Process for producing highly pure chlorinated alkane

A process for producing highly pure chlorinated alkane in which a chlorinated alkene is contacted with chlorine in a primary reaction zone to produce a reaction mixture containing the chlorinated alkane and the chlorinated alkene, and extracting a portion of the reaction mixture from the primary reaction zone, wherein the molar ratio of chlorinated alkane:chlorinated alkene in the reaction mixture extracted from the primary reaction zone does not exceed 95:5, wherein the reaction mixture extracted from the primary reaction zone is subjected to a principal conversion step in a principal reaction zone to produce a chlorinated alkane rich product, which is extracted from the principal reaction zone, and wherein the principal conversion step comprises a reduced temperature conversion step in which the reaction mixture extracted from the primary reaction is fed into a principal reaction zone operated at a reduced temperature of about −30° C. to about 30° C., and the chlorinated alkane rich product is extracted from the principal reaction zone.

A process for producing a product rich in a chlorinated alkane comprising a reduced temperature conversion step in which a reaction mixture comprising chlorine, chlorinated alkene and the chlorinated alkane is fed into a principal reaction zone operated at a temperature of about −30° C. to about 10° C., and extracting the product rich in the chlorinated alkane from the principal reaction zone.

A process for producing a product rich in a chlorinated alkane comprising a reduced temperature conversion step in which a reaction mixture comprising chlorine, chlorinated alkene and the chlorinated alkane is fed into a principal reaction zone operated at a temperature of about −30° C. to about 30° C., and extracting the product rich in the chlorinated alkane from the principal reaction zone.

A process for producing a product rich in a chlorinated alkane comprising a reduced temperature conversion step in which a reaction mixture comprising chlorine, chlorinated alkene and the chlorinated alkane is fed into a principal reaction zone operated at a temperature of about −30° C. to about 10° C., and extracting the product rich in the chlorinated alkane from the principal reaction zone, wherein the principal reaction zone is exposed to visible light and/or ultraviolet light.

A process for producing a product rich in a chlorinated alkane comprising a reduced temperature conversion step in which a reaction mixture comprising chlorine, chlorinated alkene and the chlorinated alkane is fed into a principal reaction zone operated at a temperature of about −30° C. to about 30° C., and extracting the product rich in the chlorinated alkane from the principal reaction zone, wherein the principal reaction zone is exposed to visible light and/or ultraviolet light.

A process for producing a product rich in a chlorinated alkane comprising a reduced temperature conversion step in which a reaction mixture comprising chlorine, chlorinated alkene and the chlorinated alkane is fed into a principal reaction zone operated at a temperature of about −30° C. to about 10° C., and extracting the product rich in the chlorinated alkane from the principal reaction zone, wherein the chlorinated alkane rich product is subjected to a hydrolysis step.

A process for producing a product rich in a chlorinated alkane comprising a reduced temperature conversion step in which a reaction mixture comprising chlorine, chlorinated alkene and the chlorinated alkane is fed into a principal reaction zone operated at a temperature of about −30° C. to about 30° C., and extracting the product rich in the chlorinated alkane from the principal reaction zone, wherein the chlorinated alkane rich product is subjected to a hydrolysis step.