SG11201906217PA - Isomerization process using feedstock containing dissolved hydrogen - Google Patents
Isomerization process using feedstock containing dissolved hydrogenInfo
- Publication number
- SG11201906217PA SG11201906217PA SG11201906217PA SG11201906217PA SG11201906217PA SG 11201906217P A SG11201906217P A SG 11201906217PA SG 11201906217P A SG11201906217P A SG 11201906217PA SG 11201906217P A SG11201906217P A SG 11201906217PA SG 11201906217P A SG11201906217P A SG 11201906217PA
- Authority
- SG
- Singapore
- Prior art keywords
- international
- pct
- phase
- dissolved hydrogen
- high octane
- Prior art date
Links
- 229910052739 hydrogen Inorganic materials 0.000 title abstract 3
- 239000001257 hydrogen Substances 0.000 title abstract 3
- 238000006317 isomerization reaction Methods 0.000 title abstract 3
- 238000000034 method Methods 0.000 title abstract 3
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 title abstract 2
- 239000007788 liquid Substances 0.000 abstract 3
- TVMXDCGIABBOFY-UHFFFAOYSA-N octane Chemical compound CCCCCCCC TVMXDCGIABBOFY-UHFFFAOYSA-N 0.000 abstract 3
- 239000012071 phase Substances 0.000 abstract 3
- 238000006243 chemical reaction Methods 0.000 abstract 2
- 239000003795 chemical substances by application Substances 0.000 abstract 2
- 238000002156 mixing Methods 0.000 abstract 2
- 239000003054 catalyst Substances 0.000 abstract 1
- 150000002431 hydrogen Chemical class 0.000 abstract 1
- 238000010348 incorporation Methods 0.000 abstract 1
- 238000004519 manufacturing process Methods 0.000 abstract 1
- 230000008520 organization Effects 0.000 abstract 1
- 239000007790 solid phase Substances 0.000 abstract 1
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
- C10G45/00—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds
- C10G45/58—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to change the structural skeleton of some of the hydrocarbon content without cracking the other hydrocarbons present, e.g. lowering pour point; Selective hydrocracking of normal paraffins
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C5/00—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms
- C07C5/22—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms by isomerisation
- C07C5/27—Rearrangement of carbon atoms in the hydrocarbon skeleton
- C07C5/2767—Changing the number of side-chains
- C07C5/277—Catalytic processes
- C07C5/2791—Catalytic processes with metals
-
- 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
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2523/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00
- C07C2523/38—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of noble metals
- C07C2523/40—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of noble metals of the platinum group metals
- C07C2523/42—Platinum
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2527/00—Catalysts comprising the elements or compounds of halogens, sulfur, selenium, tellurium, phosphorus or nitrogen; Catalysts comprising carbon compounds
- C07C2527/06—Halogens; Compounds thereof
- C07C2527/125—Compounds comprising a halogen and scandium, yttrium, aluminium, gallium, indium or thallium
- C07C2527/126—Aluminium chloride
-
- 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
- C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
- C10G2300/20—Characteristics of the feedstock or the products
- C10G2300/30—Physical properties of feedstocks or products
- C10G2300/305—Octane number, e.g. motor octane number [MON], research octane number [RON]
-
- 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
- C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
- C10G2300/40—Characteristics of the process deviating from typical ways of processing
- C10G2300/42—Hydrogen of special source or of special composition
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- General Chemical & Material Sciences (AREA)
- Crystallography & Structural Chemistry (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
- Catalysts (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
