CA2037684C - Vinyl chloride polymerization process and pvc obtained with said process - Google Patents

Abstract

Process for the suspension polymerization of vinyl chloride, either pure or mixed with other monomers, to produce PVC resins. The process uses, as suspending agent, a newly structured polyvinyl alcohol, so as to obtain PVC resins substantially exempt from closed cells and having an improved thermal stability, no electrostatic charges and a low content of ions of alkaline or earthy-alkaline metals, which make them particularly suited for use as insulating materials in the electrical field.

Description

VINYL CHLORIDE POLYMERIZATION PROCESS AND PVC OBTAINED WITH SAID PROCESS
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The present invention concerns a process for the suspension po-lymerization of vinyl chloride, either pure or mixed with other monomers, to obtain PVC resins particularly suited for use as insulating materials in the electrical field.
The invention also concerns the PVC resin obtained with said process, which resin distinguishes itself for the substantial absence of closed cells inside the particles forming the same.
As known, vinyl chloride suspension polymers are produced using, as suspension system, a mixture of different suspending agents.
Said mixture of suspending agents can for example be formed of one or more colloids, of a ionogenic or non-ionogenic wetting agent, and of a suspending agent which influences the ionic strength and improves the final characteristics of the polymer.
As protection colloids, use is made of gelatine, alginates, tragacanth gum, polyethylene oxides, polyvinyl alcohols with different degrees of hydrolysis, cellulose ethers.
As ionogenic and non-ionogenic emulsifying and wetting agents, use is made of alkyl sulphonic and alkyl sulphonated acids, alkyl naph-thalene sulphonates, salts of fatty acids, alkyl-aryl-polyglycol ethers, polyacrylates, and so on.
It is known to use vinyl acetate/vinyl alcohol copolymers - more simply, polyvinyl alcohols - as suspending agents for PVC, and their ef-fect on the morphological characteristics of PVC resins is equally known.
Examples of processes of this type are described in US-B-2,812,318 and in DE-A-1.171.158. The proportion of suspending agents used in these known processes varies from 0.03 to 1% by weight, on the weight of the monomer or mixture of monomers employed.
In PVC production processes using the known type polyvinyl alco-hols as suspending agents, it has however not been possible to obtain up to date PVC resins not showing, in fairly high percentages, the phenome-~ ~76 ~ 4 non of occluded or closed porosity, which influences negatively the eLimination of the residual monomer retained in the cells during the conventional production processes.
Said residual monomer therefore remains in the final resin and is thus gradually transferred into the environment, causing great health problems to the workers dealing with the production and conversion of said PVC.
The object of the present invention is a process for the suspension polymerization of vinyl chloride, either pure or mixed with other monomers, to produce PVC resins substantially exempt from closed ceLLs.
Another object of the invention is a vinyl chloride poLymerization process allowing to produce PVC resins with a low content of ions of alkaline or earthy-alkaline metals and with a very low electrical conductivity, which make them particularly suited for use as insulating materials in the electrical field.
According to the present invention, these and other objects are reached with a process for the suspension polymerization of vinyl chloride, either pure or mixed with other monomers, characterized in that use is made, as a primary suspending agent, of a polyvinyl alcohol of the type in which the alcohol groups and the acetate groups are distributed in blocks in the polymeric chains, the average degree of polymerization is between 150 and 1500 and the molar degree of hydrolysis is between 60% and 80%, and preferably between 65% and 75%, and between 5% and 10% of oligomers with a degree of polymerization between 5 and 30 are present in the distribution of the molecular weights.
The polyvinyl alcohol used as primary suspending agent in the polymerization process of the present invention, and the relative production process, form the object of a Canadian Patent application being simultaneously filed on march 6, 1991 by the Applicant under No. 2037685.
The present invention will anyhow be described more in detail hereinafter, also with reference to some examples ~ ~7~ ~ ~
of vinyl chloride polymerization which are however not meant to limit its scope.
The object of the polymerization process according to the pre-/
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2a ; -, ,~1 2037~&4 sent invention is to allow producing PVC resins - the PVC being pure or copolymerized with other monomers - substantially exempt from closed po-rosity. Closed porosity consists of cavities formed into the PVC parti-cles and not connected with the exterior; the monomer retained therein during the polymerization process then finds it very difficult to rapidly permeate through such cavities outside the particle at the end of the process. Closed porosity, and the consequent structural heterogeneity of the PVC resin, also leads to an overall deterioration of the general characteristics of said resin.
Closed porosity is determined by measuring the inherent density of the PVC particles (Bolakirkaya-Shtarkman), while open or accessible porosity is determined by mercury intrusion, using a porosimeter produced by the firm Carlo Erba of Milan, and determining the porosity on the resin as such and on the >100ju and <100,u fractions.
During studies carried out on the polymerization of PVC with different suspending agents, the Applicant has conceived a new process which, by using a particular polyvinyl alcohol as primary suspending agent and carrying out the polymerization reaction at a temperature bet-ween 50~ and 80~C, has surprisingly allowed to produce a PVC resin where-in the phenomenon of closed porosity is practically absent and which thus has an improved structural homogeneity. This new characteristic of PVC
resins, together with a very uniform distribution of their porosity, allows to reach high release speeds of the residual monomer contained in the cells of each PVC particle, so that, at the end of production, the PVC is practically exempt therefrom.
The polyvinyl alcohol used, in the present invention, as primary suspending agent of the polymerization process, is a polyvinyl alcohol in which the alcohol groups and the acetate groups are distributed in blocks in the polymeric chains, the average degree of polymerization is between 150 and 1500 and the molar degree of hydrolysis is between 60% and 80%, and preferably between 65% and 75%, and between 5% and 10% of oligomers with a degree of polymerization between 5 and 30 are present in the dis-2037~

