EP0000430A1

EP0000430A1 - Vinyl halide polymerization process

Info

Publication number: EP0000430A1
Application number: EP78300113A
Authority: EP
Inventors: Boris Englin
Original assignee: ICI Australia Ltd
Current assignee: Orica Ltd
Priority date: 1977-07-15
Filing date: 1978-06-30
Publication date: 1979-01-24
Also published as: DE2860931D1; EP0000430B1

Abstract

A process for the homo- or copolymerization of vinyl halide, particularly vinyl chloride, in an aqueous dispersion, which process is characterized by the addition, to the polymerization reaction medium, of a composition comprising metal ions selected from the group consisting of chromium, copper, cobalt, nickel, manganese, tungsten and molybdenum; the composition may also contain a water-soluble aliphatic amine and a substituted quinone or substituted hydroquinone.

Description

The present invention relates to a process for the polymerization of vinyl halide monomers such as vinyl chloride in aqueous dispersion.
By polymerization in aqueous dispersion is meant polymerization in aqueous emulsion or aqueous suspension (including aqueous microsuspension), optionally in the presence of colloids such as polyvinyl alcohol and/or surfactants.
When vinyl halide monomers, particularly vinyl chloride, are polymerized in aqueous dispersion in a reactor it is well known that a problem arises in that the surfaces inside the reactor become coated with tenaciously adhering polymeric material known as build-up. The formation of tenaciously adhering build-up is undesirable from the point of view of achieving efficient heat transfer for cooling and heating the reactor contents, effective usage of monomer, effective control and monitoring of the polymerization reaction, and acceptable polymer quality (in view of contamination by dislodged particles of the build-up).
This deposit, which varies in thickness, hardness and degree of adhesion to the metal is composed of polymer in several different physical forms. The main type, particularly from the standpoint of routine cleaning, is a hard film over the whole surface of the reactor. The thickness of this film varies from batch to batch but is normally a few thousandths of an inch thick. The other types are hard or soft lumps which accumulate locally in the reactor or powder which is more generally distributed. The soft lumps are composed of material that has escaped the washing out process and are comparatively easy/to remove. The hard lumps are believed to originate as soft material that has been allowed to stay in the reactor for more than one batch or simply by polymerization of vinyl chloride in an area of very high or very low agitation, i.e. an area where the normal droplet protection of the granulating agent is ineffective. They are normally found in roof ports, on staging brackets, on the impeller, or indeed any area where there is a sever discontinuity to the surface in the reactor. They are very difficult to remove, normally requiring a hammer and chisel. A somewhat similar type of build-up can be formed, when a reactor is inadequately cleaned, by growth on to skin build-up remaining. This type of build-up along with lumps from impellers can detach itself from the reactor wall during a batch and has to be removed manually from the reactor at frequent intervals, otherwise blockage of the valve or slurry transfer lines will result. It is known that the amount of build-up produced is much larger if the reactor is inadequately cleaned. Powder type build-up is often quite firmly attached to the surface and is at its thickest at or above the liquid level in the reactor where it has been deposited by splashing.
Because of the problems in respect of heat transfer, polymerization control and polymer quality, it is necessary to clean the reactor between each polymerization cycle wherein the deposited material is removed as completely as possible, e.g. by scraping by hand, solvent cleaning or pressure-washing. This is wasteful in terms of the expense of the equipment and manpower required to carry out such cleaning and also in terms of the loss of productivity for a given reactor arising from the time taken to effect the cleaning operation.
This formation of build-up, which increases with polymerization time, is also a major difficulty in the development of a trouble-free continuous process for the aqueous dispersion polymerization of vinyl halide monomers such as vinyl chloride.
There have been proposals in the published literature of processes of coating the internal surfaces of reactors used for vinyl halide polymerization with numerous substances, both inorganic and organic, in order to prevent or reduce the formation of build-up therein.
