共查询到20条相似文献,搜索用时 203 毫秒
1.
研究了以HY分子筛为催化剂合成对乙酰氨基酚的工艺,对反应物的物质的量比、反应温度、反应时间、催化剂用量等反应条件进行了优化,实验确定最佳反应条件:对氨基苯酚与冰乙酸物质的量比为1∶10,反应温度为120℃,催化剂用量为1.5%,反应时间为5h。最佳条件下对乙酰氨基酚的收率可达92.05%,且实验证明HY分子筛催化活性具有良好的稳定性。 相似文献
2.
相转移催化法合成苯乙腈 总被引:2,自引:0,他引:2
采用相转移催化法对合成苯乙腈工艺进行改进,降低了反应温度,缩短了反应时间,最佳反应条件为氯苄:氰化钠=1:1.05,反应温度约为95℃,反应时间大约1.5h,所得苯乙腈收率可达97.7%,相转移催化剂DTC-2^#用量为1%。 相似文献
3.
采用吡啶为催化剂氯化亚砜与异丁醇反应合成氯代异丁烷,探讨了合成反应条件对氯代异丁烷收率的影响。在氯化亚砜:异丁醇=1.25:1(物质的量比),反应温度70℃,催化剂浓度3.13%,反应时间4h的优化工艺条件下,氯代异丁烷的收率为65.7%。 相似文献
4.
5.
本文以对硝基甲苯为原料经还原、磺化二步反应合成邻氨基间甲苯磺酸。通过正交试验确定最佳工艺条件的磺化温度175℃、硫酸与对甲苯胺的物质的量比为1.1:1,活性炭用量3g,分出反应生成的水,在优化条件下,磺化收率为93.7%,产品含量达98%。 相似文献
6.
7.
影响环氧树脂604软化点和色泽的因素 总被引:1,自引:0,他引:1
介绍了环氧树脂604的合成过程,确定了最佳工艺条件:双酚A:环氧氯丙烷:氢氧化钠(摩尔比)为1.000:1.214:1.214,先在85~90℃反应1h,再在90~95℃反应1h;并对影响产品软化点和色泽的因素进行了探讨。 相似文献
8.
进行了乙酸和正丁醇在Al2O3·TiO2·ZnO·CuSO4/高岭土固体酸催化剂上合成乙酸正丁酯的气固相反应,试验了催化剂用量、醇/酸摩尔比、反应温度和反应时间等工艺条件对催化剂性能的影响,得到较佳的工艺条件为:催化剂用量0.9-1.0g/mol乙酸,醇/酸摩尔比1.1-1.2,反应温度130℃-140℃和反应时间4-6h。在此条件下酯化率97%和选择性100%。 相似文献
9.
棉油酸经氯化-酯化-蒸馏制得氯化棉油酸甲酯。采用正交实验法筛选出了此工艺的最佳工艺条件。棉油酸氯化最佳工艺条件:反应时间为3.5h,催化剂用量为棉油酸重量的0.3%,反应温度为70℃,通氯量(氯气与棉油酸的摩尔比)为20:1。氯化棉油酸甲酯化最佳工艺条件:反应温度为180℃,催化剂用量为氯化棉油酸质量的2%,甲醉:氯化棉油酸=1:2.0(mol),反应时间为4h。在此条件下进行平行试验,精酯收率均在80%以上。 相似文献
10.
丁二酮制备新工艺研究 总被引:3,自引:0,他引:3
叙述了异丁醛气相氧化制备丁二酮的一种新工艺,对气相氧化反应条件进行了试验研究,其适宜的工艺条件为:反应温度为200℃,氧醛物质的量比为1.05,空速为1150h^-1,异丁醛体积分数为10%,产品总收率的28%。 相似文献
11.
乙烯酮(双乙烯酮)是十分重要的化工中间体,其下游产品较多。江苏某化工厂开发生产乙烯酮(双乙烯酮)下游产品三十多个,年生产规模三万多吨,是国内以乙烯酮(双乙烯酮)为中间体生产精细化学品的综合骨干企业。针对乙烯酮(双乙烯酮)下游产品废水特点,该厂结合企业实际,开展了产品优化,结构调整,清洁生产,资源循环利用,节水降耗等工作,从源头削减了污染物的生产。同时投资二千多万元新建预处理装置三套,6000m3/d废水生化处理装置一套,使全厂乙烯酮(双乙烯酮)下游产品的废水得到了有效的治理。 相似文献
12.
D. G. Gordeev L. F. Gudarenko M. V. Zhernokletov V. G. Kudel’kin M. A. Mochalov 《Combustion, Explosion, and Shock Waves》2008,44(2):177-189
A semi-empirical equation of state for metals is described. Its capabilities are demonstrated by the example of the equation
of state for aluminum. New experimental data are presented on the location of the isentrope of aluminum for unloading from
the state at p = 229.71 GPa on the shock adiabat to an aerogel (SiO2) of density 0.08 g/cm3.
__________
Translated from Fizika Goreniya i Vzryva, Vol. 44, No. 2, pp. 61–75, March–April, 2008. 相似文献
14.
15.
16.
Jorge Marcelo Romero Soledad Bustillo Hugo Enrique Ramirez Maisuls Nelly Lidia Jorge Manuel Eduardo Gómez Vara Eduardo Alberto Castro Alicia H. Jubert 《International journal of molecular sciences》2007,8(7):688-694
A thermochemical rather simple experimental technique is applied to determine the enthalpy of formation of Diperoxide of ciclohexanone. The study is complemented with suitable theoretical calculations at the semiempirical and ab initio levels. A particular satisfactory agreement between both ways is found for the ab initio calculation at the 6–311G basis This set level. Some possible extensions of the present procedure are pointed out. 相似文献
17.
18.
19.
A perturbation viscometer is a differential capillary viscometer that measures the logarithmic viscosity gradient of the viscosity-composition curve for gas mixtures. Measurements are made at different gas mixture compositions. Integration of the logarithmic viscosity gradients measured over the full composition range gives the mixture viscosity relative to the viscosity of one of the pure components of the gas mixture. This method is attractive because, for measurements of equal precision, integration of the gradients is potentially an order of magnitude more precise than measurement of the viscosities directly. It can also work at high and low temperatures and perhaps high pressures.The perturbation viscometer has been used to make measurements on ideal gas mixtures at ambient and elevated temperatures. The situation is more complicated when the gas mixtures are non-ideal. Extra effects due to density differences, molar volume change on mixing and differential thermal expansion may be measured in addition to the desired viscosity change producing systematic errors in the results. Thus, a more sophisticated apparatus is required. The standard perturbation viscometer has been modified to separate out the extra effects to permit measurement of the true change in viscosity. In addition, the theoretical operation of the modified apparatus has been revised to account for the design changes to permit calculation of the viscosity-composition profiles from the results.The apparatus has been tested using helium-HFC-125 mixtures and two new viscosity-composition profiles are presented for these mixtures at 23 and . Internal consistency tests have been used to confirm that the data produced are of high quality with an estimated uncertainty in the viscosity ratio data at of 0.9% and at of 1.5%. 相似文献
20.
塔设备改造选型的分析 总被引:2,自引:0,他引:2
就当前扩产增容中塔设备设计和改造时板式塔和填料塔的选型问题加以分析。在评述目前国内常用的几种塔板和新型填料之后,着重介绍一种新型塔板(导向梯形浮阀塔板)和一种新型填料(波环填料——乾隆帕克)。 相似文献