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碳酸甲乙酯是一种重要的化工原料,市场潜力巨大。相对于传统制备方法,酯交换法制备碳酸甲乙酯具有明显优势。综述碳酸二甲酯酯交换反应合成碳酸甲乙酯的路线,对比碳酸二甲酯分别与乙醇和碳酸二乙酯进行反应的特点,表明碳酸二甲酯与乙醇反应需要解决产物分离的问题,而碳酸二甲酯和碳酸二乙酯酯交换反应则需要提高转化率。两种方法均具有良好的发展前景。 相似文献
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碳酸二甲酯的合成研究受到了国内外研究者的广泛关注,合成路线正朝着简单化、无毒化和无污染化的方向发展。笔者从催化剂体系方面,综述了酯交换法合成碳酸二甲酯的研究新进展,并分析了几种合成方法的优缺点。 相似文献
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碳酸二甲酯合成技术与经济分析 总被引:1,自引:0,他引:1
本文介绍了碳酸二甲酯的性质、应用领域和生产消费情况,从工艺特点、催化剂等方面介绍了4种合成路线,并对其技术经济性做了简要对比分析,指出目前较好的合成路线为尿素甲醇法,存在的问题是高效催化剂的开发。将尿素甲醇法和二氧化碳甲醇直接合成法进行了对比,认为这两种方法是碳酸二甲酯合成技术的未来发展方向。 相似文献
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用碳酸二甲酯(DMC)与正丙醇(n-PrOH)酯交换反应合成了碳酸二丙酯(DPC),考察了催化剂种类、物料摩尔比、催化剂用量、温度和时间等因素对反应的影响。结果表明,碳酸钾(K2CO3)具有较好的催化活性和选择性,反应最佳工艺条件为:常压,反应温度95℃,n(n-PrOH)∶n(DMC)=3∶1,w(K2CO3)=1%,反应时间5 h,DMC转化率95.9%,DPC产率73.7%。优化条件下的重复实验表明,该反应易于控制,重复性好。测定了常压下DPC和DMC的气液相平衡数据,结果表明,在常压下DPC和DMC二元物系不形成共沸物。 相似文献
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A large-scale dimethyl carbonate (DMC) production process from ethylene oxide (EO), CO2, and methanol was simulated and optimized. Unlike most industrial processes of DMC production, the direct conversion of EO and CO2 to ethylene carbonate (EC) and EC transesterification to DMC were performed in a single reactor. The reaction volume and the reactor operating pressure were selected as decision variables and evaluated. The key performance parameters, e.g., conversion per pass and CO2 intensity, were compared with conventional commercialized routes or novel promising processes in the literature. 相似文献
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综述了固碳技术的研发历程,从资源化利用的角度看,CO2是一种大存量的“碳源”,化学固碳兼具碳减排和资源化的优势,是未来固碳技术的重点发展方向。基于化学固碳技术存在的问题及已形成的技术成果,将CO2资源化利用工艺与现有新材料合成工艺相结合,提出了以CO2为基础原料深度延伸产业链生产聚碳酸酯,并形成多元化产品结构、具备工业化实施条件的新型固碳工艺。针对新工艺主要涉及到的CO2合成尿素、尿素法DMC、酯交换法DPC、异丙苯法苯酚工艺、离子交换树脂法BPA合成工艺及非光气法PC等生产过程,进行了技术可行性分析。 相似文献
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碳酸二甲酯(DMC)是一种重要的绿色化工原料,在工业、农业、医药行业等领域得到广泛的应用。碳酸二甲酯的合成方法有多种,其中光气甲醇法、酯交换法、氧化羰基化法已经工业化,但由于各自的缺点,限制了其规模化。近年来,研究较多的也是公认最绿色环保的合成方法是用二氧化碳与甲醇直接合成碳酸二甲酯。介绍了这种方法所应用的催化剂及其催化机理研究的进展状况,并对诸多催化剂存在的问题提出建议。 相似文献
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A process for the production of glycerol carbonate (GC) is proposed with the transesterification of glycerol (GL) and dimethyl carbonate (DMC) with CaO as catalyst by reactive distil ation and extractive distil ation. The perfor-mance of solvents in separating DMC-methanol azeotrope and the effects of operation parameters on the reactive distillation process are investigated experimental y. The results indicate that both the GL conversion and GC yield increase with the DMC/GL molar ratio, reflux ratio, final temperature of tower bottom, and CaO/GL molar ratio and decrease as the recycle number of CaO increases. The calcium concentration in the residual reaction mixture also decreases remarkably as the DMC/GL molar ratio increases. At DMC/GL molar ratio 4.0, reflux ratio 1.0, final temperature of tower bottom 358 K, and CaO/GL molar ratio 0.05, both the GL conversion and GC yield can reach above 99.0%, and the mass concentration of calcium in the product is less than 0.08%. 相似文献
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《Applied Catalysis A: General》2007,316(1):1-21
Diphenyl carbonate (DPC) is considered as a substitution for phosgene to synthesize polycarbonate resins. Conventional production of DPC involves reactions of phosgene and phenol. However, the phosgene process has drawbacks such as environmental and safety problems associated with using highly toxic phosgene as the reagent, which results in the formation of chlorine salts, and copious amounts of methylene chloride as the solvent. For these reasons, environmentally friendly processes for DPC production without using phosgene have been proposed and developed in the past decades. So far, the most promising alternatives appear to be the transesterification of dimethyl carbonate (DMC) and phenol, the direct oxidative carbonylation of phenol, and transesterification of dialkyl oxalates and phenol. This paper attempts to review recent literature concerning process design and catalytic chemistry for these phosgene-free approaches. The advantages and disadvantages are discussed for each reaction. Strategies to overcome potential problems are provided. The perspectives to improve catalytic efficiency of phosgene-free process are proposed. 相似文献