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Document Number
US Patent 3689578
Issued Date
PROCESS FOR THE PRODUCTION OF VINYLICALLY CHLORINATED OLEFINS
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Abstract
A process for producing tetrachloroethylene comprising passing a gas stream of ethylene over a catalyst composition of cupric chloride and an inert material at a temperature in the range of 400 to 525.degree. C. and at a flow rate of less than 5 cc of gas stream per minute per gram of cupric chloride. 6 Claims, No Drawings
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Number of Claims:
6
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Published
PROCESS FOR THE PRODUCTION OF VINYLICALLY CHLORINATED OLEFINS
Application Number
04/870,949
Filed
October 7, 1969
US Classification
570/227   570/230
Int'l Classification
C07C   17/10   (20060101)   C07C   17/00   (20060101)   B01J   27/06   (20060101)   B01J   27/10   (20060101)  
Examiner
Assistant Examiner
Parent Case
This application is a division of Ser. No. 499,041 filed on 10/20/65 and now U.S. Pat. No. 3,501,539.
USPTO Field of Search
260/656R   260/654R   260/659A   260/654A   260/662A   260/659R  
Related Patents
4157380 - Recovery of hydrogen chloride and chlorine from chlorine-containing organic wastes

This invention relates to a process of removing chlorine (Cl.sub.2) and hydrogen chloride (HCl) from a combustion gas, such as a combustion gas formed from incinerating chlorine-containing organic materials, which comprises: (1) Lowering the temperature of the combustion gas below the melting point of cupric chloride or mixture thereof with other salts; (2) Contacting the cooled combustion gas of step (1), in the presence of oxygen, with copper of lower than a divalent oxidation state, such as a cuprous compound or its equivalent in a quantity sufficient to absorb chlorine and hydrogen chloride present in gas, thereby converting the cuprous compound to cupric chloride (in order to absorb substantially all HCl and Cl.sub.2 it is desirable to employ a stoichiometric excess of cuprous compound); (3) Contacting cupric chloride with a reducing agent, thereby converting the cupric chloride to cuprous chloride or an equivalent compound of lower than divalent oxidation state and the reducing agent to a chlorinated product. The products formed from the reducing agent in step (3) can be removed; and cuprous chloride formed in step (3) can be reused in step (2).

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