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共沉淀法制备Cr-Zn-A1型催化剂,用于催化1,1,1-三氟-2-氯乙烷(HCFC-133a)与HF反应,制备1,1,1,2-四氟乙烷(HFC-134a)。BET法表征了催化剂的比表面积;CC-MS方法,分析了不同反应条件下HCFC-133a的转化率、HFC-134a的收率、以及副产物组成。结果表明,催化剂按一定程序烧结、活化后,温度为350-370℃、HF与HCFC-133a摩尔比为8-12时,HFC-134a的收率约为30%-38%,反应产物中HFC-134a的选择性大于99%。连续反应720h后,催化剂的活性不变。 相似文献
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采用共混法制得Cr—Mg—Zn催化剂,以HCFC-133a(1,1,1-三氟-2-氯乙烷)与无水HF合成HFC-134a(1,1,1,2-四氟乙烷)为目标反应,考察了不同条件下该催化剂的性能。用BET法表征了催化剂的比表面积、孔容、孔径,并对催化剂进行XRD、TG—DSC表征。结果表明,在AHF/HCFC-133a摩尔比为7和300℃条件下转化率为25.4%。选择性为95.7%。连续反应90天后活性下降到原来的80%;在O2中再生,发现转化率比再生前提高,可能是由于再生过程中氟化物产生水解生成了氟氧化物.而该类物质为本反应的活性物质。 相似文献
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采用共混法制得Cr-Mg-zn催化剂,以HCFC-133a(1,1,1-三氟-2-氯乙烷)与无水HF合成HFC-134a(1,1,1,2-四氟乙烷)为目标反应,考察了不同条件下该催化剂的性能。用BET法表征了催化剂的比表面积、孔容、孔径,并对催化剂进行XRD、TG—DSC表征。结果表明,在AHF/HCFC-133a摩尔比为7和300℃条件下转化率为25.4%,选择性为95.7%,连续反应90天后活性下降到原来的80%;在O2中再生,发现转化率比再生前提高,可能是由于再生过程中氟化物产生水解生成了氟氧化物,而该类物质为本反应的活性物质。 相似文献
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乙烷系氟碳化合物如1,1-二氟乙烷、1,1,1-三氟乙烷、1,1,1,2-四氟乙烷、五氟乙烷、六氟乙烷等在近代工业上有着广泛的用途,一般用作致冷剂、喷射剂、灭火剂、超大集成电路的等离子化学制剂等等,它们的世界需求量每年约上万吨。 相似文献
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催化氟化合成1,1,1,2—四氟乙烷 总被引:1,自引:0,他引:1
论述了三氯乙烯路线气相催化氟化合成1,1,1,2-四氟乙烷的催化剂、载体的制备方法以及氟化氢与三氟乙烯、HCFC-133a反应的特点,认为控制生成HCFC-133a的反应热、提高HFC-134a的选择性是反应研究的关键。建议开发具有高活性、高选择性的氟化物载体负载的低铬或无铬催化剂。 相似文献
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Cr-Zn-Al催化剂气相氟化法合成HFC-134a 总被引:2,自引:0,他引:2
用共沉淀法制备了Cr-Zn-A l型催化剂,用于催化1,1,1-三氟-2-氯乙烷(HCFC-133 a)与HF的反应,制备了1,1,1,2-四氟乙烷(HFC-134 a)。BET法表征了催化剂的比表面积;GC-MS方法分析了不同反应条件下HCFC-133 a的转化率、HFC-134 a的收率、以及副产物组成。结果表明,催化剂按一定程序烧结、活化后,反应温度为350~370℃、n(HF)/n(HCFC-133 a)=8~12时,HFC-134 a的收率为30%~38%,反应产物中HFC-134 a的选择性大于99%。连续反应720 h后,催化剂的活性不变。 相似文献
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以偏氟乙烯为原料,经光氯化、脱氯化氢、溴化加成3步反应合成1,2-二溴-1,1-二氯-2,2-二氟乙烷,试验了各种因素对反应的影响.光氯化反应时温度低有利于2,2-二氟-1,1,2-三氯乙烷选择性的提高,相转移催化剂四丁基溴化铵能加快反应脱氯化氢的速率,溴加成的合适温度为15~20℃.结果表明此合成路线是可行的. 相似文献
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Tae Uk Han Beom-Sik Yoo Young-Min Kim ByeongAh Hwang Gamal Luckman Sudibya Young-Kwon Park Seungdo Kim 《Korean Journal of Chemical Engineering》2018,35(8):1611-1619
We examined the conversion of HFC-134a over five catalysts, Na2CO3, CaO, CaCO3, and two types of γ-Al2O3 with different surface areas, between 300 and 600 °C. HFC-134a was barely converted via the non-catalytic reaction, even at the highest temperature (600 °C). The operating temperatures for the catalytic conversion of HFC-134a were reduced dramatically and its efficiency increased with increasing temperature. Among the catalysts used, γ-Al2O3 with the larger surface area showed the highest conversion rate of HFC-134a, which was followed, in order, by γ-Al2O3 with the smaller surface area, CaCO3, CaO, and Na2CO3. The conversion rate of γ-Al2O3 decreased rapidly due to catalyst deactivation. The catalytic efficiency of γ-Al2O3 was maintained for a longer period by water addition. Water acted as a hydrogen donor for the dehydrofluorination reaction. 相似文献
