packs for pills.
By kind permission of Valmai Firth.
Chloroethene (vinyl chloride) is also used to produce co-polymers, for example with ethenyl ethanoate (vinyl acetate). The co-
polymer can be processed at much lower temperatures than poly(chloroethene) homopolymers of the same relative molecular
mass. It is used for coating metals and wood. The film is flexible, hard wearing, resistant to chemical attack and can be
pigmented so that it is particularly suitable, for example, for ships. The co-polymer is also used in adhesives and in inks.
Annual production of poly(chloroethene) (polyvinyl chloride)
World43 million tonnes
Europe10 million tonnes
Russia0.51 million tonnes
1
Data from:
1. Federal State Statistics Service: Russian Federation 2011
Manufacture of poly(chloroethene) (polyvinyl chloride)
The production of PVC involves several stages:
a) ethene is converted into 1,2-dichloroethane
b) 1,2-dichloroethane is cracked to chloroethene (vinyl chloride)
c) polymerization of chloroethene (vinyl chloride)
(a) Production of 1,2-dichloroethane
Ethene is obtained from the cracking of ethane, propane, naphtha and gas oil. In practice, two processes for the overall
conversion of ethene to chloroethene are used in parallel.
(i) Direct chlorination
Ethene is reacted with chlorine in the liquid phase, using excess chloroethene as solvent. The catalyst, iron(lll) chloride, is
soluble in chloroethene. The reaction is exothermic, and no external heat is needed.
The reaction temperature is maintained at 320-350 K and with a pressure of ca 4 atm. Higher temperatures give unwanted
polychlorinated compounds.
(ii) Oxychlorination route
The cracking of 1,2-dichloroethane during stage (b) of the overall process forms hydrogen chloride as a by-product. It is
unwanted as hydrogen chloride and is very detrimental to the environment. However, it can be used in this second method of
making 1,2-dichloroethane.
Ethene is mixed with hydrogen chloride and air (enriched with oxygen). The gases are passed over a heated solid catalyst in
metal tubes, in a fluid bed reactor, maintained at ca 500 K and 5 atm.
Figure 4 A diagram to illustrate the use of a fluid bed reactor for the
oxychlorination of ethene to chloroethene. On the left hand side, the
catalyst particles are at rest. On the right hand side, the the particles are
now acting as a fluid, as the gaseous reactants pass through the solid.
The catalyst generally used is a mixture of copper(ll) and potassium chlorides, deposited on alumina.
As the reaction is highly exothermic, the reactor vessel is cooled to give the optimum reaction temperature and to reduce
unwanted by-product formation of, for example, chloroethane and 1,1,1,2-tetrachloroethane. 95% conversion of ethene to 1,2-