金刚烷合成新工艺

金刚烷（Ａｄａｍａｎｔａｎｅ,简称ＡｄＨ）是一种周正对称、非常稳定的笼状烃,它在医药、功能高分子、表面活性剂、润滑剂、照相感光材料等方面具有潜在用途［１,２］,因而被誉为新一代精细化工原料。国外预言,随着金刚烷制备方法的改进及其应用领域的拓展,不久的...     

7-羟甲基-7-羟基双环[3,3,1]壬烷-3-酮的合成并转换成1-羟基-4-原金刚烷酮（英文）

３,７－二取代双环［３,３,１］壬烷衍生物具有许多有趣的反应特异性,可合成各种官能性金刚烷衍生物。本文以１－金刚烷醇为原料经二步反应合成７－亚甲基双环［３,３,１］壬烷－３－酮。再用催化量四氧化锇进行氧化几乎定量地得到７－羟甲基－７－羟基双环［３,３,１］壬烷－３－酮（９）。９用对甲苯磺酰氯处理得１１,然后转换成１－羟基－４－原金刚烷酮（８）。根据光谱数据分析,（９）有一互变异构体（１０）,研究表明１０的存在对合成８没有影响。预计８可以作为合成各种三取代金刚烷的原料。     

具有不同类型桥基的双核Cu(Ⅱ)-Schiff碱配合物的合成和晶体结构

合成了３个分别以Ｃ２Ｏ２－４（［Ｃｕ２（Ｌ１）２（ｏｘ）］，１），ＡｃＯ－（［Ｃｕ２（ＡｃＯ）（Ｌ２）２］ＢＦ４，２）和酚氧（［Ｃｕ２（Ｌ３）２］（ＣｌＯ４）２，３）为桥基的双核铜配合物，并测定了１的复配合物［Ｃｕ２（Ｌ１）２（ｏｘ）］·［Ｆｅ（ＯＨ）２（Ｈ２Ｏ）４］ＣｌＯ４·Ｈ２Ｏ（１′）及２和３的晶体结构．Ｘ射线衍射结果表明：１′，２和３分别属于Ｆｄｄｄ，Ｐ２１／ｃ和Ｐ２１／ｃ空间群．晶胞参数：［Ｃｕ２（Ｌ１）２（ｏｘ）］［Ｆｅ（ＯＨ）２（Ｈ２Ｏ）４］ＣｌＯ４·Ｈ２Ｏ，ａ＝２．４３９０（４）ｎｍ，ｂ＝３．０５３８（６）ｎｍ，ｃ＝１．８４９４（６）ｎｍ，α＝β＝γ＝９０．００°；２，ａ＝０．８４７（１）ｎｍ，ｂ＝２．６５４２（８）ｎｍ，ｃ＝１．４１００（６）ｎｍ，β＝９１．３４（６）°；３，ａ＝０．７６４６（３）ｎｍ，ｂ＝１．６９８３（３）ｎｍ，ｃ＝２．４４１７（３）ｎｍ，β＝９７．１１°     

[Ln(EO_2)_3](ClO_4)_3·3H_2O的晶体结构研究

合成了希土高氯酸盐开环冠醚二缩乙二醇（ＥＯ２）晶体，（Ｌｎ＝Ｎｄ，Ｈｏ），测定了结构，文内以Ｎｄ－Ｌ的数据为主要研究对象（方括号内是Ｈｏ－Ｌ的数据）。晶体属单斜晶系，Ｐ２１／ｎ空间群，化学式［Ｌｎ（ＥＯ２）３］（ＣｌＯ４）３·３Ｈ２Ｏ，晶胞参数为：ａ＝１４．１２４（１）［１４．０８７］，ｂ＝１３．９９０（１）［１４．０３９］，ｃ＝１５．２６５（１）［１５．０１４］；β＝９５．７８（１）［９５．６４］°；Ｖ＝３００１．１（６）［２９５５］３；Ｍｒ＝８１５．０１［８３５．７０］；Ｚ＝４；Ｄｃ＝１．８０４［１．８６５］ｇ／ｃｍ３；石墨单色器，μ（ＭｏＫα）＝２．０９［３．０７］ｍｍ－１，最终偏离因子Ｒ＝０．０５５［０．０７４］，ＲＷ＝０．０７１［０．１０９］。研究结果表明晶体具有相同的结构，配位多面体为九配位三帽三棱柱。发现ＥＯ２醚链有绕Ｃ－Ｃ键呈ＳＴＴＳ分布的规律。弱配体高氯酸根不参加配位。     

