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Frontiers of Chemical Science and Engineering

ISSN 2095-0179

ISSN 2095-0187(Online)

CN 11-5981/TQ

邮发代号 80-969

2019 Impact Factor: 3.552

Frontiers of Chemical Science and Engineering  2011, Vol. 5 Issue (1): 89-95   https://doi.org/10.1007/s11705-010-0558-x
  RESEARCH ARTICLE 本期目录
Gas phase ethylene polymerization over SiO2-supported organosilyl chromate UCC S-2 catalyst using a high-speed stirred-autoclave reactor
Gas phase ethylene polymerization over SiO2-supported organosilyl chromate UCC S-2 catalyst using a high-speed stirred-autoclave reactor
Liuzhong LI1,3, Aiyou HAO1(), Ruihua CHENG2, Boping LIU2()
1. School of Chemistry and Chemical Engineering, Shandong University, Jinan 250100, China; 2. State Key Laboratory of Chemical Engineering, East China University of Science and Technology, Shanghai 200237, China; 3. Research Institute of Qilu Branch Co., SINOPEC, Zibo 255400, China
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Abstract

Although an important industrial catalyst for producing high density polyethylene, the SiO2-supported organosilyl chromate UCC S-2 catalyst has not been fully investigated compared with the SiO2-supported oxo chromium Phillips catalyst. In this work, gas phase ethylene polymerization by S-2 catalysts (Cat-1, Cat-2, and Cat-3) was carried out in a high-speed stirred-autoclave reactor. The effects of temperature, time, and pressure on kinetics, activity, and product properties were studied. All kinetics were typical built-up types with slow decay. Compared to the simple physical mixtures of Cat-1 and Cat-2, Cat-3 showed higher activity and its product had a broader molecular weight distribution, indicating new active species induced during blending of Cat-1 and Cat-2 in n-hexane. The innovation by a simple catalyst technology created a new application to meet market demands.

Key wordsUCC S-2 catalyst    Al-alkyl co-catalyst    gas-phase ethylene polymerization    high density polyethylene
收稿日期: 2010-04-28      出版日期: 2011-03-05
Corresponding Author(s): HAO Aiyou,Email:haoay@sdu.edu.cn; LIU Boping,Email:boping@ecust.edu.cn   
 引用本文:   
. Gas phase ethylene polymerization over SiO2-supported organosilyl chromate UCC S-2 catalyst using a high-speed stirred-autoclave reactor[J]. Frontiers of Chemical Science and Engineering, 2011, 5(1): 89-95.
Liuzhong LI, Aiyou HAO, Ruihua CHENG, Boping LIU. Gas phase ethylene polymerization over SiO2-supported organosilyl chromate UCC S-2 catalyst using a high-speed stirred-autoclave reactor. Front Chem Sci Eng, 2011, 5(1): 89-95.
 链接本文:  
https://academic.hep.com.cn/fcse/CN/10.1007/s11705-010-0558-x
https://academic.hep.com.cn/fcse/CN/Y2011/V5/I1/89
Fig.1  
Fig.2  
Cat.Temp./°Cyield / (gPE·gcat-1)MWb) / × 104MI/21.6kgdensity / (g·mL-1)bulk density / (g·mL-1)Mnc)/(× 103)Mwc)/(× 104)MWDc)
Cat-18890.4843.33.30>0.96000.3818.6835.440.8
92106.732.44.690.95880.4009.1629.432.1
95137.3830.18.120.93980.37012.525.420.4
Cat-288113.2532.64.530.95950.4179.3139.736.5
92153.7630.75.52>0.96000.4067.9236.546.1
95189.0923.512.80.96010.4267.4229.139.1
Tab.1  
Fig.3  
Fig.4  
Cat.pressure / MPayield / (gPE·gcat-1)MW b) / (× 104)MI/21.6kgdensity / (g·mL-1)bulk density / (g·mL-1)
Cat-10.871.428.716.260.95780.390
1.0111.229.411.360.95870.400
1.2103.230.010.000.95800.409
1.4140.330.99.970.95920.360
1.6143.634.78.110.95970.330
Cat-20.872.332.610.190.95950.410
1.096.033.57.310.96000.377
1.2121.133.15.170.95860.430
1.4130.734.44.410.95090.400
1.6140.936.34.300.95920.364
Tab.2  
Cat.time / hyield / (gPE·gcat-1)MW b) / (× 104)MI 21.6kgdensity / (g·mL-1)bulk density / (g·mL-1)Mn c) / (× 103 )Mw c) / (× 104)MWD c)
Cat-11140 0.329.410.000.95880.4097.7632.742.1
3610.628.59.090.95760.3979.3134.036.5
4670.424.69.020.95950.4108.3833.840.3
Cat-21121.134.45.000.95860.4098.6931.536.2
3632.837.04.340.95680.4029.5134.235.9
4747.8336.13.220.95830.45010.035.535.3
Tab.3  
Temp. /°Cyield / (gPE·gcat-1)MW b) / (× 104)MI / 21.6kgdensity / (g·mL-1)bulk density / (g·mL-1)Mn c) / (× 103)Mw c) / (× 104)MWD c)
88194.944.03.580.95860.4359.1543.547.5
92226.035.06.900.95970.4104.8128.559.3
95207.630.68.710.95930.46510.034.734.7
Tab.4  
pressure / MPayield / (gPE·gcat-1)MW b) / (× 104)MI / 21.6kgdensity / (g·mL-1)bulk density / (g·mL-1)Mn c) / (× 103)Mw c) / (× 104)MWD c)
0.875.333.68.140.95970.4178.3928.233.7
1.2226.035.06.900.95970.4104.8128.559.3
1.6127.042.05.440.95750.4454.6330.966.7
Tab.5  
Fig.5  
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