Influence of Impregnation and Coprecipitation Method in Preparation of Cu/ZnO Catalyst for Methanol Synthesis
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作者:
Prasetyaningsih, Yusi
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Politekn TEDC Bandung, Jalan Politekn, Dept Chem Engn, Pesantren Km 2 Cibabat, Cimahi Utara, IndonesiaPolitekn TEDC Bandung, Jalan Politekn, Dept Chem Engn, Pesantren Km 2 Cibabat, Cimahi Utara, Indonesia
Prasetyaningsih, Yusi
[1
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Hendriyana
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UNJANI, Fac Engn, Dept Chem Engn, Jalan Ters Jend Sudirman, Cimahi, IndonesiaPolitekn TEDC Bandung, Jalan Politekn, Dept Chem Engn, Pesantren Km 2 Cibabat, Cimahi Utara, Indonesia
Hendriyana
[2
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Susanto, Herri
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Inst Teknol Bandung, Fac Ind Technol, Dept Chem Engn, Jalan Ganesha 10, Bandung 40132, IndonesiaPolitekn TEDC Bandung, Jalan Politekn, Dept Chem Engn, Pesantren Km 2 Cibabat, Cimahi Utara, Indonesia
Susanto, Herri
[3
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机构:
[1] Politekn TEDC Bandung, Jalan Politekn, Dept Chem Engn, Pesantren Km 2 Cibabat, Cimahi Utara, Indonesia
[2] UNJANI, Fac Engn, Dept Chem Engn, Jalan Ters Jend Sudirman, Cimahi, Indonesia
[3] Inst Teknol Bandung, Fac Ind Technol, Dept Chem Engn, Jalan Ganesha 10, Bandung 40132, Indonesia
Cu/ZnO catalyst was succesfully prepared using a coprecipitation method. The mixing procedure of the Cu(NO3)(2), Zn(NO3)(2) and Na2CO3 solutions had an important influence on the characteristics of the catalyst. The best catalyst obtained was the one prepared with slow mixing of the salt solutions and a CuO/ZnO molar ratio of 50:50. This raw catalyst had a maximum surface area of about 61.6 m(2)/g. Increasing the CuO/ZnO molar ratio caused an agglomeration of precipitated particles, reducing the surface area. A much better catalyst was obtained using an impregnation method, in which gamma-Al2O3 was used as support. The impregnated catalyst had a surface area of about 151 m(2)/g. Activity tests were carried out in a fixed-bed reactor containing 1 g of catalyst and a flow of syngas at a rate of 60 mL/min. The reaction temperature was 170 degrees C and the pressure was 20 barg. The best coprecipitated catalyst gave a CO conversion of about 10%, while the impregnated catalyst gave a CO conversion of up to 69%.
机构:
Zhejiang Univ Technol, Inst Ind Catalysis, State Key Lab Green Chem Synth Technol, Hangzhou 310032, Zhejiang, Peoples R ChinaZhejiang Univ Technol, Inst Ind Catalysis, State Key Lab Green Chem Synth Technol, Hangzhou 310032, Zhejiang, Peoples R China
Xia Wangqiong
Tang Haodong
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Zhejiang Univ Technol, Inst Ind Catalysis, State Key Lab Green Chem Synth Technol, Hangzhou 310032, Zhejiang, Peoples R ChinaZhejiang Univ Technol, Inst Ind Catalysis, State Key Lab Green Chem Synth Technol, Hangzhou 310032, Zhejiang, Peoples R China
Tang Haodong
Lin Shengda
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Zhejiang Univ Technol, Inst Ind Catalysis, State Key Lab Green Chem Synth Technol, Hangzhou 310032, Zhejiang, Peoples R ChinaZhejiang Univ Technol, Inst Ind Catalysis, State Key Lab Green Chem Synth Technol, Hangzhou 310032, Zhejiang, Peoples R China
Lin Shengda
Cen Yaqing
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Zhejiang Univ Technol, Inst Ind Catalysis, State Key Lab Green Chem Synth Technol, Hangzhou 310032, Zhejiang, Peoples R ChinaZhejiang Univ Technol, Inst Ind Catalysis, State Key Lab Green Chem Synth Technol, Hangzhou 310032, Zhejiang, Peoples R China
Cen Yaqing
Liu Huazhang
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Zhejiang Univ Technol, Inst Ind Catalysis, State Key Lab Green Chem Synth Technol, Hangzhou 310032, Zhejiang, Peoples R ChinaZhejiang Univ Technol, Inst Ind Catalysis, State Key Lab Green Chem Synth Technol, Hangzhou 310032, Zhejiang, Peoples R China