302U (en) * | 2011-01-25 | 2011-09-28 | 杭州联合超滤净化设备有限公司 | Air water separating device |
CN202270430U (en) * | 2011-09-16 | 2012-06-13 | 固耐重工(苏州)有限公司 | Gas-liquid separator |
CN202277752U (en) * | 2011-09-29 | 2012-06-20 | 西安航空动力股份有限公司 | Refrigeration type drying machine gas-liquid separation device |
CN202808742U (en) * | 2012-10-29 | 2013-03-20 | 中国石油天然气集团公司 | Spiral-flow type natural gas dehydration device |
CN203591672U (en) * | 2013-12-17 | 2014-05-14 | 成都展望能源机械有限公司 | Whirlwind type natural gas washing pot |
-
2013
- 2013-12-17 CN CN201310689816.5A patent/CN103706211B/en not_active Expired - Fee Related
Patent Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4668256A (en) * | 1984-11-23 | 1987-05-26 | Domnick Hunter Filters Limited | Liquid/gas separation |
CN101869780A (en) * | 2009-04-27 | 2010-10-27 | 上海金属丝网制品有限公司 | High-efficiency foam destroyer adopting metal base composite PTFE (Polytetrafluoroethylene) |
CN201988302U (en) * | 2011-01-25 | 2011-09-28 | 杭州联合超滤净化设备有限公司 | Air water separating device |
CN202270430U (en) * | 2011-09-16 | 2012-06-13 | 固耐重工(苏州)有限公司 | Gas-liquid separator |
CN202277752U (en) * | 2011-09-29 | 2012-06-20 | 西安航空动力股份有限公司 | Refrigeration type drying machine gas-liquid separation device |
CN202808742U (en) * | 2012-10-29 | 2013-03-20 | 中国石油天然气集团公司 | Spiral-flow type natural gas dehydration device |
CN203591672U (en) * | 2013-12-17 | 2014-05-14 | 成都展望能源机械有限公司 | Whirlwind type natural gas washing pot |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105038888A (en) * | 2015-08-15 | 2015-11-11 | 重庆联合机器制造有限公司 | Natural gas second-stage gas-liquid separator |
CN106440575A (en) * | 2016-11-09 | 2017-02-22 | 珠海格力电器股份有限公司 | Gas-liquid separator and air conditioning system |
CN106440575B (en) * | 2016-11-09 | 2022-03-18 | 珠海格力电器股份有限公司 | Gas-liquid separator and air conditioning system |
CN107353956A (en) * | 2017-08-04 | 2017-11-17 | 华东理工大学 | A kind of compact natural gas suitable for offshore platform pre-processes purification method and device |
CN107353956B (en) * | 2017-08-04 | 2020-06-19 | 华东理工大学 | A compact natural gas pretreatment and purification method and device suitable for offshore platforms |
Also Published As
Publication number | Publication date |
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CN103706211B (en) | 2015-11-18 |
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CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20151118 Termination date: 20201217 |
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CF01 | Termination of patent right due to non-payment of annual fee |