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Catalytic system for preparation of low-molecular-weight polypropylene, low-molecular-weight polypropylene, and preparation method for low-molecular-weight polypropylene

A catalytic system and low molecular weight technology, which is applied in the field of low molecular weight polypropylene and low molecular weight polypropylene preparation, can solve the problem of high molecular weight polypropylene and achieve high-efficiency preparation

Inactive Publication Date: 2019-03-05
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0007] However, the molecular weight of polypropylene catalyzed by metallocene catalysts is relatively high. Therefore, it is urgent to provide a catalytic system that can efficiently prepare low-molecular-weight propylene polymers, and the molecular weight and distribution of the polymers can be well controlled.

Method used

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  • Catalytic system for preparation of low-molecular-weight polypropylene, low-molecular-weight polypropylene, and preparation method for low-molecular-weight polypropylene
  • Catalytic system for preparation of low-molecular-weight polypropylene, low-molecular-weight polypropylene, and preparation method for low-molecular-weight polypropylene
  • Catalytic system for preparation of low-molecular-weight polypropylene, low-molecular-weight polypropylene, and preparation method for low-molecular-weight polypropylene

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preparation example Construction

[0041] According to the second aspect of the present invention, the present invention provides a method for preparing low-molecular-weight polypropylene, the preparation method comprising: contacting the above-mentioned components of the catalytic system under olefin polymerization reaction conditions.

[0042] The olefin polymerization reaction of the present invention is carried out according to known polymerization methods. For example, the olefin polymerization reaction can be carried out in liquid phase or gas phase, or can also be carried out under the operation of combining liquid phase and gas phase polymerization stages. Conventional techniques such as slurry method, gas-phase fluidized bed, etc. are used. The polymerization temperature may be 0 to 150°C, preferably 60 to 90°C.

[0043] The medium used for liquid phase polymerization can be selected from saturated aliphatic hydrocarbons such as isobutane, hexane, heptane, cyclohexane, naphtha, raffinate, hydrogenated ...

Embodiment 1

[0052] Fully dry the 250mL polymerization bottle, vacuumize and flush with nitrogen, repeat three times. Vacuumize, controlled by a solenoid valve, fill with 1 atmosphere of propylene, add 26.5 ml of toluene at 70 ° C, add 1.5 mL of MAO toluene solution (2.5 mmol), add 1 ml of diethylzinc toluene solution (100 micromol), 1 ml of rac-dimethylsilyl[bis(2-methyl-4-phenylindenyl)]zirconium dichloride in toluene (2.0 micromole) and start the timer. After 20 minutes, close the propylene, pour the reaction solution into a beaker, add acidified ethanol, stir for more than 6 hours, filter to obtain the polymer, vacuum dry at 60°C for 24 hours, weigh to obtain 3.78 grams of the polymer, and the gel penetration of the polymer Chromatograms such as figure 1 shown. The aggregation results are shown in Table 1.

Embodiment 2

[0054] Fully dry the 250mL polymerization bottle, vacuumize and flush with nitrogen, repeat three times. Vacuumize, controlled by a solenoid valve, fill with 1 atmosphere of propylene, add 25.5 ml of toluene at 80 ° C, add 1.5 mL of MAO toluene solution (2.5 mmol), add 2 ml of diethylzinc toluene solution (200 micromol), 1 ml of rac-dimethylsilyl[bis(2-methyl-4-phenylindenyl)]zirconium dichloride in toluene (2.0 micromole) and start the timer. After 20 minutes, turn off the propylene, pour the reaction solution into a beaker, add acidified ethanol, stir for more than 6 hours, filter to obtain the polymer, vacuum dry at 60°C for 24 hours, and weigh to obtain 3.08 grams of the polymer. The aggregation results are shown in Table 1.

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Abstract

The invention belongs to the field of catalysis of olefin polymerization, and specifically discloses a catalytic system for preparation of low-molecular-weight polypropylene, the low-molecular-weightpolypropylene, and a preparation method for the low-molecular-weight polypropylene. The catalytic system comprises the following components: a) a bridged metallocene compound, which has a general formula of R'Cp'Cp"MX'X", wherein Cp' and Cp" are the same or different and are selected from the group consisting of substituted or unsubstituted cyclopentadienyl groups, substituted or unsubstituted indenyl groups and substituted or unsubstituted fluorenyl groups, R' is a group formed by connection of a silicon atom or a carbon atom with Cp' and Cp", M is a fourth-subgroup metal atom, and X' and X"are the same or different and are separately selected from the group consisting of halogen, hydrocarbyl or alkoxy; b) alkyl aluminoxane; c) an organic zinc compound; d) propylene; and e) optionally one or more alpha-olefin comonomers. By adoption of the catalytic system provided by the invention for polymerization, the polypropylene with low molecular weight and narrow molecular weight distribution can be more efficiently prepared.

Description

technical field [0001] The invention belongs to the field of olefin polymerization catalysis, and in particular relates to a catalytic system for preparing low-molecular-weight polypropylene, a method for preparing low-molecular-weight polypropylene, and the low-molecular-weight polypropylene prepared by the preparation method. Background technique [0002] Single-site transition metal catalysts for olefin polymerization have been a research hotspot in organometallic chemistry, catalysis, polymer chemistry, and materials science in recent decades. Olefin polymerization uses this type of catalyst to obtain polymers with uniform molecular weight distribution and chemical composition distribution. At the same time, the molecular structure and molecular weight of the polymer can be highly controlled by adjusting the catalyst structure. Using single-site transition metal catalysts, traditional Ziegler - Olefin polymers not available with Natta catalysts. [0003] Low-molecular-w...

Claims

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Application Information

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IPC IPC(8): C08F10/06C08F110/06C08F210/06C08F210/14C08F4/6592C08F4/646
CPCC08F10/06C08F110/06C08F210/06C08F4/6592C08F4/65927C08F4/646C08F4/6465C08F2500/02C08F2500/03C08F210/14
Inventor 王伟范国强侯莉萍张韬毅刘长城盛建昉郑刚李森胡青
Owner CHINA PETROLEUM & CHEM CORP