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烷基化装置工艺技术选择 被引量:3
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作者 谢辉 《化工管理》 2017年第1期180-181,共2页
随着国内对汽油等成品油质量标准不断提高,以及环境保护要求日益严格,烷基化油的重要性也日益突出。本文介绍了烷基化油的市场前景,传统液体烷基化技术和固体酸法烷基化技术特点,并在技术可靠性、投资、运行成本、流程和操作复杂性、安... 随着国内对汽油等成品油质量标准不断提高,以及环境保护要求日益严格,烷基化油的重要性也日益突出。本文介绍了烷基化油的市场前景,传统液体烷基化技术和固体酸法烷基化技术特点,并在技术可靠性、投资、运行成本、流程和操作复杂性、安全环保等方面进行对比。 展开更多
关键词 烷基化油 氢氟 固体酸法 烷基化技术
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烷基化装置产能及技术进展 被引量:5
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作者 张英杰 王冬梅 +1 位作者 李学 王美淇 《炼油与化工》 2020年第3期1-3,共3页
文中介绍了国内外烷基化产能分布情况,对比了烷基化4种不同技术路线,详细介绍了氢氟酸法、硫酸法、固体酸法、离子液体法烷基化技术和工业化情况,展望了烷基化技术的发展趋势。
关键词 烷基化 氢氟 固体酸法 离子液体
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烷基化装置工艺技术选择探析 被引量:1
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作者 冯瑞 《化工管理》 2017年第22期190-190,共1页
目前,常见的烷基化装置工艺技术有固体酸法、硫酸法、氢氟酸法等。本文基于大量的文献资料和工作经验,对固体酸法、硫酸法、氢氟酸法进行了简要分析,并从工艺流程、操作复杂性、一次性投资、安全性、环保性、运行成本、技术可靠性等方... 目前,常见的烷基化装置工艺技术有固体酸法、硫酸法、氢氟酸法等。本文基于大量的文献资料和工作经验,对固体酸法、硫酸法、氢氟酸法进行了简要分析,并从工艺流程、操作复杂性、一次性投资、安全性、环保性、运行成本、技术可靠性等方面对比分析了以上技术,合理选用适合的烷基化装置工艺技术。 展开更多
关键词 固体酸法 氢氟 综合对比
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煤的适应性对水煤浆加压气化的影响研究 被引量:1
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作者 高智武 张海国 刘剑 《化工管理》 2017年第22期191-191,共1页
煤的适应性直接决定了水煤浆加压气化工艺运行效果,煤的热量、灰分含量、元素、浓度及粉度等是水煤浆加压气化工艺参数的重要影响因素。本文分析了水煤浆加压气化的工艺原理及水煤浆的特性,概述了水煤浆加压技术的优缺点。
关键词 固体酸法 氢氟 综合对比
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One Step Preparation of Sulfonated Solid Catalyst and Its Effect in Esterification Reaction 被引量:2
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作者 康世民 常杰 范娟 《Chinese Journal of Chemical Engineering》 SCIE EI CAS CSCD 2014年第4期392-397,共6页
A carbon-based sulfonated catalyst was prepared by direct sulfonation and carbonization (in moderate conditions:200 &#176;C, 12 h) of red liquor solids, a by-product of paper-making process. The prepared sulfonate... A carbon-based sulfonated catalyst was prepared by direct sulfonation and carbonization (in moderate conditions:200 &#176;C, 12 h) of red liquor solids, a by-product of paper-making process. The prepared sulfonated cata-lyst (SC) had aromatic structure, composed of carbon enriched inner core, and oxygen-containing (SO3H, COOH, OH) groups enriched surface. The SO3H, COOH, OH groups amounted to 0.74 mmol·g^-1, 0.78 mmol·g^-1, 2.18 mmol·g^-1, respectively. The fresh SC showed much higher catalytic activity than that of the traditional solid acid catalysts (strong^-acid 732 cation exchange resin, hydrogen type zeolite socony mobile-five (HZSM-5), sulfated zir-conia) in esterification of oleic acid. SC was deactivated during the reactions, through the mechanisms of leaching of sulfonated species and formation of sulfonate esters. Two regeneration methods were developed, and the catalytic activity can be mostly regenerated by regeneration Method 1 and be fully regenerated by regeneration Method 2, respectively. 展开更多
关键词 red liquor solids sulfonated solid catalyst CARBONIZATION ESTERIFICATION
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A new solid acid SO_4^(2-)/TiO_2 catalyst modified with tin to synthesize 1,6-hexanediol diacrylate 被引量:8
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作者 Xiaxia Bai Liuyi Pan +2 位作者 Peng Zhao Daidi Fan Wenhong Li 《Chinese Journal of Catalysis》 SCIE EI CAS CSCD 北大核心 2016年第9期1469-1476,共8页
A new solid acid catalyst,SO4^2-/TiO2 modified with tin,was prepared using a sol-gel method and its physicochemical properties were revealed by nitrogen adsorption-desorption,X-ray powder diffraction,scanning electron... A new solid acid catalyst,SO4^2-/TiO2 modified with tin,was prepared using a sol-gel method and its physicochemical properties were revealed by nitrogen adsorption-desorption,X-ray powder diffraction,scanning electron microscopy,Fourier transform infrared spectroscopy,infrared spectroscopy of adsorbed pyridine,temperature-programmed desorption of ammonia and thermal gravimetric analysis.The structure,acidity and thermal stability of the SO4^2-/TiO2-SnO2 catalyst were studied.Incorporating tin enlarged the specific surface area and decreased crystallite size of the SO4^2-/TiO2 catalyst.The total acid sites of the modified catalyst increased and Bronsted acid strength remarkably increased with increasing tin content.The decomposition temperature of sulfate radical in the modified catalyst was 100 ℃ greater and its mass loss was more than twice that of the SO4^2-/TiO2 catalyst.The SO4^2-/TiO2-SnO2 catalyst was designed to synthesize 1,6-hexanediol diacrylate by esterification of 1,6-hexanediol with crylic acid.The yield of 1,6-hexanediol diacrylate exceeded 87% under the optimal reaction conditions:crylic acid to 1,6-hexanediol molar ratio = 3.5,catalyst loading = 7%,reaction temperature = 130 ℃ and reaction time = 3 h.The modified catalyst exhibited excellent reusability and after 10 cycles the conversion of 1,6-hexanediol was above 81%. 展开更多
关键词 Solid acid catalyst TIN Sol-gel method 1 6-Hexanediol diacrylate Esterification reaction
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抗氧剂
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《橡塑助剂信息》 2005年第5期23-24,共2页
辛基化二苯胺抗氧剂组成物;抗氧化性能优异的成模材料;耐水解、抗氧化的有机磷体系;固体酸法制备抗氧剂;抗冲击聚苯乙烯抗氧剂及其应用。
关键词 抗氧剂 成模材料 有机磷体系 苯乙烯化酚 固体酸法
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