CN201834898U - Skid-mounted deep natural gas deacidification apparatus - Google Patents
Skid-mounted deep natural gas deacidification apparatus Download PDFInfo
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- CN201834898U CN201834898U CN2010205125176U CN201020512517U CN201834898U CN 201834898 U CN201834898 U CN 201834898U CN 2010205125176 U CN2010205125176 U CN 2010205125176U CN 201020512517 U CN201020512517 U CN 201020512517U CN 201834898 U CN201834898 U CN 201834898U
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Abstract
The utility model discloses a skid-mounted deep natural gas deacidification apparatus, which belongs to the field of natural gas purification equipment. The structure of the apparatus comprises a raw gas separator, a pre-deacidification tower, a deep deacidification tower, a purified gas separator, a rich solution flash drum, a lean/rich solution heat exchanger, lean solution pumps, an amine solution regeneration tower, a reboiler, a carbon dioxide cooler, a carbon dioxide gas-liquid separator and a reflux pump, and all the units are mounted on a skid. Compared with the prior art, the apparatus is characterized by reasonable design, quick mounting, quick commissioning, convenience in transportation, high adaptability and the like.
Description
Technical field
The utility model relates to the natural gas conditioning apparatus field, specifically a kind of Sweet natural gas degree of depth deacidifying device of skid-mounted.
Background technology
Natural gas liquids (LNG) is as the energy of a kind of cleaning, high-efficiency high-quality, China and even the fastest field of world energy supplies rate of growth have been become, LNG is except can be used on industrial fuel and industrial chemicals, can also make domestic fuel, especially in municipal gas distribution system as the means of peak regulation, can fully guarantee urban safety, air feed stably.
Comprise a large amount of scattered gas fields Sweet natural gas, gas field, border Sweet natural gas, associated gas and coal-seam gas etc. in China's natural gas upstream resource, for cost consideration, a lot of discomforts are built the transport pipe of long distance jointly, also discomfort is built fixed large-scale natural gas liquefying plant jointly, so should consider to build small-sized sledge dress natural gas liquefaction device.Compare with large-scale liquefying plant, small-sized sledge dress natural gas liquefaction device not only has raw material advantage, the market advantage, and invest low, can move, handiness is big, and very wide application prospect is arranged.Part as small-sized sledge dress natural gas liquefaction device, the Sweet natural gas degree of depth deacidifying device of front end also should be the sledge dressization, and can adapt to the variation of multiple source of the gas, but traditional hydramine absorption unit is difficult for into sledge and transportation, device according to the fixed gas source design, does not have enough suitabilities to multiple source of the gas yet.
Summary of the invention
Technical assignment of the present utility model is at above weak point, and a kind of fast, Sweet natural gas degree of depth deacidifying device fast, that transport convenient removal, adaptable a kind of skid-mounted of going into operation of installing is provided.
The technical scheme that its technical problem that solves the utility model adopts is: this deacidifying device comprises unstripped gas separator, pre-extracting tower, degree of depth extracting tower, purge gas separator, rich solution flash tank, poor rich liquid heat exchanger, lean solution water cooler, lean pump, amine liquid regenerator column, reboiler, carbon dioxide cooler, carbonic acid gas gas-liquid separator and reflux pump, it is characterized in that above-mentioned each device all is installed on the sledge piece base.
Described unstripped gas separator is communicated with pre-extracting tower, degree of depth extracting tower respectively by pipeline, and amine liquid regenerator column is communicated with pre-extracting tower, degree of depth extracting tower respectively by pipeline.
On described amine liquid regenerator column and the pipeline that pre-extracting tower, degree of depth extracting tower are communicated with poor rich liquid heat exchanger, lean solution water cooler and lean pump are installed successively.
The bottom of described amine liquid regenerator column is connected with reboiler.
On the pipeline between described pre-extracting tower and degree of depth extracting tower and the amine liquid regenerator column rich solution flash tank is installed.
The top of described degree of depth extracting tower is connected with purge gas separator by pipeline.