International Patent Classification: ClOG 45/58 (2006.01) ClOG 65/04 (2006.01) (21) International Application Number: PCT/US2018/014195 (22) International Filing Date: 18 January 2018 (18.01.2018) (25) Filing Language: English (26) Publication Language: English (30) Priority Data: 15/417,897 27 January 2017 (27.01.2017) US (71) Applicant: SAUDI ARABIAN OIL COMPANY [SA/SA]; Box 5000, Dhahran, 31311 (SA). (72) Inventor; and (71) Applicant (for US only): KOSEOGLU, Omer, Refa [US/SA]; P.o. Box 8560, Saudi Aramco, Dhahran, 31311 (SA). (74) Agent: CRISPINO, Ralph, J.; Abelman, Frayne & Sch- wab, 666 Third Avenue, New York, NY 10017-5621 (US). (81) Designated States (unless otherwise indicated, for every kind of national protection available): AE, AG, AL, AM, AO, AT, AU, AZ, BA, BB, BG, BH, BN, BR, BW, BY, BZ, CA, CH, CL, CN, CO, CR, CU, CZ, DE, DJ, DK, DM, DO, DZ, EC, EE, EG, ES, FI, GB, GD, GE, GH, GM, GT, HN, HR, HU, ID, IL, IN, IR, IS, JO, JP, KE, KG, KH, KN, KP, KR, KW, KZ, LA, LC, LK, LR, LS, LU, LY, MA, MD, ME, MG, MK, MN, MW, MX, MY, MZ, NA, NG, NI, NO, NZ, OM, PA, PE, PG, PH, PL, PT, QA, RO, RS, RU, RW, SA, SC, SD, SE, SG, SK, SL, SM, ST, SV, SY, TH, TJ, TM, TN, TR, TT, TZ, UA, UG, US, UZ, VC, VN, ZA, ZM, ZW. (84) Designated States (unless otherwise indicated, for every kind of regional protection available): ARIPO (BW, GH, GM, KE, LR, LS, MW, MZ, NA, RW, SD, SL, ST, SZ, TZ, UG, ZM, ZW), Eurasian (AM, AZ, BY, KG, KZ, RU, TJ, TM), European (AL, AT, BE, BG, CH, CY, CZ, DE, DK, EE, ES, FI, FR, GB, GR, HR, HU, IE, IS, IT, LT, LU, LV, MC, MK, MT, NL, NO, PL, PT, RO, RS, SE, SI, SK, SM, (54) Title: ISOMERIZATION PROCESS USING FEEDSTOCK CONTAINING DISSOLVED HYDROGEN 100 156 FIG. 1 N O 00 O O (12) INTERNATIONAL APPLICATION PUBLISHED UNDER THE PATENT COOPERATION TREATY (PCT) (19) World Intellectual Property Organization International Bureau (43) International Publication Date 02 August 2018 (02.08.2018) WIP0 I PCT °Ens °nolo olomoliololomilioluom (10) International Publication Number WO 2018/140279 Al (57) : A process and system is provided including hydroisomerization reaction zone for production of high octane gasoline blending components that provide high selectivity for producing high octane isomers of light paraffins. A light paraffm feed is enriched by incorporation of dissolved hydrogen, thereby permitting a reaction phase that is liquid or substantially liquid to produce high octane gasoline blending components. Accordingly, a substantially two phase isomerization reactor system is provided, with a hydrogen- enriched liquid feedstock phase and a solid phase catalyst. [Continued on next page] WO 2018/140279 Al MIDEDIMOMMIONE1013010M011010FIMMOVOIMIE TR), OAPI (BF, BJ, CF, CG, CI, CM, GA, GN, GQ, GW, KM, ML, MR, NE, SN, TD, TG). Published: — with international search report (Art. 21(3))
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US15/417,897 US20180215683A1 (en) | 2017-01-27 | 2017-01-27 | Isomerization process using feedstock containing dissolved hydrogen |
PCT/US2018/014195 WO2018140279A1 (en) | 2017-01-27 | 2018-01-18 | Isomerization process using feedstock containing dissolved hydrogen |
Publications (1)
Publication Number | Publication Date |
---|---|
SG11201906217PA true SG11201906217PA (en) | 2019-08-27 |
Family
ID=61569401
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
SG11201906217PA SG11201906217PA (en) | 2017-01-27 | 2018-01-18 | Isomerization process using feedstock containing dissolved hydrogen |
Country Status (7)
Country | Link |
---|---|
US (1) | US20180215683A1 (en) |
EP (1) | EP3574063A1 (en) |
JP (1) | JP2020506265A (en) |
KR (1) | KR20190108593A (en) |
CN (1) | CN110234743A (en) |
SG (1) | SG11201906217PA (en) |
WO (1) | WO2018140279A1 (en) |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US11084991B2 (en) * | 2019-06-25 | 2021-08-10 | Saudi Arabian Oil Company | Two-phase moving bed reactor utilizing hydrogen-enriched feed |
US11873455B2 (en) * | 2020-12-30 | 2024-01-16 | Chevron U.S.A. Inc. | Process having improved base oil yield |
DE102021110092A1 (en) * | 2021-04-21 | 2022-10-27 | Clariant International Ltd | LIGHT PETROL ISOMERIZATION PLANT AND PROCESS |
