共查询到20条相似文献,搜索用时 866 毫秒
1.
粗异戊烯产自浙石化50万t/a裂解C5分离装置,年产8.8万t/a,粗异戊烯经过加氢后可作为汽油、乙烯原料或与甲醇反应生成高纯度的异戊烯。浙石化粗异戊烯可通过石脑油加氢装置、汽油加氢装置、S-Zorb装置加工。在石脑油加氢装置加工时,粗异戊烯进入拔头油作为乙烯原料送乙烯,解决了粗异戊烯因烯烃含量高不能直接送乙烯加工的问题;在汽油加氢装置加工时,粗异戊烯作为轻汽油馏分送至汽油醚化装置与甲醇反应,增加了工艺附加值;在S-Zorb装置加工时,由于粗异戊烯中的二烯烃自聚,使原料/反应产物换热器管程堵塞,造成偏流及换热效果下降,不能长期加工。 相似文献
2.
3.
焦化液化气作为延迟焦化装置产品,长期以来作为民用烃出厂,经济效益未得到充分开发.镇海炼化公司采用中石化大连石油化工研究院的焦化液化气和汽油混合加氢制备乙烯裂解料技术,建设了一套60万t·a-1的焦化液化气与焦化汽油混合加氢装置.生产出烯烃质量分数不大于1.0%的精制液化气和溴价不大于2.5 g Br·(100 g)-1的精制石脑油,可作为优质的乙烯裂解原料.对该工艺路线的技术特点、工业运行状况、经济效益等进行探讨分析,数据表明,焦化液化气和焦化汽油经新工艺路线加工后作为乙烯裂解原料,工艺路线简洁,经济效益显著. 相似文献
4.
4 合成气直接制烃催化剂提高合成过程竞争力的总趋势是控制选择性,开发定向合成催化过程和催化剂。目的产品是液体燃料汽油、柴油,化工原料乙烯、丙烯、异丁烯等低碳烯烃以及裂解原料低碳烷烃。4.1 合成低碳烯烃 相似文献
5.
6.
7.
日前,西德林德公司 Karl Stork 先生一行到广州与广州石化总厂就林德-西拉斯裂解技术进行了技术交流。林德公司自1951年与美国西拉斯公司合作建设了第一套乙烯装置之后,便买下了西拉斯的裂解技术专利,并不断拓新。采用的原料以轻石脑油至加氢减压柴油等各种液态烃为主。目前林德-西拉斯裂解炉的主要参数如下表所示。 相似文献
8.
9.
乙烯低聚制低碳烃是利用催化干气乙烯资源的有效途径。本文以催化干气为原料,在固定床反应装置上,采用HZSM-5催化剂,对乙烯低聚催化剂活性组分进行了研究。结果表明,活性组分含量20%~30%对提高烯烃收率有利;调节离子交换温度可以改善烯烃收率,但采用较快再生的流化床反应器更为合适。 相似文献
10.
11.
It has been found that ethylene and propylene could be effectively hydrogenated by formic acid vapour over a Pd/carbon catalyst at low temperatures (<440 K). Surface hydrogen formation from formic acid is the rate-determining step for this hydrogenation reaction. Interaction of this hydrogen with the olefins is then fast. The conversion of formic acid in the presence of either of the olefins at any temperature is higher than in their absence. This has been explained by a much lower surface hydrogen concentration in the presence of the olefins. Direct experiments have confirmed that hydrogen inhibits the formic acid decomposition. Water vapour addition has a small positive effect on the decomposition of formic acid as well as on the hydrogenation of the olefins with formic acid. Catalysts consisting of gold supported on carbon or titania are both active in the production of hydrogen from formic acid. However, in contrast to the Pd/C catalyst, neither gives hydrogenation of the olefins with this acid. 相似文献
12.