The top of described amine liquid regenerator column connects carbon dioxide cooler, carbonic acid gas gas-liquid separator and reflux pump successively by pipeline.
The Sweet natural gas degree of depth deacidifying device of a kind of skid-mounted of the present utility model is compared with prior art, has characteristics such as reasonable in design, that installation is fast, it is fast to go into operation, transport convenient removal, adaptability is strong.
Description of drawings
Below in conjunction with accompanying drawing the utility model is further specified.
Accompanying drawing 1 is the structural representation of the Sweet natural gas degree of depth deacidifying device of skid-mounted.
Accompanying drawing 2 is each member connection structure synoptic diagram of the Sweet natural gas degree of depth deacidifying device of skid-mounted.
Among the figure: 1, unstripped gas separator, 2, pre-extracting tower, 3, degree of depth extracting tower, 4, purge gas separator, 5, the rich solution flash tank, 6, poor rich liquid heat exchanger, 7, lean solution water cooler, 8, lean pump, 9, amine liquid regenerator column, 10, reboiler, 11, carbon dioxide cooler, 12, carbonic acid gas gas-liquid separator, 13, reflux pump, 14, sledge piece base.
Embodiment
The utility model is described in further detail below in conjunction with the drawings and specific embodiments.
The Sweet natural gas degree of depth deacidifying device of a kind of skid-mounted of the present utility model, its structure comprises unstripped gas separator 1, pre-extracting tower 2, degree of depth extracting tower 3, purge gas separator 4, rich solution flash tank 5, poor rich liquid heat exchanger 6, lean solution water cooler 7, lean pump 8, amine liquid regenerator column 9, reboiler 10, carbon dioxide cooler 11, carbonic acid gas gas-liquid separator 12 and reflux pump 13, and above-mentioned each device all is installed on the sledge piece base 14.
Unstripped gas separator 1 is communicated with pre-extracting tower 2, degree of depth extracting tower 3 respectively by pipeline, and amine liquid regenerator column 9 is communicated with pre-extracting tower 2, degree of depth extracting tower 3 respectively by pipeline; On amine liquid regenerator column 9 and the pipeline that pre-extracting tower 2, degree of depth extracting tower 3 are communicated with poor rich liquid heat exchanger 6, lean solution water cooler 7 and lean pump 8 are installed successively, on the pipeline between extracting tower 2 and degree of depth extracting tower 3 and the amine liquid regenerator column 9 rich solution flash tank 5 are installed also in advance in addition; The top of degree of depth extracting tower 3 is connected with purge gas separator 4 by pipeline; The bottom of amine liquid regenerator column 9 is connected with reboiler 10; The top of amine liquid regenerator column 9 connects carbon dioxide cooler 11, carbonic acid gas gas-liquid separator 12 and reflux pump 13 successively by pipeline.
When acid gas components content is at 20～10%V in the unstripped gas, be introduced into pre-extracting tower 2, unstripped gas is carried out pre-depickling handle, acid gas components is reduced to enters degree of depth extracting tower below 10% again; When acid gas components content in the unstripped gas when 10%V is following, then directly enter degree of depth extracting tower 3 and remove sour gas, its content is removed to≤50ppm, satisfy the natural gas liquefaction requirement.
Its processing and fabricating of Sweet natural gas degree of depth deacidifying device of a kind of skid-mounted of the present utility model is very simple and convenient, and processing and fabricating gets final product shown in the by specification accompanying drawing.
Except that the described technical characterictic of specification sheets, be the known technology of those skilled in the art.
Claims (7)
1. the Sweet natural gas degree of depth deacidifying device of a skid-mounted, comprise unstripped gas separator, pre-extracting tower, degree of depth extracting tower, purge gas separator, rich solution flash tank, poor rich liquid heat exchanger, lean solution water cooler, lean pump, amine liquid regenerator column, reboiler, carbon dioxide cooler, carbonic acid gas gas-liquid separator and reflux pump, it is characterized in that above-mentioned each device all is installed on the sledge piece base.
