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Propylene homopolymerization or random copolymerization method

A technology of random copolymerization and propylene, which is applied in the field of propylene polymerization industrialization, can solve the problems of poor catalyst adaptability, low equipment efficiency, small device scale, etc., to reduce energy consumption per unit product, reduce usage and cost, and reduce plasticization Effect of Block Chance

Inactive Publication Date: 2019-05-21
BEIJING HUAFU ENG
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Its advantages include high heat removal efficiency of the reactor, stable production operation, uniform residence time of materials during the reaction period, wide range of melting index of the products produced, and low energy consumption; its disadvantages are that hot spots and plasticized blocks are easily generated in the reactor, and the reactor High processing difficulty, key equipment needs to be imported, high investment
[0010] Hypol process of Mitsui, Japan: the combination process of liquid phase body and gas phase body produces polypropylene. The first two reactors are vertical stirring tanks, and the latter two are vertical gas fluidized bed polymerization tanks; its advantages can produce random copolymerization and Block copolymerization products; its disadvantages are long process, low equipment efficiency, fully mixed gas phase reaction, uneven product quality, poor catalyst adaptability, and small device scale; there are no new Hypol process devices in China in recent years
[0011] However, in the process of industrialization of the above-mentioned various processes, there are defects of high energy consumption per unit of propylene polymer production, which in turn affects the quality and stability of polymer products, as well as the safety of device operation, and increases the investment in project industrialization. Affects the economics of the project

Method used

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  • Propylene homopolymerization or random copolymerization method

Examples

Experimental program
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Effect test

Embodiment 1

[0099] (1) Prepolymerization

[0100] Pressurize propylene to obtain liquid phase propylene with a pressure of about 4.2MPaG and a temperature of about 42°C; with liquid phase propylene as a carrier, Ti catalyst (CS-1) and 0.3 % by weight of triethylaluminum and 0.05% by weight of cyclohexylmethyldimethoxysilane; then all are directly input into the pre-polymerization tank to form a polymerization slurry, and then carried out at 42°C, 3.2MPaG, and a residence time of 4min Propylene pre-polymerization, the polymerization ratio of polypropylene in the obtained raw material slurry is 75 times;

[0101] (2) Liquid phase bulk polymerization

[0102] The raw material slurry obtained in (1) is added to recovery liquid phase propylene and hydrogen to form a liquid phase polymerization raw material (wherein the concentration of polypropylene is 200g / L, the recovery liquid phase propylene addition is about 25% by weight of the liquid phase propylene, and the hydrogen addition 0.08kg / 1...

Embodiment 2

[0110] (1) Prepolymerization

[0111]Propylene is pressurized to obtain liquid phase propylene with a pressure of about 4 MPaG and a temperature of about 45° C.; using liquid phase propylene as a carrier, adding Ti catalyst (CS-1) and 0.2 wt. % of triethylaluminum and 0.06% by weight of cyclohexylmethyldimethoxysilane; then all are directly input into the pre-polymerization tank to form a polymerization slurry, followed by propylene at 45°C, 3.6MPaG, and a residence time of 4min. Pre-polymerization, the polymerization ratio of polypropylene in the obtained raw material slurry is 50 times;

[0112] (2) Liquid phase bulk polymerization

[0113] The raw material slurry that (1) obtains is added reclaiming propylene and hydrogen to form liquid-phase polymerization raw material (wherein the concentration of polypropylene is 150g / L, reclaiming propylene add-on is about 27% by weight of liquid-phase propylene, and hydrogen add-on is 0.12kg / L 1000kg polypropylene), carry out liquid ...

Embodiment 3

[0121] (1) Prepolymerization

[0122] The propylene is pressurized to obtain liquid phase propylene with a pressure of about 4.5 MPaG and a temperature of about 40° C.; with the liquid phase propylene as a carrier, Ti catalyst (CS-1) and 0.4 % by weight of triethylaluminum and 0.04% by weight of cyclohexylmethyldimethoxysilane; then all are directly input into the prepolymerization tank to form a polymerization slurry, and then carried out at 40°C, 3.8MPaG, and a residence time of 5min Propylene pre-polymerization, the polymerization ratio of polypropylene in the obtained raw material slurry is 100 times;

[0123] (2) Liquid phase bulk polymerization

[0124] The raw material slurry that (1) obtains is added reclaiming propylene and hydrogen to mix liquid-phase polymerization raw material (wherein the concentration of polypropylene is 300g / L, and reclaiming propylene add-on is about 30% by weight of liquid-phase propylene, and hydrogen add-on is 0.2kg / L 1000kg polypropylene)...

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Abstract

The invention relates to the field of propylene homopolymerization or random copolymerization and discloses a propylene homopolymerization or random copolymerization method which comprises the steps:(1) performing propylene prepolymerization on liquid-phase propylene carrying a polymerization catalyst to obtain raw material slurry containing propylene prepolymer, wherein a prepolymerization temperature is 40 to 45 DEG C, prepolymerization pressure is 3.2 to 3.9 MPaG, and the olefin polymerization catalyst is 0.04 to 0.06 weight% of the liquid-phase propylene; (2) mixing the raw material slurry, recycled liquid-phase propylene and recycled circulation hydrogen into a liquid-phase polymerization raw material; (3a) performing propylene liquid-phase homopolymerization and propylene gas-phasehomopolymerization on the liquid-phase polymerization raw material to obtain a product containing propylene homopolymer; or (3b) performing liquid-phase random copolymerization and gas-phase random copolymerization on the liquid-phase polymerization raw material and ethylene to obtain a product containing propylene ethylene random copolymer, wherein the ethylene feeding quantity is 5 weight% or less of the liquid-phase propylene. The method can reduce unit product energy consumption and propylene loss in propylene polymerization.

Description

technical field [0001] The invention relates to the field of industrialization of propylene polymerization, in particular to a method for homopolymerization or random copolymerization of propylene in a three-stage process. Background technique [0002] Polypropylene is a polymer polymerized from propylene as a monomer. It is a very important variety of general-purpose plastics. It has the characteristics of abundant raw materials, low price, easy processing and molding, and non-toxicity. It can also be used through copolymerization, blending, It has a very broad application field, and it is the second largest plastic after polyethylene among polyolefin resins. And propylene can also be copolymerized with ethylene to prepare propylene-ethylene random copolymer. [0003] At present, the domestic and foreign production technologies of polypropylene mainly include: liquid phase bulk method, gas phase bulk method and polymerization method in which liquid phase bulk and gas phase...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C08F110/06C08F210/16C08F210/06C08F210/02C08F4/646C08F2/34C08F2/02
CPCC08F2/00C08F2/02C08F2/34C08F4/646C08F10/06C08F110/06C08F210/02C08F210/06C08F210/16
Inventor 李泽民刘立新陈红刘利妍吴霞张毅
Owner BEIJING HUAFU ENG
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