GB803184A - Improvements in or relating to the separation of normal paraffins from hydrocarbon mixtures - Google Patents

Improvements in or relating to the separation of normal paraffins from hydrocarbon mixtures

Info

Publication number
GB803184A
GB803184A GB6684/57A GB668457A GB803184A GB 803184 A GB803184 A GB 803184A GB 6684/57 A GB6684/57 A GB 6684/57A GB 668457 A GB668457 A GB 668457A GB 803184 A GB803184 A GB 803184A
Authority
GB
United Kingdom
Prior art keywords
hydrocarbon
separation
normal
paraffin
desorbed
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
GB6684/57A
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 GB803184A publication Critical patent/GB803184A/en
Expired legal-status Critical Current

Links

Classifications

    • 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
    • C10G25/00Refining of hydrocarbon oils in the absence of hydrogen, with solid sorbents
    • C10G25/02Refining of hydrocarbon oils in the absence of hydrogen, with solid sorbents with ion-exchange material
    • C10G25/03Refining of hydrocarbon oils in the absence of hydrogen, with solid sorbents with ion-exchange material with crystalline alumino-silicates, e.g. molecular sieves
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C7/00Purification; Separation; Use of additives
    • C07C7/12Purification; Separation; Use of additives by adsorption, i.e. purification or separation of hydrocarbons with the aid of solids, e.g. with ion-exchangers
    • C07C7/13Purification; 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

Abstract

In a process for separating a normal paraffin from a normally liquid hydrocarbon mixture also containing branched-chain and/or cyclic hydrocarbons by contacting the mixture in the liquid phase with a solid absorbent which selectively absorbs normal paraffins, the absorbed paraffin is desorbed with a normal paraffin in the liquid phase which contains at least four carbon atoms per molecule and of lower molecular weight than the absorbed paraffin. Desorbed hydrocarbon is readily separated from any desorbing hydrocarbon by fractionation. The feed for separation may be a gasoline mixture, e.g. a reformate, and the normal paraffins separated may be subjected to isomerization or other treatment to improve the octane number. Traces of isobutane and lower boiling hydrocarbons are preferably removed prior to the separation by distillation. Absorption and desorption are both preferably carried out at 80-152 DEG C. and 13.5-68 atmospheres, the pressure being sufficient to maintain the hydrocarbons in the liquid phase. The desorbing hydrocarbon may be removed from the absorbent by reducing the pressure. Normal butane is the preferred desorbing hydrocarbon. Absorbents which may be used preferably have a pore size of about 5.1 and include the crystalline alumino-silicates of calcium, magnesium, barium, strontium, sodium and potassium. The calcium compound is preferably heated to remove water of hydration. In a preferred embodiment separation is carried out continuously by the use of two absorption zones, one being used for absorption while the other is desorbed.
GB6684/57A 1956-03-01 1957-02-28 Improvements in or relating to the separation of normal paraffins from hydrocarbon mixtures Expired GB803184A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US568809A US2920037A (en) 1956-03-01 1956-03-01 Separation of normal paraffins from hydrocarbon mixtures using zeolitic molecular sieves

Publications (1)

Publication Number Publication Date
GB803184A true GB803184A (en) 1958-10-22

Family

ID=24272832

Family Applications (1)

Application Number Title Priority Date Filing Date
GB6684/57A Expired GB803184A (en) 1956-03-01 1957-02-28 Improvements in or relating to the separation of normal paraffins from hydrocarbon mixtures

Country Status (7)

Country Link
US (1) US2920037A (en)
CA (1) CA1016873A (en)
DE (2) DE1418428C2 (en)
ES (1) ES233939A1 (en)
FR (1) FR1172788A (en)
GB (1) GB803184A (en)
NL (1) NL108239C (en)

