US4014859A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Production of polyethylene
Assignee: Imperial Chemical Industries Ltd
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Filing: 1974-03-29
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Granted: 1977-03-29
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Expires: 1994-03-29
Abstract
Abstract Ethylene is polymerized or copolymerized using a pressure of at least 300 kgm/cm 2 and a multi-zone (i.e. two or more) reaction vessel wherein the feed to the first zone is fresh ethylene, which is preferably mixed with recycle gas from the low pressure hopper and into at least a subsequent zone there is introduced a feed containing return gas recycled from the separator. By this technique the composition of the gas feed to the various zones can be varied, for example the hydrogen content of the gas streams to the various zones can be varied and this can produce a polymer of broader molecular weight distribution.
Inventors
- 👤 Richard Roy Cooper
- 👤 Kenneth Stephenson Whiteley
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-24 19:32
CPC Classifications
B; B01; B01J; B01J19/00; B01J19/0006; C; C08; C08F; C08F10/00
Claims Analysis
Total Claims: 19
Claim 1
Independent Claim
254 words
A process for the polymerization or copolymerization of ethylene in at least two reaction zones comprising: a. passing a product mixture of ethylene, an ethylene polymer, and at least one further component selected from the group consisting of comonomer, chain transfer agent and inert diluent at a pressure in the range 300 to 3000 kgm/cm 2 from a reaction zone into a separator maintained at a pressure below the pressure of the product mixture, effecting separation into a gas phase and a liquid phase, said liquid phase comprising the ethylene polymer and dissolved gas; b. passing said liquid phase to a low pressure hopper maintained at a pressure below that of said separator and removing the major portion of the dissolved gas from the polymer and low pressure hopper; c. compressing the gas removed from said low pressure hopper to an intermediate pressure; d. providing a stream of fresh ethylene and passing it to a compressor; e. compressing the gas stream of fresh ethylene and passing it to the first zone of the polymerization reactor, f. optionally mixing the gas phase from the separator with either a chain transfer agent, a stream of fresh ethylene or both which stream of fresh ethylene optionally contains comonomer, inert diluent or both, g. passing the resulting gas phase to a compressor and compressing this gas phase, and passing this gas phase to at least one zone, other than the first zone of the polymerization reactor; h. mixing the compressed gas from the low pressure hopper with either
Claim 2
Dependent Claim
254 words
A process for the polymerization or copolymerization of ethylene in at least two reaction zones comprising: a. passing a product mixture of ethylene, an ethylene polymer, and at least one further component selected from the group consisting of comonomer, chain transfer agent and inert diluent at a pressure in the range 300 to 3000 kgm/cm 2 from a reaction zone into a separator maintained at a pressure below the pressure of the product mixture, effecting separation into a gas phase and a liquid phase, said liquid phase comprising the ethylene polymer and dissolved gas; b. passing said liquid phase to a low pressure hopper maintained at a pressure below that of said separator and removing the major portion of the dissolved gas from the polymer and low pressure hopper; c. compressing the gas removed from said low pressure hopper to an intermediate pressure; d. providing a stream of fresh ethylene and passing it to a compressor; e. compressing the gas stream of fresh ethylene and passing it to the first zone of the polymerization reactor, f. optionally mixing the gas phase from the separator with either a chain transfer agent, a stream of fresh ethylene or both which stream of fresh ethylene optionally contains comonomer, inert diluent or both, g. passing the resulting gas phase to a compressor and compressing this gas phase, and passing this gas phase to at least one zone, other than the first zone of the polymerization reactor; h. mixing the compressed gas from the low pressure hopper with either
Claim 3
Dependent Claim
51 words
the stream of fresh ethylene which is compressed and passed to the first stage of the polymerization reactor, or 2. the gas phase from the separator which is compressed and passed to the polymerization reactor; and i. introducing a polymerization catalyst into at least the first zone of the polymerization reactor.
Claim 4
Dependent Claim
51 words
the stream of fresh ethylene which is compressed and passed to the first stage of the polymerization reactor, or 2. the gas phase from the separator which is compressed and passed to the polymerization reactor; and i. introducing a polymerization catalyst into at least the first zone of the polymerization reactor.
Claim 5
Dependent Claim
78 words
The process of claim 1 wherein polymerisation is effected in two zones, the gas from the low pressure hopper is compressed to an intermediate pressure, mixed with fresh ethylene, compressed further and introduced into the first zone of the polymerisation reactor, and the gas from the separator is mixed with fresh ethylene and sufficient quantity of a chain transfer agent to replace that lost from the system, compressed and introduced into the second zone of the polymerisation reactor.
Claim 6
Dependent Claim
101 words
The process of claim 1 wherein polymerisation is effected in at least three zones, the gas from the low pressure hopper is compressed, mixed with fresh ethylene, compressed further and introduced into the first zone of the polymerisation reactor, the gas from the separator is mixed with fresh ethylene and a sufficient quantity of a chain transfer agent to replace that lost from the system, compressed and introduced into the second or subsequent zone of the polymerisation reactor and the product mixture is withdrawn from a zone into which there is no direct feed of ethylene from the high pressure compressor.
