US4383093A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Tubular polymerization reactor, and process for polymerization
Assignee: Mitsui Chemicals Inc
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Filing: 1981-06-03
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Granted: 1983-05-10
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Expires: 2001-06-03
Abstract
Abstract A tubular polymerization reactor comprising a feed opening for a polymerizable material at one end portion, a withdrawal opening for the resultant polymer at the other end portion, a tubular reaction space within the reactor extending from said feed opening to said withdrawal opening, and a rotary conveying member disposed within the reaction space and extending therealong with some clearance from the inner wall surface of the polymerization reactor; characterized in that (i) the length-to-diameter ratio of the tubular reaction space is about 20 or more, and (ii) the rotary conveying member is of a tubular coil-like shape; and a process for polymerization using the aforesaid tubular polymerization reactor.
Inventors
- 👤 Shigemi Shiraki
- 👤 Saiji Nakano
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-26 20:19
CPC Classifications
B; B01; B01F; B01F27/00; B01F27/05; B01F27/11; B01F27/114; B01F27/1142; B01F27/60; B01F27/72; B01F27/725; B01J; B01J19/00; B01J19/18; B01J19/20; C; C08; C08F; C08F10/00; Y; Y10; Y10S; Y10S526/00; Y10S526/901
Claims Analysis
Total Claims: 10
Claim 1
Independent Claim
183 words
A process for polymerization in a tubular polymerization reactor comprising a feed opening for a polymerizable material at one end portion, a withdrawal opening for the resultant polymer at the other end portion, a tubular reaction space within the reactor extending from said feed opening to said withdrawal opening, and a rotary conveying member disposed within the reaction space and extending therealong with some clearance from the inner wall surface of the polymerization reactor, which comprises feeding the polymerizable material into said feed opening and withdrawing the resultant polymer from said withdrawal opening; characterized in that (A) in said polymerization reactor, (i) the length-to-diameter ratio of the tubular reaction space is about 20 or more, (ii) the rotary conveying member is a tubular coil-like shape, and (iii) the ratio of the outside diameter of a cylinder defined by the coil-like rotary conveying member to the diameter of the tubular reaction space is 0.7 to 0.9, and (B) the polymerization is carried out while the peripheral speed of a cylinder defined by the tubular coil-like conveying member is not less than about 0.3 meters/sec.
Claim 2
Dependent Claim
183 words
A process for polymerization in a tubular polymerization reactor comprising a feed opening for a polymerizable material at one end portion, a withdrawal opening for the resultant polymer at the other end portion, a tubular reaction space within the reactor extending from said feed opening to said withdrawal opening, and a rotary conveying member disposed within the reaction space and extending therealong with some clearance from the inner wall surface of the polymerization reactor, which comprises feeding the polymerizable material into said feed opening and withdrawing the resultant polymer from said withdrawal opening; characterized in that (A) in said polymerization reactor, (i) the length-to-diameter ratio of the tubular reaction space is about 20 or more, (ii) the rotary conveying member is a tubular coil-like shape, and (iii) the ratio of the outside diameter of a cylinder defined by the coil-like rotary conveying member to the diameter of the tubular reaction space is 0.7 to 0.9, and (B) the polymerization is carried out while the peripheral speed of a cylinder defined by the tubular coil-like conveying member is not less than about 0.3 meters/sec.
Claim 3
Dependent Claim
32 words
The process of claim 1 wherein the feed direction generated by the rotation of the tubular coil-like rotary conveying member is reverse to the direction in which the polymerization reaction mixture flows.
Claim 4
Dependent Claim
33 words
The process of claim 1 wherein the feed direction generated by the rotation of the tubular coil-like rotary conveying member is the same as the direction in which the polymerization reaction mixture flows.
Claim 5
Dependent Claim
30 words
The process of claim 1 wherein the polymerization is carried out while the average flow rate of the polymerization reaction mixture is maintained at about 0.03 to about 0.8 meter/sec.
Claim 6
Dependent Claim
36 words
The process of claim 1 wherein the polymerization is carried out while recycling a part of a flow of the polymerization reaction mixture on the downstream side of the polymerization reactor to the upstream side thereof.
Claim 7
Dependent Claim
35 words
The process of claim 5 wherein the number of circulations, in terms of the ratio of the weight of the circulating polymer to the weight of the withdrawn polymer is about 1.05 to about 6.
Claim 8
Dependent Claim
15 words
The process of claim 1 wherein the polymerization is carried out under gaseous-phase polymerization conditions.
Claim 9
Dependent Claim
12 words
The process of claim 1 wherein the polymerizable material is an olefin.
Claim 10
Dependent Claim
50 words
The process of claim 8 wherein the polymerization is carried out in the presence of a catalyst composed of a transition metal compound catalyst component and an organometallic compound catalyst component, said catalyst capable of forming at least about 5,000 g of an olefin polymer per millimole of transition metal.
References Cited (Backward Citations)
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1986-05-09 | 1986-11-08 | 1987-05-10 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1990-05-09 | 1990-11-08 | 1991-05-10 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1994-05-09 | 1994-11-08 | 1995-05-10 | $7700.00 | Window Closed / Lapsed |