High temperature reaction of SiCl4 and O2 in quartz tubes

The reaction between SiCl₄ and O₂ at 1 atm between 25 and 1200°C has been followed by mass spectrometry. Below 600°C no reaction with O₂ is noted. Above 600°C the reaction proceeds in two steps. Between 800 and 1000°C the ²⁸Si/³²O₂ peak height ratio is constant with no evolution of Cl₂. It is suggested that silicon oxychlorides are being formed in this temperature regime. Above 1000°C the reaction between SiCl₄ and O₂ intensifies with concomitant production of Cl₂. It is suggested that above 1000°C the reaction SiCl₄ + O₂ → SiO₂ + Cl₂ becomes important.

At low temperatures (<800°C) adsorbed H₂O and OH groups from the surface of the fused silica tube react with SiCl₄ to form HCl. The importance of this reaction decreases with increasing temperature. The increased production of HCl above 1000°C is ascribed to H₂O and H₂ diffusing from the tube.     

ansa-Metallocene (R-Ph)2C(Cp)(Ind)MCl2 with electron withdrawing substituents on phenyl groups for olefin polymerization

The new ansa-complexes (R-Ph)₂C(Cp)(Ind)MCl₂ (R = CF₃, F, Cl; M = Ti, Zr or Hf) were synthesized from the reaction of dilithium salt of the corresponding ligands with appropriate group 4 metal halides. They were tested for ethylene homopolymerization and copolymerization in the presence of methylaluminoxane (MAO) at various ethylene pressures and temperatures. In the case of zirconocenes, complexes 2 (R = CF₃) and 8 (R = Cl) demonstrated much higher catalytic activity than complexes 10 (Ph₂C(Cp)(Ind)ZrCl₂) and 5 (R = F) in ethylene polymerization. The same trend was observed in titanocenes and hafnocenes. The electronic and geometric effects of substituents at the phenyl group on the polymerization activity were easily noticed. For the ethylene/1-hexene or 1-octene copolymerization, 2 also showed the highest catalytic activity, and the copolymers from complex 8 possessed the highest 1-hexene and 1-octene contents.     

Ethylene hydrogenation by the hydride alkoxide species Ir(H)2(OCH2CF3)(PBu2Ph)2. Ethylene-induced reductive elimination of alcohol from Ir

Ir(H)₂(OR_f)P₂ (P = P^tBu₂Ph, R_f = CH₂CF₃) reacts with ethylene at 25°C to give R_fOH, ethane and Ir(P C)P(C₂H₄) (2) then Ir(P C)(C₂H₄)₂ (1) and Ir(P C)H(OR_f)P (3) (P C = η²-C₆H₄P^tBu₂). It is shown that 2 and 1 are in equilibrium by P and C₂H₄ addition/dissociation. Compound 3 is a product “late” in the reaction sequence, and results from H---OR_f oxidative addition to 2. Since 3 reacts with ethylene to give 2, 2 and 3 are in thermal equilibrium. Compound 3 reacts readily with H₂ to give IrH₅P₂ and R_fOH. The reason why OR_f and ethylene ligands seem to be mutually incompatible is discussed.     

An ESR study of the ·SiCl4 radical anion

Exposure of a dilute solution of SiCl₄ in adamantane to ⁶⁰Co γ-rays at 77 K gave anisotropic ESR features which are shown to be characteristic of SiCl⁻₄ anions with a trigonal bipyramidal structure.     

Ethylene homo- and copolymerization using (nBuCp)2ZrCl2 grafted on silica modified with different spacers

(nBuCp)₂ZrCl₂ was grafted on a series of modified silica and evaluated in ethylene/1-hexene copolymerization and their performance was compared with the homogenous system and with that resulting from its immobilization on bare silica. Silica was modified by polymethylhydrosiloxane (PMHS), Me₃SiCl, Ph₃SiOH, SnCl₄, isodrin and aldrin. (nBuCp)₂ZrCl₂ grafted on PMHS-modified silica afforded the catalyst with the highest activity. Comonomer incorporation, melting point and polydispersity was shown to be dependent on the catalyst nature. Bimodality was observed in the case of ethylene homopolymerization employing PMHS-silica-based catalysts.     

