Process for polymerizing ethylene

Claim 2

Process for the polymerization or copolymerization of ethylene in the presence of a catalyst in at least one reactor comprising two or more reaction zones, at a pressure of 300 to 2,500 bars and at a temperature of 150 to 350° C., comprising: (a) passing a reaction mixture comprising gas and polymer from said at least one reactor into a separator at a pressure of 50 to 500 bars; (b) separating said polymer from said gas in said separator; (c) passing said polymer from said separator to a hopper at a pressure of 1 to 20 bars; (d) removing the major part of the gas remaining dissolved in said polymer in said hopper; (e) recompressing said gas from said separator; (f) returning said recompressed gas only to the first zone of said at least one reactor; and (g) passing fresh gas supplied to said at least one reactor only to the zones subsequent to the first zone of said at least one reactor.

Claim 3

Process according to claim 1, further comprising recompressing the gas removed from the polymer in the hopper and then mixing said recompressed gas from said hopper with said gas from the separator.

Claim 4

Process according to claim 1, further comprising recompressing the gas removed from the polymer in the hopper and mixing said gas from said hopper with fresh gas supplied to said at least one reactor.

Claim 5

Process according to claim 1, further comprising injecting gas between said at least one reactor and said separator at a pressure below that of said separator.

Claim 6

Process according to claim 4, wherein said gas injected between said at least one reactor and said separator comprises fresh gas supplied to said at least one reactor.

Claim 7

Process according to claim 4, wherein said gas injected between said at least one reactor and said separator comprises said gas from said separator.

Claim 8

Process according to claim 1, wherein said at least one reactor is of the stirred autoclave type.

Claim 9

Process according to claim 1, wherein said at least one reactor is of the tubular type.

Claim 10

Process according to claim 1, wherein polymerization is carried out in two reactors arranged in parallel, each of them comprising two or more zones, said process further comprising passing reaction mixtures from said two reactors into the same separator, recompressing the gas from said separator, and returning said recompressed gas only to the first zone of at least one of said reactors.

Claim 11

Process according to claim 9, wherein part of said compressed gas from said separator is passed to the first zone of one of said reactors and the rest is passed to the first zone of the other of said reactors, the supply of fresh gas being passed only to the second zone of the other of said reactors.

Claim 12

Process according to claim 9, further comprising operating said two reactors at different pressures.

Claim 13

Process according to claim 1, wherein polymerization is carried out in the presence of at least one chain transfer agent.

Claim 14

Process according to claim 1, wherein polymerization is carried out in the presence of a free-radical yielding catalyst.

Claim 15

Process according to claim 1, wherein polymerization is carried out in the presence of a catalyst comprising a transition metal compound.

Claim 16

Process according to claim 1, wherein polymerization is carried out in the presence of an inert diluent.

Claim 17

Process according to claim 14, further comprising terminating polymerization by injecting into the reaction mixture an alkali metal salt or alkaline earth metal salt of carboxylic acid which upon reaction with the catalyst will form reaction products that remain in the polymer.

Claim 18

Apparatus for carrying out the polymerization of ethylene, comprising: (a) at least one reactor having two or more zones; (b) a separator; (c) a pipe connecting said separator to said at least one reactor; (d) a low pressure hopper; (e) a pipe connecting said hopper to said separator; (f) a booster compressor; (g) a first high pressure compressor; (h) a second high pressure compressor; (i) a first (intermediate pressure) gas transfer pipe extending from said separator to the intake of said second high pressure compressor; (j) a second (low pressure) gas transfer pipe extending from said hopper to the intake of said booster compressor; (k) a connecting pipe extending from the outlet of said booster compressor to the intake of said first high pressure compressor; (l) a fresh ethylene feed pipe for supplying fresh ethylene to the gas from said hopper at a point between said hopper and said first high pressure compressor; (m) a high pressure connecting pipe extending from the outlet of said first high pressure compressor to at least one zone different from the first zone of said at least one reactor; and (n) another high pressure connecting pipe extending from the outlet of said second high pressure compressor to the first zone of said at least one reactor.