In our experience, we have found that while some substances certainly inhibit the formation of build-up, they tend to form coatings whose adherence to the reactor surface becomes weakened during the course of the polymerization reaction; such coatings are therefore liable to become partly or wholly detached from the reactor surface during subsequent polymerizations in the reactor leading to the formation of build-up. Consequently it is necessary to recoat the reactor internal surfaces between each polymerization cycle if the anti-build-up action of the coating substance is to be effective in the following polymerizations in the reactor. This adds to the cost of the polymerization process.
We have now discovered a process whereby vinyl halide monomers such as vinyl chloride may be polymerized in aqueous dispersion without any or with very much reduced formation of build-up.
According to the present invention there is provided a process for the polymerization of vinyl halide monomers in aqueous dispersion which process is characterized by the addition of a composition comprising metal ions. The metal ions are those derived from the metals of Groups Ib to VIIb inclusive, and Group VIII, but are preferably selected from the group consisting of chromium, copper, cobalt, nickel, tungsten, molybdenum, and manganese. Ferric and ferrous ions are also effective but may lead to contamination of the product polymer.
While the compositions of our invention can be applied to the internal surfaces of the polymerization reactor, we prefer to add the compositions to the polymerization reaction medium. It is a particular advantage of our process that the composition can be added to the reaction medium without opening the reactor. The reactors used for the polymerization do not need to be opened between each polymerization cycle, either to remove adhering build-up, or to apply or remove anti-build-up coatings.
The nature of the composition comprising these ions is not narrowly critical. We have found for example that good results may be obtained using an aqueous solution of the ion in the form of simple salts such as for example, nitrates, sulphates and acetates. Particularly good results are obtained using the chlorides. The ion may also be in the form of complex ions such as amine complexes or complexes of the metallic ion with polyethers.
Typical compositions comprising these metal ions are cuprous chloride, cupric sulphate, nickelous chloride cobaltous chloride,chromic chloride, manganese sulphate and ammonium molybdate. Oxide compositions, for example chrominum trioxide and tungsten trioxide, may conveniently be dissolved in dilute acids such as hydrochloric and sulphuric acids. Preferably the composition comprises copper, nickel, and cobalt ions, and most preferably the composition comprises chromium ions. Compositions comprising two or more of the said metal ions may also be used.
While the metal ion can beadded to the reactor contents during the polymerization, we prefer to add the metal ion at or before the start of the polymerization reaction. It is a surprising feature of the process of our invention that small or catalytic amounts of the metal ions are effective in inhibiting build-up. The actual amount is not narrowly critical and we have found good results may be obtained if the amounts added are in the range from 0.001% to 0.1% w/w based on the monomer content in the polymerization.
Other additives known to suppress build-up may also be added to the autoclave. In particular we have found that good results may be obtained if the metal ion is added to the reaction mixture prior to the polymerization and during the polymerization a solution of a hydroquinone or a quinone, such as benzoquinone or naphthoquinone, is injected into the reaction mixture. Preferably the concentration of hydroquinone or quinone is less than 0.02 to 0.03% w/w based on the monomer content, since above this level the polymerization reaction may be inhibited.
The operating conditions for polymerization according to the process of the present invention may be those customarily used. For example, in the case of vinyl chloride polymerisation, the temperature is generally below 110°C and typically between 40 and 80°C and the pressure generally below 15 kg/cm². Compositions of metal ions of our invention comprising bromides are preferably used in polymerization processes carried out at temperatures below 60°C.
Although the invention has been described with reference hereinbefore to the polymerization of vinyl chloride, it is also applicable to vinyl halide monomers in general.
