GB1338612A - Aromatic gasoline production - Google Patents

Aromatic gasoline production

Info

Publication number
GB1338612A
GB1338612A GB5968970A GB5968970A GB1338612A GB 1338612 A GB1338612 A GB 1338612A GB 5968970 A GB5968970 A GB 5968970A GB 5968970 A GB5968970 A GB 5968970A GB 1338612 A GB1338612 A GB 1338612A
Authority
GB
United Kingdom
Prior art keywords
stream
gasoline
hydrocarbons
reforming
line
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
Application number
GB5968970A
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Universal Oil Products Co
Original Assignee
Universal Oil Products Co
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Universal Oil Products Co filed Critical Universal Oil Products Co
Publication of GB1338612A publication Critical patent/GB1338612A/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/04Liquid carbonaceous fuels essentially based on blends of hydrocarbons
    • C10L1/06Liquid carbonaceous fuels essentially based on blends of hydrocarbons for spark ignition
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING 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
    • C10G59/00Treatment of naphtha by two or more reforming processes only or by at least one reforming process and at least one process which does not substantially change the boiling range of the naphtha
    • C10G59/02Treatment of naphtha by two or more reforming processes only or by at least one reforming process and at least one process which does not substantially change the boiling range of the naphtha plural serial stages only
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING 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
    • C10G63/00Treatment of naphtha by at least one reforming process and at least one other conversion process
    • C10G63/02Treatment of naphtha by at least one reforming process and at least one other conversion process plural serial stages only
    • C10G63/04Treatment of naphtha by at least one reforming process and at least one other conversion process plural serial stages only including at least one cracking step
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00Liquid carbonaceous fuels
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/02Liquid carbonaceous fuels essentially based on components consisting of carbon, hydrogen, and oxygen only
    • C10L1/023Liquid carbonaceous fuels essentially based on components consisting of carbon, hydrogen, and oxygen only for spark ignition

Abstract

1338612 Cracking and reforming naphtha UNIVERSAL OIL PRODUCTS CO 16 Dec 1970 [17 Dec 1969] 59689/70 Heading C5E An aromatic gasoline and saturated and unsaturated hydrocarbons having three or four carbon atoms in the molecule are made from a feedstock comprising both alkanes and naphthenes boiling in the range 82‹ to 204‹ C. by first reforming the feed under conditions to convert more than 80% of the naphthenes but less than 40% of the alkanes to aromatics, then separating the product into an aromatic gasoline stream and a saturated hydrocarbon stream by solvent extraction and finally cracking the saturated stream in a fluidized bed of catalyst without added hydrogen. The hydrocarbons of three or four carbon atoms may be used to make alkylate gasoline, or hydrolysed to alcohols or converted to amines, esters, ethers or ketones, all of which can be used as gasoline components. Suitable feedstocks are straight-run gasoline, natural gasolines, and thermally or catalytically cracked gasolines, and may be of full boiling range, or higher-boiling fractions only. Catalysts for the reforming step comprise carriers such as alumina, faujasite, mordenite or combinations of these and a reactive metal component such as Fe, Co, Ni, Ru, Rh, Pd, Os, Ir, Pt or Re and may also contain a combined halogen. The catalyst may be fluidized or otherwise moving, but is preferably in a fixed bed. Catalysts for the cracking step are silica-alumina, silica-magnesia, silica-zirconia and zeolites, natural or synthetic, and may be compounded by ion-exchange or impregnation with alkali metals, alkaline-earth metals, rare-earth metals or metals of Group VIII. As shown, feed in line 20 and hydrogen in line 21 pass to reforming at 15. The reformate is fractionated at 16 to give a hydrogen-rich gas stream 23, a stream 24 of hydrocarbons up to C 4 , a stream 25 of C 5 and C 6 hydrocarbons and a stream 26 of heavier hydrocarbons. Stream 26 is or streams 25 and 26 are extracted by a solvent at 17, and the aromatic extract taken off at 28. The raffinate in line 27 is cracked at 18 and fractionated at 19 to give cracked gasoline 31 and light hydrocarbons (C 3 and C 4 ) 30. The cracked gasoline can be recycled by line 33.
GB5968970A 1969-12-17 1970-12-16 Aromatic gasoline production Expired GB1338612A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US88585969A 1969-12-17 1969-12-17