tribution of the moLecular weights. Preferably, the degree of polymeriza-tion is between 200 and 1ûO0, the average length of the blocks of the alcohol groups is between 8 and 12 units, and the average length of the blocks of the acetate groups is between 3 and 5 units. Furthermore, the polyv;nyl alcohol used in the process of the present invention advanta-geously contains at least 0.20% by weight of carbonyl radicals.
The PVC resins obtained with the process of the present inven-tion differ from the similar resins existing on the market also for an improved thermal stability, for the absence of electrostatic charges, and for a higher percentage of polyvinyl alcohol grafted onto the PVC parti-cles during polymerization. Finally, thanks to the low content of ions of alkaline and earthy-alkaline metals in the suspending agents used in the process of the present invention, the PVC resins produced therewith have a high resistivity which make them particularly suited for use as insula-ting materials in the electrical field.
EXAMPLES
Polymerization of v1_yl_c_~ g_ Ex_mel_s_1-16 The following components are charged into a reaction vessel having a volume of 15 cubic meters and equipped with a Pfaudler stirrer:
100 parts of vinyl chloride 120 parts of demineralized water 0.045 parts of bis(4-terz.butyl-cyclohexyl)peroxidicarbonate x ppm of a polyvinyl alcohol.
The chemical-physical properties of the different samples of polyvinyl alcohols used in the Examples as suspending agents are reported in Table I. The proportion x in which said suspending agents are used in the polymerization process is reported in Table II. Table I reports the following parameters:
- average degree of polymerization - content of oligomers - viscosity at 4%

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- molar degree of hydrolysis - average number of units of the vinyl alcohol blocks - average number of units of the vinyl acetate blocks - average dimension of the particle - concentration in water - clouding temperature - surface tension - ions of alkaline or earthy-alkaline metals - toxic solvents: methanol and methanol acetate.
Table 1 also reports the data of comparison samples a) and b), consisting of polyvinyl alcohols available on the market. In particular, sample a) is sold by the British firm REVERTEX under the commercial name of ALCOTEX 72.5, while sample b) is sold by the German firm WACKER under the commercial name of POLYVIOL 05/290.
The polymerization is carried out at 54~C, at a stirring speed of 120 r.p.m., in the absence of oxygen. The reaction is stopped when a 90% conversion is reached, to which there corresponds an ~ P of 4.5 kg/cm . The reaction product is stripped under vacuum at 90~C for at least 100 minutes, dried, and analyzed for what concerns the following properties:
- K value of the PVC, measured according to DIN 53726 - closed porosity - open porosity - average diameter of the particle - granulometry - apparent density - residual vinyl chloride monomer - volume resistivity - VAc/VOH copolymer grafted on PVC
- thermal stability Ca-Zn - presence/absence of electrostatic charges.
The results of the tests are reported in Table II. Examples 1 to 2U~7~

4 refer to polyvinyL alcohols of known technique, while Examples 5 to 16 refer to the polyvinyl alcohols of the present invention, or to mixtures thereof.
_xamples 17-19 The aforedescribed polymerization process is repeated changing the polymerization temperature, which is now raised to 70~C. Examples 17 and 18 use the same polyvinyl alcohols as the previous Examples 1 and 9, while Example 19 uses the mixture of copolymers used in Example 13, in different proportions. The results of the tests carried out on the PVC
thus obtained are also reported in Table II. Example 17 refers to a VAc/VOH copolymer of known technique, while Examples 18 and 19 refer to the copolymers of the present invention, or to mixtures thereof.

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1 2,7 22,6 38,7 27,6 7,2 1,1 0,1 470 18 0,1 80 75 present 2 70,3 16,2 5,8 3,1 1,3 2,1 1,2 505 8 0,3 82 70 "

3 4,8 14,6 21,4 28,9 21,8 8,4 0,1 498 5 0,1 80 75 "
UD 4 11,3 26,1 40,4 15,4 4,3 2,4 0,1 492 10 0,2 80 70 "
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7 - 0,1 0,9 10,5 46,0 41,2 1,3 487 < 0,1 5,0 100 8j "
8 - 0,1 1,6 22,6 54,7 20,7 0,3 4~5 < 0,1 11,0 100 80 "
9 - 0,6 4,3 26,8 50,8 17,3 0,2 485 < 0,1 14,0 100 85 "
0,1 1 13,7 40,6 34,8 9,7 0,1 480 < 0,1 18,0 100 80 "
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Claims (5)

1) Process for the suspension polymerization of vinyl chloride, either pure or mixed with other monomers, characterized in that use is made, as a primary suspending agent, of a polyvinyl alcohol of the type in which the alcohol groups and the acetate groups are distributed in blocks in the polymeric chains, the average degree of polymerization is between 150 and 1500 and the molar degree of hydrolysis is between 60%
and 80% , and between 5% and 10% of oligomers with a degree of polymerization between 5 and 30 are present in the distribution of the molecular weights.

2) Process as in claim 1), wherein said polyvinyl alcohol contains at least 0.20% by weight of carbonyl radicals.

3) Process as in claim 1), wherein the molar degree of hydrolysis of said polyvinyl alcohol is between 65% and 75%.

4) Process as in claim 1), wherein the polymerization temperature is between 50° and 80°C.

5) PVC resin obtained with a process as in claims 1) or 2), characterized in that it is substantially exempt from closed cells.