GB1154966A - Fuel Composition with a Depressed Pour Point - Google Patents

Fuel Composition with a Depressed Pour Point

Info

Publication number
GB1154966A
GB1154966A GB1209467A GB1209467A GB1154966A GB 1154966 A GB1154966 A GB 1154966A GB 1209467 A GB1209467 A GB 1209467A GB 1209467 A GB1209467 A GB 1209467A GB 1154966 A GB1154966 A GB 1154966A
Authority
GB
United Kingdom
Prior art keywords
mono
olefinically unsaturated
polymers
compounds
aliphatic
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
GB1209467A
Inventor
Pieter Hendrikus Van Der Meij
Henricus Georgius Peter Voort
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.)
Shell Internationale Research Maatschappij BV
Original Assignee
Shell Internationale Research Maatschappij BV
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 Shell Internationale Research Maatschappij BV filed Critical Shell Internationale Research Maatschappij BV
Publication of GB1154966A publication Critical patent/GB1154966A/en
Expired legal-status Critical Current

Links

Classifications

    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10L—FUELS 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
    • C10L1/00—Liquid carbonaceous fuels
    • C10L1/10—Liquid carbonaceous fuels containing additives
    • C10L1/14—Organic compounds
    • C10L1/146—Macromolecular compounds according to different macromolecular groups, mixtures thereof
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10L—FUELS 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
    • C10L1/00—Liquid carbonaceous fuels
    • C10L1/10—Liquid carbonaceous fuels containing additives
    • C10L1/14—Organic compounds
    • C10L1/16—Hydrocarbons
    • C10L1/1625—Hydrocarbons macromolecular compounds
    • C10L1/1633—Hydrocarbons macromolecular compounds homo- or copolymers obtained by reactions only involving carbon-to carbon unsaturated bonds
    • C10L1/1641—Hydrocarbons macromolecular compounds homo- or copolymers obtained by reactions only involving carbon-to carbon unsaturated bonds from compounds containing aliphatic monomers
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10L—FUELS 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
    • C10L1/00—Liquid carbonaceous fuels
    • C10L1/10—Liquid carbonaceous fuels containing additives
    • C10L1/14—Organic compounds
    • C10L1/18—Organic compounds containing oxygen
    • C10L1/192—Macromolecular compounds
    • C10L1/195—Macromolecular compounds obtained by reactions involving only carbon-to-carbon unsaturated bonds
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10L—FUELS 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
    • C10L1/00—Liquid carbonaceous fuels
    • C10L1/10—Liquid carbonaceous fuels containing additives
    • C10L1/14—Organic compounds
    • C10L1/22—Organic compounds containing nitrogen
    • C10L1/234—Macromolecular compounds
    • C10L1/236—Macromolecular compounds obtained by reactions involving only carbon-to-carbon unsaturated bonds derivatives thereof

Landscapes

  • Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Liquid Carbonaceous Fuels (AREA)
  • Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)

Abstract

1,154,966. Distillate fuel. SHELL INTERNATIONALE RESEARCH MAATSCHAPPIJ N.V. 15 March, 1967 [17 March, 1966], No. 12094/67. Heading C5G. The pour point of a wax containing distillate fuel, which contains at least 3% by weight of waxes have a melting point above 35‹ C. and a boiling point above 350‹ C., is depressed by adding one or more polymers which may be considered as having been obtained by the polymerization of mono-olefinically unsaturated compounds consisting at least partly of monoolefinically unsaturated aliphatic compounds having an unbranched saturated hydrocarbon chain of at least 18 carbon atoms (such chains being referred to as long hydrocarbon chains). The polymers are generally added in an amount of 0À001-2À0% by weight and generally have an average molecular weight of 1,000-1,000,000. Suitable polymers have a main chain of carbon atoms which carries at least one long hydrocarbon side chain which is attached to the main chain either directly or indirectly via one or more other atoms such as carbon, oxygen, sulphur, nitrogen and/or phosphorus atoms. The polymers may be prepared directly by polymerizing mono-olefinically unsaturated compounds which at least partly consist of monoolefinically unsaturated aliphatic compounds having long hydrocarbon chains; examples of such compounds are;-vinyl and allyl esters of mono-olefinically saturated aliphatic monocarboxylic acids, alkyl esters of mono-olefinically unsaturated aliphatic monocarboxylic acids, alkyl amides, dialkyl esters of mono-olefinically unsaturated aliphatic carboxylic acids, dialkyl amides and imides of mono-olefinically unsaturated aliphatic dicarboxylic acids, alkylvinyl ethers and mono-olefins, polymerized alone or in admixture with similar compounds not containing long hydrocarbon chains. The polymers may also be prepared by polymerizing mono-olefinically unsaturated compounds which do not have any long hydrocarbon chains and then introducing long chains into the polymer by an after-treatment such as alkylation or acylation, examples of such polymers are:- homopolymers and copolymers of mono-olefinically unsaturated monocarboxylic acids, dicarboxylic acids or acid anhydrides thereof and mono-olefins, vinyl esters of mono-olefinically saturated monocarboxylic acids or dialkyl esters of mono-olefinically unsaturated dicarboxylic acids after-treated with aliphatic alcohols or amines having long hydrocarbon chains; polymers and copolymers of monoolefinically unsaturated aliphatic alcohols aftertreated with aliphatic carboxylic acids or carboxylic acid chlorides; homopolymers of mono-olefinically unsaturated aliphatic aldehydes or alkylvinyl ketones and copolymers of anhydrides of mono-olefinically unsaturated dicarboxylic acids and mono-olefines or other mono-olefinically unsaturated compounds aftertreated with aliphatic amines. Polar groups may be incorporated in the polymer by adding monomers containing hydroxyl, carboxyl, acid anhydride-, or nitrogen-, containing groups, to the polymerization reaction to give the polymer dispersant properties.
GB1209467A 1966-03-17 1967-03-15 Fuel Composition with a Depressed Pour Point Expired GB1154966A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
NL6603483A NL148099B (en) 1966-03-17 1966-03-17 PROCEDURE FOR REDUCING THE FLOOD POINT OF A FUEL MIXTURE.