含硫、氮Schiff碱配合物—二水二分之一二甲基亚砜醋酸四邻香草醛缩胺基硫脲合镉（Ⅱ）的合成及晶体结构

Ｘ射线单晶衍射结果表明，三核镉配合物Ｃｄ３［ＣＨ３Ｏ（Ｏ）Ｃ６Ｈ３ＣＨ＝ＮＮＨＣ（Ｓ）ＮＨ２］４·［ＣＨ３ＣＯＯ］２·１／２［ＣＨ３Ｓ（Ｏ）ＣＨ３］·２Ｈ２Ｏ为单斜晶系，空间群为Ｃ２／ｃ，ａ＝３．４２１４（４），ｂ＝１．１５８１（２），ｃ＝１．７９３２（５）ｎｍ，β＝１１９．７６（１）°，Ｖ＝６．１６８ｎｍ３，Ｍｒ＝１４２７．４３，Ｚ＝４，Ｄｃ＝１．５４ｇ／ｃｍ３，μ＝１２．４８ｃｍ（－１），Ｆ（０００）＝２８６０，最后偏离因子Ｒ＝０．０６６．     

穴状Schiff碱铈配合物的合成与晶体结构

２，６－二甲酰对甲苯酚和三（２－氨乙基）胺在硝酸铈的模板作用下缩合得到单核穴状Ｓｃｈｉｆｆ碱配合物［ＣｅＮＯ３·Ｌ］（ＮＯ３）２，铈为九配位。配合物的晶体属三斜晶系，Ｐ１↑－空间群，ａ＝１．０８３３（３）ｎｍ，ｂ＝１．２６５４（４）ｎｍ，ｃ＝１．７６２６（７）ｎｍ，α＝８３．４８°（３），β＝８９．２８（３）°，γ＝８３．７０（３）°，Ｖ＝２．３８６（２）ｎｍ＾３，Ｚ＝２。     

新型金属-双二硫杂戊烯(M-BDT)配合物的合成、 表征及X射线的指标化

合成了４个新型ＮｉＢＤＴ配位化合物，ＢＤＴ为具有９个Ｓ原子的杂戊烯．元素分析、ＩＲ谱、ＵＶ谱确定这４个新配合物的化学式分别为［（ＣＨ３）４Ｎ］２［Ｎｉ（Ｃ５Ｓ９）２］（１），［（Ｃ２Ｈ５）４Ｎ］２·［Ｎｉ（Ｃ５Ｓ９）２］（２），［（Ｃ４Ｈ９）４Ｎ］２［Ｎｉ（Ｃ５Ｓ９）２］（３），［（Ｃ６Ｈ５）（ＣＨ３）３Ｎ］２［Ｎｉ（Ｃ５Ｓ９）２］（４）．采用Ｉｔｏ法对配合物１的Ｘ射线粉末图进行了指标化，确定该晶体属单斜晶系，简单晶格，晶胞参数：ａ＝０６８０ｎｍ，ｂ＝０．７１４ｎｍ，ｃ＝２．３０２ｎｍ，γ＝１１１．４°，Ｚ＝     

一经式异构体[Co(N-(3-Aminopropyl)-1,3-propanediamine)(1,2-diamino-2-methylpropane)Cl][ZnCl4]·2H2O的合成及晶体结构

