Synthetic resins or natural rubbers -- part of the class 520 ser – Synthetic resins – Mixing of two or more solid polymers; mixing of solid...
Reexamination Certificate
2000-03-23
2003-02-25
Lu, Caixia (Department: 1713)
Synthetic resins or natural rubbers -- part of the class 520 ser
Synthetic resins
Mixing of two or more solid polymers; mixing of solid...
C525S332300, C525S342000, C525S370000, C525S371000, C526S078000, C526S173000, C526S335000
Reexamination Certificate
active
06525140
ABSTRACT:
FIELD OF INVENTION
This invention relates to a method for preparing linear and branched copolymers in a single process. Particularly, this invention relates to a process for the continuous production of polymers having linear chains and branched chains.
BACKGROUND OF THE INVENTION
Polymers and copolymers of conjugated dienes such as polybutadiene, polyisoprene and styrene-butadiene rubbers possess physical properties which make them suitable for many important applications such as synthetic rubbers and as additives to other polymeric systems such as, for example, high impact polystyrene (HIPS). Moreover, HIPS can be manufactured by polymerization of styrene in the presence of 5-10% dissolved polybutadiene or butadiene copolymer rubber. Early in the polymerization, phase separation begins because of the immiscibility of the rubber within the polystyrene being formed and the depletion of the styrene phase. Grafting of polybutadiene with the polystyrene then takes place. Toughness, as well as other mechanical and rheological properties of HIPS, is strongly affected by the nature of the rubber phase. In this regard, some of the characteristics of the rubber which may be modified to control the overall HIPS performance include concentration, volume, particle size, grafting and cross-linking ability, molecular weight, and viscosity.
One focus of the present invention is use of polybutadiene as an additive in HIPS or ABS resins. Specifically, the present invention addresses the desire that the polybutadiene additive have useful molecular weight and viscosity ranges. In this regard, strictly linear polybutadiene of low molecular weight typically has a low Mooney viscosity, making the polybutadiene difficult to handle, while a tetra-coupled version of the same low molecular weight polymer is too high to be processed. One mechanism to achieve a desired molecular weight and viscosity is to use a blend of tetra-coupled and linear polymer chains.
One method for the manufacture of copolymers having linear and branched segments rubbery composition includes a blend of from 40-94 parts by weight (pbw) Component A and from 60-66 pbw of Component B. Component A includes a rubbery (co)polymer(s) of conjugated dienes, and at least 60% by weight of the components in the A portion are branched polymers. Component B is generally the same as Component A, but consists of linear (co)polymer(s). The process of manufacture involves forming Component A in a first step, Component B in a second step and performing a third step of blending A and B.
Another process is directed to polymerizing at least one diene monomer to a conversion between 30 and 70% to produce low molecular polydiene chains; joining from 20 to 70% of those chains with a suitable branching agent; and allowing the polymerization to continue to produce a polydiene rubber blend. However, by failing to perform sufficient conversion in the first step, insufficient solution viscosity is produced.
BRIEF SUMMARY OF THE INVENTION
In an exemplary embodiment of the invention, a continuous process for the manufacture of a polymer composition is disclosed. Particularly, the process is directed to the manufacture of a polymer including branched and linear segments by polymerizing diene monomers in the presence of an organolithium initiator of the general formula MR
x
to at least 90%, preferably 99% conversion, to produce polydiene chains. Thereafter, a coupling agent is added to obtain a polymer of mixed branched and linear polydiene units. The coupling agent is added at a ratio of about 0.3 to about 0.6 equivalents to organometallic initiator equivalents. The resulting polymer mixture has a solution viscosity in the range of about 150 to 190 cP (0.15 kg/m.s+0.19 kg/m.s) and a Mooney viscosity in the range of about 60 to 85 (ML4).
The process advantageously produces a mixture of linear and branched polymers, thereby gaining the benefits of the individual polymers without requiring separate production segments to make the individual products. Moreover, the process is performed continuously, not requiring separate polymerization stages and a subsequent blending of components. The present invention limits the coupled polymer percentage in the overall mixture to produce a high molecular weight fraction that would otherwise would be difficult to process by itself. The resultant polymer is particularly suited for use as an additive in the manufacture of HIPS and ABS resins.
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Firestone Polymers LLC
Lu Caixia
McCollister Scott
Palmer Meredith
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