GB1202787A - Gas dehydration - Google Patents
Gas dehydrationInfo
- Publication number
- GB1202787A GB1202787A GB5641268A GB5641268A GB1202787A GB 1202787 A GB1202787 A GB 1202787A GB 5641268 A GB5641268 A GB 5641268A GB 5641268 A GB5641268 A GB 5641268A GB 1202787 A GB1202787 A GB 1202787A
- Authority
- GB
- United Kingdom
- Prior art keywords
- bed
- water separator
- free water
- line
- effluent
- 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.)
- Expired
Links
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B21/00—Arrangements or duct systems, e.g. in combination with pallet boxes, for supplying and controlling air or gases for drying solid materials or objects
- F26B21/06—Controlling, e.g. regulating, parameters of gas supply
- F26B21/08—Humidity
- F26B21/083—Humidity by using sorbent or hygroscopic materials, e.g. chemical substances, molecular sieves
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/02—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography
- B01D53/04—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography with stationary adsorbents
- B01D53/0454—Controlling adsorption
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/26—Drying gases or vapours
- B01D53/261—Drying gases or vapours by adsorption
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C7/00—Purification; Separation; Use of additives
- C07C7/12—Purification; Separation; Use of additives by adsorption, i.e. purification or separation of hydrocarbons with the aid of solids, e.g. with ion-exchangers
- C07C7/13—Purification; Separation; Use of additives by adsorption, i.e. purification or separation of hydrocarbons with the aid of solids, e.g. with ion-exchangers by molecular-sieve technique
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Analytical Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Chemistry (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Water Supply & Treatment (AREA)
- Drying Of Gases (AREA)
Abstract
1,202,787. Drying natural gas. UNION CARBIDE CORP. 28 Nov., 1968 [29 Nov., 1967], No. 56412/68. Heading B1L. Wellhead natural gas is dried by passing the feed by line 3, through free water separator 4, to zeolite molecular sieve bed 1, valve 10 being open and 13 closed. 1-10% sidestream of the feed is passed by line 9, through heater 12, where it is heated to 500-700‹F. and thence downward through exhausted bed 2, thereby regenerating it, valve 14 being open and 11 closed. Dry effluent from bed 1 leaves by lines 15, 20 and 21, while wet effluent from bed 2 passes by lines 16 and 24 to cooler 25 and free water separator 23; the two effluents are then mixed in line 19 as the product gas. When bed 1 is exhausted the roles of the two beds are reversed. Suitable zeolites are types A, D, S, R, T or X having a pore size of 3-10A. In a modification (see Fig. 2, not shown), the effluents from each bed are passed in heat exchange relationship with each other, before each passes to its own free water separator, the gaseous effluent from the two separators being combined.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CA6309 | 1967-11-29 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB1202787A true GB1202787A (en) | 1970-08-19 |
Family
ID=4083922
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB5641268A Expired GB1202787A (en) | 1967-11-29 | 1968-11-28 | Gas dehydration |
Country Status (5)
Country | Link |
---|---|
BE (1) | BE724734A (en) |
DE (1) | DE1811310A1 (en) |
FR (1) | FR1595863A (en) |
GB (1) | GB1202787A (en) |
NL (1) | NL6817148A (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102732348A (en) * | 2012-07-06 | 2012-10-17 | 四川金星石油化工机械设备有限公司 | Separator used for CNG (compressed natural gas) dehydrating device |
CN103254955A (en) * | 2013-05-02 | 2013-08-21 | 中国海洋石油总公司 | Closed-type three-tower molecular sieve dehydration device |
WO2014099622A1 (en) * | 2012-12-18 | 2014-06-26 | Invista North America S.A.R.L. | Apparatus and method for decreasing humidity during an andrussow process |
CN111089935A (en) * | 2018-10-24 | 2020-05-01 | 中国石油化工股份有限公司 | On-site natural gas dry desulfurizing agent sulfur capacity testing method |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE3022583A1 (en) * | 1980-06-16 | 1981-12-17 | Rudolf Prof. Dr. 8000 München Sizmann | METHOD FOR THE USE AND STORAGE OF ENERGY FROM THE ENVIRONMENT |
-
1968
- 1968-11-28 DE DE19681811310 patent/DE1811310A1/en active Pending
- 1968-11-28 GB GB5641268A patent/GB1202787A/en not_active Expired
- 1968-11-29 FR FR1595863D patent/FR1595863A/fr not_active Expired
- 1968-11-29 BE BE724734D patent/BE724734A/xx unknown
- 1968-11-29 NL NL6817148A patent/NL6817148A/xx unknown
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102732348A (en) * | 2012-07-06 | 2012-10-17 | 四川金星石油化工机械设备有限公司 | Separator used for CNG (compressed natural gas) dehydrating device |
WO2014099622A1 (en) * | 2012-12-18 | 2014-06-26 | Invista North America S.A.R.L. | Apparatus and method for decreasing humidity during an andrussow process |
CN103254955A (en) * | 2013-05-02 | 2013-08-21 | 中国海洋石油总公司 | Closed-type three-tower molecular sieve dehydration device |
CN103254955B (en) * | 2013-05-02 | 2014-12-24 | 中国海洋石油总公司 | Closed-type three-tower molecular sieve dehydration device |
CN111089935A (en) * | 2018-10-24 | 2020-05-01 | 中国石油化工股份有限公司 | On-site natural gas dry desulfurizing agent sulfur capacity testing method |
Also Published As
Publication number | Publication date |
---|---|
NL6817148A (en) | 1969-06-02 |
DE1811310A1 (en) | 1969-07-10 |
BE724734A (en) | 1969-05-29 |
FR1595863A (en) | 1970-06-15 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
PS | Patent sealed | ||
PLNP | Patent lapsed through nonpayment of renewal fees |