Interpolymers of ethylene and unsaturated carboxylic acids
AssigneeThe Dow Chemical Company
InventorsOsborne K. McKinney, David P. Flores, David A. Eversdyk
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Abstract
Homogeneous, random interpolymers of ethylene and lesser amounts by weight of olefinically-unsaturated comonomers are prepared in a substantially constant environment, substantially steady-state reaction mixture, in a well-stirred autoclave reactor, in continuous single-phase operation, using elevated synthesis conditions wherein the temperature and pressure are elevated to an amount high enough to approach, reach, or surpass the molecular weight distribution boundary.
Claims38
A process for producing homogeneous, random interpolymers comprising about 99% to about 65% by weight of ethylene monomer and about 1% to about 35% by weight of at least one olefinically unsaturated comonomer selected from the group comprising unsaturated carboxylic acids, alkylacrylates, alkyl methacrylates and vinyl esters, said process comprising interpolymerizing the monomers in a substantially constant constant environment, under steady state conditions, in a single-phase reaction mixture, under the influence of a free-radical initiator, and in a well-stirred autoclave reactor operated in a continuous manner as the monomers are fed into the reactor and the raection mixture is withdrawn, said process being characterized by
- the use of synthesis conditions of temperature and pressure which are elevated to a level high enough above the phase boundary between two-phase and single-phase operation such that the molecular weight distribution (MWD) boundary is reached, or surpassed, the said molecular weight distribution boundary being the highest ratio of weight average molecular weight/number average molecular weight obtainable in single-phase operation, said elevated pressure being greater than 2000 psi above, and said elevated temperature being greater than 15.degree. C. above, the synthesis conditions required at the phase boundary for a given mixture of ethylene and comonomer,
- thereby producing an interpolymer having less gels and/or grain.
A process for producing substantially homogeneous, random interpolymers comprising about 99% to about 65% by weight of ethylene monomer with about 1% to about 35% by weight of at least one copolymerizable olefinically-unsaturated comonomer selected from the group comprising an unsaturated carboxylic acid, alkyl acrylates, alkyl methacrylates and vinyl esters, said process comprising interpolymerizing the monomers in a well-stirred autoclave reactor operated in a continuous manner at steady state conditions using a free-radical polymerization initiator under substantially constant conditions of temperature, pressure, and flow rates,
- wherein the conditions of temperature and pressure required to produce operation at the phase boundary are exceeded, respectively, by using a temperature of at least 15.degree. C. above that at the phase boundary and a pressure of more than 2000 psi above that at the phase boundary,
- whereby the molecular weight distribution (MWD) boundary is reached or surpassed,
- thereby producing an interpolymer having less gels and/or grain.
A random, homogeneous, single-phase interpolymer product comprising about 65% to about 99% by weight of ethylene monomer, the remaining percentage comprising at least one olefinically-unsaturated comonomer selected from the group comprising unsaturated carboxylic acids, alkyl acrylates, alkyl methacrylates and vinyl esters,
- said interpolymer being further characterized as having a weight average molecular weight/number average molecular weight ratio as defined by the formula
- log(MWw/MWn)=(C.sub.1 +(C.sub.2)(wt.fraction comonomer)).times.(C.sub.4)
- where MWw is the weight average molecular weight,
- MWn is the number average molecular weight, C.sub.1 is the intercept of the wt. fraction comonomer versus log(MWw/MWn).sub.max. plot for a given comonomer, where (MWw/MWn).sub.max. is the ratio of weight average molecular weight to number average molecular weight at the MWD boundary for a given comonomer,
- C.sub.2 is the slope of the wt. fraction comonomer versus log(MWw/MWn).sub.max. plot for a given comonomer,
- C.sub.4 is a numerical value in the range of about 1.0 to about 0.1, representing conditions at, and beyond, the MWD boundary,
- with C.sub.4 being equal to unity at the MWD boundary,
- said interpolymer being further characterized as having a ratio of weight percent adjacent comonomer unit to total weight percent comonomer in the polymer of less than 0.44 and as having lower levels of gels and/or grain.
A process for producing homogeneous, random interpolymers comprising about 99% to about 65% by weight of ethylene monomer and about 1% to about 35% by weight of acrylic acid comonomer, said process comprising interpolymerizing the monomers in a substantially constant environment, under steady state conditions, in a single-phase reaction mixture, under the influence of a free-radical initiator, and in a well-stirred autoclave reactor operated in a continuous manner as the monomers are fed into the reactor and the reaction mixture is withdrawn, said process being characterized by
- the use of synthesis conditions of temperature and pressure which are elevated to a level high enough above the phase boundary between two-phase and single-phase operation such that the molecular weight distribution (MWD) boundary is reached, or surpassed, the said molecular weight distribution boundary being the highest ratio of weight average molecular weight/number average molecular weight obtainable in single-phase operation, said elevated pressure being greater than 2000 psi above, and said elevated temperature being greater than 15.degree. C. above, the synthesis conditions required at the phase boundary for a given mixture of ethylene and comonomer, thereby producing an interpolymer having less gels and/or grain.
