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Evaluation method of polypropylene metallocene catalyst

A metallocene catalyst and evaluation method technology, which is applied in the evaluation field of polypropylene metallocene catalyst, can solve problems such as lack of evaluation methods, and achieve the effect of avoiding amplification difficulties or even failures

Inactive Publication Date: 2019-06-28
XIAMEN UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, evaluation methods specifically for industrial applications of metallocene catalysts are lacking.

Method used

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  • Evaluation method of polypropylene metallocene catalyst

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0046]Heat a 5L stainless steel high-pressure reactor with hot water to 80°C, replace it with nitrogen three times, use a vacuum device to evacuate the reactor to 5Pa, and replace reactor 1 with propylene for three times. Add 0.1 g of atmospheric pressure hydrogen into the reaction kettle, and then add 1.6 kg of liquid propylene while stirring. The temperature of the reaction kettle was raised to 35° C., and the pressure therein was 1.5-1.7 MPa at this time. In the glove box, 90 mg of the metallocene catalyst to be tested were charged to the high pressure feeder. Add the metallocene catalyst in the high-pressure feeding device into the reactor, react at 35° C. for 20 minutes, then raise the temperature in the reactor to 60° C., and carry out polymerization at this temperature for 2 hours. After the polymerization is completed, the temperature is lowered, and the obtained polypropylene product is extruded, and its yield is measured. The catalyst evaluation results are shown i...

Embodiment 2

[0050] Heat a 5L stainless steel high-pressure reactor with hot water to 80°C, replace it with nitrogen three times, use a vacuum device to evacuate the reactor to 5Pa, and replace reactor 1 with propylene for three times. Add 0.1 g of atmospheric pressure hydrogen into the reaction kettle, and then add 1.6 kg of liquid propylene while stirring. The temperature of the reaction kettle was raised to 35° C., and the pressure therein was 1.5-1.7 MPa at this time. In the glove box, 90 mg of the metallocene catalyst to be tested were charged to the high pressure feeder. Add the metallocene catalyst in the high-pressure feeding device into the reactor, react at 35° C. for 20 minutes, then raise the temperature in the reactor to 70° C., and carry out polymerization at this temperature for 2 hours. After the polymerization is completed, the temperature is lowered, and the obtained polypropylene product is extruded, and its yield is measured. The catalyst evaluation results are shown ...

Embodiment 3

[0054] Heat a 5L stainless steel high-pressure reactor with hot water to 80°C, replace it with nitrogen three times, use a vacuum device to evacuate the reactor to 5Pa, and replace reactor 1 with propylene for three times. Add 0.1 g of atmospheric pressure hydrogen into the reaction kettle, and then add 1.6 kg of liquid propylene while stirring. The temperature of the reaction kettle was raised to 35° C., and the pressure therein was 1.5-1.7 MPa at this time. In the glove box, 90 mg of the metallocene catalyst to be tested were charged to the high pressure feeder. Add the metallocene catalyst in the high-pressure feeding device into the reactor, react at 35° C. for 20 minutes, then raise the temperature in the reactor to 80° C., and carry out polymerization at this temperature for 2 hours. After the polymerization is completed, the temperature is lowered, and the obtained polypropylene product is extruded, and its yield is measured. The catalyst evaluation results are shown ...

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Abstract

The invention discloses an evaluation method of a polypropylene metallocene catalyst and relates to the polypropylene metallocene catalyst. The evaluation method comprises the following steps: heatinga reactor to 60-90 DEG C with hot water; replacing gas in the reactor with nitrogen for 1-5 times; vacuumizing the reactor and reducing the temperature to normal temperature; replacing gas in the reactor with propylene for 1-5 times; adding hydrogen and propylene into the reactor and then raising the temperature to 30-40 DEG C; adding a metallocene catalyst into the reactor by using high-pressurenitrogen through a high-pressure feeding device under protection of N2 gas; maintaining a reaction temperature of the materials in the reactor at 30-40 DEG C, carrying out a reaction for 10-30 min, controlling the pressure to be 1.3-1.7 MPa, and then raising the temperature for reaction; cooling after the reaction, and pressing out a generated polypropylene product; analyzing the obtained polypropylene product and calculating the yield of the polypropylene product.

Description

technical field [0001] The invention relates to a polypropylene metallocene catalyst, in particular to an evaluation method for a polypropylene metallocene catalyst. Background technique [0002] Polypropylene is one of the five general-purpose plastics, second only to polyethylene in consumption, and is one of the important industrial raw materials in modern production and life. According to the type of polymerization, the production process of polypropylene can be divided into five categories: solution method, slurry method, bulk method, gas phase method and bulk method-gas phase method combined process. The specific processes mainly include BP's gas-phase Innovene process, Chisso's gas-phase process, Dow's Unipol process, Novolene gas-phase process, Sumitomo gas-phase process, Basell's bulk process, Mitsui's Hypol process and Borealis' Borstar craft etc. [0003] Since the Ziegler-Natta catalyst came out in the 1950s, the polypropylene catalyst has been continuously imp...

Claims

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Application Information

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IPC IPC(8): G01N31/10
Inventor 蒋文军朱红平陈志康张公平江巧珠
Owner XIAMEN UNIV
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