Publications (1)

Publication Number Publication Date
GB1154966A true GB1154966A (en) 1969-06-11

Family

ID=19796006

Family Applications (1)

Application Number Title Priority Date Filing Date
GB1209467A Expired GB1154966A (en) 1966-03-17 1967-03-15 Fuel Composition with a Depressed Pour Point

Country Status (6)

Country Link
CA (1) CA980117A (en)
DE (1) DE1645785C3 (en)
FR (1) FR1514629A (en)
GB (1) GB1154966A (en)
NL (1) NL148099B (en)
SE (1) SE334699B (en)

Cited By (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3765849A (en) * 1971-07-07 1973-10-16 Exxon Research Engineering Co Flow improvers for hydrocarbon oils and method of preparing same
US3854893A (en) * 1972-06-14 1974-12-17 Exxon Research Engineering Co Long side chain polymeric flow improvers for waxy hydrocarbon oils
US3966428A (en) * 1973-10-31 1976-06-29 Exxon Research And Engineering Company Ethylene backbone polymers in combination with ester polymers having long alkyl side chains are low viscosity distillate fuel cold flow improvers
US3999960A (en) * 1972-08-30 1976-12-28 Exxon Research And Engineering Company Wax crystal modifiers for petroleum oils
US4074978A (en) * 1973-10-12 1978-02-21 Exxon Research & Engineering Co. Combination of asphaltenes with flow improver polymers to improve the flow properties of high boiling fuel oils
US4156434A (en) * 1972-06-21 1979-05-29 Texaco Inc. Low pour point fuel compositions
JPS59179591A (en) * 1983-03-18 1984-10-12 シエル・インタ−ナシヨナル・リサ−チ・マ−トスハツペイ・ベ−・ヴエ− Wax-containing petroleum or fuel oil containing pour point lowering agent
EP0320766A2 (en) * 1987-12-16 1989-06-21 Hoechst Aktiengesellschaft Viscosity index-modifying polymer blends for petroleum fractions
EP0342497A2 (en) * 1988-05-19 1989-11-23 BASF Aktiengesellschaft Fuel for spark ignition engines
EP0360419A1 (en) * 1988-08-24 1990-03-28 Exxon Chemical Patents Inc. Fuel compositions
EP0407906A1 (en) * 1989-07-14 1991-01-16 Röhm Gmbh Mineral oils with improved flow behaviour
EP0486836A1 (en) * 1990-11-14 1992-05-27 BASF Aktiengesellschaft Petroleum middle distillate with improved cold flow characteristics
US5281329A (en) * 1989-07-14 1994-01-25 Rohm Gmbh Method for improving the pour point of petroleum oils
WO2004035715A1 (en) * 2002-10-14 2004-04-29 Basf Aktiengesellschaft Use of ether vinyl hydrocarbyl homopolymers for increasing effect of a cold flow improving agent
WO2004048502A1 (en) * 2002-11-22 2004-06-10 Basf Aktiengesellschaft Use of homopolymers of ethylenically unsaturated esters for improving the action of cold flow improvers