A process for producing substantially homogeneous, random interpolymers comprising about 99% to about 65% by weight of ethylene monomer with about 1% to aboul 35% by weight of acrylic acid comonomer, said process comprising interpolymerizing the monomers in a well-stirred autoclave reactor operated in a continuous manner at steady state conditions using a free-radical polymerization initiator under substantially constant conditions of temperature, pressure, and flow rates,
- wherein the conditions of temperature and pressure required to produce operation at the phase boundary are exceeded, respectively, by using a temperature of at least 15.degree. C. above that at the phase boundary and a pressure of more than 2000 psi above that at the phase boundary,
- whereby the molecular weight distribution (MWD) boundary is reached or surpassed, thereby producing an interpolymer having less gels and/or grain.
A random, homogeneous, single-phase interpolymer product comprising about 65% to about 99% by weight of ethylene monomer, the remaining percentage comprising acrylic acid comonomer,
- said interpolymer being further characterized as having a weight average molecular weight/number average molecuar weight ratio a defined by the formula
- log(MWw/MWn)=(C.sub.1 +(C.sub.2) (wt. fraction comonomer)).times.(C.sub.4)
- where MWw is the weight average molecular weight,
- MWn is the number average molecular weight,
- C.sub.1 is the intercept of the wt. fraction comonomer versus log (MWw/MWn).sub.max. plot for the comonomer, where (MWw/MWn).sub.max. is the ratio of weight average molecular weight to number average molecular weight at the MWD boundary for the comonomer,
- C.sub.2 is the slope of the wt. fraction comonomer versus log(MWw/MWn).sub.max. plot for the comonomer, and
- C.sub.4 is a numerical value in the range of about 1.0 to about 0.1, representing conditions at, and beyond, the MWD boundary,
- with C.sub.4 being equal to unity at the MWD boundary,
- said interpolymer being further characterized as having a ratio of weight percent adjacent comonomer unit to total weight percent comonomer in the polymer of less than 0.44, and as having lower levels of gels and/or grains.
A process for producing homogeneous, random interpolymers comprising about 99% to about 65% by weight of ethylene monomer and about 1% to about 35% by weight of methacrylic acid comonomer, said process comprising interpolymerizing the monomers in a substantially constant environment, under steady state conditions, in a single-phase reaction mixture, under the influence of a free-radical initiator, and in a well-stirred autoclave reactor operated in a continuous manner as the monomers are fed into the reactor and the reaction mixture is withdrawn, said process being characterized by
- the use of synthesis conditions of temperature and pressure which are elevated to a level high enough above the phase boundary between two-phase and single-phase operation such that the molecular weight distribution (MWD) boundary is reached, or surpassed, the said molecular weight distribution boundary being the highest ratio of weight average molecular weight/number average molecular weight obtainable in single-phase operation, said elevated pressure being greater than 2000 psi above, and said elevated temperature being greater than 15.degree. C. above, the synthesis conditions required at the phase boundary for a given mixture of ethylene and comonomer thereby producing an interpolymer having less gels and/or grain.
A process for producing substantially homogeneous, random interpolymers comprising about 99% to about 65% by weight of ethylene monomer with about 1% to about 35% by weight of methacrylic acid comonomer, said process comprising interpolymerizing the monomers in a well-stirred autoclave reactor operated in a continuous manner at steady state conditions using a free-radical polymerization initiator under substantially constant conditions of temperature, pressure, and flow rates,
- wherein the conditions of temperature and pressure required to produce operation at the phase boundary are exceeded, respectively, by using a temperature of at least 15.degree. C. above that at the phase boundary and a pressure of more than 2000 psi above that at the phase boundary,
- whereby the molecular weight distribution (MWD) boundary is reached or surpassed, thereby producing an interpolymer having less gels and/or grain.
A random, homogeneous, single-phase interpolymer product comprising about 65% to about 99% by weight of ethylene monomer, the remaining percentage comprising methacrylic acid comonomer,
- said interpolymer being further characterized as having a weight average molecular weight/number average molecular weight ratio as defined by the formula
- log(MWw/MWn)=(C.sub.1 +(C.sub.2)(wt.fraction comonomer)).times.(C.sub.4)
- where MWw is the weight average molecular weight,
- MWn is the number average molecular weight,
- C.sub.1 is the intercept of the wt. fraction comonomer versus log(MWw/MWn).sub.max. plot for the comonomer, where (MWw/MWn).sub.max. is the ratio of weight average molecular weight to number average molecular weight at the MWD boundary for the comonomer,
- C.sub.2 is the slope of the wt. fraction comonomer versus log(MWw/MWn).sub.max. plot for the given comonomer, and
- C.sub.4 is a numerical value in the range of about 1.0 to about 0.1, representing conditions at, and beyond, the MWD boundary,
- with C.sub.4 being equal to unity at the MWD boundary,
- said interpolymer being further characterized as having a ratio of weight percent adjacent comonomer unit to total weight percent comonomer in the polymer of less than 0.44, and as having lower levels of gels and/or grains.
Dependencies are inferred from the claim text.