Synthetic resins or natural rubbers -- part of the class 520 ser – Synthetic resins – Treating polymer containing material or treating a solid...
Reexamination Certificate
2000-02-16
2001-01-30
Acquah, Samuel A. (Department: 1721)
Synthetic resins or natural rubbers -- part of the class 520 ser
Synthetic resins
Treating polymer containing material or treating a solid...
C528S487000, C528S490000, C528S491000, C528S492000, C528S503000, C524S081000, C524S115000, C524S155000, C524S167000, C524S284000, C524S297000, C524S366000
Reexamination Certificate
active
06180756
ABSTRACT:
FIELD OF THE INVENTION
This invention concerns a process for the addition of volatile materials, such as catalysts or treatment agents, to prepolymers prior to or during solid state polymerization processes and the subsequent solid state polymerization process. Optionally, the volatile materials, having completed their function, may be removed from the polymer during or after the solid state polymerization process.
TECHNICAL BACKGROUND
Various publications describe the uses of and methods of using catalysts or other additives during a solid state polymerization process of condensation polymers.
In these polymerization processes, it has been customary to introduce the catalyst species into the melt phase of the polymerization process followed by solidification and, optionally, crystallization. Thus, when said catalyst treated polymer is subjected to solid state polymerization, the catalyst is available to exert its catalytic action. Catalyst remains in the finished, solid state polymerized product and all end use polymer products contain measurable quantities of the catalytic species. In any subsequent use, where the catalyst-containing polymer is exposed to heat, a molecular weight increasing condensation reaction may start to occur because the catalyst is still present.
The present invention adds the catalyst or other treatment agent as a gas or dissolved in a liquid, which improves the contact of the polymer, typically in the form of a particle or a pastille, with the catalyst or treatment material and, if the agent is sufficiently volatile, also facilitates removal of the agent from the system. The agent is then removed easily from the system after contact with the polymer by the inert gas sweep employed in solid state polymerization processes and the resulting polymerization product is substantially free of catalyst or treatment agent.
SUMMARY OF THE INVENTION
This invention provides a process for the addition of volatile treatment agents to a solid state polymerization in a condensation polymerization process comprising:
a) establishing a recirculating gas flow over polymer particles undergoing solid state polymerization;
b) introducing a volatile treatment agent into said recirculating gas flow; and
c) contacting said polymer particles with said volatile treatment agent under solid phase polymerization conditions.
This invention further provides a process for the addition of volatile treatment agents to a solid state polymerization in a condensation polymerization process comprising:
a) contacting polymer particles with a solution of a volatile treatment agent in a suitable solvent;
b) removing said solvent to yield polymer particles coated with or containing said treatment agent;
c) subjecting said polymer particles to solid state polymerization in the presence of a gas flow.
This invention may be used with additive materials such as catalysts, treatment agents, catalyst deactivators, nucleating agents, antioxidants, ultraviolet stabilizing agents, plasticizers, thermal stabilizers, comonomers, tinting agents and barrier property enhancers. In some of these embodiments it is desirable to remove the additive material after contact with the polymer, although in some embodiments herein the additive is incorporated into the polymer as part of the final product.
DETAILED DESCRIPTION OF THE INVENTION
The process of the present invention applies to the polymerization of polymers where the polymerization process is subject to catalysis or other treatment. Suitable polymer types include polyesters, polyamides and polycarbonates, including homopolymers and copolymers of these various polymer types. The polymer to which the process of the present invention is applied typically has a degree of polymerization in the range of from 5 to 25.
In working with these polymers it has been customary to introduce the catalyst species into the melt phase of the polymerization process followed by solidification and crystallization.
According to the practice of the present invention, a catalyst or treatment material effective in solid state polymerization is introduced into the solid state polymerization stage via a gas stream that is introduced to, and vented from, the solid state polymerizer. It is also within the scope of the present invention to introduce the catalyst or treatment agent via a gas stream introduced to a preheater or conditioner vessel upstream of the solid phase polymerizer.
The catalyst or treatment material must be sufficiently volatile, i.e., it has a high enough vapor pressure, to be introduced via the gas stream, and, optionally, to also be removed via the gas stream. Thus, if desirable, by stopping the vapor borne supply of catalyst or treatment material, but continuing the vapor sweep through the solid state polymerization vessel, the amount of catalyst remaining in the subject polymer may be substantially reduced. This offers potential utility both in polymer purity and stability. In certain condensation polymers known in the art, residual catalyst lends itself to polymer instability, especially during the course of post-polymerization treatment steps or uses that involve exposure to elevated temperatures.
Alternatively, the additive may be introduced by use of a solution of the additive in a suitable solvent, followed by removal of said solvent. In this embodiment, polymer particles are contacted with the treatment agent, then after solvent removal, the coated polymer particles are subjected to solid state polymerization in the presence of a vapor sweep. If the agent is sufficiently volatile, and the solid state polymerization is sufficiently lengthy, the additive may be completely removed by the vapor sweep leading to the same potential advantages as described above for vapor state addition of volatile agents.
As mentioned above additives such as catalysts, treatment agents, catalyst deactivators, nucleating agents, antioxidants, ultraviolet stabilizing agents, plasticizers, thermal stabilizers, co-monomers, tinting agents and barrier property enhancers may be contacted with the polymer in the solid state polymerizer. Examples of catalyst additives useful herein include the following: benzene-sulfonic acid, methanesulfonic acid triflic acid (trifluoromethanesulfonic acid), toluene sulfonic acids, especially p-toluene sulfonic acid, other volatile Bronsted and Lewis acids, tetra isopropoxy titanate and tri butoxy antimonate. Volatile Bronsted acids are preferred. It is to be noted that Bronsted acids are generally not useful in conventional solid state polymerization processes of polyesters due to excessive dialkylene glycol formation.
Certain grades of polyester, such as for the bottle resin market, are typically polymerized to high molecular weight in the melt phase, i.e., to ~0.65 IV, and then subjected to post-polymerization solid phasing to raise the molecular weight even further to levels needed for bottle resins or for industrial fibers. Example 4 shows that the process of the present invention can be used to increase rates of this post polymerization solid phasing.
Viscosities reported below were obtained with a Viscotek Forced Flow Viscometer. Polyesters were dissolved in trifluoroacetic acid/methylene chloride. The viscosity data reported have been correlated to the intrinsic viscosity in 60/40 wt % phenol/tetrachloroethane following ASTM D4603-96.
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W. A. Herrmann et al., Volatile Metal Alkoxides According to the Concept of Donor Functionalization,Angew Chem. Int. Ed. Engl., 34, 2187-2206, 1995.
Kanak B. Dass et al., Solid State Polymerisation—A Review, 11, 39, 501-405, 1996.
H. A. Ghatta et al., Le Reazioni Allo Stato Solido, 1, 98, 33-42, 1996.
Acquah Samuel A.
E. I. Du Pont de Nemours and Company
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