1,3-丙二醇的生产技术 总被引:9,自引:0,他引:9
综述了环氧乙烷羰基化法、丙烯醛水合加氢法和微生物发酵法生产 1 ,3-丙二醇工艺路线的原料、催化体系、工艺过程及研发状况。比较了 3种工艺路线的工艺特征、装置投资和生产成本。指出环氧乙烷羰基化法原料易得、成本较低 ,但技术难度高、设备投资大 ;丙烯醛水合加氢法成本略高 ,但反应条件缓和、技术开发相对容易 ,且拥有丙烯醛生产技术和基础 ;微生物发酵法反应条件温和、原料价廉易得、成本低 ,但距离工业化还有一定差距。 相似文献
13.
一氧化碳对乙烯工业的影响 总被引:1,自引:0,他引:1
文章论述乙烯联合装置中一氧化碳(CO)的产生过程和控制方法、Co对乙烯装置、汽油加氢装置、聚内烯装置和全密度聚乙烯的影响、Co在乙烯联合装置的脱除方法以及Co变化对碳二加氢系统、甲烷化系统的操作方法. 相似文献
14.
Three reactions, CO hydrogenation, metathesis of C2H4 and CO hydrogenation in the presence of C2H4, have been investigated on Mo(+2)/Al2O3 under identical experimental conditions. The products of hydrogenation reactions were methane, ethylene and propylene. The results show that the initial rate of propylene formation for CO hydrogenation in the presence of ethylene is much larger, by a factor of 7, than the sum of the rate of propylene formation for CO hydrogenation and metathesis alone. Furthermore, it was found that13C labelled propylene was formed in the hydrogenation of13CO in the presence of ethylene. These results, taken as a whole, suggest that the same intermediate is formed in both CO hydrogenation and metathesis of ethylene, and that these intermediates can be either incorporated into ethylene and higher hydrocarbons by polymerization or incorporated into ethylene to form propylene via olefin metathesis. 相似文献
15.
Nanosized ethylene–propylene rubber (EPM) latex with a particle size of 47 nm was synthesized via an alternative route consisting of isoprene (IP) polymerization followed by hydrogenation. First, the IP monomer was polymerized by differential microemulsion polymerization to obtain polyisoprene (PIP) rubber latex with a particle size of 42 nm. The structure of synthetic PIP was hydrogenated at the carbon–carbon double bonds to produce an ethylene–propylene copolymer by diimide reduction in the presence of hydrazine and hydrogen peroxide using boric acid as promotor. The degree of hydrogenation was determined by proton nuclear magnetic resonance (1H‐NMR) spectroscopy and the structure of the ethylene–propylene copolymer was identified by 13C‐NMR spectroscopy. In nanosized PIP hydrogenation, the hydrogenation level was found to be increased by boric acid addition. An EPM yield of 94% was achieved using a hydrogen peroxide : hydrazine ratio of 1.5 : 1. The EPM produced from PIP has high thermal stability with the maximum decomposition temperature of 510°C and a glass transition temperature of ‐42.4°C close to commercial ethylene–propylene diene rubber. Dynamic mechanical analysis indicated that EPM had a maximum storage modulus due to the saturated carbons domains of the ethylene segments in the polymer chains. © 2012 Wiley Periodicals, Inc. J. Appl. Polym. Sci., 2013 相似文献
16.