Family Cites Families (25)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3378349A (en) | 1965-09-17 | 1968-04-16 | Air Prod & Chem | Apparatus for treating mixed-phase fluid reactants |
US3598541A (en) | 1969-06-23 | 1971-08-10 | Universal Oil Prod Co | Fluid contacting apparatus for fluid-solid contacting chambers |
GB1397051A (en) | 1973-01-23 | 1975-06-11 | British Petroleum Co | Multi-bed reactors |
US4804803A (en) * | 1987-12-07 | 1989-02-14 | Uop Inc. | Isomerization with once-through hydrogen |
US4783575A (en) * | 1987-12-17 | 1988-11-08 | Uop Inc. | Isomerization with cyclic hydrocarbon conversion |
US4960571A (en) | 1988-12-14 | 1990-10-02 | Exxon Research And Engineering Company | Quench assembly design |
US5294328A (en) * | 1990-05-24 | 1994-03-15 | Uop | Production of reformulated gasoline |
US5158714A (en) | 1991-05-30 | 1992-10-27 | Union Oil Company Of California | Vapor-liquid distribution method and apparatus |
FR2679245B1 (en) * | 1991-07-18 | 1993-11-05 | Institut Francais Petrole | PROCESS FOR ISOMERIZING NORMAL C5 / C6 PARAFFINS WITH RECYCLING NORMAL PARAFFINS. |
JPH0662957B2 (en) * | 1991-08-26 | 1994-08-17 | ユーオーピー | Integrated isomerization and adsorption method for C5 and C6 hydrocarbon reforming |
FR2688213B1 (en) * | 1992-03-06 | 1995-05-24 | Inst Francais Du Petrole | PROCESS FOR THE ISOMERIZATION OF NORMAL C5 / C6 PARAFFINS WITH RECYCLING OF NORMAL PARAFFINS AND METHYL-PENTANES. |
US5484578A (en) | 1994-06-20 | 1996-01-16 | Mobil Oil Corporation | Two-phase distributor system for downflow reactors |
US5837208A (en) | 1996-06-12 | 1998-11-17 | Uop | Hydroprocessing reactor mixer/distributor |
US5942197A (en) | 1996-08-23 | 1999-08-24 | Exxon Research And Engineering Co | Countercurrent reactor |
JP2001040367A (en) * | 1999-01-21 | 2001-02-13 | Japan Energy Corp | Isomerization method for hydrocarbon, solid acid catalyst used therein, and isomerization apparatus |
US7015175B2 (en) * | 2001-08-29 | 2006-03-21 | Uop Llc | High-activity isomerization catalyst and process |
JP2003277769A (en) * | 2002-03-27 | 2003-10-02 | Japan Energy Corp | Method for isomerization of hydrocarbon |
US20040247498A1 (en) * | 2003-06-04 | 2004-12-09 | Jonathan Phillips | Catalytic reactor system |
JP4851197B2 (en) * | 2006-02-17 | 2012-01-11 | Jx日鉱日石エネルギー株式会社 | Method for producing gasoline base material and gasoline composition |
CN103857771B (en) * | 2011-07-29 | 2016-06-01 | 沙特阿拉伯石油公司 | For the ebullated bed method of the raw material containing the hydrogen dissolved |
US8951406B2 (en) * | 2011-07-29 | 2015-02-10 | Saudi Arabian Oil Company | Hydrogen-enriched feedstock for fluidized catalytic cracking process |
US20130165713A1 (en) * | 2011-12-21 | 2013-06-27 | Chevron U.S.A. Inc. | Isomerization of light paraffins |
US20140171706A1 (en) * | 2012-12-14 | 2014-06-19 | Uop Llc | Methods and apparatuses for forming low-aromatic high-octane product streams |
US9669382B2 (en) * | 2013-12-20 | 2017-06-06 | Uop Llc | Methods and apparatuses for isomerizing hydrocarbons |
CN105602619B (en) * | 2015-12-18 | 2017-10-17 | 中国石油天然气股份有限公司 | A kind of liquid-phase hydrogenatin heterogeneous system and its technique and application |
-
2017
- 2017-01-27 US US15/417,897 patent/US20180215683A1/en not_active Abandoned
-
2018
- 2018-01-18 WO PCT/US2018/014195 patent/WO2018140279A1/en unknown
- 2018-01-18 JP JP2019540560A patent/JP2020506265A/en active Pending
- 2018-01-18 EP EP18709179.8A patent/EP3574063A1/en not_active Withdrawn
- 2018-01-18 SG SG11201906217PA patent/SG11201906217PA/en unknown
- 2018-01-18 CN CN201880008634.8A patent/CN110234743A/en active Pending
- 2018-01-18 KR KR1020197023698A patent/KR20190108593A/en not_active Application Discontinuation
Also Published As
Publication number | Publication date |
---|---|
US20180215683A1 (en) | 2018-08-02 |
EP3574063A1 (en) | 2019-12-04 |
KR20190108593A (en) | 2019-09-24 |
JP2020506265A (en) | 2020-02-27 |
WO2018140279A1 (en) | 2018-08-02 |
CN110234743A (en) | 2019-09-13 |
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