CN204939418U - Natural gas conditioning sledge regenerator column - Google Patents
Natural gas conditioning sledge regenerator column Download PDFInfo
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- CN204939418U CN204939418U CN201520426348.7U CN201520426348U CN204939418U CN 204939418 U CN204939418 U CN 204939418U CN 201520426348 U CN201520426348 U CN 201520426348U CN 204939418 U CN204939418 U CN 204939418U
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- sledge
- natural gas
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Abstract
The utility model is a kind of natural gas conditioning sledge regenerator column, comprises tower body, and this tower body is made up of tower reactor section, the again section of boiling, mass transfer segregation section, condensation segment and aerosol segregation section five sections from down to up successively, and all passes through Flange joint between adjacent segment; Wherein tower reactor section is tower reactor, offer lean solution outlet, then the section of boiling is reboiler in the bottom of this tower reactor; Be provided with liquid re-distributor in the middle part of mass transfer segregation section, be respectively packing layer at the two ends up and down of this liquid re-distributor, have rich solution entrance on the top of this mass transfer segregation section; Condenser is provided with in condensation segment; The bottom of aerosol segregation section is provided with wire mesh demister, and middle part is provided with Coalescence filter core, and top offers discharge outlet.The utility model one-piece construction is simple, Highgrade integration, and realize regeneration of waste liquor function in gas purifying process, floor space is little again, gives and installs and transport all bringing great convenience property, invests in addition more to economize and production cost is lower.
Description
Technical field
The utility model relates to Sweet natural gas pre-processing device field, is specifically related to a kind of natural gas conditioning sledge regenerator column.
Background technology
Along with the application of China's natural gas and universal, numerous natural air-air sources such as coal-seam gas, chicken coop gas, lonely gas well gas, small-sized shale gas, oil field gas, biogas are developed, be applicable to the integrated packaged type Qiao Zhuan factory of the height of this type of source of the gas because of its take up an area less, invest little, the advantage such as fast of founding the factory is more and more welcome.
Decarbonizing solution regenerates, as an important part for Sweet natural gas pre-treatment link, because complex structure, equipment pipe valve and Controlling System are numerous, pre-treatment sledge is caused to take up an area more, and cost of investment is high, therefore meeting under process function prerequisite, Optimization Technology, minimizing equipment takes up an area and quantity, will bring very large economic benefit.
Utility model content
The utility model is for the deficiencies in the prior art, and propose a kind of collection heating, rectifying, condensation, be located away from one, the natural gas conditioning skid-mounted regenerator column that diverse in function, structure are simple, easy for installation, concrete technical scheme is as follows:
A kind of natural gas conditioning sledge regenerator column, comprise tower body (1), this tower body (1) is made up of tower reactor section (2), the again section of boiling (3), mass transfer segregation section (4), condensation segment (5) and aerosol segregation section (6) five sections from down to up successively, and all passes through Flange joint between adjacent segment;
Wherein said tower reactor section (2) is tower reactor, offers lean solution outlet (24) in the bottom of this tower reactor;
The described section of boiling again (3) is reboiler (7);
Described mass transfer segregation section (4) middle part is provided with liquid re-distributor (8), be respectively packing layer (9) at the two ends up and down of this liquid re-distributor (8), have rich solution entrance (10) on the top of this mass transfer segregation section (4);
Condenser (11) is provided with in described condensation segment (5);
The bottom of described aerosol segregation section (6) is provided with wire mesh demister (12), and middle part is provided with Coalescence filter core (13), and top offers discharge outlet (14).
The utility model is such realization: be connected with skirt in tower reactor section (2) bottom, reboiler (7) in traditional technology and condenser (11) are highly integrated on tower body, volume is less, it is all more convenient to transport and install, shorten the length of connecting pipeline simultaneously, decrease material cost and production cost, the built-in wire mesh demister of tower top and Coalescence filter core, solve solution entrainment problem in carbonic acid gas, carbonic acid gas is made to reach direct emission standard, energy-conserving and environment-protective more.
