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      reaction
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  反应
    A Study on Hydrogen Transfer Reaction over Catalytic Materials Used in FCC Process
    FCC催化材料上的氢转移反应研究
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    MATHEMATICAL MODELLING OF COAL-WATER SLURRY GASIFICATION-CALCULATION OF THE EQUILIBRIUM COMPOSITION FOR A COMPLEX REACTION SYSTEM
    煤浆气化过程数学模型的探讨——复杂反应系统平衡组成的计算
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    A Preliminary Study of Condensation Reaction in the “K-Method”
    “K—法”中缩合反应过程的初步探讨
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    REACTION RATES OF TNT/RDX(35/65)explosive
    梯恩梯/黑索今(35/65)炸药的反应速率函数
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    The Introduction of the Reaction Network of Oil Refining Catalytics Process and the Lumped Kinetics Model
    炼油催化过程反应网络及集总动力学模型
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  化学反应
    REACTION OF SOLID PROPELLANTS UNDER SHOCK LOADING
    固体推进剂在冲击波作用下化学反应过程的研究
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    The apparent activation energy of chemical reaction and corresponding frequency factor are 19.11kJ/mol and 8.01×102 m/s,respectively.
    表观化学反应速率常数的指前因子为8.01×10-2m/s,活化能为19.11 kJ/mol;
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    The chemical reaction time of TNT explosive detonating of experiment No. 1~4 was 0.11 μs, 0.12 μs,0.16 μs and 0.15 μs,respectively.
    四发实验得到TNT炸药爆炸的化学反应时间分别为0.11μs、0.12μs、0.16μs和0.15μs。
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    The ignition and growth model by Lee-Tarver is used to the chemistry reaction law of explosives.
    炸药的化学反应率采用Lee-Tarver的点火成长模型,假设在化学反应区里由未反应炸药与反应产物组成的混合物质:1)具有体积可加性;
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    STUDY OF EFFECTS OF DIFFERENT CHEMICAL REACTION MECHANISMS ON COMPUTATION RESULTS FOR METHANE JET TURBULENCE DIFFUSION FLAME
    不同化学反应机理对甲烷射流湍流扩散火焰计算结果影响的研究
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  “reaction”译为未确定词的双语例句
    AN ANION-VACANCY EXPLANATION FOR THE MECHANISM OF THERMAL EXPLOSION REACTION OF α-Pb(N_3)_2
    α-Pb(N_3)_2热起爆阴离子空位机理
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    THE CROSS ACTION BETWEEN BURNING RATE AND CURING REACTION CATALYSTS
    燃速催化剂与固化催化剂的交叉作用
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    An Investigation into Char Combustion Reaction under Pressure
    加压煤焦燃烧过程的研究
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    REACTION KINETICS AND SURFACE VARIATION OF MACERAL CHARS IN CO_2 GASIFICATION
    显微组分焦样的CO_2气化动力学和表面变化
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    PERFORMANCE OF CETANE NUMBER IMPROVER NT-11 AND ITS REACTION MECHANISM
    NT-11柴油十六烷值增进剂的添加性能及作用机理
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  reaction
       Several 1-(substituted phenoxy)-3-{[4-(4-trifluoromethyl) phenoxy] piperidin-1-yl} propan-2-ols (str.II) were prepared in a six-step reaction sequence starting from methylamine and ethyl acrylate and evaluated for antidepressant activity.
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       Substituents at the 4th and 5th positions of the target thiazoles were introduced by a Hantzsch reaction, and the chain at the second position was extended through a Sandmeyer reaction, formylation, and Wittig olefination.
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       A series of ortho- meta- and para-N9-[(chloromethylphenyl)methyl]chloropurines 4-12 and N7-[(chloromethylphenyl)methyl]chloropurines 13-21 were obtained by the reaction of various substituted chloropurines with α,α'-dichloroxylenes.
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       A series of 1-[(sub)]-6-fluoro-3- [(sub)]-1, 3, 4-oxadiazol-2-yl-7-piperazino-1, 4-dihydro 4-quinolinones were synthesized by the reaction between ciprofloxacin and norfloxacin with an appropriate acid hydrazide in phosphorous oxychloride.