用过氧化物法合成了新体系［ Ｃｏ（ ３, ３－ｔｒｉ）（ ｉｂｎ） ＣＩ］［ ＺｎＣｌ４］（ ３, ３－ｔｒｉ＝ Ｎ－（ ３－Ａｍｉｎｏｐｒｏｐｙｌ）－ １, ３－ｐｒｏｐａｎｅｄｉａ－ｍｉｎｅ; ｉｂｎ＝１, ２－ｄｉａｍｉｎｏ－２－ｍｅｔｈｙｌｐｒｏｐａｎｅ）中的一经式异构体［Ｃｏ（３, ３ｔｒｉ）（ｉｂｎ）ＣＩ］［ＺｎＣｌ４］·２Ｈ２Ｏ,解析了其晶体结构。晶体学参数：三斜晶系,空间群Ｐ１（＃２）,ａ＝９９．５８（２）ｎｍ,ｂ＝１１４．８３（２）ｎｍ,ｃ＝９８．８１（１）ｎｍ,ａ＝９６．７９（２）°,β＝９７．２４３（１０）°,ｙ＝９６．８９（１）°,Ｖ＝１．１０５５（３）Ｘ １０６ｎｍ３,Ｄｅ＝１．６７８ｇ·ｃｍ－３,Ｚ＝２,Ｆ０００＝５７２．００,μ（ Ｍｏ Ｋａ）＝ ２４． ５９ｃｍ－１, Ｒ＝ ０． ０２５, Ｒｗ＝ ０． ０３４。晶胞中含 ２个配位阳离子, ２个 ［ＺｎＣｌ４］２－阴离子及 ４个水分子。     

合成CFC-12替代物HFC-134a的CrF_3/AlF_3催化剂研究(Ⅴ)──CrF_3与AlF_3的相互作用

由于氟氯烃（ＣＦＣｓ）对大气臭氧层的破坏作用，使得开发ＣＦＣｓ无污染替代品的研究成为热门课题［１～４］．氢氟烃（ＨＦＣｓ，如ＨＦＣ－１３４ａ）是ＣＦＣｓ的理想替代物．在氟氯交换合成ＨＦＣ－１３４ａ的反应中，ＡｌＦ３基催化剂的活性、稳定性明显优于ＣｒＦ...     

铒—谷氨酸配合物的晶体结构及表征

合成了铒与Ｌ－谷氨酸形成的配合物［Ｅｒ２（Ｌ－Ｇｌｕ）２．（Ｈ２Ｏ）８］［ＣｌＯ４）４．３Ｈ２Ｏ，由元素分析、红外光谱、热分析对配合物进行了表征。得到了配合物的单晶，该晶体属于单斜晶系，空间群Ｐ２１，晶胞参数ａ＝１．９９８７（３）ｎｍ，ｂ＝１．６５０５（３）ｎｍ，ｃ＝１．１０４０（２）ｎｍ，β＝１０４．６９（１）＾ｏ，Ｖ＝３．５３８ｎｍ＾３，Ｚ＝２，Ｒ＝０．０４３。晶体结构中每一个独立区含有二个晶     

Catalytic Synthesis of Hexyl-naphthalene over H-type Zeolites

H-type zeolites（ HY, Hβ, and HM） were synthesized and characterized by XRD, NH3-TPD, and Py-IR. Selectively catalytic alkylation of naphthalene with n-hexanol to hexyl-naphthalene over the zeolites was carried out. The experimental results show that the catalytic activities of the zeolites are mainly determined by their acid properties and pore structures. The larger the pore diameter is, the higher the catalytic activity is. NH3-TPD profiles show that Hβ and HM have lower acid strengths than HY. HY has both the highest activity and highest selectivity for the hexylnaphthalene. Higher reaction temperatures and longer reaction time are beneficial to the production of β-hexyl-naphthalene over the HY zeolite.     

Synthesis of adamantane on zeolite catalysts

The synthesis of adamantane from tetrahydrodicyclopentadiene on zeolites with different framework structures was studied. The adamantane yield on HY zeolites is higher than on HM and HZSM-5 zeolites. Among various types of dealuminated HY zeolites the HEY and HUSY zeolites give higher adamantane yields than conventional HY zeolite. The changes in activity and selectivity of the main and side reactions are correlated with the acidity and the pore structure of the zeolites. To ion-exchange the HY and HUSY zeolites with Ni2+ and La3+ cations may further improve the activity and selectivity of the zeolite catalysts.     