By "vinyl halide monomers" is meant those monomers polymerizable by free-radical polymerization which are olefinically unsaturated in the alpha position and substituted by at least one halogen atom. These monomers are preferably selected from substituted derivatives of ethylene and contain only two carbon atoms. Examples of such monomers include vinyl chloride, vinyl bromide, vinyl fluoride, vinylidene chloride, vinylidene fluoride, chlorotrifluoroethylene and tetrafluoroethylene. The invention is preferably applied to the polymerization of fluorine- or chlorine-containing vinyl monomers, especially vinyl chloride.
By "polymerization" is meant both the homopolymerization of the vinyl halide monomers and the copolymerization with each other or with other comonomers copolymerizable therewith. Examples of the latter include vinyl esters such as vinyl acetate, acrylic esters such as methyl acrylate and butyl methacrylate, acrylic nitriles such as acrylonitrile and methacrylonitrile, unsaturated diesters such as diethyl maleate, allyl esters such as allyl acetate, α-olefines such as ethylene and propylene, vinyl ethers and styrene compounds.
However, we prefer to apply the invention to the production of polymers containing at least 50% molar, and more particularly at least 8Q% molar, of units derived from vinyl halide monomers, particularly vinyl chloride.
The process according to the invention may be employed in any polymerization technique where the monomer(s) is dispersed in the form of droplets in a liquid aqueous phase. For example it may be used for polymerization in aqueous emulsion in which case any suitable emulsifying agent such as sodium lauryl sulphonate or sodium dodecyl benzene sulphonate and non-ionic emulsifying agents may be used.
The process of the invention is also most applicable to polymerization in aqueous suspension and microsuspension.
Any suitable dispersing agent may be used for polymerization in aqueous suspension, and particularly finely dispersed solids, gelatin, polyvinyl acetates of various degrees of hydrolysis, water-soluble cellulosic ethers and polyvinyl pyrrolidones. These dispersing agents can be used together with surface-active agents if desired. The amount employed may vary widely and is generally between 0.05 and 1.5% by weight calculated on the amount of water used.
Any suitable free-radical polymerisation initiator that is monomer-soluble may be used for polymerization in aqueous suspension. Examples of these include peroxy compounds such as di-tertiary-butyl peroxide, lauroyl peroxide and acetyl cyclohexyl sulphonyl peroxide, t-butyl perpivalate,azo compounds such azo-bis-isobutyronitrile and 2,2'-azo-bis-2,4-dimethyl-valeronitrile,and boron alkyls. Monomer-soluble free-radical polymerization initiators that are particularly suitable for use in the process according to the invention are the dialkyl peroxydicarbonates whose alkyl radicals contain up to 20 carbon atoms, such as diethyl peroxydicarbonate, diisopropyl peroxydicarbonate and di(tertiarybutyl-cyclohexyl)peroxydicarbonate, and 2,2'-azo-bis-2,4-dimethylvaleronitrile and azo-bis-isobutyronitrile. These initiators may be used in conventional quantities - generally speaking from 0.01 to 1% by weight calculated on monomer.
Polymerization in homogenised aqueous dispersion, sometimes known as polymerization in microsuspension, comprises mechanically homogenising an aqueous dispersion of the monomer or monomers in the presence of a surface-active agent (for example by subjecting it to a violent shearing action), and polymerizing the homogenised dispersion in the presence of an initiator that is monomer soluble.
Conventional emulsifying agents and monomer-soluble initiators can be used for polymerization in microsuspension such as for example an ionic emulsifying agent like sodium dodecylbenzenesulphonate, and peroxide initiators of the dialkanoyl peroxide type, e.g. lauroyl peroxide.
In addition to the emulsifying or dispersing agents and initiators, the aqueous dispersions (i.e. suspensions, microsuspensions and emulsions) may contain one or more additives that are normally employed in conventional processes for polymerization in aqueous dispersion. Examples of such additives include particle size regulators, molecular weight regulators, stabilisers, plasticisers, colouring agents, reinforcing agents and processing aids.
The polymerization medium may also contain one or more substances which themselves inhibit polymerization build-up.
Our invention is illustrated by, but by no means limited to the following examples.