Families Citing this family (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB1268089A (en) * 1966-10-14 1972-03-22 Exxon Research Engineering Co Method for preparing a petroleum residual fuel having improved flow characteristics
NL6709453A (en) * 1967-07-07 1969-01-09
US3841850A (en) * 1967-11-30 1974-10-15 Exxon Research Engineering Co Hydrocarbon oil containing ethylene copolymer pour depressant
GB1267604A (en) * 1968-09-16 1972-03-22 Exxon Research Engineering Co Petroleum crude oils having improved flow properties and reduced tendency to deposit wax
US4010006A (en) * 1969-05-09 1977-03-01 Exxon Research And Engineering Company Flow improvers
US3790358A (en) * 1971-07-30 1974-02-05 Exxon Research Engineering Co Residual fuels improved in its flow characteristics by a copolymer of c{11 {11 to c{11 {11 linear alpha-olefin and styrene or a c{11 {11 to c{11 {11 alpha-olefin
FR2471405A1 (en) * 1979-12-13 1981-06-19 Inst Francais Du Petrole Terpolymer from acrylic! ester, di:isobutylene! - and di:carboxylic acid deriv., as low temp. flow improver for hydrocarbon oils
DE3112456A1 (en) * 1981-03-28 1982-10-07 Hoechst Ag, 6000 Frankfurt "METHOD FOR IMPROVING THE FLOWABILITY OF MINERAL OILS"
FR2528066A1 (en) * 1982-06-04 1983-12-09 Inst Francais Du Petrole NITROGEN ADDITIVES FOR USE AS HYDROCARBON MOISTURE DISTILLATE DISORDER DISORDERS AND HYDROCARBON MEAL DISTILLATE COMPOSITIONS COMPRISING THE SAME
FR2528067B1 (en) * 1982-06-07 1985-10-11 Inst Francais Du Petrole NITROGEN ADDITIVES FOR USE AS DISORDERS TO REDUCE THE POINT OF MEDIUM HYDROCARBON DISTILLATES AND COMPOSITIONS OF MEDIUM HYDROCARBON DISTILLATES CONTAINING THE ADDITIVES
DE4036226A1 (en) * 1990-11-14 1992-05-21 Basf Ag PETROLEUM DISTILLATES WITH IMPROVED FLOW PROPERTIES IN THE COLD
BR112015013261A2 (en) 2012-12-18 2017-07-11 Basf Se process for producing a polymer formulation, polymer formulation, and, use of a polymer formulation
CA2889070C (en) 2012-12-18 2017-11-28 Basf Se Polymeric compositions composed of ethylene-vinyl ester copolymers alkyl (meth)acrylates, processes for production thereof and use thereof as pour point depressants for crude oils, mineral oils or mineral oil products
US9574146B2 (en) 2012-12-18 2017-02-21 Basf Se Polymeric compositions composed of ethylene-vinyl ester copolymers alkyl (meth)acrylates, processes for production thereof and use thereof as pour point depressants for crude oils, mineral oils or mineral oil products

Cited By (17)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3765849A (en) * 1971-07-07 1973-10-16 Exxon Research Engineering Co Flow improvers for hydrocarbon oils and method of preparing same
US3854893A (en) * 1972-06-14 1974-12-17 Exxon Research Engineering Co Long side chain polymeric flow improvers for waxy hydrocarbon oils
US4156434A (en) * 1972-06-21 1979-05-29 Texaco Inc. Low pour point fuel compositions
US3999960A (en) * 1972-08-30 1976-12-28 Exxon Research And Engineering Company Wax crystal modifiers for petroleum oils
US4074978A (en) * 1973-10-12 1978-02-21 Exxon Research & Engineering Co. Combination of asphaltenes with flow improver polymers to improve the flow properties of high boiling fuel oils
US3966428A (en) * 1973-10-31 1976-06-29 Exxon Research And Engineering Company Ethylene backbone polymers in combination with ester polymers having long alkyl side chains are low viscosity distillate fuel cold flow improvers
JPS59179591A (en) * 1983-03-18 1984-10-12 シエル・インタ−ナシヨナル・リサ−チ・マ−トスハツペイ・ベ−・ヴエ− Wax-containing petroleum or fuel oil containing pour point lowering agent
EP0320766A3 (en) * 1987-12-16 1989-12-20 Hoechst Aktiengesellschaft Viscosity index-modifying polymer blends for petroleum fractions
EP0320766A2 (en) * 1987-12-16 1989-06-21 Hoechst Aktiengesellschaft Viscosity index-modifying polymer blends for petroleum fractions
EP0342497A2 (en) * 1988-05-19 1989-11-23 BASF Aktiengesellschaft Fuel for spark ignition engines
EP0342497A3 (en) * 1988-05-19 1990-03-28 Basf Aktiengesellschaft Fuel for spark ignition engines
EP0360419A1 (en) * 1988-08-24 1990-03-28 Exxon Chemical Patents Inc. Fuel compositions
EP0407906A1 (en) * 1989-07-14 1991-01-16 Röhm Gmbh Mineral oils with improved flow behaviour
US5281329A (en) * 1989-07-14 1994-01-25 Rohm Gmbh Method for improving the pour point of petroleum oils
EP0486836A1 (en) * 1990-11-14 1992-05-27 BASF Aktiengesellschaft Petroleum middle distillate with improved cold flow characteristics
WO2004035715A1 (en) * 2002-10-14 2004-04-29 Basf Aktiengesellschaft Use of ether vinyl hydrocarbyl homopolymers for increasing effect of a cold flow improving agent
WO2004048502A1 (en) * 2002-11-22 2004-06-10 Basf Aktiengesellschaft Use of homopolymers of ethylenically unsaturated esters for improving the action of cold flow improvers

Also Published As

Publication number Publication date
SE334699B (en) 1971-05-03
NL6603483A (en) 1967-09-18
FR1514629A (en) 1968-02-23
NL148099B (en) 1975-12-15
DE1645785C3 (en) 1982-11-04
DE1645785A1 (en) 1969-08-21
CA980117A (en) 1975-12-23
DE1645785B2 (en) 1974-08-08

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