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为了制备具有工业化应用价值的1,1,1,2-四氟乙烷脱氟化氢制备三氟乙烯用催化剂,在固定床反应器上考察了催化剂制备条件如溶剂、沉淀温度、沉淀剂浓度对氟化铝基催化剂性能的影响。结果表明不同制备条件下得到的催化剂均为β-AlF3。当乙醇为溶剂、室温沉淀、氢氟酸浓度为22.5 mol/L时,制得的AlF3催化剂初始活性最高。在反应温度450℃,接触时间3.2(g·s)/mL的条件下,1,1,1,2-四氟乙烷初始转化率达36%,三氟乙烯选择性为100%,运行8 h后催化剂活性保持在26%,选择性为100%。 相似文献
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气相催化氟化合成1,1,1,3,3-五氟丙烷研究进展 总被引:5,自引:0,他引:5
综述了以1,1,1,3,3-五氯丙烷(HCC-240fa)为原料,经1-氯-3,3,3-三氟丙烯(HCFC-1233zd)和1,3,3,3-四氟丙烯(HFC-1234ze)中间体气相氟化合成1,1,1,3,3-五氟丙烷(HFC-245fa)的催化剂、反应条件选择等的研究进展。建议开发在低温下具有较高氟化性能的催化剂。 相似文献
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Jian Lu Huie Yang Shukang Chen Lei Shi Jiangang Ren Huili Li Shaoyi Peng 《Catalysis Letters》1996,41(3-4):221-224
The effect of the structure of AlF3 supports in CrF3/AlF3 catalysts and their activity were studied, and a selection of suitable reaction conditions for fluorination of trichloroethylene and HCFC-133a was made. We found that neither AlF3 (- and -modifications) nor CrF3/-AlF3 exhibits significant activity for the reaction of HF with CCl2=CHC1 or CF3CH2Cl. However, CrF3/-AlF3 exhibits high activity, which increases with increasing surface area and decreasing crystallite size of the -AlF3 support, and that dramatically affects the fiuorination of CF3CH2Cl. Investigation of a series of CrF3/-AlF3 catalysts shows that the turnover rates per unit of the total surface area and of the free CrF3 surface area significantly increase with increasing content of Cr3+ loading. Optimum temperature for the reaction of HF with CCl2=CHCl is 260°C, while with CF3CH2Cl it is 350°C, with flow ratios HFTCE = 61 andHFHCFC-133a = 101. 相似文献
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Dong Jin Suh Tae-Jin Park Byung-Gwon Lee Kun-You Park 《Korean Journal of Chemical Engineering》1996,13(1):75-81
For the preparation of HFC-134a, the isomerization of CFC-114 and the hydrogenation of CFC-114a were investigated. Both reactions
were catalyzed by AlC3 and supported Pd catalysts, respectively. For the comparison purpose, the isomerization of CFC-113 was carried out also.
With virgin AICI3 catalyst, both isomerization reactions proceeded after a certain induction period probably because the catalyst needed the
activation by the halogen exchange. The catalyst deactivated gradually with the time on stream. However, the deactivation
rate could be reduced by removing impurities from the reactants. Isomerization rate of CFC-114 was much slower than that of
CFC-113. Palladium supported on carbon catalyzed the hydrogenation reaction quite selectively while the selectivity declined
when the support was replaced with different supports. The catalytic activity and selectivity to desired products increased
in the following order. Pd/kieselguhr Pd/silica-alumina ≅Pd/silica gel Pd/TiO2Pd/Al2O3Pd/C 相似文献