Production method of PPR (Polypropylene) pipe special material
A technology for special materials and production methods for pipes is applied in the field of polypropylene production, which can solve the problems of poor processing performance and difficulty in obtaining a wide molecular weight distribution, and achieve the effects of improving product processing performance and reducing equipment investment and production costs.
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Embodiment 1
[0025] This embodiment provides a method for producing special materials for PPR pipes, comprising the following steps:
[0026] Reduce the flow rate of catalyst solids to 0.52kg / h, adjust the partial pressure of propylene to 2Mpa, the partial pressure of ethylene to 0.05Mpa, the reaction temperature is 72°C, the pressure is 3.24Mpa, when the hydrogen partial pressure in the reactor is 0.008Mpa, ensure the hydrogen-carbon ratio and Al / Ti control is smooth.
[0027] When the melt index of the extrusion granulation powder is 0.2g / 10min, the extrusion granulation unit uses specific additives for PPR pipe materials and switches to the finished product silo, where the additives include the following components: main antioxidant (1010) added 3000ppm; primary antioxidant (330) 3000ppm; auxiliary antioxidant (168) 800ppm; calcium stearate 500ppm, processing aid (PPA) 300ppm, nucleating agent (NA-82) 200ppm.
[0028] Continuously increase the reaction load to 20t / h. When the melt inde...
Embodiment 2
[0037] This embodiment provides a method for producing special materials for PPR pipes, comprising the following steps:
[0038] Reduce the flow rate of catalyst solids to 0.52kg / h, adjust the partial pressure of propylene to 2Mpa, the partial pressure of ethylene to 0.06Mpa, the reaction temperature is 72°C, the pressure is 3.24Mpa, when the partial pressure of hydrogen in the reactor is 0.008Mpa, ensure the hydrogen-carbon ratio and Al / Ti control is smooth.
[0039] When the melt index of the extrusion granulation powder is 0.2g / 10min, the extrusion granulation unit uses specific additives for PPR pipe materials and switches to the finished product silo, where the additives include the following components: main antioxidant (1010) added 3000ppm; primary antioxidant (330) 3000ppm; secondary antioxidant (168) 800ppm; calcium stearate 500ppm, processing aid PPA 300ppm, no nucleating agent added.
[0040] Continuously increase the reaction load to 20t / h. When the melt index and...
Embodiment 3
[0049] A production method for special materials for PPR pipes. Propylene and ethylene are placed in a fluidized bed reactor in the Unipol gas phase polypropylene process technology for binary random copolymerization. The bed weight of the fluidized bed reactor is 15t , the bed height is 17m, the superficial gas velocity is 0.25m / s, and the product is degassed and granulated, wherein:
[0050] The copolymerization reaction of propylene and ethylene is carried out under the joint action of Cat-A catalyst and external electron donor D-A.
[0051] The Cat-A catalyst is a Z-N series catalyst, and the Z-N series catalyst is based on MgCl 2 as carrier, TiCl 4 As the active center, the internal electron donors are alkyl-substituted 1,3-diethers and aryl-substituted 1,3-diethers;
[0052] The external electron donor D-A is p-dicyclopentyldimethoxysilane and cyclohexylmethyldimethoxysilane;
[0053] During the reaction, the partial pressure of propylene is 1.5Mpa, and the partial pres...
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