共查询到20条相似文献,搜索用时 93 毫秒
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针对某炼厂的原油,采用电脱盐试验装置开展了原油脱钙技术研究,对脱钙剂进行筛选和复配。实验结果表明:在电脱盐温度145℃、电压1 800 V、注水量8%,混合强度为手工振荡400次,破乳剂DM添加量为25μg/g,复配的脱钙剂“乙二胺四乙酸二钠+马来酸酐”(“EDTA-2Na+MA”)添加量为100μg/g的优化工艺条件下,原油经过脱钙处理后,其钙含量可降低至1.2μg/g,脱钙率高达99%,铁含量可降低至4.0μg/g,脱铁率高达92%。通过“电脱盐+脱钙剂”的组合工艺,可有效地脱除原油中的钙、铁等金属含量,减轻了金属杂质对后续装置的不利影响。 相似文献
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随着原油开采程度的逐步加深及掺炼原油趋于劣质化,原油中的金属杂质含量也越来越高。为了解决钙、镁等金属杂质对原油加工过程中带来的危害,本装置通过在电脱盐注水系统上加注脱钙剂,使其在原油与注水相互混合的过程中,将原油中的金属杂质脱除。经过两次脱钙剂实验得出,脱钙剂对原油脱金属效果较明显,脱除率在40%左右,适用于原油脱金属。 相似文献
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采用(NH4)2S2O8为氧化剂,对烧结脱硫灰中CaSO3进行催化氧化研究,研究氧化剂的量、催化剂种类、反应时间、反应温度及(NH4)2SO4的添加量等因素对亚硫酸钙的转化率的影响。实验结果表明,CuSO4催化效果最佳;反应温度越高,CaSO3的氧化率越高;少量(NH4)2SO4明显增加CaSO3的氧化率。当CaSO3与(NH4)2S2O8物质量比为20∶1时,加入的(NH4)2SO4占脱硫灰重量0.2%,以CuSO4作为催化剂,40℃中反应1 h,CaSO3的氧化率达到50%以上。 相似文献
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朱玲;张佳亮;石英;王瑞 《化工中间体》2013,(12):15-18
本文选取了两种脱钙剂:原油脱金属剂A、稠油金属脱除剂B,在原油中分别加入两种脱钙剂,通过对比加入前后钙含量的变化,将两种脱钙剂的脱钙性能进行评价。由于原油脱金属剂A、稠油金属脱除剂B都呈酸性,模拟常减压破乳剂罐的工艺条件和电脱盐罐的工艺条件,测试药剂的腐蚀速度。 相似文献
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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
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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.
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Translated from Fizika Goreniya i Vzryva, Vol. 44, No. 2, pp. 61–75, March–April, 2008. 相似文献
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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
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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
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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