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US3887610A Expired / Lapsed US ⏱️ 0.0 years remaining

Emulsion polymerization of ethylene with chain transfer agents to form copolymers

Assignee: ExxonMobil Technology and Engineering Co
•
Filing: 1971-12-09
•
Granted: 1975-06-03
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Expires: 1991-12-09
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Abstract

Abstract Ethylene-containing copolymers useful in oil compositions for modifying flow properties are made by free radical emulsion polymerization using as a molecular weight modifying agent chain transfer agents such as halo-alkanes or hydrocarbyl mercaptans.

Inventors

  • 👤 Alfred E Kober

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-27 11:00
CPC Classifications
C; C10; C10L; C10L1/00; C10L1/10; C10L1/14; C10L1/18; C10L1/192; C10L1/195; C08; C08F; C08F210/00; C08F210/02; C10L1/196; C10L1/1963; C10L1/1966; C10L1/197; C10L1/1973

Claims Analysis

Total Claims: 7
Claim 1
Independent Claim 208 words
AN EMULSION POLYMERIZATION PROCESS FOR PREPARING AN OI SOLUBLE COPOLYMER USEFUL FOR IMPROVEING THE FLOW PROPERTIES O PETROLEUM FUEL OILS, SAID COPOLYMER CONSISTING ESSENTIALLY O ABOUT 4 TO 15 MOLAR PROPORTIONS OF ETHYLENE PER MOLAR PROPORTION OF VINYL ACETATE, SAID COPOLYMER HAVING A NUMBER AVERAGE MOLECULAR WEIGHT OF ABOUT 3500 TO 15,000, WHICH PROCESS COMPRISES FORMING AN AQUEOUS EMULSIFIED SYSTEM COMPRISING WATER, VINYL ACETATE, A WATER SOLUBLE FREE RADICAL INITIATOR, AN EMULSIFIER AND A CHAIN TRANSFER AGENT, INTRODUCING ETHYLENE AND COPOLYMERIZING SAID ETHYLENE AND SAID VINYL ACETATE FOR ABOUT 6 TO 600 MINUTES UNDER ETHYLENE PRESSURE OF 50 TO 500 ATOMOSPHERES, AT A TEMPERATURE IN THE RANGE OF ABOUT 60* TO 120*C., AND RECOVERING SAID COPOLYMER, WHEREIN SAID CHAIN TRANSFER AGENT IS SELECTED FROM THE GROUP CONSISTING OF C1 TO C18 ALKYL MERCAPTAN AND C1 TO C4 CHLOROALKANES CONTAINING UP TO 4 CHLORINE ATOMS PER MOLECULE, WHEREIN SAID INITIATOR IS PRESENT IN AN AMOUNT OF 0.001 TO 0.05 MOLE PRE MOLE OF SAID VINYL ACETATE, WHEREIN SAID CHAIN TRANSFER AGENT IS PRESENT IN THE AMOUNT OF 0.005 TO 0.25 MOLE PER MOLE OF SAID PRESENT IN TATE, WHEREIN THE AQUEOUS PHASE IS CONTINUOUS, AND WHEREIN SAID VINYL ACETATE AND SAID CHAIN TRANSFER AGENTS ARE IN THE DISPERSED PHASE.
Claim 2
Dependent Claim 208 words
AN EMULSION POLYMERIZATION PROCESS FOR PREPARING AN OI SOLUBLE COPOLYMER USEFUL FOR IMPROVEING THE FLOW PROPERTIES O PETROLEUM FUEL OILS, SAID COPOLYMER CONSISTING ESSENTIALLY O ABOUT 4 TO 15 MOLAR PROPORTIONS OF ETHYLENE PER MOLAR PROPORTION OF VINYL ACETATE, SAID COPOLYMER HAVING A NUMBER AVERAGE MOLECULAR WEIGHT OF ABOUT 3500 TO 15,000, WHICH PROCESS COMPRISES FORMING AN AQUEOUS EMULSIFIED SYSTEM COMPRISING WATER, VINYL ACETATE, A WATER SOLUBLE FREE RADICAL INITIATOR, AN EMULSIFIER AND A CHAIN TRANSFER AGENT, INTRODUCING ETHYLENE AND COPOLYMERIZING SAID ETHYLENE AND SAID VINYL ACETATE FOR ABOUT 6 TO 600 MINUTES UNDER ETHYLENE PRESSURE OF 50 TO 500 ATOMOSPHERES, AT A TEMPERATURE IN THE RANGE OF ABOUT 60* TO 120*C., AND RECOVERING SAID COPOLYMER, WHEREIN SAID CHAIN TRANSFER AGENT IS SELECTED FROM THE GROUP CONSISTING OF C1 TO C18 ALKYL MERCAPTAN AND C1 TO C4 CHLOROALKANES CONTAINING UP TO 4 CHLORINE ATOMS PER MOLECULE, WHEREIN SAID INITIATOR IS PRESENT IN AN AMOUNT OF 0.001 TO 0.05 MOLE PRE MOLE OF SAID VINYL ACETATE, WHEREIN SAID CHAIN TRANSFER AGENT IS PRESENT IN THE AMOUNT OF 0.005 TO 0.25 MOLE PER MOLE OF SAID PRESENT IN TATE, WHEREIN THE AQUEOUS PHASE IS CONTINUOUS, AND WHEREIN SAID VINYL ACETATE AND SAID CHAIN TRANSFER AGENTS ARE IN THE DISPERSED PHASE.