Families Citing this family (19)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2978407A (en) * 1958-05-28 1961-04-04 Exxon Research Engineering Co Molecular sieve separation process
US3007980A (en) * 1958-06-20 1961-11-07 Sun Oil Co Removal of impurities from volatile liquids
US3054838A (en) * 1958-09-08 1962-09-18 California Research Corp Method for separating n-hydrocarbons using molecular sieves
US3053913A (en) * 1959-01-21 1962-09-11 Gulf Research Development Co Separation of high molecular weight hydrocarbons with molecular sieves
DE1194084B (en) * 1959-08-29 1965-06-03 Deutsche Erdoel Ag Process for the separation of hydrocarbon mixtures
BE598183A (en) * 1959-12-15
US3184518A (en) * 1960-08-22 1965-05-18 Standard Oil Co Increased efficiency in molecular sieve adsorption system
US3121757A (en) * 1960-10-28 1964-02-18 Universal Oil Prod Co Vibratory sorption separation process utilizing molecular sieves
NL272082A (en) * 1960-12-09
GB966770A (en) * 1961-09-08 1964-08-12 British Petroleum Co Improvements relating to hydrocarbon separation processes
US3141748A (en) * 1961-11-20 1964-07-21 Exxon Research Engineering Co Hydrogen purification process
US3226914A (en) * 1962-09-04 1966-01-04 Union Carbide Corp Pressure cycle for molecular sieve separation of normal paraffins from hydrocarbon mixtures
US3426086A (en) * 1965-01-04 1969-02-04 Phillips Petroleum Co Production and/or recovery of primary haloalkanes
US4394254A (en) * 1982-04-26 1983-07-19 Texaco Inc. Method for separating straight chain hydrocarbons using zeolites having large crystals
US5510564A (en) * 1994-12-12 1996-04-23 Uop N-paraffin purification process with removal of aromatics
US20060236595A1 (en) * 2005-04-22 2006-10-26 Norikazu Nakamura Biofuel conversion process
US20100116711A1 (en) * 2008-11-12 2010-05-13 Kellogg Brown & Root Llc Systems and Methods for Producing N-Paraffins From Low Value Feedstocks
EP2186785A3 (en) 2010-01-27 2010-09-01 Shell Internationale Research Maatschappij B.V. Process for the separation of olefins from paraffins
EP2186784A3 (en) 2010-01-27 2010-09-01 Shell Internationale Research Maatschappij B.V. Process for the preparation and recovery of olefins

Family Cites Families (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE624912C (en) * 1931-12-21 1936-02-07 Metallgesellschaft Akt Ges Process for the extraction of hydrocarbons from gases by means of solid adsorbents
US2306610A (en) * 1941-02-24 1942-12-29 Barrer Richard Maling Fractionation of mixtures of hydrocarbons
GB548905A (en) * 1941-02-24 1942-10-29 Richard Maling Barrer A process for the fractionation of hydrocarbon mixtures
US2376425A (en) * 1941-06-02 1945-05-22 Phillips Petroleum Co Diolefin production
DE871886C (en) * 1942-07-02 1953-03-26 Linde Eismasch Ag Adsorption process
US2522426A (en) * 1945-05-30 1950-09-12 Standard Oil Dev Co Method of extrcting hydrocarbons
US2425535A (en) * 1945-07-25 1947-08-12 Standard Oil Dev Co Separation of normal paraffins from iso-paraffins by means of activated cocoanut charcoal
US2574434A (en) * 1949-06-04 1951-11-06 Socony Vacuum Oil Co Inc Method for refining petroleum hydrocarbons
US2586889A (en) * 1949-08-23 1952-02-26 Standard Oil Dev Co Separation of straight-chain from branched-chain hydrocarbons
US2859256A (en) * 1955-01-28 1958-11-04 Texas Co Separation process involving adsorption and desorption
US2818455A (en) * 1955-03-28 1957-12-31 Texas Co Desorption of straight chain hydrocarbons from selective adsorbents
US2818137A (en) * 1955-10-24 1957-12-31 Texas Co Adsorptive separation process

Also Published As

Publication number Publication date
CA1016873A (en) 1977-09-06
ES233939A1 (en) 1957-08-01
DE1795548A1 (en) 1972-04-13
DE1795548B2 (en) 1973-08-02
NL108239C (en)
DE1418428C2 (en) 1974-04-04
DE1418428B1 (en) 1970-12-10
FR1172788A (en) 1959-02-16
US2920037A (en) 1960-01-05

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