Publications (1)

Publication Number Publication Date
GB1338612A true GB1338612A (en) 1973-11-28

Family

ID=25387844

Family Applications (1)

Application Number Title Priority Date Filing Date
GB5968970A Expired GB1338612A (en) 1969-12-17 1970-12-16 Aromatic gasoline production

Country Status (16)

Country Link
US (1) US3714023A (en)
AR (1) AR212954A1 (en)
CA (1) CA943484A (en)
CS (1) CS153570B2 (en)
DE (1) DE2061945C3 (en)
DK (1) DK137765B (en)
EG (1) EG10506A (en)
ES (1) ES386517A1 (en)
FR (1) FR2070902B1 (en)
GB (1) GB1338612A (en)
IL (1) IL35865A (en)
NL (1) NL7018328A (en)
PL (1) PL81513B1 (en)
TR (1) TR17194A (en)
YU (1) YU35270B (en)
ZA (1) ZA708450B (en)

Families Citing this family (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3650943A (en) * 1970-07-10 1972-03-21 Universal Oil Prod Co High octane unleaded gasoline production
US3873439A (en) * 1973-02-26 1975-03-25 Universal Oil Prod Co Process for the simultaneous production of an aromatic concentrate and isobutane
US3928175A (en) * 1973-05-24 1975-12-23 Mobil Oil Corp Upgrading crude oil by combination processing
US4067798A (en) * 1976-02-26 1978-01-10 Standard Oil Company (Indiana) Catalytic cracking process
US4053388A (en) * 1976-12-06 1977-10-11 Moore-Mccormack Energy, Inc. Process for preparing aromatics from naphtha
US5292976A (en) * 1993-04-27 1994-03-08 Mobil Oil Corporation Process for the selective conversion of naphtha to aromatics and olefins
WO2019136434A1 (en) 2018-01-08 2019-07-11 Swift Fuels, Llc Processes for an improvement to gasoline octane for long-chain paraffin feed streams
US10941357B2 (en) 2018-04-16 2021-03-09 Swift Fuels, Llc Process for converting C2—C5 hydrocarbons to gasoline and diesel fuel blendstocks
US11965136B2 (en) * 2021-01-15 2024-04-23 Saudi Arabian Oil Company Cyclization and fluid catalytic cracking systems and methods for upgrading naphtha

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2908629A (en) * 1955-05-31 1959-10-13 Sun Oil Co High octane gasoline manufacture
US3060116A (en) * 1959-11-06 1962-10-23 Socony Mobil Oil Co Inc Combination reforming and cracking process

Also Published As

Publication number Publication date
DK137765C (en) 1978-10-09
CS153570B2 (en) 1974-02-25
IL35865A0 (en) 1971-02-25
FR2070902B1 (en) 1973-12-07
DE2061945A1 (en) 1971-06-24
DK137765B (en) 1978-05-01
YU35270B (en) 1980-10-31
NL7018328A (en) 1971-06-21
DE2061945C3 (en) 1974-06-27
TR17194A (en) 1974-04-25
DE2061945B2 (en) 1973-11-29
CA943484A (en) 1974-03-12
ZA708450B (en) 1971-11-24
PL81513B1 (en) 1975-08-30
US3714023A (en) 1973-01-30
EG10506A (en) 1977-03-31
FR2070902A1 (en) 1971-09-17
IL35865A (en) 1973-11-28
ES386517A1 (en) 1973-03-16
AR212954A1 (en) 1978-11-30
YU306070A (en) 1980-04-30

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Legal Events

Date Code Title Description
PS Patent sealed [section 19, patents act 1949]
PCNP Patent ceased through non-payment of renewal fee