氮气吹扫和费托合成的脉冲过程以提高α-烯烃的选择性

费托合成可以将煤炭或者生物质气化得到的合成气转化为α-烯烃等重要的化工产品。研究将费托合成和氮气吹扫操作组合成一脉冲过程,在稳定的操作状态下保证费托合成和氮气吹扫交替进行。在传统的费托合成条件下(反应气速为2 000 h^-1,温度为497 K, 压力为 2.0 MPa, 氢碳体积比为2.0)考察了Fe-Co催化剂在脉冲过程中费托合成的活性和选择性。结果表明,N₂吹扫温度和压力分别为517 K和0.2 MPa下的费托合成的C₃烯烷比是未脉冲的相同反应条件下的九倍左右。同时,反应过程中CH₄的选择性和CO的转化率有所下降。在此基础上,通过间歇反应在固定床反应器中进行该脉冲过程,实验结果表明,利用脉冲操作在费托反应中可以获得更高的烯烃选择性。     

Synthesis of titanium(IV) complexes that contain the Bis(silylamide) ligand of the type [1,8-C10H6(NR)2], and alkene polymerization catalyzed by [1,8-C10H6(NR)2]TiCl2-cocatalyst system

[1,8-C₁₀H₆(NR)₂]TiCl₂ (3; R=SiMe₃, SiⁱBuMe₂, SiⁱPr₃) complexes have been prepared from dilithio salts [1,8-C₁₀H₆(NR)₂]Li₂ (2) and TiCl₄ in diethyl ether in moderate yields (60–63%). These complexes showed significant catalytic activities for ethylene polymerization and for ethylene/1-hexene copolymerization in the presence of methylaluminoxane (MAO), methyl isobutyl aluminoxane (MMAO), AlⁱBu₃– or AlEt₃–Ph₃CB(C₆F₅)₄ as a cocatalyst. The catalytic activities performed in heptane (cocatalyst MMAO) were higher than those carried out in toluene (cocatalyst MAO): 709 kg-PE/mol-Ti·h could be attained for ethylene polymerization by using [1,8-C₁₀H₆(NSiⁱBuMe₂)₂]TiCl₂–MMAO catalyst system.     

Fe3O4@PI催化剂的制备及其费托合成性能

分别采用水热、水热-包覆、球磨法制备了Fe_3O_4、聚酰亚胺(PI)改性的Fe_3O_4@PI和Fe_3O_4-PI催化剂用于费托合成反应,对比研究了PI改性及其含量变化对Fe基催化剂催化CO加氢产物分布的影响规律。结合XRD、SEM、TEM、H_2-TPR、COTPD、FT-IR、XPS、TG和接触角实验等手段对催化剂样品进行了表征。结果表明,Fe_3O_4、Fe_3O_4@PI和Fe_3O_4-PI样品均为球形颗粒; PI改性促进了Fe_3O_4的还原,亲水性增强。Fe_3O_4@PI样品中,PI均匀包覆于Fe_3O_4表面,具有较好的热稳定性;与Fe_3O_4、Fe_3O_4-PI相比,Fe_3O_4@PI样品CO吸附增强。在CO加氢反应中,与Fe_3O_4相比,PI改性的Fe_3O_4@PI和Fe_3O_4-PI样品催化活性下降,二次加氢能力受到抑制,烯烃选择性提高; Fe_3O_4@PI样品烯烃选择性增加明显,烯烷比(O/P)由改性前的0.50提高至2.15;适宜含量的PI改性促进C5+烃生成。     

新型高活性催化剂乙烯气相聚合的研究(Ⅰ)──气相均聚和共聚反应及气相均聚动力学

研究了新型高活性乙烯气相聚合催化剂TiCl₄/MgCl₂/ZnCl₂/SiCl₄/醇/Al(i-Bu)₃体系中钛和醇组分含量对聚合反应和产物颗粒形态的影响。测定了乙烯气相聚合反应动力学曲线,确定了聚合动力学方程。用SEM、DSC、WAXD、¹³CNMR对催化剂及聚合物的形态、结构和性能进行了分析和表征。     

Effect of ligand in ethylene/styrene copolymerization by [Me2Si(C5Me4)(NR)]TiCl2 (R = tert-Bu, cyclohexyl) and (1,3-Me2C5H3)TiCl2(O-2,6-Pr2C6H3)-MAO catalyst system

Copolymerization of ethylene with styrene using linked cyclopentadienyl-amide titanium(IV) complexes, [Me₂Si(C₅Me₄)(R)]TiCl₂ [R=tert-Bu (1), cyclohexyl (2)], and non-bridged (1,3-Me₂C₅H₃)TiCl₂(O-2,6-ⁱPr₂C₆H₃) (3)-MAO catalysts have been explored. Although the catalytic activity by 2 was lower than 1, 2 showed more efficient styrene incorporation than 1 under the same conditions. Moreover, the resultant copolymer prepared by 2 possessed completely different microstructure from those by 1, indicating that the nature of amide ligand affects both styrene incorporation and monomer sequence.     

