Catalytic dehydrogenation of ethylbenzene is an important method for production of styrene.
乙苯催化脫氫是生產(chǎn)苯乙烯的主要方法.
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Methanol dehydrogenation is a promising route for commercial production of anhydrous formaldehyde.
甲醇直接脫氫制無水甲醛是具有工業(yè)化前景的新工藝.
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The key for isobutane dehydrogenation is to synthesize non - noble mental catalysts.
詳細總結(jié)了不同載體和助劑對脫氫反應(yīng)的影響,尤其是載體和助劑的酸堿性以及載體的孔結(jié)構(gòu).
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Advances in ethane dehydrogenation to ethene have been reviewed.
乙烷脫氫制乙烯是乙烷利用的有效途徑.
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First, the nature of dehydrogenation of ethylbenzene to styrene was studied in an experilmen - tal adiabatic reactor.
針對乙苯脫氫絕熱反應(yīng)器工程特點建立了有關(guān)轉(zhuǎn)化率和選擇性的數(shù)學模型.
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The kinetics of dehydrogenation of 2 - butanol to butanone on Ni Ultrafine particle catalyst has been studied.
本文研究了鎳超細粒子催化2-丁醇液相脫氫反應(yīng)的動力學.
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The applications of metal membranes and metal composite membranes to hydrogenation and dehydrogenation reaction are introduced.
本文介紹了金屬膜和金屬復合膜在加氫和脫氫反應(yīng)中的應(yīng)用及金屬復合膜的常用制備方法和發(fā)展趨勢.
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The research progress in catechol synthesis by dehydrogenation of 1, 2 cyclohehanediol were reviewed.
綜述了1, 2環(huán)己二醇催化脫氫制取鄰苯二酚的研究進展.
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A mathematical model was established for catalytic dehydrogenation of butane in plug flow membrane reactor.
建立了模擬真實實驗室膜反應(yīng)器的數(shù)學模型:活塞流數(shù)學模型.
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In this paper. the dehydrogenation activities of Secondary Alcohol over Ni - ultrafine particle catalyst has been studied.
本文研究了鎳超細粒子催化劑對二級醇液相脫氫反應(yīng)的催化性能.
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In - situ thermal degrdn. of a com. dehydrogenation catalyst in a fixed - bed reactor is studied exptl.
用實驗研究了在固定床式反應(yīng)器中一種普通脫氫用催化劑的實時熱降解.
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The mechanism of dehydrogenation of secondary butanol and the catalyst characteristics and regeneration steps were introduced.
簡單地介紹了仲丁醇脫氫反應(yīng)的機理、催化劑的特點和催化劑的再生步驟.
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The catalytic dehydrogenation of ethylbenzene to styrene in zeolite membrane reactors was studies.
采用管式沸石膜反應(yīng)器,研究了乙苯脫氫反應(yīng)生成苯乙烯的性能.
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The catalytic systems and their main results of propane oxidative dehydrogenation to propylene are reviewed.
綜述了丙烷氧化脫氫制丙烯反應(yīng)催化劑體系及其主要研究結(jié)果.
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