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国外用过氧化氢环氧化丙烯制环氧丙烷研发近况 总被引:3,自引:3,他引:0
胡长诚 《化学推进剂与高分子材料》2006,4(2):1-5,10
介绍了国外用过氧化氢环氧化丙烯制备环氧丙烷(PO)工艺技术近期研发概况,内容包括所用过氧化氢来源(来自蒽醌法或氢、氧直接化合法)、丙烯环氧化反应以及反应产物精制和原料回收循环利用过程,工艺涉及催化剂、溶剂、流程、反应器、操作方法和试验结果等。不少工艺是将过氧化氢合成与丙烯环氧化加以耦合,形成完整体系,提高运转效率和经济效益。此外,简略介绍了用过氧化氢制PO工艺在产业化方面的最新进展。 相似文献
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介绍了环氧丙烷的用途及国内外合成技术和经济概况。详细介绍了住友化学公司的以异丙苯过氧化氢作氧化剂合成环氧丙烷的工艺,该工艺包括异丙苯氧化、丙烯环氧化、丙烯和环氧丙烷回收与精制、二甲基苄醇脱水与氢化以及有害杂质去除等步骤,整个工艺无联产品生成,装置建设费用比传统的Halcon法工艺约低1/3。 相似文献
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丙烯直接氧气环氧化制环氧丙烷是催化领域最关键的挑战之一,被誉为工业界的"圣杯"。文章对近年来开展的以氧气为氧化剂的Au基、Ag基催化剂上丙烯环氧化制备环氧丙烷的研究结果进行了综述,并对其前景和发展方向进行了分析展望。 相似文献
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以钛硅分子筛TS-2为催化剂,过氧化氢为氧化剂,甲醇为溶剂,研究TS-2催化剂催化丙烯生成环氧丙烷.考察了停留时间、反应温度、反应压力和催化剂用量对环氧丙烷收率和选择性的影响.实验结果表明,合适的反应条件为50℃,0.30 MPa,催化剂用量为反应物质量的3.44%,停留时间90 min.在该条件下反应,过氧化氢的平均转化率和环氧丙烷的选择性分别为45%和96%左右.TS-2催化剂的重复使用实验表明,TS-2催化剂在催化丙烯环氧化制环氧丙烷的反应中具有较好的催化活性和稳定性. 相似文献
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对环氧丙烷生产技术的现状及新动向进行了综述,提出以Si-Ti分子筛为催化剂的丙烯直接环氧化法是今后发展的方向。 相似文献
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环氧丙烷合成技术的研究进展及展望 总被引:1,自引:0,他引:1
介绍了丙烯氧化制环氧丙烷的催化工艺和催化剂的研究现状,包括现有环氧丙烷的生产工艺,分子氧为氧化剂、过氧化氢为氧化剂、O2/H2为氧化剂、有机过氧化物为氧化剂的丙烯直接环氧化以及光催化氧化等;并对各反应工艺和催化剂、催化反应机理和发展前景进行了讨论。 相似文献
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环氧丙烷生产工艺述评及发展设想 总被引:2,自引:0,他引:2
介绍国内环氧丙烷生产概况和氯醇法、联产法及过氧化氢直接氧化丙烯制环氧丙烷工艺,以及近期国内外环氧丙烷生产工艺研发情况。并对比3种生产工艺,提出对国内环氧丙烷改造和发展的意见。 相似文献
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环氧丙烷(PO)在全球产能最高的35种化学品中,是仅次于聚丙烯的第二大丙烯衍生物,主要用于生产聚醚多元醇、聚氨酯等。相比传统的氯醇法、共氧化法和双氧水直接氧化法(HPPO)等PO生产工艺,丙烯在氢氧混合气中一步环氧化制PO(HOPO)具有工艺简单、选择性高、产物易分离、能耗低等突出优势,是生产PO的理想工艺。重点介绍了丙烯氢氧环氧化反应动力学研究进展,包括主、副反应动力学模型以及催化剂失活模型。总结了基于该过程安全操作的反应器概念设计进展。分析了丙烯氢氧环氧化反应存在的挑战,从副产物生成途径、失活动力学及颗粒催化剂上的动力学等方面展望了可能的研究方向。 相似文献
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The direct oxidation of propylene to propylene oxide (PO) using molecular oxygen has many advantages over existing chlorohydrin and hydroperoxide process, which produce side products and require complex purification schemes. Recent advances in liquid-phase and gas-phase catalytic oxidation of propylene in the presence of only molecular oxygen as oxidant and in absence of reducing agents are summarized. Liquid-phase PO processes involving soluble or insoluble Mo, W, or V catalysts have been reported which provide moderate conversions and selectivities, but these likely involve autoxidation by homogeneous chain reactions. Gas-phase PO catalysts have been mostly Ag-, Cu-, or TiO2-based substances, although other compositions such as Au-, MoO3-, Bi-based catalysts and photocatalysts have also been suggested as possibilities. The Ag catalysts differ from those used for ethylene oxide production in having high Ag contents and numerous additives. The additives are solid-phase alkali metals, alkaline earth metals, and halogens, with the most common substances being NaCl and CaCO3. Nitrogen oxides in the form of gas-phase species or nitrates have also been found to be effective in enhancing PO production. Direct epoxidation by surface nitrates is a possibility. Titania catalysts supported on silicates have also been reported. These have higher PO selectivities at high conversion than silver catalysts. 相似文献