Example 1

Conventional method used as a control to compare with the improved methods.
A stainless steel pressure vessel of 7 litres nominal capacity equipped with heating and cooling means was charged with 3500 ml of demineralized water, 2.4 g of a peroxydicarbonate catalyst and 1.75 g polyvinyl alcohol (partially hydrolyzed polyvinyl acetate). The contents of the vessel were stirred and the air above the liquid was removed by evacuation. Vinyl chloride monomer (3000 g) was added to the evacuated vessel and the contents were heated to 56°C. The temperature was maintained until pressure drop indicated the end of the reaction of polymerization.
The residual gas was vented off and the slurry of polyvinyl chloride in water was dropped down through the bottom valve. The lid was opened and the remaining loose polymer was rinsed with water and the firm deposition of the polymer inside the autoclave was examined.
There was a deposit of polymer firmly attached to the wall, to the stirrer shaft and to the thermometer well. The build-up was particularly prominent at the liquid-gas boundary.
To remove the deposit use of a scraper was necessary. The deposit on the stirrer shaft and on the stirrer blades was particularly hard to dislodge and it was necessary to use a screw driver with a gentle blow of a hammer to chip off particularly hard portions of the build-up.
The total weight of the deposit constituted 0.6% w/w of the vinyl chloride monomer charged to the autoclave.

Example 2

The pressure vessel of Example 1 was thoroughly cleaned free from all deposit, washed and dried. The charging procedure of Example 1 was repeated and 5 minutes after vinyl chloride addition, a solution of 0.22 g of copper chloride dihydrate (0.003% w/w copper ion on vinyl chloride charge) in 35 mls water was injected into the polymerization mixture. When reaction was on temperature for an hour 0.25 g of hydroquinone, in 35 mls of water were injected and the reaction was finished as described in

Example 1.

In this batch a deposit not exceeding 0.05% w/w of the initial charge of the monomer remained in the autoclave. This deposit could be readily removed.

Example 3

The pressure vessel of Example 1 was thoroughly cleaned free from all deposit, washed and dried. Nickel chloride (0.4 g; 0.003% w/w nickel ion on vinyl chloride) was added to the water charge and the procedure of Example 1 repeated.
The autoclave walls and roof were virtually free from build-up. Very little easily removed deposit was found on the shaft and around the gland. The overall amount of build-up was ca. 0.02% w/w of the initial monomer charge.

Example 4

A solution of cuprous polyether complex was prepared as follows:
To 100 ml of a saturated sodium chloride solution was added 7 g of purified cuprous chloride powder. To prevent oxidation the resulting mixture was stirred by passage of nitrogen until the cuprous chloride was completely dissolved. Sufficient sulphur dioxide was added to Lhe solution to give it a concentration of approximately 0.5 g/1 of sulphur dioxide. This solution was then extracted with 70 ml of a polyether prepared by sequentially condensing one mole of methanol with four moles of ethylene oxide and two moles of propylene oxide. The phases were allowed to separate and the colourless polyether layer removed. The polyether solution contained 5 g/litres of cuprous ion.
The pressure vessel of Example 1 was thoroughly cleaned free from all deposit, washed and dried. The charging procedure of Example 1 was repeated followed by two consecutive injections of 35 ml of aqueous solution of the cuprous/polyether solution prepared above, and 5 mls of 0.43 g triethylenetetramine solution in alcohol. The general process of Example 1 was repeated. After polymerization the autoclave walls, roof and paddle were virtually clean from any build-up. Firmly attached polymer deposit was situated only around the shaft. The overall amount of hard build-up was ca. 0.2% w/w of the monomer charge.

Example 5

The pressure vessel of Example 1 was thoroughly cleaned free from all deposit, washed and dried. A solution of nickel chloride hexahydrate and tetraethylenepentamine (1:1 w/w) in water (50 w) was sprayed on the internal surfaces of the vessel which had been preheated to 60°C. After 5 min drying the surfaces were resprayed and dried again. Then the reactor was left at 60 to 70°C for 30 min. Nickel chloride hexahydrate (1 g, 0.008% w/w nickel ion on vinyl chloride) was added to the water charge and the procedure of Example 1 repeated.
The autoclave walls and roof were free from build-up except for a few small patches of skin build-up on top of the autoclave. Some seed-like build-up was found on the shaft and around the gland.