Kitikorn Charmondusit Pattarapan Prasassarakich Neil T. McManus Garry L. Rempel 《应用聚合物科学杂志》2003,89(1):142-152
The quantitative hydrogenation of cis‐1,4‐poly(isoprene) (CPIP) provides an easy entry to the alternating copolymer of ethylene–propylene, which is difficult to prepare by conventional polymerization. The homogeneous hydrogenation of CPIP, in the presence of OsHCl(CO)(O2)(PCy3)2 as catalyst, has been studied by monitoring the amount of hydrogen consumed during the reaction. The final degree of olefin conversion measured by computer‐controlled gas uptake apparatus was confirmed by infrared spectroscopy and 1H nuclear magnetic resonance analysis. Kinetic experiments for CPIP hydrogenation in toluene solvent indicate that the hydrogenation rate is first order with respect to catalyst and carbon–carbon double bond concentration. A second‐order dependence on hydrogen concentration for low values and a zero‐order dependence for higher values of the hydrogen concentration was observed. The apparent activation energy for the hydrogenation of CPIP over the temperature range of 115–140°C was 109.3 kJ/mole. Mechanistic aspects of this catalytic process are discussed. © 2003 Wiley Periodicals, Inc. J Appl Polym Sci 89: 142–152, 2003 相似文献
17.
我国作为煤炭大国,燃烧化石燃料产生大量CO2。通过化学作用将CO2转化为能源燃料、基础化学品或高分子材料,有利于实现碳氧资源综合利用。从CO2直接利用和间接利用的角度出发,分别综述了CO2资源化利用研究进展。直接利用方面,重点阐述了CO2直接加氢合成甲醇和乙醇;同时CO2可作为羰化剂合成有机碳酸酯和高分子材料,包括碳酸二乙酯、聚碳酸酯和CO2基可降解聚合物。在间接利用方面,重点综述了CO2经碳酸乙烯酯的酯交换反应合成碳酸二甲酯,以及碳酸乙烯酯加氢制备甲醇联产乙二醇的研究进展。CO2加氢直接合成甲醇催化剂主要包括铜基催化剂、贵金属催化剂,由于贵金属的成本高,廉价的Cu基催化剂研究较为广泛。CO2加氢直接合成乙醇研究较广泛的催化剂为贵金属(Rh、Pd、Ru)基催化剂体系,还需进一步研究廉价、高活性和高稳定性的催化剂。CO2与乙醇直接合成碳酸二乙酯(DEC)研究较多的催化剂为铈基多相催化剂,但由于生成物中水分的影响,限制了DEC的收率。环氧化物和CO2耦合反应生成DEC过程中不产生水,可以有效克服热力学的限制,因此高能化合物与CO2的耦合路线是高效制备DEC的有效途径。CO2与环氧化物共聚制备聚碳酸酯材料多采用稀土三元催化剂体系,环氧化物的转化率和聚碳酸酯选择性较高,目前已经实现工业应用。CO2通过碳酸乙烯酯与甲醇酯交换合成DMC,多使用碱性较强的催化剂和含碱性基团的离子交换树脂。CO2经碳酸乙烯酯加氢制备甲醇和乙二醇的反应中,铜基催化剂展现出优异的催化性能。CO2化学转化利用是CO2碳氧资源综合利用的重要途径,将有效支撑我国未来碳中和目标实现。 相似文献
18.
The addition of promoters to rhodium catalysts has been studied for CO hydrogenation. Differences in temperature programmed desorption and reaction show that the support and promoter have an influence on the dissociation of carbon monoxide. A low temperature methane peak appears at 110°C in the CO temperature programmed hydrogenation on the unpromoted catalyst. The mechanistic implications of these results are discussed. 相似文献
19.
20.
A series of telechelic additives with molecular weights of 500–1500 for polyolefins was prepared by reaction of telechelic polyolefins with amino-, carboxy-and aldehyde end groups were obtained by hydrogenation of the corresponding telechelic polybutadienes which were prepared by radical polymerization of butadiene with appropriate functional initiators as well as by anionic polymerization of butadiene and termination with carbon dioxide, ethylene oxide and chloroacetaldehyde dimethyl acetal. Oligomeric polyolefins with stabilizer end groups attached by non-hydrolyzable C C-bonds were obtained by end-capping of living polybutadiene with appropriate functional additive components and subsequent hydrogenation. Preliminary tests of some of the telechelic additives demonstrated excellent compatibility with polypropylene and efficiencies similar to low-molecular standard additives. 相似文献