Claim 7
Dependent Claim
131 words
The process of claim 1 wherein polymerisation is effected in at least three zones, the gas from the low pressure hopper is compressed, mixed with fresh ethylene, compressed further and introduced into the first zone of the polymerisation reactor, the gas from the separator is divided into two streams, fresh ethylene is introduced into one of these streams which is compressed and passed to at least the second zone of the polymerisation reactor, a chain transfer agent, and optionally further fresh ethylene, is introduced into the other of the gas streams from the separator, this gas stream is compressed and introduced into a zone of the polymerisation reactor which is distinct from, and subsequent to, any zone into which the first part of the gas stream from the separator is introduced.
Claim 8
Dependent Claim
22 words
The process of claim 4 wherein polymerisation is effected in three zones and the product mixture is withdrawn from the second zone.
Claim 9
Dependent Claim
33 words
The process of claim 4 wherein polymerisation is effected in four zones, gas streams are introduced into the first, second and fourth zones, and the product mixture is withdrawn from the third zone.
Claim 10
Dependent Claim
28 words
The process of claim 1 which comprises subjecting at least some of the fresh ethylene to a dimerisation stage and converting a proportion of the ethylene to butene-1.
Claim 11
Dependent Claim
69 words
The process of claim 1 wherein a mixture of 0-80% by weight of a volatile, inert diluent, 0-95% by weight of at least one 1-olefine monomer and from 5 up to 80% by weight of ethylene is introduced into the polymerisation reactor and contacted with a transition metal polymerisation catalyst at a temperature of from 100°C to 350°C and a pressure of from 300 to 1000 kgm/cm 2 .
Claim 12
Dependent Claim
204 words
Apparatus for the polymerization or copolymerization of ethylene comprising a polymerization reactor having at least two zones, one of said zones being in communication with, a separator, a low pressure hopper in communication with the separator, said low pressure hopper having a product withdrawal line, a booster compressor and a high pressure compressor, a valve to control the pressure within the polymerization reactor, a fresh ethylene supply line connected to the high pressure compressor and a high pressure connecting line from said high pressure compressor to the first zone of the polymerization reactor, a gas transfer line from the separator to a further high pressure compressor and a further high pressure connecting line from the further high pressure compressor to at least one zone, other than the first zone, of the polymerization reactor, and a low pressure gas transfer line from the low pressure hopper to the booster compressor and a connecting line from the booster compressor either to the fresh ethylene supply line or to the gas transfer line from the separator and at least one catalyst injection point either in the first zone of the polymerization reactor or in the high pressure connecting line to the first zone of the polymerization reactor.
Claim 13
Dependent Claim
204 words
Apparatus for the polymerization or copolymerization of ethylene comprising a polymerization reactor having at least two zones, one of said zones being in communication with, a separator, a low pressure hopper in communication with the separator, said low pressure hopper having a product withdrawal line, a booster compressor and a high pressure compressor, a valve to control the pressure within the polymerization reactor, a fresh ethylene supply line connected to the high pressure compressor and a high pressure connecting line from said high pressure compressor to the first zone of the polymerization reactor, a gas transfer line from the separator to a further high pressure compressor and a further high pressure connecting line from the further high pressure compressor to at least one zone, other than the first zone, of the polymerization reactor, and a low pressure gas transfer line from the low pressure hopper to the booster compressor and a connecting line from the booster compressor either to the fresh ethylene supply line or to the gas transfer line from the separator and at least one catalyst injection point either in the first zone of the polymerization reactor or in the high pressure connecting line to the first zone of the polymerization reactor.
Claim 14
Dependent Claim
43 words
The apparatus of claim 9 wherein a comonomer supply line and/or an inert diluent supply line are connected to the fresh ethylene supply line and a supply line for a chain transfer agent is connected to the gas transfer line from the separator.
Claim 15
Dependent Claim
22 words
The apparatus of claim 9 wherein a further fresh ethylene supply line is connected to the gas transfer line from the separator.
Claim 16
Dependent Claim
116 words
The apparatus of claim 9 wherein the polymerisation reactor has at least three zones, and the gas transfer line from the separator is divided into two subsidiary transfer lines, one of said subsidiary lines being connected to the further high pressure compressor, and the further high pressure connecting line leads to the second zone of the polymerisation reactor, and a supply line for a chain transfer agent is connected to the other of said subsidiary lines and the combined line is connected to a second further high pressure compressor and a second further high pressure connecting line leads from the second further high pressure compressor to the third or a subsequent zone of the polymerisation reactor.
Claim 17
Dependent Claim
28 words
The apparatus of claim 12 wherein the polymerisation reactor has three zones and a polymer withdrawal line connects the second zone of the polymerisation reactor to the separator.
Claim 18
Dependent Claim
41 words
The apparatus of claim 12 wherein the polymerisation reactor has four zones, the second further high pressure connecting line is connected to the fourth zone and a polymer withdrawal line connects the third zone of the polymerisation reactor to the separator.
Claim 19
Dependent Claim
35 words
A process according to claim 1 comprising mixing at least one further component selected from the group consisting of comonomer, inert diluent and chain transfer agent with said stream of fresh ethylene in step (d).
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USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1980-03-28 | 1980-09-27 | 1981-03-29 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1984-03-28 | 1984-09-27 | 1985-03-29 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1988-03-28 | 1988-09-27 | 1989-03-29 | $7700.00 | Window Closed / Lapsed |