Example 6

The pressure vessel of· Example 1 was thoroughly cleaned free from all deposit, washed and dried. The vessel was heated to 70°C, sprayed with a 2% w/w solution of hydroquinone and tetraethylenepentamine (1:1) in a mixture (1:1) of water and ethanol and kept at 60 to 80°C for 30 min. All surfaces were then washed with cold water. Copper chloride dihydrate .7 g, 0.011% w/w copper ion on vinyl chloride) was added to the water charge and the procedure of Example 1 repeated.
The autoclave walls were free from build-up. Few patches of build-up film were found on the shaft and paddle. The overall amount of build-up was a negligible .02% w/w of the initial monomer charge.

Example 7

The procedure of Example 6 was repeated except that the solutions of hydroquinone/tetraethylenepentamine and copper chloride, respectively, were replaced by:

(ii) Nickel chloride hexahydrate 0.7 g

(0.006% w/w nickel ion on vinyl chloride)
After the polymerization reaction was completed the internal surfaces of the vessel were inspected. Only a few patches of build-up were found on the lid, walls, and gland. A few loose lumps were removed from the shaft and paddle.

Example 8

The pressure vessel of Example 1 was thoroughly cleaned free from all deposit, washed and dried. Nickel chloride hexahydrate (0.39 g, 0.0032% w/w nickel ion on vinyl chloride) and copper chloride dihydrate (0.22 g, 0.0035% w/w copper ion on vinyl chloride) was added to the water charge and the procedure of Example 1 repeated.
The autoclave walls and lid were clean and shiny. The paddle was partly covered by skin build-up. A few loosely attached lumps and some powdery build-up was found around the shaft and glands.

Example 9

The pressure vessel of Example 1 was thoroughly cleaned free from all deposit, washed and dried. The charging procedure of Example 1 was repeated and 5 min after vinyl chloride addition a solution of 0.78 g nickel chloride hexahydrate (0.006% w/w nickel ion on vinyl chloride) in 21.3 ml of water and 1 ml of concentrated hydrochloric acid was injected into the polymerisation mixture.
The autoclave surfaces were covered by a film of a light build-up with lumps on the shaft and in the gland area. The amount of build-up was 0.5% w/w on the initial monomer charge.

Example 10

The procedure of Example 9 was repeated except that ;he solution of nickel chloride was replaced by a solution of manganese chloride tetrahydrate (0.48 g) in 14 ml water (0.004% w/w manganese ion based on vinyl chloride). After the reaction the internal surfaces of the vessel were inspected and the amount of residual build-up was similar to that observed in Example 9.

Example 11

The pressure vessel of Example 1 was thoroughly cleaned free from all deposit, washed and dried. The charging procedure of Example 1 was repeated and 5 min after vinyl chloride addition a solution of 0.22 g of copper chloride dihydrate (0.003% w/w copper ion based on vinyl chloride) in 10 ml of water and .5 ml concentrated hydrochloric acid was injected into the polymerisation mixture.
One hour after the start of the polymerization reaction 0.25 g of hydroquinone in 10 ml of water were injected, followed after one and a half hour by injection of 0.20 g of sodium nitrite in lp ml of water. The reaction was then finished as described in Example 1.
In this batch the autoclave walls, lid and gland were very clean and shiny throughout. Only a few minor patches of build-up were found on the shaft and paddle. The overall amount of the build-up deposit was only 0.2 g, or 0.007% w/w of the initial monomer charge.

Example 12

The procedure of Example 3 was repeated except that the nickel chloride was replaced by 0.22 g of copper chloride dihyrate. After the polymerization reaction was completed the internal surfaces of the vessel were inspected and found to be substantially free of build-up. The total amount of build-up was ca. 0.03% w/w of the initial monomer charge. This build-up was mainly restricted to a film around the top edge of the vessel.