Claim 19

Apparatus for carrying out the polymerization of ethylene, comprising: (a) at least one reactor having two or more zones; (b) a separator; (c) a pipe connecting said separator to said at least one reactor; (d) a low pressure hopper; (e) a pipe connecting said hopper to said separator; (f) a booster compressor; (g) a first high pressure compressor; (h) a second high pressure compressor; (i) a first (intermediate pressure) gas transfer pipe extending from said separator to the intake of said second high pressure compressor; (j) a second (low pressure) gas transfer pipe extending from said hopper to the intake of said booster compressor; (k) a connecting pipe extending from the outlet of said booster compressor to the intake of said first high pressure compressor; (l) a fresh ethylene feed pipe for supplying fresh ethylene to the gas from said hopper at a point between said hopper and said first high pressure compressor; (m) a high pressure connecting pipe extending from the outlet of said first high pressure compressor to at least one zone different from the first zone of said at least one reactor; and (n) another high pressure connecting pipe extending from the outlet of said second high pressure compressor to the first zone of said at least one reactor.

Claim 20

Apparatus according to claim 17, further comprising a gas injector in said pipe connecting said separator to said at least one reactor for injecting gas between said at least one reactor and said separator at a pressure below that of said separator.

Claim 21

Apparatus according to claim 17 wherein said at least one reactor is of the stirred autoclave type.

Claim 22

Apparatus according to claim 17 wherein said at least one reactor is of the tubular type.

Claim 23

Apparatus according to claim 17 wherein said at least one reactor consists of two reactors each having two or more zones, further comprising: (o) connecting pipes extending from the outlets of each of said reactors to said pipe connecting said separator to said reactors.

Claim 24

Apparatus according to claim 21, wherein said high pressure connecting pipe extending from the outlet of said first high pressure compressor extends to only one reactor and said high pressure connecting pipe extending from the outlet of said second high pressure compressor extends to both of said reactors.

Claim 25

Process for the polymerization or copolymerization of ethylene in the presence of a catalyst in two reactors arranged in parallel, each of them comprising two or more zones, at a pressure of 300 to 2,500 bars and at a temperature of 150° to 350° C., comprising: (a) passing reaction mixtures comprising gas and polymer from said two reactors into a single separator at a pressure of 50 to 500 bars; (b) separating said polymer from said gas in said separator; (c) passing said polymer from said separator to a hopper at a pressure of 1 to 20 bars; (d) removing the major part of the gas remaining dissolved in said polymer in said hopper; (e) recompressing said gas from said separator; (f) returning all of said recompressed gas from said separator to the first zone of one of said reactors; and (g) supplying fresh gas only to the first zone of the other of said reactors.

Claim 26

Process for the polymerization or copolymerization of ethylene in the presence of a catalyst in two reactors arranged in parallel, each of them comprising two or more zones, at a pressure of 300 to 2,500 bars and at a temperature of 150° to 350° C., comprising: (a) passing reaction mixtures comprising gas and polymer from said two reactors into a single separator at a pressure of 50 to 500 bars; (b) separating said polymer from said gas in said separator; (c) passing said polymer from said separator to a hopper at a pressure of 1 to 20 bars; (d) removing the major part of the gas remaining dissolved in said polymer in said hopper; (e) recompressing said gas from said separator; (f) returning all of said recompressed gas from said separator to the first zone of one of said reactors; and (g) supplying fresh gas only to the first zone of the other of said reactors.

Claim 27

Process for the polymerization or copolymerization of ethylene in the presence of a catalyst in two reactors arranged in parallel, each of them comprising two or more zones, at a pressure of 300 to 2,500 bars and at a temperature of 150° to 350° C., comprising: (a) passing reaction mixtures comprising gas and polymer from said two reactors into a single separator at a pressure of 50 to 500 bars; (b) separating said polymer from said gas in said separator; (c) passing said polymer from said separator to a hopper at a pressure of 1 to 20 bars; (d) removing the major part of the gas remaining dissolved in said polymer in said hopper; (e) recompressing said gas from said separator; (f) returning said recompressed gas only to the first zone of at least one of said reactors; and (g) supplying gas to a zone other than the first zone of at least one of said reactors.

Claim 28

Process for the polymerization or copolymerization of ethylene in the presence of a catalyst in two reactors arranged in parallel, each of them comprising two or more zones, at a pressure of 300 to 2,500 bars and at a temperature of 150° to 350° C., comprising: (a) passing reaction mixtures comprising gas and polymer from said two reactors into a single separator at a pressure of 50 to 500 bars; (b) separating said polymer from said gas in said separator; (c) passing said polymer from said separator to a hopper at a pressure of 1 to 20 bars; (d) removing the major part of the gas remaining dissolved in said polymer in said hopper; (e) recompressing said gas from said separator; (f) returning said recompressed gas only to the first zone of at least one of said reactors; and (g) supplying gas to a zone other than the first zone of at least one of said reactors.