共查询到20条相似文献,搜索用时 148 毫秒
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谭捷 《精细与专用化学品》2022,(1):5-7,22
分析了我国高纯异丁烯及其主要下游产品丁基橡胶、甲基丙烯酸甲酯以及聚异丁烯等的供需现状及发展前景,指出了我国高纯异丁烯行业今后的发展趋势. 相似文献
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氨基甲酸甲酯作为一种重要的精细化学品,在众多领域中有着广泛的应用,当前已成为尿素下游领域竞相开发的重点。概述了常温常压催化合成、中温中压催化合成及无催化剂高压合成尿素醇解法生产氨基甲酸甲酯工艺研究进展,同时展望其在有机合成、医药、农药等领域的应用,以期对氨基甲酸甲酯行业的发展有较为深入的了解。 相似文献
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A laboratory fixed-bed reaction column is presented, in which a heterogeneouslyl catalyzed reversible fluid-phase reaction and the separation of the reaction product from unreacted or inert components by distillation are performed simultaneously. The rection studied, the formation of methyl tertiary butyl ether (MTBE) from methanol and isobutylene, is catalyzed by strongly acidic macroreticular ion exchange resins. Packing elements are Raschig rings, manufactured for the first time from the above-mentioned ion exchange resins. This in-house made catalyst shows practically the same ion exchange capacity as the commercial products. The control system installed in the equipment is capable of correcting strong disturbances os the steady state. As shown by expwrimental results, the superimposed distillation process occurs in such a way that the chemical equilibrium of the MTBE synthesis does not limit isobutylene conversion. 相似文献
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制备了Cs/SiO2催化剂,在固定床反应器中研究了其催化甲醛与丙酸甲酯羟醛缩合反应性能,并采用X射线衍射、场发射扫描电镜、X射线荧光光谱分析和热分析等手段,对催化剂组成和结构变化跟踪分析。采用80%的浓缩甲醛为甲醛源,单程1000h反应过程中,丙酸甲酯转化率13%~15%,甲醛转化率60%~65%,丙酸甲酯为基准的甲基丙烯酸甲酯(MMA)选择性93%~95%。长周期反应后,催化剂晶型结构和形貌未发生显著变化,活性组分Cs未出现明显聚集和流失,积炭量有所增加。原位烧碳再生后,催化剂活性得到恢复,初始活性高于新鲜催化剂,随着反应的进行,甲醛、丙酸甲酯转化率等指标逐渐趋稳,接近再生前的平均水平。在近1700h的反应时长内,丙酸甲酯为基准的MMA选择性93%~95%,催化剂总体稳定性较好。技术经济分析表明,以羟醛缩合为核心技术的煤基MMA合成新路线,较传统的丙酮氰醇法和异丁烯氧化法MMA技术安全环保、经济高效,契合我国富煤、贫油、少气的资源结构和国家煤化工产业升级鼓励政策,可突破C2和C4路线商业技术的专利封锁,改变MMA行业现有技术格局,为煤化工企业进军MMA合成技术领域提供重要途径,同时可消化国内乙酸、甲醛的过剩产能以及大量低值化利用的副产乙酸甲酯,丰富我国煤化工产品链。 相似文献
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以醋酸甲酯为原料,经羰基化合成亚乙基二乙酸酯中间产物、再裂解生成醋酸乙烯的技术方法是一种新型煤化工合成醋酸乙烯工艺路线。综述了国内外醋酸甲酯制备醋酸乙烯工艺过程以及催化剂体系,使用廉价醋酸甲酯为原料开发高附加值的下游产品,充分挖掘醋酸甲酯的经济效益,减少对苯二甲酸和聚乙烯醇生产成本,符合我国石油化工生产现状,具有良好的经济效益和社会价值。 相似文献
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异丁烯为原料制备甲基丙烯酸甲酯的催化剂 总被引:4,自引:1,他引:3
The catalysts used for manufacturing methyl methacrylate (MMA) by two-step conversion of isobutylene via methacrolein (MAID were studied. The selective oxidation of isobutylene to MAL was carried out in a fixed-bed flow microreactor using a series of Mo-Bi-containing catalysts and the oxidative esterification of MAL to MMA was carried out in a slurry-bed reactor using a series of palladiumcontaining catalysts. By means of BET and XPS, the properties of the catalysts were characterized. It was found that the performance of Mo-Bi-Co-Fe-Ce-O catalyst was improved distinctly when Cs was added for the selective oxidation of isobutylene to MAL, and the Pd5Bi2PbFe/CaCO3 catalyst with the loading sequence of Pd, Pb and Bi, Fe showed the best performance for the oxidative esterification of MAL to MMA. 相似文献