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因此,通过异丁烷脱氢扩大异丁烯的来源是必要的。Therefore, it is necessary to extend the resource of isobutene by dehydrogenation of butanes.
甲醇和异丁烯反应生产甲基叔丁基醚是目前最主要的工业化生产方法。The synthesis route from methanol and isobutene was the most important industrial production methods.
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首先通过机理分析建立了齐聚反应动力学模型。The discussion on the mechanics indicated that the oligomerization reaction model of isobutene was reasonable.
本文综述了近年来MTBE裂解制备高纯异丁烯催化剂的新进展。The latest research progress on the catalysts used in the cracking reaction of MTBE to produce isobutene was reviewed.
由异丁烯二聚物与苯酚合成的辛基酚是制造橡胶工业的硫化促进剂所必需的原料。The octylphenoi synthesized from dimer of isobutene and phenol is indispensable to the vulcanizing agents in rubber industry.
研究了硫化异丁烯的绿色合成方法,降低了碱性含硫废水排放。A green synthesis method of sulphide isobutene was investigated to reduce discharge of alkaline sulphide waste water in this paper.
异丁烯的需求量始终在增长,它不但可用于制汽油和润滑油的添加剂,而且还可用作其它精细化工产品的原料。The demand isobutene is still increasing, it can be used not only in producing additive of gasoline and lubricant, but also as raw material for other speciality chemicals.
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在半连续浆态搅拌釜中,使用NKC-9离子交换树脂细粉作为催化剂,考察了颗粒粒径对异丁烯水合反应速率的影响。The effect of particle size on reaction rate of isobutene hydration was investigated in the slurry semibatch agitated reactor with fine powder of NKC-9 ion exchange resin.
通过考察反应温度、反应时间、催化剂用量、原料配比等因素对烷基化反应的影响,确定了苯与丙烯及异丁烷与丁烯烷基化反应的适宜工艺条件。By investigating the temperature, reaction time, amount of the ionic liquid, ratio of benzene to propylene or isobutene to butene, the better processing conditions were ascertained.
本文综述了国内外叔丁胺的生产工艺和催化合成方法的研究进展,重点介绍了叔丁胺清洁生产工艺异丁烯催化氨化法合成技术进展。The advances in the technologies and catalytic synthesis methods for tert-butylamine were summarized. The green process-the catalytic amination of isobutene process are introduced emphatically.
采用内标法,利用填充柱测定了由异丁烯和一氧化碳经加压催化合成三甲基乙酸工艺的合成液中的三甲基乙酸。Using internal standard method, the content of trimethylacetic acid in its synthetic fluid prepared by pressure catalytic process from isobutene and carbon monoxide was measured with packed column.
小规模装置多采用间歇搅拌釜式反应器,但存在着单位反应器容积生产能力低,异丁烯单耗高的缺陷。The batch stirring tank reactor is usually employed in the small scale production unit, but there are some shorttcomes, such as low productivity of unit reactor volume and high isobutene consumption.