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EP0059080A2 Expired / Lapsed EP ⏱️ 0.0 years remaining

Process and apparatus for gas phase polymerization of olefins

Assignee: JNC Corp
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Filing: 1982-02-19
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Granted: —
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Expires: 2002-02-19
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Abstract

Abstract Process and apparatus for gas phase polymerization of olefins. Olefin gas phase polymerization mainly comprises a combination of (i) use of a new fluidized bed reaction vessel 3 of which the main part has an inverted truncated cone shape equipped with an agitator, (ii) use of a catalyst subjected to a preliminary polymerization treatment and (iii) removal of the polymerization reaction heat mainly by way of the latent heat of vaporization of a liquid organic quenching agent fed as a dispersion through many ports into the fluidized bed consisting of catalyst and polymer particles. According to the process and by use of the apparatus, it becomes possible to carry out the gas phase polymerization easily, continuously and for a long term, and produce good quality polyolefin.

Inventors

  • 👤 Nobutaka Hattori
  • 👤 Wataru Funahashi
  • 👤 Minoru Yanoshita

Bibliographic Details

Application Number —
Jurisdiction EP
Data Source google_patents
Last Synchronized 2026-11-03 12:09
CPC Classifications
C; C08; C08F; C08F10/00; B; B01; B01J; B01J19/00; B01J19/18; B01J19/20; B01J8/00; B01J8/18; B01J8/24; B01J8/38; B01J2219/00; B01J2219/19; B01J2219/194; B01J2219/1941; B01J2219/1946

Claims Analysis

Total Claims: 9
Claim 1
Independent Claim 299 words
A process for gas phase polymerization of olefins by the use of a catalyst subjected to a preliminary polymerization treatment, characterised by the following steps (a) to (f): (a) using as said catalyst subjected to a preliminary polymerization treatment, a catalyst having a density of 1.2 to 2.5 g /cm ; (b) feeding said catalyst subjected to a preliminary polymerization treatment, into a fluidized bed polymerization reaction vessel of which the main part has an inverted truncated cone shape with a ratio of the height to the diameter of the bottom part of the cone of 1:1 to 5:1 and an angle of the conical axis with the conical surface of 1 to 10°, has a vertical type agitator therein and has a distribution plate at the bottom part of the cone for forming a fluidized bed, and feeding an olefin gas, a mixed gas of an inert gas with the olefin or a circulating olefin gas, to the bottom part of the vessel to form a fluidized bed of the catalyst; (c) initiating polymerization of said olefin under agitation by means of said agitator, while maintaining a termperature inside the vessel of 30 to 130°C and a pressure of 0 to 50 k g/cm 2 G; (d) continuously feeding into the fluidized bed through dispersed injection ports a liquid organic quenching agent having a favourable latent heat of vaporization for offsetting at least almost all of the polymerization heat of said olefin; (e) continuously withdrawing from the top part of said polymerization vessel a mixed gas consisting of unpolymerized olefin gas, vaporized organic quenching agent and any inert gas; and (f) removing by liquefaction, most of said organic quenching agent from said mixed gas and feeding by circulation, the resulting olefin gas mixture to the above step (b).
Claim 2
Dependent Claim 299 words
A process for gas phase polymerization of olefins by the use of a catalyst subjected to a preliminary polymerization treatment, characterised by the following steps (a) to (f): (a) using as said catalyst subjected to a preliminary polymerization treatment, a catalyst having a density of 1.2 to 2.5 g /cm ; (b) feeding said catalyst subjected to a preliminary polymerization treatment, into a fluidized bed polymerization reaction vessel of which the main part has an inverted truncated cone shape with a ratio of the height to the diameter of the bottom part of the cone of 1:1 to 5:1 and an angle of the conical axis with the conical surface of 1 to 10°, has a vertical type agitator therein and has a distribution plate at the bottom part of the cone for forming a fluidized bed, and feeding an olefin gas, a mixed gas of an inert gas with the olefin or a circulating olefin gas, to the bottom part of the vessel to form a fluidized bed of the catalyst; (c) initiating polymerization of said olefin under agitation by means of said agitator, while maintaining a termperature inside the vessel of 30 to 130°C and a pressure of 0 to 50 k g/cm 2 G; (d) continuously feeding into the fluidized bed through dispersed injection ports a liquid organic quenching agent having a favourable latent heat of vaporization for offsetting at least almost all of the polymerization heat of said olefin; (e) continuously withdrawing from the top part of said polymerization vessel a mixed gas consisting of unpolymerized olefin gas, vaporized organic quenching agent and any inert gas; and (f) removing by liquefaction, most of said organic quenching agent from said mixed gas and feeding by circulation, the resulting olefin gas mixture to the above step (b).
Claim 3
Dependent Claim 19 words
A process according to claim 1 wherein the olefin comprises one or more of ethylene, propylene, butene-1 and 4-methylpentene-l.
Claim 4
Dependent Claim 24 words
A process according to claim 1 or 2, wherein hydrogen is fed to the polymerization vessel as a polymerization rate- or polymerization degree-adjusting agent.
Claim 5
Dependent Claim 37 words
A process according to claim 1, 2, or 3, wherein the catalyst subjected to a preliminary polymerization treatment is continuously fed to the polymerization vessel and the resulting polyolefin powder is continuously withdrawn from the polymerization vessel.
Claim 6
Independent Claim 185 words
An apparatus for gas phase polymerization of olefins, comprising: a fluidized bed polymerization reaction vessel (3) of which the main part has an inverted truncated cone shape with a ratio of the height of the cone to the diameter of the bottom part of the cone of 1:1 to 5:1 and an angle of the conical axis with the conical surface of 1 to 10°, has a vertical agitator (7) therein and has a distribution plate (2) for forming at the bottom part of the cone a fluidized bed; means (8) at the top part of said polymerization reaction vessel for withdrawing inert gas or unreacted gas or unreacted olefin; means (4,4') for feeding a catalyst subjected to a preliminary polymerization treatment and means for feeding a liquid organic quenching agent (5) for removing polymerization heat, both feeding means being at locations removed from the central to the top part of said vessel; and means (9) for withdrawing polyolefin at a location between the central part and bottom part of said vessel, but above the location of the distribution plate for forming a fluidized bed.
Claim 7
Independent Claim 185 words
An apparatus for gas phase polymerization of olefins, comprising: a fluidized bed polymerization reaction vessel (3) of which the main part has an inverted truncated cone shape with a ratio of the height of the cone to the diameter of the bottom part of the cone of 1:1 to 5:1 and an angle of the conical axis with the conical surface of 1 to 10°, has a vertical agitator (7) therein and has a distribution plate (2) for forming at the bottom part of the cone a fluidized bed; means (8) at the top part of said polymerization reaction vessel for withdrawing inert gas or unreacted gas or unreacted olefin; means (4,4') for feeding a catalyst subjected to a preliminary polymerization treatment and means for feeding a liquid organic quenching agent (5) for removing polymerization heat, both feeding means being at locations removed from the central to the top part of said vessel; and means (9) for withdrawing polyolefin at a location between the central part and bottom part of said vessel, but above the location of the distribution plate for forming a fluidized bed.
Claim 8
Dependent Claim 20 words
An apparatus according to claim 5, wherein the body of the vessel is provided with a heating or cooling jacket.
Claim 9
Dependent Claim 33 words
An apparatus according to claim 5 or 6, wherein the means for feeding liquid organic uenching agent is so devised that the agent can be fed to the fluidized bed in dispersion form.

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