GB1008335A - Two-stage adsorption process - Google Patents
Two-stage adsorption processInfo
- Publication number
- GB1008335A GB1008335A GB1171163A GB1171163A GB1008335A GB 1008335 A GB1008335 A GB 1008335A GB 1171163 A GB1171163 A GB 1171163A GB 1171163 A GB1171163 A GB 1171163A GB 1008335 A GB1008335 A GB 1008335A
- Authority
- GB
- United Kingdom
- Prior art keywords
- zone
- olefins
- sulphur
- adsorb
- molecular sieve
- 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
-
- 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
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2253/00—Adsorbents used in seperation treatment of gases and vapours
- B01D2253/10—Inorganic adsorbents
- B01D2253/106—Silica or silicates
- B01D2253/108—Zeolites
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2253/00—Adsorbents used in seperation treatment of gases and vapours
- B01D2253/30—Physical properties of adsorbents
- B01D2253/302—Dimensions
- B01D2253/308—Pore size
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2256/00—Main component in the product gas stream after treatment
- B01D2256/24—Hydrocarbons
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2259/00—Type of treatment
- B01D2259/40—Further details for adsorption processes and devices
- B01D2259/402—Further details for adsorption processes and devices using two beds
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2259/00—Type of treatment
- B01D2259/40—Further details for adsorption processes and devices
- B01D2259/41—Further details for adsorption processes and devices using plural beds of the same adsorbent in series
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2259/00—Type of treatment
- B01D2259/40—Further details for adsorption processes and devices
- B01D2259/414—Further details for adsorption processes and devices using different types of adsorbents
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)
- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
- Treatment Of Liquids With Adsorbents In General (AREA)
Abstract
A process for removing aromatics, sulphur, and olefins from hydrocarbon feed streams comprises vaporizing the feed passing over a first adsorption zone containing a 6-15 <\>rA zeolitic molecular sieve of uniform pore size to adsorb aromatics and sulphur, condensing the vapour, and passing the condensate through a second adsorption zone containing a 6-15 <\>rA zeolitic molecular sieve of uniform pore size whilst maintaining a liquid phase in the second zone, to adsorb the olefins. The preferred conditions in the two zones are:- .Feed rate .. ...0.1-10.0 w./w./hr .Pressure .. ...0-100 p.s.i.a .Temperature:-. .First zone .. ...150-500 DEG F .Second zone ...0-200 DEG F Preferably the zeolite is of the formula:- 0.9\sB0.2 M2 nO: Al2O3: 2.5\sB0.5 SiO2 where M is a cation of valency n, for example magnesium, barium, or sodium, which last may be at least in part replaced by calcium. The purified hydrocarbon feed may be passed to an isomerization process.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB1171163A GB1008335A (en) | 1963-03-25 | 1963-03-25 | Two-stage adsorption process |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB1171163A GB1008335A (en) | 1963-03-25 | 1963-03-25 | Two-stage adsorption process |
Publications (1)
Publication Number | Publication Date |
---|---|
GB1008335A true GB1008335A (en) | 1965-10-27 |
Family
ID=9991282
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB1171163A Expired GB1008335A (en) | 1963-03-25 | 1963-03-25 | Two-stage adsorption process |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB1008335A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2000050154A1 (en) * | 1999-02-22 | 2000-08-31 | Engelhard Corporation | Humidity swing adsorption process and apparatus |
-
1963
- 1963-03-25 GB GB1171163A patent/GB1008335A/en not_active Expired
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2000050154A1 (en) * | 1999-02-22 | 2000-08-31 | Engelhard Corporation | Humidity swing adsorption process and apparatus |
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