Selective methane chlorination to methyl chloride by zeolite Y-based catalysts

The CH₄ chlorination over Y zeolites was investigated to produce CH₃Cl in a high yield. Three different catalytic systems based on Y zeolite were tested for enhancement of CH₄ conversion and CH₃Cl selectivity: (i) HY zeolites in H⁺-form having various Si/Al ratios, (ii) Pt/HY zeolites supporting Pt metal nanoparticles, (iii) Pt/NaY zeolites in Na⁺-form supporting Pt metal nanoparticles. The reaction was carried out using the gas mixture of CH₄ and Cl₂ with the respective flow rates of 15 and 10 mL min⁻¹ at 300–350 °C using a fixed-bed reactor under a continuous gas flow condition (gas hourly space velocity = 3000 mL g⁻¹ h⁻¹). Above the reaction temperature of 300 °C, the CH₄ chlorination is spontaneous even in the absence of catalyst, achieving 23.6% of CH₄ conversion with 73.4% of CH₃Cl selectivity. Under sufficient supplement of thermal energy, Cl₂ molecules can be dissociated to two chlorine radicals, which triggered the C-H bond activation of CH₄ molecule and thereby various chlorinated methane products (i.e., CH₃Cl, CH₂Cl₂, CHCl₃, CCl₄) could be produced. When the catalysts were used under the same reaction condition, enhancement in the CH₄ conversion was observed. The Pt-free HY zeolite series with varied Si/Al ratios gave around 27% of CH₄ conversion, but there was a slight decrease in CH₃Cl selectivity with about 64%. Despite the difference in acidity of HY zeolites having different Si/Al ratios, no prominent effect of the Si/Al ratios on the catalytic performance was observed. This suggests that the catalytic contribution of HY zeolites under the present reaction condition is not strong enough to overcome the spontaneous CH₄ chlorination. When the Pt/HY zeolite catalysts were used, the CH₄ conversion reached further up to 30% but the CH₃Cl selectivity decreased to 60%. Such an enhancement of CH₄ conversion could be attributed to the strong catalytic activity of HY and Pt/HY zeolite catalysts. However, both catalysts induced the radical cleavage of Cl₂ more favorably, which ultimately decreased the CH₃Cl selectivity. Such trade-off relationship between CH₄ conversion and CH₃Cl selectivity can be slightly broken by using Pt/NaY zeolite catalyst that is known to possess Frustrated Lewis Pairs (FLP) that are very useful for ionic cleavage of H₂ to H⁺ and H⁻. Similarly, in the present work, Pt/NaY(FLP) catalysts enhanced the CH₄ conversion while keeping the CH₃Cl selectivity as compared to the Pt/HY zeolite catalysts.     

Alkylation of Ethylbenzene with Methanol on HY,HM and HZSM-5 Zeolite

The alkylation of ethylbenzene with methanol on various zeolites has been studied at atmospheric pressure, 300–500 °C and with ethylbenzene/methanol = 3 mol/mol in a fixed-bed, integral-flow reactor. The catalytic activity decreased in the order HZSM-5 > HY > HM. The optimum conditions for the formation of ethyltoluene were HY zeolite, 400 °C and W/F = 4.1 g-cat h/g-feed. The catalyst decay rate increased in the order HZSM-5 << HY < HM; coking of the zeolite increased the fraction of para-isomer in the ethyltoluenes. On HZSM-5 modified with alkaline earth metal, the conversion of ethylbenzene decreased with concomitantly increased selectivity of para-ethyltoluene especially evident in cases of magnesium and calcium (> 93% para-selectivity). These results are interpreted in terms of diminution of both the strong acid sites and the pore size of zeolites. For the reaction on HY at 400 °C, the reaction paths were determined; the ethylbenzene reacted via alkylation, disproportionation and dealkylation with initial selectivities 84.7%, 13.1% and 2.2%, respectively.     

Ru/HY催化剂催化对苯二酚加氢研究

对苯二酚液相加氢制备1,4-环己二醇的途径环境友好,关键是研究高催化活性的催化剂来提高产物产率.我们以Ru/HY为催化剂用于对苯二酚加氢.用XRD,TEM对催化剂进行了表征,通过吡啶吸附红外对HY酸性的变化进行了讨论.对其反应条件进行了优化.结果表明3.0%Ru/HY的催化剂表现出高的活性,对苯二酚的转化率和1,4-环己二醇的选择性分别为96.5%和68.3%.我们还基于对Ru/HY催化剂结构的研究探讨并提出相应的反应机理.     

