Process for producing ultrahigh molecular weight polymer in powder form
An ultra-high molecular weight, polymer technology, used in gas/liquid distribution and storage, piping systems, mechanical equipment, etc.
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Embodiment
[0110] The following examples are included herein for illustrative purposes only. Those skilled in the art will appreciate that many modifications can be made to the invention without changing the essence of the invention.
[0111] All monomers and solvents were used as received and contained less than 20 ppm moisture. All chemicals were handled under nitrogen atmosphere and used as received. Before the polymerization, the polymerization reactor was heated to 120° C. for 2 hours under nitrogen flow and cooled accordingly.
Embodiment I
[0112] Example I The production method of free-flowing ultra-high molecular weight polymer in powder form is shown:
[0113] The polymerization process was carried out in a kneader reactor with a single screw configuration with a capacity of 7 L equipped with a gear pump. The catalyst and cocatalyst were treated under nitrogen. The molar ratios of catalyst, cocatalyst and monomer are in accordance with US 10,094,399 written by the applicant. The monomer used was 1-decene. The polymerization mixture (mixture of catalyst, cocatalyst and monomer) was prepared under nitrogen atmosphere and transferred to the kneader reactor maintained at 10°C through the charge inlet port located on the reactor. Once the mixture is in the reactor, agitation is started to maintain the homogeneity of the solution. The reactor was maintained under nitrogen pressure adjusted to 0.5 bar to 1.0 bar. Stirrer speed is adjusted according to the viscosity of the mixture. The average residence time of...
Embodiment II
[0114] Example II A process for the production of free-flowing ultra-high molecular weight polymers in powder form is shown
[0115] The polymerization procedure was the same as Example 1 except that the monomers used were 80 / 20 by volume 1-dodecene / 1-hexene. The conversion after this process was about 93% and the intrinsic viscosity as polymer was 21 dL / g.
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