Fixed-frequency and threshold molecular photoelectron spectra of S 1s, Si 1s and Cl 1s core levels

Fixed-frequency and threshold photoelectron spectra have been recorded for ionization from the S ls shells in SF₆, CS₂ and COS, the Si 1s shells in SiH₄ and SiCl₄ and the Cl 1s shell in SiCl₄ using synchrotron radiation. Fixed-frequency spectra generally showed a single strong ionization feature with associated weak satellite structure due to excited ionized states. Threshold spectra closely resembled X-ray absorption spectra but with an additional feature due to direct ionization. In cases where resonant process enhanced the NEXAFS spectrum direct ionization was not observed.     

The reaction of (μ-H)2Os3(CO)9(PPh3) with ethylene affords the ethylidene complex (μ-H)2Os3(CO)9(PPh3)(μ-CHCH3)

The product isolated from the reaction of (μ-H)₂Os₃(CO)₉(PPh₃) with ethylene is shown to be the ethylidene complex (μ-H)₂Os₃(CO)₉(PPh₃)(μ-CHCH₃) (1) rather than the ethylene complex (μ-H)(H)Os₃(CO)₉(PPh₃)(C₂H₄), as previously claimed. The characterization of 1 is based on a combination of ¹H and ¹³C NMR results. The ¹H NMR data (δ 6.84 (1 H_D), 2.53 (3 H_C), J(CD) = 7.4 Hz) establish the presence of the ethylidene moiety, whereas detailed analysis of the 1-D and 2-D ¹³C NMR spectra of ¹³CO-enriched 1 indicates the relative positions of the ethylidene, hydride, and phosphine ligands on the triosmium framework.     

Pd修饰对Cd0.8Zn0.2S/SiO2光催化甘油水溶液制氢性能的影响

用等体积浸渍法制备了不同Pd负载量的Pd/Cd_0.8Zn_0.2S/SiO₂光催化材料,采用XRD、H₂-TPR、XPS、UV-vis DRS和光催化反应评价等方法对光催化材料的表面结构、光吸收性能以及光催化甘油水溶液制氢反应性能进行了考察。研究结果表明,ZnS与CdS在SiO₂表面形成了Cd_0.8Zn_0.2S固溶体,金属Pd负载未对固溶体Cd_0.8Zn_0.2S/SiO₂的结构造成影响;金属Pd修饰明显地提高了原固溶体的光响应性能,拓展了其吸光域,增强了吸光效率。金属Pd修饰后,Cd_0.8Zn_0.2S/SiO₂的光解甘油水溶液产氢速率显著提高,Pd负载量为0.5%的Pd/Cd_0.8Zn_0.2S/SiO₂具有最佳的光催化甘油水溶液制氢性能,其在紫外光照射下的氢气生成速率为831 μmol/h,较未负载时提高了近四倍;模拟太阳光下为153 μmol/h,较未负载时提高了近两倍。     

Mg改性对Co/γ-Al2O3-TiO2催化燃烧丙烷性能影响

采用分步浸渍法制备了系列Mg改性的Co/γ-Al_2O_3-TiO_2催化剂,通过X射线衍射(XRD)、紫外可见漫反射光谱(DR-UV-vis)、N_2吸附-脱附(BET)、X射线光电子能谱(XPS)和H_2程序升温还原(H_2-TPR)等技术对催化剂进行表征,并考察了其对丙烷燃烧的催化性能。结果表明,Co在原始γ-Al_2O_3-TiO_2载体和Mg改性MgO/γ-Al_2O_3-TiO_2载体上均以Co_3O_4的形式存在;Mg掺入后与Al_2O_3作用形成MgAl_2O_4尖晶石,改善了载体的织构性质,提升了Co_3O_4在催化剂载体表面的暴露数量和分散程度。此外,MgAl_2O_4与Co_3O_4相互作用提升了Co_3O_4颗粒表面Co~(3+)/Co~(2+)和O_(ads)/O_(latt)的比例,并削弱了Co-O键键能,从而提升了其对丙烷的催化燃烧活性。当Mg负载量为15%(质量分数)时,在Co/MgO(15%)/γ-Al_2O_3-TiO_2催化剂上进行丙烷燃烧,丙烷90%转化率的温度比无Mg掺杂的Co/γ-Al_2O_3-TiO_2催化剂的降低了45℃,并且连续反应40 h其活性保持稳定。     