Study on catalytic synthesis of 1,3-benzodioxoles by HY zeolite

The acetalization and ketalization of various aldehydes and ketones with catechol by using HY zeolite as catalyst were studied. Effect of the reaction time, mole ratio of reactants, and amount of catalyst on the yield of benzodioxoles were investigated. Results show that HY is an efficient catalyst for the acetalization and ketalization with high conversion and selectivity in mild conditions. The best reaction conditions: molar ratio of catechol to aldehydes or ketones is 1:1.4, catalyst amount is 3.5 g/l mol catechol, reaction time is 5 h. Under these conditions, the conversion and selectivity were over 50% and 97%, respectively. Translated from Huaxue Tongbao 2006, 69(6) (in Chinese)     

菲加氢裂解制BTX的催化剂研究

采用等体积浸渍法制备了Ni/ZSM-5、Ni/HY、Ni/Al₂O₃和Ni/USY四个系列Ni含量不同的催化剂,在固定床反应器中考察了四类催化剂对菲的加氢裂化制BTX反应的催化性能。借助BET、SEM、热重和差热分析对催化剂的形貌、比表面积、平均孔径及积炭情况进行了表征,结合其结果对催化剂性能进行了分析。结果表明,Ni/HY和Ni/USY催化剂中Ni含量为12%时性能最优,收率可达52%。Al₂O₃催化剂的最佳Ni含量为6%,该系催化剂初始性能尚可,但失活较快;ZSM-5型分子筛催化剂性能较差。     

Fe-Zn-Zr/分子筛复合催化剂上CO2加氢合成异构烷烃Ⅰ.不同分子筛对催化剂性能的影响

 在Fe-Zn-Zr/分子筛复合催化剂上考察了不同类型的分子筛对CO2加氢反应性能的影响. 结果表明,不同分子筛对复合催化剂性能的影响不同,Fe-Zn-Zr/HY是合成异构烷烃有效的复合催化剂. 分子筛的酸性及酸强度对复合催化剂性能有较大的影响,中等强度和较高强度的酸性位有利于异构烃的生成.     

复合分子筛催化微晶纤维素水解

采用水热晶化法制备了HY/ZSM-5复合分子筛。通过XRD、SEM、N2-吸附脱附、NH3-TPD及吡啶吸附红外光谱等手段表征催化剂的结构和性质。结果表明,HY与HZSM-5复合后HY型分子筛完全被HZSM-5紧密包裹,形成致密的核壳结构。与机械混合物相比,复合分子筛微孔比表面积及孔体积均有所减少,总酸量略高,弱酸量小,而强酸量大,Br9nsted酸量与之相似,而Lewis酸量有所减少。将所制备的HY/ZSM-5复合分子筛催化剂应用于以离子液体氯化1-乙基-3-甲基咪唑鎓([Emim]Cl)为溶剂的纤维素水解反应中,与HY催化的纤维素水解相比,HY/ZSM-5催化纤维素水解反应获得的最佳葡萄糖收率由28.04%提高到38.78%,葡萄糖选择性由28.91%提高至48.29%。     

Synthesis of jet fuel through the oligomerization of butenes on zeolite catalysts

In this study, the oligomerization of a butene mixture composed of 1-butene, cis-2-butene and trans-2-butene over several types of zeolites in a fixed-bed catalytic reactor at an elevated pressure was studied to produce hydrocarbons in the jet fuel range (C₈–C₁₆). Three types of zeolites, HZSM-5, Hβ and HY, were compared to evaluate the performance during the synthesis of jet fuel via the oligomerization of the aforementioned butene mixture. Compared to HY and Hβ, HZSM-5 showed a very stable butene conversion rate with high selectivity to jet-fuel-range hydrocarbon, which could be attributed to high resistance to coke resulting from the pore structure. HZSM-5 (50) shows the best quantitative conversion performance and yield for jet fuel for a time-on-stream of up to 6 h. It was also noted that the branched-to-linear hydrocarbon ratio reached 8.7 over the HZSM-5 (50) catalyst, which is beneficial to improve the cold properties of jet fuel. The present study reveals that HZSM-5 (50) is a potential catalyst for jet fuel synthesis through the oligomerization of butene mixture, exhibiting high stability and a high yield.