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Ag-CuCl catalysts were found to be active and selective for the epoxidation of propylene using air as the oxidant. Ag catalyst gives a propylene conversion of 31.6%, with a propylene oxide (PO) selectivity of 0.42% at a reaction temperature of 350 °C after 220 min of reaction. Addition of CuCl significantly improves the selectivity to PO, and suppresses the conversion of propylene. The Ag-CuCl (1/0.6) catalyst gives propylene conversion of about 3% and a PO selectivity of about 30% at a reaction temperature of 350 °C after 500 min of reaction. The activity of the Ag-CuCl catalyst increases with the reaction time and the selectivity to PO is very stable for this catalyst. It is found that AgCl and CuO phases formed during the catalyst preparation are beneficial to the epoxidation of propylene. 相似文献
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Selective propylene epoxidation to propylene oxide(PO) with hydrogen peroxide(H_2O_2) was carried out in a catalytic semi-batch reactor.High propylene epoxidation activity(44 h~(-1)) was observed over Nb based mesoporous silicate materials Nb-TUD-1 under mild operating conditions.The physical and chemical properties of the Nb based silicates characterized using BET,FTIR,TPD,TEM and UV–Vis revealed that the site isolation and surface acidity are crucial for PO production.Catalyst synthesis methods were investigated for their effects on PO productivity,PO selectivity and H_2O_2 utilization efficiency.It is found that Nb-TUD-1 material synthesized by the sol–gel method is more active and selective than impregnated materials for liquid phase propylene epoxidation.Surface characterization confirms that thus synthesized Nb-TUD-1 catalysts have more Lewis acidity and less Bronsted acidity compared to the catalysts by impregnation. 相似文献
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Apoorva Kulkarni Marco Bedolla-Pantoja Suyash Singh Raul F. Lobo Manos Mavrikakis Mark A. Barteau 《Topics in Catalysis》2012,55(1-2):3-12
The reactions of propylene oxide (PO) on silver catalysts were studied to understand the network of parallel and sequential reactions that may limit the selectivity of propylene epoxidation by these catalysts. The products of the anaerobic reaction of PO on Ag/??-Al2O3 were propanal, acetone and allyl alcohol for PO conversions below 2?C3%. As the conversion of PO was increased either by increasing the temperature or the contact time, acrolein was formed at the expense of propanal, indicating that acrolein is a secondary reaction product in PO decomposition. With addition of oxygen to the feedstream the conversion of PO increased moderately. In contrast to the experiments in absence of oxygen, CO2 was a significant product while the selectivity to propanal decreased as soon as oxygen was introduced in the system. Allyl alcohol disappeared completely from the product stream in the presence of oxygen, reacting to form acrolein and CO2. The product distribution may be explained by a network of reactions involving two types of oxametallacycles formed by ring opening of PO: one with the oxygen bonded to C1 (OMC1, linear) and the other with oxygen bonded to C2 (OMC2, branched). OMC1 reacts to form PO, propanal, and allyl alcohol. OMC2 can give rise to acetone and PO. (DFT) calculations have verified accessibility to the two oxametallacycle structures from propylene and PO, and have provided energy barriers for each of the steps involved in PO isomerization. This work illustrates the complex manifold of sequential reactions that contribute to the difficulty of achieving high selectivity in direct propylene epoxidation with silver catalysts. 相似文献