For better realizing the utility model, may further be:
Described reboiler (7) comprises cylindrical shell (25), heat transfer tube (15) is vertically distributed with in this cylindrical shell (25), this heat transfer tube (15) is arranged on the inwall of described cylindrical shell (25) by upper and lower two pieces of stationary tubesheets (16), have thermal oil outlet (17) on this cylindrical shell (25) top, bottom has thermal oil entrance (18).In use, thermal oil walks shell side, and solution walks tube side.
Between described heat transfer tube (15), be provided with reboiler traverse baffle (19), make the S-shaped flowing of the thermal oil in its shell side, increase flow process, improve heat exchange efficiency, its volume can be reduced to greatest extent.
Described condenser (11) comprises shell (26), tubulation (20) is vertically provided with in this shell (26), this tubulation (20) is arranged on the inwall of described shell (26) by upper and lower two pieces of condenser stationary tubesheets (21), have circulating water outlet (27) on described shell (26) top, bottom has recirculated water entrance (22).In use, water of condensation walks shell side, and carbonic acid gas walks tube side, good effect of heat exchange, and make use of space to greatest extent, and one-piece construction is simple, easy to maintenance.
Laterally condenser traverse baffle (23) is provided with in described tubulation (20), make the S-shaped flowing of water of condensation in condenser (11) shell side, increase flow process, improve heat exchange efficiency, condensation vessel volume can farthest be reduced.
The beneficial effects of the utility model are: compare traditional distributing regenerator column technique, in the utility model, reboiler is built in tower reactor, can reduce reboiler external take up space and the space of connecting pipeline, reduce reboiler be connected with tower reactor needed for pipeline and valve, decrease thermosteresis; Condenser is built in tower body top, can reduce condenser external time take up space and the space of connecting pipeline, reduce respective line and valve; Condenser is built in tower body top, and directly can return in tower as backflow after the solution condensation that carbonic acid gas is carried secretly and again carry out mass transfer separation, eliminate separating device and associated pipe, valve and Controlling System, volume is less, and cost is lower; The built-in wire mesh demister of tower top and Coalescence filter core, solution entrainment problem when solving traditional technology Carbon emission, not containing mechanical water solution when making Carbon emission, reduce solution consume,, greatly simplify conventional solution reclaiming process, greatly save production cost; Adopt Flange joint between each functional section, easily dismantle, maintain easily; The utility model one-piece construction is simple, Highgrade integration, and realize regeneration of waste liquor function in sledge formula refining plant, floor space is little, gives and installs and transport all bringing great convenience property.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
Embodiment
Below in conjunction with drawings and the specific embodiments, the utility model is described in further detail.
As shown in Figure 1: a kind of natural gas conditioning sledge regenerator column, comprise tower body 1, this tower body 1 is made up of tower reactor section 2, the again section of boiling 3, mass transfer segregation section 4, condensation segment 5 and aerosol segregation section 6 five sections from down to up successively, and all passes through Flange joint between adjacent segment, assembly and disassembly is easy, is convenient to maintenance;
Wherein said tower reactor section 2 is tower reactor, is connected with skirt in the bottom of this tower reactor, and offers lean solution outlet 24;
The described section of boiling again 3 is reboiler 7, this reboiler 7 comprises cylindrical shell 25, heat transfer tube 15 is vertically distributed with in this cylindrical shell 25, this heat transfer tube 15 is arranged on the inwall of described cylindrical shell 25 by upper and lower two blocks of stationary tubesheets 16, have thermal oil outlet 17 on this cylindrical shell 25 top, bottom has thermal oil entrance 18, is provided with reboiler traverse baffle 19 between heat transfer tube 15, the flow process of thermal oil in shell side can be lengthened, improve heat exchange efficiency;
Liquid re-distributor 8 is provided with in the middle part of described mass transfer segregation section 4, packing layer 9 is respectively at the two ends up and down of this liquid re-distributor 8, rich solution entrance 10 is had on the top of this mass transfer segregation section 4, wherein the setting of liquid re-distributor 8 can make solution again be uniformly distributed, and reduces the scale effect caused by the bad distribution of liquid;
Condenser 11 is provided with in described condensation segment 5, this condenser 11 comprises shell 26, tubulation 20 is vertically provided with in this shell 26, condenser traverse baffle 23 is provided with in tubulation 20, this tubulation 20 is arranged on the inwall of described shell 26 by upper and lower two blocks of condenser stationary tubesheets 21, have circulating water outlet 27 on described shell 26 top, bottom has recirculated water entrance 22;
The bottom of described aerosol segregation section 6 is provided with wire mesh demister 12, middle part is provided with Coalescence filter core 13, top offers discharge outlet 14, wire mesh demister 12 can remove most of liquor of carrying secretly in carbonic acid gas, Coalescence filter core can remove the micro solution of carrying secretly in carbonic acid gas further, make the solution carried secretly in the carbonic acid gas of discharge at below 1ppm, can directly discharge, well solve the problem of Carbon emission entrained solution in traditional technology.