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       The pyrazolo[4,3-d]oxazinone 4 was obtained from direct reaction of the acid 1 with hydroxylamine hydrochloride.
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         The following vector equations express the steady-state heat balance, material balance and rate of chemical reaction in a fixed bed reactor: div(C_pρT)=div(K grad T)+γ△H div(C)=div(E_1 gard C)+γ γ=bf(C)e~(-E/RT). A direct-current electric analog method is developed for the design of fixed bed catalytic reactors.. The following circumstances have been used-to test the present method: (1) Neglect the effect of mass transfer and assume γ△H=constant; (2) Neglect the effect of mass transfer and assume γ△H=...
            在穩定狀態下,固定床接觸反應器內的傳熱、傳質和化學反應的過程可用下列微分方程式來表示: div(C_pρT)=div(K grad T)+γΔH div(C)=div(E_ grad C)+γγ=bf(C)e~(-E/(RT))。作者應用直流電模擬法解以下四種情况: (ⅰ)不考慮傳質,並假設γΔH=q_0,即反應速率與溫度和作用物濃度無關; (ⅱ)不考慮傳質,假設γΔH=q_0+α_0T; (ⅲ)不考慮傳質,假設γΔH=Ae~(-E/(RT)); (ⅳ)考慮傳質和溫度及濃度對反應速率的影響;並採用了Wilhelm的傳質數據(Et),作者,Argo和Smith的傳熱數據(Ke),Smith的SO_2氧化成SO_3的動力學數據。由(ⅰ)、(ⅱ)求得的溫度分佈和文獻上發表的理論解進行了比較,由(ⅳ)求得的溫度分佈和濃度分佈與Smith等實驗測定的數據進行了比較,結果基本上是一致的。
文摘来源
         In order to investigate the effect of operating variabls on the yield of aromatics,a certain fraction of a straight run gasoline containing 48.4% (wt.)naphthenes was catalytically converted into aromatics over a bed of 100 ml 14—20 mesh,granular,platforming catalyst under various opera- ting conditions.The ranges of these investigations were:temperature 430— 510℃,pressure 20—50 atm.,WHSV 1.58—6.32 and hydrogen-oil molar ratio 4:1—10:1.The single pass fresh hydrogen process was adopted. The result of data tr...
            用直馏汽油的某一馏分在装有100毫升14—20筛眼颗粒形铂重整催化剂的反应设备中,进行单程纯氢操作的铂重整反应条件试验以考察芳烃的生成与反应条件变化的关系.试验的反应条件为:溫度430—510°压力20—50大气压,空间流速1.58—6.32重量/重量/小时,氢油分子比4:1—10:1.处理所获试验数据的结果,发现芳烃生成速度γ可用下列二次反应式来关连:
文摘来源
         The possibility of using granular nitrided fused iron catalyst for Fischer-Tropsch synthesis at high space velocities is investigated. It is observed that the activity of granular catalyst decreases seriously with time when used at low reaction temperatures,while the use of relatively high reaction temperatures stimulates carbon formation on the catalyst,resulting in the clogging up of the reactor.These phenomena differ from what occurs on a powdered catalyst. The effect of the operating variabl...
            为进行高速固定床以水煤气为原料的合成,研究了颗粒熔铁催化剂.发现随颗粒加大,在低温和压力下合成时活性无法维持;在高温合成时,则又发现生炭粉碎而很快使床层堵塞.为了使催化剂维持足够的寿命,设法消除低温合成过程中的障碍是重要研究方向之一.试验了温度、压力、空速、再生方法和不同催化剂组成及不同成型方法等对活性维持的影响,认为:在高空速下,氮化熔铁颗粒催化剂活性随时间下降主要是由于生成的重质产物堵塞了颗粒孔隙所引起;在颗粒孔隙堵塞同时,反应速度控制步骤由原为化学反应速度控制转为内扩散控制的慢反应.从而指明,解决熔铁剂活性维持问题的关键在于改善孔隙结构.
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