A kind of preparation method of low volatile resin
A low-volatility resin technology, applied in the field of low-volatility resin preparation, can solve the problems of high volatile component content, complex process, high cost, etc., and achieve good melt fluidity, simple process and low production cost Effect
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Embodiment 2
[0075] Prepare according to the following formula:
[0076] 1) 97 parts by mass of polyethylene
[0077] 2) 0.9 parts by mass of deionized water
[0078] 3) Surfactant (polyoxyethylene 20 oleyl ether) 0.1 parts by mass
[0079] 4) Antioxidant 1010 2.0ppm parts by mass
[0080] First with the certain high-density polyethylene powder identical with embodiment 1 impurity removal, deblocking by 12kg / h processing capacity, with low molecular weight auxiliary agent (water, deionized water), antioxidant by the above-mentioned formula proportioning, Mix for 5 minutes at a speed of 300 rpm with a high mixer to obtain a premix. The detected total carbon value of the powder is 82.5μgC / g sample, in figure 1 In the extruder shown, the premixed material is added through the feeding port, the first-stage exhaust port is enabled, and the gauge pressure of the exhaust port is -0.04MPaG. Special materials for pipes. In this example, the temperature of the cooling water tank is 25-30°C, th...
Embodiment 3
[0095] Prepare according to the following formula:
[0096] 1) 97 parts by mass of polyethylene
[0097] 2) 0.9 parts by mass of deionized water
[0098] 3) Surfactant (polyoxyethylene 20 oleyl ether / polyoxyethylene lauryl ether / nonanol polyethylene glycol ether) 0.1 parts by mass (ratio 3:1:1)
[0099] 4) Antioxidant 1076 2.0ppm parts by mass
[0100] After removing impurities and blocks from a certain high-density polyethylene powder, mix low-molecular-weight additives (water, deionized water) and antioxidants according to the above formula through a high-speed mixer according to the processing capacity of 17kg / h. figure 1 In the vented extruder with the structure shown, it is added through the feeding funnel. After being mixed in the pre-mixing section, it enters the exhaust section, and the gauge pressure of the primary exhaust port is controlled to -0.03MPaG, and the gauge pressure of the secondary exhaust port is -0.06MPaG to exhaust, extrude and granulate to obtain l...
Embodiment 4
[0115] Prepare according to the following formula:
[0116]
[0117] First remove impurities and blocks from a certain linear low density polyethylene powder, and then add it together with antioxidants according to the above formula at a processing rate of 14kg / h. figure 1 For the vented screw extruder shown, after mixing the surfactant and deionized water with a premixer, add the first-level liquid injection port and the second-level liquid injection port at a ratio of 6:4, and the melt is pre-mixed After mixing in the first section, enter the exhaust section, control the gauge pressure of the primary exhaust port to -0.03MPaG, and the gauge pressure of the secondary exhaust port to -0.05MPaG to exhaust, extrude, and granulate to obtain a pipeline with low volatile content. material. After testing, the total carbon value of the raw material powder is 124.9 μgC / g sample. In this example, the temperature of the cooling water tank is 25-30°C, the rotational speed of the pel...
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