Claims (5)
1. a natural gas conditioning sledge regenerator column, it is characterized in that: comprise tower body (1), this tower body (1) is made up of tower reactor section (2), the again section of boiling (3), mass transfer segregation section (4), condensation segment (5) and aerosol segregation section (6) five sections from down to up successively, and all passes through Flange joint between adjacent segment;
Wherein said tower reactor section (2) is tower reactor, offers lean solution outlet (24) in the bottom of this tower reactor;
The described section of boiling again (3) is reboiler (7);
Described mass transfer segregation section (4) middle part is provided with liquid re-distributor (8), be respectively packing layer (9) at the two ends up and down of this liquid re-distributor (8), have rich solution entrance (10) on the top of this mass transfer segregation section (4);
Condenser (11) is provided with in described condensation segment (5);
The bottom of described aerosol segregation section (6) is provided with wire mesh demister (12), and middle part is provided with Coalescence filter core (13), and top offers discharge outlet (14).
2. natural gas conditioning sledge regenerator column according to claim 1, it is characterized in that: described reboiler (7) comprises cylindrical shell (25), heat transfer tube (15) is vertically distributed with in this cylindrical shell (25), this heat transfer tube (15) is arranged on the inwall of described cylindrical shell (25) by upper and lower two pieces of stationary tubesheets (16), have thermal oil outlet (17) on the top of this cylindrical shell (25), bottom has thermal oil entrance (18).
3. natural gas conditioning sledge regenerator column according to claim 2, is characterized in that: between described heat transfer tube (15), be provided with reboiler traverse baffle (19).
4. natural gas conditioning sledge regenerator column according to claim 1, it is characterized in that: described condenser (11) comprises shell (26), tubulation (20) is vertically provided with in this shell (26), this tubulation (20) is arranged on the inwall of described shell (26) by upper and lower two pieces of condenser stationary tubesheets (21), have circulating water outlet (27) on described shell (26) top, bottom has recirculated water entrance (22).
5. natural gas conditioning sledge regenerator column according to claim 4, is characterized in that: in described tubulation (20), be provided with condenser traverse baffle (23).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520426348.7U CN204939418U (en) | 2015-06-19 | 2015-06-19 | Natural gas conditioning sledge regenerator column |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520426348.7U CN204939418U (en) | 2015-06-19 | 2015-06-19 | Natural gas conditioning sledge regenerator column |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204939418U true CN204939418U (en) | 2016-01-06 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520426348.7U Expired - Fee Related CN204939418U (en) | 2015-06-19 | 2015-06-19 | Natural gas conditioning sledge regenerator column |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204939418U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108815873A (en) * | 2018-06-30 | 2018-11-16 | 淮阴工学院 | A kind of acetic acid rectifying column built in condenser, reboiler |
| CN109603178A (en) * | 2018-12-26 | 2019-04-12 | 佛山市金银河智能装备股份有限公司 | A method of it taking off low kettle and takes off low kettle and heat broken matchmaker |
-
2015
- 2015-06-19 CN CN201520426348.7U patent/CN204939418U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108815873A (en) * | 2018-06-30 | 2018-11-16 | 淮阴工学院 | A kind of acetic acid rectifying column built in condenser, reboiler |
| CN108815873B (en) * | 2018-06-30 | 2020-07-24 | 淮阴工学院 | Acetic acid rectifying tower with built-in condenser and reboiler |
| CN109603178A (en) * | 2018-12-26 | 2019-04-12 | 佛山市金银河智能装备股份有限公司 | A method of it taking off low kettle and takes off low kettle and heat broken matchmaker |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160106 Termination date: 20200619 |