Example 13

The procedure of Example 12 was repeated except that the solution of .22 g of copper chloride dihydrate in water was injected into the polymerisation mixture 5 min after charging the vinyl chloride. The amount of build-up on the internal surfaces of the polymerization vessel after the reaction was completed was similar to that obtained in Example 9.

Example 14

The pressure vessel of Example 1 was thoroughly cleaned free from all deposit, washed and dried. Manganese chloride tetrahydrate .(0.4 g; 0.004% w/w manganese ion on vinyl chloride) was dissolved in the polyether referred to hereinbefore and the solution injected into the autoclave 5 min after the vinyl chloride was charged.
A light skin of build-up covered the internal walls and lid of the vessel. A somewhat heavier build-up deposit was found on the paddle, shaft and around the gland. The amount of deposit was ca. 0.07% w/w on the initial charge of the monomer.

Example 15

The procedure of Example 1 was followed except that copper chloride (0.5 g dihydrate; 0.006% w/w copper ion on vinyl chloride) was added to the water charge.
No retardation or inhibition of the reaction occurred as compared to a control run. The walls of the vessel were shiny and completely free from build-up. A few small patches of film build-up were found on the lid. There was some lumpy powder build-up on the shaft, gland and paddle.

Example 16

The procedure of Example 15 was repeated except that the copper chloride was replaced by 0.75 g of cobaltous chloride hexahydrate (0.006% w/w cobalt ion on vinyl chloride).
There were patches of film build-up on the autoclave walls. The lid surface was marginally better than in control experiment. Most of the build-up was around the gland and top part of the shaft.

Example 17

The procedure of Example 15 was repeated except that the copper chloride was replaced by 0.6 g of cupric acetate monohydrate (0.006% copper ion on vinyl chloride). No retardation or inhibition of the polymerization reaction occurred as compared to a control run.
The autoclave walls were shiny and completely free from build-up. Again, as in Example l5, only few small patches of film build-up were found on the lid and paddle. Powder-like build-up and some film build-up (partly peeled off) were found on the shaft and gland.

Example 18

The procedure of Example 15 was repeated except that the copper chloride was replaced by a solution of 1.55 g of chromyl chloride (0.017% w/w chromium ion on vinyl chloride) prepared by dissolving 1 g of chromium tioxide in 3.4 ml of 32% w/w hydrochloric acid and diluting to 100 ml with water.
The internal walls of the vessel, including the lid and paddle and shaft, were very shiny and completely free from any build-up;

Claims

1. A process for the polymerization of vinyl halide monomers in aqueous dispersion which process is characterized by addition to the polymerization reaction medium of a composition comprising metal ions selected from the group consisting of chromium, copper, cobalt, nickel, manganese, tungsten and molybdenum.

2. A process according to claim 1 wherein the said polymerization is carried out at a temperature below 110°C.

3. A process according to claim 2 wherein the temperature is in the range from 40⁰ to 80°C.

4. A process according to any one of claims 1 to 3 wherein the weight of metal ion is in the range of 0.001 to 0.1% of the weight of the monomer.

5. A process according to any one of claims 1 to 4 wherein the metal ion is in the form of a water-soluble salt.

6. A process according to claim 5 wherein the salt is selected from the group consisting of nitrate, sulphate, chloride, and acetate.

7. A process according to claim 5 wherein the composition contains a water-soluble aliphatic amine.

8. A process according to any one of claims 1 to 7 wherein the composition comprises a substituted quinone or substituted hydroquinone.

9. A process according to any one of claims 1 to 7 wherein the composition comprising the metal ion is added prior to the start of the polymerization reaction and hydroquinone is added during the polymerization reaction.

10. A process according to any one of claims 1 to 9 wherein the composition comprises cupric chloride.

11. A process according to any one of claims 1 to 9 wherein the composition comprises chromyl chloride.

12. A process according to any one of claims 1 to 11 wherein the vinyl halide monomer is vinyl chloride.