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苯系硝化工艺危险性分析与安全设施设计研究 被引量:2
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作者 靳松 《河南科技》 2020年第22期110-112,共3页
本文以一硝基苯系物生产为例,结合工业化生产实践,分析了苯系硝化工艺的危险点,并对照其危险特点,在连续化工艺、自动化设计基础、进料控制、安全仪表系统、紧急冷却系统、危险废物、精馏、设备防腐蚀、建筑等9个方面提出了安全设施设... 本文以一硝基苯系物生产为例,结合工业化生产实践,分析了苯系硝化工艺的危险点,并对照其危险特点,在连续化工艺、自动化设计基础、进料控制、安全仪表系统、紧急冷却系统、危险废物、精馏、设备防腐蚀、建筑等9个方面提出了安全设施设计要点,以期为苯系硝化工艺的工程设计提供参考。 展开更多
关键词 苯系硝化 安全设施 连续化工艺 设备防腐蚀
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苯系硝化工艺危险性分析与安全设施设计方法初探
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作者 杜胜 《化工管理》 2021年第21期115-116,共2页
在化学工艺产品的生产过程中,很多危险的化学产品由于自身特有的性质,比如易燃易爆、带有一定的腐蚀性、并且很多的化学产品具有有毒的性质,所以会引发一些危险的事故,在这样的化工企业中是频发的。苯硝在其生产的过程中,本身具有很强... 在化学工艺产品的生产过程中,很多危险的化学产品由于自身特有的性质,比如易燃易爆、带有一定的腐蚀性、并且很多的化学产品具有有毒的性质,所以会引发一些危险的事故,在这样的化工企业中是频发的。苯硝在其生产的过程中,本身具有很强的毒性,涉及到的危险物品种类是非常多的,因此,在苯硝的实际生产过程中,不管工厂规模的大小,对必须对其安全性进行合理有效的保证。所以在生产过程中,需要及时了解并认识到其危害性,合理有效的规避潜在的危险。所以需要及时对苯系硝化的整个过程中存在的危险因素进行深入地探析。 展开更多
关键词 苯系硝化工艺 危险性 安全设施
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A Highly Efficient and Selective Water-Soluble Bimetallic Catalyst for Hydrogenation of Chloronitrobenzene to Chloroaniline 被引量:1
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作者 Zhou Yafen Yang Wenjuan +2 位作者 Zhou Limei Wang Manman Ma Xiaoyan 《China Petroleum Processing & Petrochemical Technology》 SCIE CAS 2015年第2期26-31,共6页
Selective hydrogenation of chloronitrobenzene(CNB) to chloroaniline(CAN) catalyzed by water-soluble Ru/Pt bimetallic catalyst in an aqueous-organic biphasic system was studied. It was found that the catalytic activity... Selective hydrogenation of chloronitrobenzene(CNB) to chloroaniline(CAN) catalyzed by water-soluble Ru/Pt bimetallic catalyst in an aqueous-organic biphasic system was studied. It was found that the catalytic activity increased obviously due to the addition of platinum. Ru/Pt bimetallic catalysts exhibited a strong synergistic effect when the molar ratio of Pt was in the range of 5%—80%. Under the mild conditions including a temperature of 25 ℃, a hydrogen pressure of 1.0 MPa and a Pt molar ratio of 20%, the conversion of p-chloronitrobenzene(p-CNB) reached 99.9%, with the selectivity to p-chloroaniline(p-CAN) equating to 99.4%. The Ru/Pt catalyst also showed high activity and selectivity for the hydrogenation of other chloro- and dichloro-nitrobenzenes with different substituted positions. In addition, the catalyst can be recycled five times without significant loss of activity. 展开更多
关键词 water-soluble bimetallic catalyst HYDROGENATION CHLORONITROBENZENE CHLOROANILINE
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Synthesis of 2-Methyl-4-methoxyaniline from o-Nitrotoluene Using Pt/C and Acidic Ionic Liquid as Catalyst System
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作者 LIU Yingxin LI Xiying FANG Yanyan ZHANG Lin 《Chinese Journal of Chemical Engineering》 SCIE EI CAS CSCD 2013年第6期701-704,共4页
2-Methyl-4-methoxyaniline (MMA) was synthesized by one-pot method through the hydrogenation and Bamberger rearrangement of o-nitrotoluene in methanol using acidic ionic liquid and 3% Pt/C as catalyst system. The eff... 2-Methyl-4-methoxyaniline (MMA) was synthesized by one-pot method through the hydrogenation and Bamberger rearrangement of o-nitrotoluene in methanol using acidic ionic liquid and 3% Pt/C as catalyst system. The effects of ionic liquid type, dosage of ionic liquid and 3% Pt/C, reaction temperature and reaction pressure on o-nitrotoluene conversion and MMA selectivity were investigated. The results indicated that the imidazolium-based acidic ionic liquid which contains SO3H-functionalized cation showed higher selectivity to MMA than other acidic ionic liquids used in this work. Using 1-(propyl-3-sulfonate)-3-methylimidazolium hydrosulfate ([HSO3-pmim][HSO4]) as the acid catalyst, the selectivity to MMA was as high as 67.6% at 97.8% of o-nitrotoluene conversion. As 3% Pt/C increased from 0.01 g to 0.025 g, the selectivity to MMA decreased from 73.4% to 62.5%, because of the hydrogenation of intermediate o-methyl-phenylhydroxylamine to o-toluidine becoming more dominant. An increase in hydrogen pressure also had obviously dramatic effect in lowering the MMA selectivity. After easy separation from the products, the catalyst system could be reused at least 3 times. 展开更多
关键词 acidic ionic liquid Bamberger rearrangement 2-methyl-4-methoxyaniline O-NITROTOLUENE hydrogenation
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