IN171273B - - Google Patents
Info
- Publication number
- IN171273B IN171273B IN401/MAS/88A IN401MA1988A IN171273B IN 171273 B IN171273 B IN 171273B IN 401MA1988 A IN401MA1988 A IN 401MA1988A IN 171273 B IN171273 B IN 171273B
- Authority
- IN
- India
- Prior art keywords
- hydrogen
- stream
- hydrocarbons
- absorber
- hot
- Prior art date
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G65/00—Treatment of hydrocarbon oils by two or more hydrotreatment processes only
- C10G65/02—Treatment of hydrocarbon oils by two or more hydrotreatment processes only plural serial stages only
- C10G65/04—Treatment of hydrocarbon oils by two or more hydrotreatment processes only plural serial stages only including only refining steps
- C10G65/043—Treatment of hydrocarbon oils by two or more hydrotreatment processes only plural serial stages only including only refining steps at least one step being a change in the structural skeleton
Abstract
Processing and apparatus are provided for upgrading the octane of a mixed hydrocarbon gasoline feedstock by an integrated adsorption-isomerization process which catalytically isomerizes normal paraffinic hydrocarbons and concentrates non-normals in a product stream, in both the reactor-lead and absorber-lead configuration. The process includes passing an absorber feed stream comprising hydrogen as well as hydrocarbons to an absorbent bed to absorb normal hydrocarbons. The hydrogen is preferably obtained from a hot hydrogen-containing process stream which is not cooled or separated into component parts prior to forming the absorber feed. In some embodiments, the hot-hydrogen containing stream comes from reactor effluent and in others from desorption effluent. According to the invention, the only hydrogen which will require cooling and separation from a hydrocarbon component is that which is recycled for desorption. The invention provides improved energy efficiency and can reduce equipment size and complexity.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US6276287A | 1987-06-15 | 1987-06-15 |
Publications (1)
Publication Number | Publication Date |
---|---|
IN171273B true IN171273B (en) | 1992-08-29 |
Family
ID=22044632
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
IN401/MAS/88A IN171273B (en) | 1987-06-15 | 1988-06-14 |
Country Status (11)
Country | Link |
---|---|
EP (1) | EP0295638B1 (en) |
JP (1) | JPH0639406B2 (en) |
AT (1) | ATE67234T1 (en) |
AU (1) | AU602587B2 (en) |
CA (1) | CA1314568C (en) |
DE (1) | DE3864755D1 (en) |
DK (1) | DK322788A (en) |
ES (1) | ES2024591B3 (en) |
GR (1) | GR3002763T3 (en) |
IN (1) | IN171273B (en) |
NO (1) | NO882612L (en) |
Families Citing this family (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2799202B1 (en) * | 1999-09-30 | 2002-04-26 | Inst Francais Du Petrole | PROCESS FOR PRODUCING ESSENCES WITH IMPROVED OCTANE INDEX |
US20050137443A1 (en) * | 2003-12-19 | 2005-06-23 | Gorawara Jayant K. | Regenerative removal of trace carbon monoxide |
US7687674B2 (en) * | 2006-12-28 | 2010-03-30 | Uop Llc | Low temperature process for recovering and producing para-xylene and heat exchange network therefore |
US9669382B2 (en) * | 2013-12-20 | 2017-06-06 | Uop Llc | Methods and apparatuses for isomerizing hydrocarbons |
Family Cites Families (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4210771A (en) * | 1978-11-02 | 1980-07-01 | Union Carbide Corporation | Total isomerization process |
GB8526812D0 (en) * | 1985-10-31 | 1985-12-04 | Shell Int Research | Separating branch-from unbranched hydrocarbons |
-
1988
- 1988-06-14 AT AT88109494T patent/ATE67234T1/en not_active IP Right Cessation
- 1988-06-14 DK DK322788A patent/DK322788A/en not_active Application Discontinuation
- 1988-06-14 AU AU17655/88A patent/AU602587B2/en not_active Ceased
- 1988-06-14 ES ES88109494T patent/ES2024591B3/en not_active Expired - Lifetime
- 1988-06-14 DE DE8888109494T patent/DE3864755D1/en not_active Expired - Fee Related
- 1988-06-14 IN IN401/MAS/88A patent/IN171273B/en unknown
- 1988-06-14 NO NO882612A patent/NO882612L/en unknown
- 1988-06-14 EP EP88109494A patent/EP0295638B1/en not_active Expired - Lifetime
- 1988-06-14 CA CA000569447A patent/CA1314568C/en not_active Expired - Fee Related
- 1988-06-15 JP JP63145605A patent/JPH0639406B2/en not_active Expired - Lifetime
-
1991
- 1991-09-19 GR GR91401374T patent/GR3002763T3/en unknown
Also Published As
Publication number | Publication date |
---|---|
AU1765588A (en) | 1988-12-15 |
ATE67234T1 (en) | 1991-09-15 |
EP0295638A1 (en) | 1988-12-21 |
DK322788A (en) | 1988-12-16 |
GR3002763T3 (en) | 1993-01-25 |
JPH01221334A (en) | 1989-09-04 |
ES2024591B3 (en) | 1992-03-01 |
JPH0639406B2 (en) | 1994-05-25 |
DK322788D0 (en) | 1988-06-14 |
DE3864755D1 (en) | 1991-10-17 |
EP0295638B1 (en) | 1991-09-11 |
NO882612D0 (en) | 1988-06-14 |
AU602587B2 (en) | 1990-10-18 |
NO882612L (en) | 1988-12-16 |
CA1314568C (en) | 1993-03-16 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
ES8504903A1 (en) | Hydrocarbon conversion process | |
EP0334114A3 (en) | Membrane process for hydrocarbon liquid recovery | |
GB1329025A (en) | Process and apparatus for contacting a liquid with solid particles | |
MX9704351A (en) | Process for the removal of mercaptans and hydrogen sulfide from hydrocarbon streams. | |
DE3263440D1 (en) | Recovery of c3+hydrocarbon conversion products and net excess hydrogen in a catalytic reforming process | |
ES420173A1 (en) | Catalytic cracking of naphtha and gas oil | |
ZA888821B (en) | Olefins production process | |
ES352795A1 (en) | Purifying make hydrogen in a catalytic reforming process | |
IN160757B (en) | ||
CA2192553A1 (en) | Process for reforming hydrocarbon feedstocks over a sulfur sensitive catalyst | |
IN171273B (en) | ||
RU97113155A (en) | METHANE PROCESSING METHOD (OPTIONS) | |
US2465462A (en) | Catalytic synthesis of hydrocarbons | |
US3248317A (en) | Combination of hydrogen producing and hydrogen consuming units | |
GB1190089A (en) | Olefin Producing Process | |
DE3569721D1 (en) | Hf alkylation with product recycle employing two reactors | |
US3208199A (en) | Method for recovering hydrogen from light gaseous materials | |
JPH0734073A (en) | Hydrogenation of petroleum and hydrogenation apparatus | |
US2380324A (en) | Method of treating and removing finely divided solid material | |
US2623009A (en) | Regenerative aluminum chloride process | |
JPS58187489A (en) | Selective removal of nh3 and h2s from hydrocarbon substance | |
SU1189504A1 (en) | Method of flotation of coal | |
JPS6424895A (en) | Refining coke-oven gas | |
FR2378847A1 (en) | Two=stage catalytic hydrocarbon cracking - with co-current and counter current reaction stages | |
SU1818835A1 (en) | Method for upgrading of oil residual stock |