2. the Sweet natural gas degree of depth deacidifying device of skid-mounted according to claim 1, it is characterized in that described unstripped gas separator is communicated with pre-extracting tower, degree of depth extracting tower respectively by pipeline, amine liquid regenerator column is communicated with pre-extracting tower, degree of depth extracting tower respectively by pipeline.
3. the Sweet natural gas degree of depth deacidifying device of skid-mounted according to claim 1 and 2 is characterized in that on described amine liquid regenerator column and the pipeline that pre-extracting tower, degree of depth extracting tower are communicated with poor rich liquid heat exchanger, lean solution water cooler and lean pump being installed successively.
4. the Sweet natural gas degree of depth deacidifying device of skid-mounted according to claim 1 and 2 is characterized in that the bottom of described amine liquid regenerator column is connected with reboiler.
5. the Sweet natural gas degree of depth deacidifying device of skid-mounted according to claim 1 and 2 is characterized in that on the pipeline between described pre-extracting tower and degree of depth extracting tower and the amine liquid regenerator column rich solution flash tank being installed.
6. the Sweet natural gas degree of depth deacidifying device of skid-mounted according to claim 1 and 2 is characterized in that the top of described degree of depth extracting tower is connected with purge gas separator by pipeline.
7. the Sweet natural gas degree of depth deacidifying device of skid-mounted according to claim 1 and 2 is characterized in that the top of described amine liquid regenerator column connects carbon dioxide cooler, carbonic acid gas gas-liquid separator and reflux pump successively by pipeline.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010205125176U CN201834898U (en) | 2010-09-01 | 2010-09-01 | Skid-mounted deep natural gas deacidification apparatus |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010205125176U CN201834898U (en) | 2010-09-01 | 2010-09-01 | Skid-mounted deep natural gas deacidification apparatus |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201834898U true CN201834898U (en) | 2011-05-18 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2010205125176U Expired - Lifetime CN201834898U (en) | 2010-09-01 | 2010-09-01 | Skid-mounted deep natural gas deacidification apparatus |
Country Status (1)
| Country | Link |
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| CN (1) | CN201834898U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103509619A (en) * | 2012-06-30 | 2014-01-15 | 中国石油化工股份有限公司 | Regeneration, condensation and separation integrated device and regeneration process for LNG (liquefied natural gas) amine method decarbonization process |
| CN103585778A (en) * | 2013-11-28 | 2014-02-19 | 西北大学 | Skid-mounted modular double-tower experimental device |
-
2010
- 2010-09-01 CN CN2010205125176U patent/CN201834898U/en not_active Expired - Lifetime
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103509619A (en) * | 2012-06-30 | 2014-01-15 | 中国石油化工股份有限公司 | Regeneration, condensation and separation integrated device and regeneration process for LNG (liquefied natural gas) amine method decarbonization process |
| CN103585778A (en) * | 2013-11-28 | 2014-02-19 | 西北大学 | Skid-mounted modular double-tower experimental device |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CP01 | Change in the name or title of a patent holder |
Address after: 100010 Beijing City, Dongcheng District Chaoyangmen North Street, No. 25 building, Chinese CNOOC Offshore Oil Corporation, the Ministry of science and technology Co-patentee after: Offshore Oil Engineering Co., Ltd. Patentee after: China Offshore Oil Group Co., Ltd. Co-patentee after: CNOOC Petrochemical Engineering Co Ltd Address before: 100010 Beijing City, Dongcheng District Chaoyangmen North Street, No. 25 building, Chinese CNOOC Offshore Oil Corporation, the Ministry of science and technology Co-patentee before: Offshore Oil Engineering Co., Ltd. Patentee before: China National Offshore Oil Corporation Co-patentee before: China National Offshore Oil Shandong Chemical Engineering Co., Ltd. |
|
| CP01 | Change in the name or title of a patent holder | ||
| CX01 | Expiry of patent term |
Granted publication date: 20110518 |
|
| CX01 | Expiry of patent term |