After-chlorinated ethylene/butene-1 copolymer and process for its production

Claim 2

An after-chlorinated ethylene/butene-1 copolymer characterized by having (a) 1 to 2 methyl groups per 100 carbon atoms, (b) a chlorine content of 25 to 35% by weight, (c) a weight average molecular weight of not less than 100,000, (d) a heat of fusion, determined by differential scanning calorimetry, of not more than 0.5 cal/g, and (e) an ethylene content of 93 to 97% by weight and a butene-1 content of 7 to 3% by weight.

Claim 3

The after-chlorinated ethylene/butene-1 copolymer of claim 1 wherein the weight average molecular weight (c) is 100,000 to 500,000, and the heat of fusion (d) is 0 to 0.5 cal/g.

Claim 4

The after-chlorinated ethylene/butene-1 copolymer of claim 1 further characterized by having (f) a 100% modulus at room temperature of not more than 10 kg/cm 2 , and (g) a 25% modulus at -20° C. of not more than 100 kg/cm 2 .

Claim 5

The after-chlorinated ethylene/butene-1 copolymer of claim 3 wherein the 100% modulus at room temperature (f) is 5 to 10 kg/cm 2 , and the 25% modulus at -20° C. (g) is 40 to 100 kg/cm 2 .

Claim 6

A process for producing an after-chlorinated ethylene/butene-1 copolymer having a 100% modulus at room temperature of not more than 10 kg/cm 2 and a 25% modulus at -20° C. of not more than 100 kg/cm 2 , which comprises a first step of chlorinating an ethylene polymer in aqueous suspension at a temperature at least 5° C. lower than the crystalline melting point determined by differential scanning calorimetry of the polymer while feeding chlorine gas, a second step of heat-treating the chlorinated ethylene polymer at a temperature higher than the crystalline melting point determined by differential scanning calorimetry of the chlorinated ethylene polymer and at least 5° C. higher than the chlorinating temperature in the first step in the substantial absence of chlorine gas without feeding chlorine gas, and a third step of chlorinating the resulting heat-treated chlorinated ethylene polymer in aqueous suspension at a temperature lower than the crystalline melting point determined by differential scanning calorimetry of the starting polymer and equal to, or lower than, the temperature in the second step with the feeding of chlorine gas until the final chlorine content is reached; characterized in that (a) in the first step, an ethylene/butene-1 copolymer having a density of 0.915 to 0.930, an ethylene content of 93 to 97% by weight, a butene-1 content of 7 to 3% by weight and a crystalline melting point, determined by differential scanning calorimetry, of 115° to 125° C., at least a part of said copolymer being a crystalline linear ethylene copolymer, and at least 30% by weight of said crystalline portion being meltable at a temperature of not more than 110°, is chlorinated at a temperature of 100° to 115° C. in aqueous suspension until its chlorine content reaches 10 to 20%, (b) the second step is carried out at a temperature at least 5° C. higher than the temperature of the first step and not higher than the crystalline melting point, determined by differential scanning calorimetry, of the starting ethylene/butene-1 copolymer, and (c) the third step is carried out at a temperature 6±2° C. lower than the crystalline melting point, determined by differential scanning calorimetry, of the starting ethylene/butene-1 copolymer until the chlorine content of the final product reaches 25 to 35% by weight.

Claim 7

A process for producing an after-chlorinated ethylene/butene-1 copolymer having a 100% modulus at room temperature of not more than 10 kg/cm 2 and a 25% modulus at -20° C. of not more than 100 kg/cm 2 , which comprises a first step of chlorinating an ethylene polymer in aqueous suspension at a temperature at least 5° C. lower than the crystalline melting point determined by differential scanning calorimetry of the polymer while feeding chlorine gas, a second step of heat-treating the chlorinated ethylene polymer at a temperature higher than the crystalline melting point determined by differential scanning calorimetry of the chlorinated ethylene polymer and at least 5° C. higher than the chlorinating temperature in the first step in the substantial absence of chlorine gas without feeding chlorine gas, and a third step of chlorinating the resulting heat-treated chlorinated ethylene polymer in aqueous suspension at a temperature lower than the crystalline melting point determined by differential scanning calorimetry of the starting polymer and equal to, or lower than, the temperature in the second step with the feeding of chlorine gas until the final chlorine content is reached; characterized in that (a) in the first step, an ethylene/butene-1 copolymer having a density of 0.915 to 0.930, an ethylene content of 93 to 97% by weight, a butene-1 content of 7 to 3% by weight and a crystalline melting point, determined by differential scanning calorimetry, of 115° to 125° C., at least a part of said copolymer being a crystalline linear ethylene copolymer, and at least 30% by weight of said crystalline portion being meltable at a temperature of not more than 110°, is chlorinated at a temperature of 100° to 115° C. in aqueous suspension until its chlorine content reaches 10 to 20%, (b) the second step is carried out at a temperature at least 5° C. higher than the temperature of the first step and not higher than the crystalline melting point, determined by differential scanning calorimetry, of the starting ethylene/butene-1 copolymer, and (c) the third step is carried out at a temperature 6±2° C. lower than the crystalline melting point, determined by differential scanning calorimetry, of the starting ethylene/butene-1 copolymer until the chlorine content of the final product reaches 25 to 35% by weight.