Claim 3
Dependent Claim 207 words
An emulsion polymerization process for preparing an oil soluble copolymer useful for improving the flow properties of petroleum fuel oils, said copolymer consisting essentially of about 4 to 15 molar proportions of ethylene per molar proportion of vinyl acetate, said copolymer having a number average molecular weight of about 3500 to 15,000, which process comprises forming an aqueous emulsified system comprising water, vinyl acetate, a water soluble free radical initiator, an emulsifier and a chain transfer agent, introducing ethylene and copolymerizing said ethylene and said vinyl acetate for about 6 to 600 minutes under ethylene pressure of 50 to 500 atomospheres, at a temperature in the range of about 60* to 120*C., and recovering said copolymer, wherein said chain transfer agent is selected from the group consisting of C1 to C18 alkyl mercaptan and C1 to C4 chloroalkanes containing up to 4 chlorine atoms per molecule, wherein said initiator is present in an amount of 0.001 to 0.05 mole per mole of said vinyl acetate, wherein said chain transfer agent is present in the amount of 0.005 to 0.25 mole per mole of said vinyl acetate, wherein the aqueous phase is continuous, and wherein said vinyl acetate and said chain transfer agents are in the dispersed phase.
Claim 4
Dependent Claim 207 words
An emulsion polymerization process for preparing an oil soluble copolymer useful for improving the flow properties of petroleum fuel oils, said copolymer consisting essentially of about 4 to 15 molar proportions of ethylene per molar proportion of vinyl acetate, said copolymer having a number average molecular weight of about 3500 to 15,000, which process comprises forming an aqueous emulsified system comprising water, vinyl acetate, a water soluble free radical initiator, an emulsifier and a chain transfer agent, introducing ethylene and copolymerizing said ethylene and said vinyl acetate for about 6 to 600 minutes under ethylene pressure of 50 to 500 atomospheres, at a temperature in the range of about 60* to 120*C., and recovering said copolymer, wherein said chain transfer agent is selected from the group consisting of C1 to C18 alkyl mercaptan and C1 to C4 chloroalkanes containing up to 4 chlorine atoms per molecule, wherein said initiator is present in an amount of 0.001 to 0.05 mole per mole of said vinyl acetate, wherein said chain transfer agent is present in the amount of 0.005 to 0.25 mole per mole of said vinyl acetate, wherein the aqueous phase is continuous, and wherein said vinyl acetate and said chain transfer agents are in the dispersed phase.
Claim 5
Dependent Claim 37 words
A process according to claim 1, wherein the chain transfer agent is present in the amount of about 0.01 to 0.15 mole per mole of vinyl acetate, and the chain transfer agent is dodecyl mercaptan or chloroform.
Claim 6
Dependent Claim 26 words
A process according to claim 2, wherein the ethylene pressure is about 135 to 350 atmospheres and the emulsion polymerization temperature is about 80* to 100*c.
Claim 7
Dependent Claim 14 words
A process according to claim 3, wherein said chain transfer agent is dodecyl mercaptan.

References Cited (Backward Citations)

No citation records indexed.

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1978-06-02 1978-12-02 1979-06-03 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1982-06-02 1982-12-02 1983-06-03 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1986-06-02 1986-12-02 1987-06-03 $7700.00 Window Closed / Lapsed

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