Solid state synthesis and characterization of iron（Ⅱ） pyrophosphate Fe2P2O7

Offwhite pure Fe_2P_2O_7 was synthesized through solid phase reaction using Fe_2O_3 and NH_4H_2PO_4 in argon atmosphere.The reaction products of Fe_2O_3 and NH4_H_2PO_4 at a series of temperatures from 400 to 900℃were characterized by XRD.Comparison and analysis of XRD patterns of resultant products indicated well-crystallized Fe_2P_2O_7 could be obtained over 630℃and Fe_2P_2O_7 prepared at 700℃was triclinic in cell type.Comparison of the cell parameters proved that the as-prepared Fe_2P_2O_7 belonged toβ- Fe_2P_2O_7 in crystal phase and SEM showed its size distribution was 0.5-2μm.     

UiO-66-NH2接枝吡啶亚胺钴系催化剂的合成及催化乙烯齐聚性能

以金属有机骨架(MOFs)UiO-66-NH2和吡啶-2-甲醛为原料,采用后合成修饰法制备一种UiO-66-NH2接枝吡啶亚胺配体,然后以UiO-66-NH2接枝吡啶亚胺配体和CoCl2·6H2O为原料,经配合反应,合成出一种UiO-66-NH2接枝吡啶亚胺钴系催化剂.采用傅里叶红外变换光谱(FT-IR)、X射线衍射(...     

LiMn_2O_4/TiO_2催化剂上甲烷氧化偶联反应性能的研究

采用固相反应法制备了具有尖晶石结构的LiMn_2O_4/TiO_2系列催化剂,探讨了TiO_2、Li/TiO_2、Mn/TiO_2、LiMn_2O_4及LiMn_2O_4/TiO_2等不同组成催化剂的甲烷氧化偶联反应性能,采用XRD、XPS、CO_2-TPD和H_2-TPR等表征方法对该系列催化剂进行了分析。结果表明,具有尖晶石结构的LiMn_2O_4化合物具有较高的甲烷氧化偶联催化活性,在775℃、0.1MPa、7200mL/(h·g),CH_4∶O_2(体积比)为2.5的条件下,甲烷转化率可达25.8%,C2选择性可达43.2%。TiO_2的存在不仅进一步提高了甲烷转化率和C2选择性,还有效抑制了甲烷完全氧化形成CO_2的过程。负载8%LiMn_2O_4的LiMn_2O_4/TiO_2催化剂性能达到最优,此时甲烷转化率达到31.6%,C2选择性为52.4%,CO_2选择性降低到26.3%。考察了不同焙烧温度对催化剂活性的影响,850℃为LiMn_2O_4/TiO_2催化剂的最佳焙烧温度。     

新型高效催化剂乙烯/1-丁烯气相齐聚和共聚制备弹性体及其结构与性能关系

用新型催化体系TiCl₄,Ti(OBu)₄/MgCl₂,SiO₂和ZnCl₂/醇/AlR₃催化乙烯与1-丁烯气相均聚及共聚,制得两种共聚物弹性体,发现新型催化剂体系具有独特的齐聚和原位共聚性能.采用¹³CNMR测定了共聚物链序列分布结构,观察到共聚单体在聚合物链中分布不均匀,存在较长的乙烯链段和较多的1-丁烯嵌段.产物DSC谱图表现出复杂的结晶熔融行为,存在多种结晶形态,出现熔融肩峰及双峰,与通常制得的LLDPE的结晶熔融行为有很大差别;结晶度和密度较低,并具有弹性体性质.     

Fe改性对Ru/Al_2O_3催化剂的马来酸二甲酯加氢性能影响

以Al2O3为载体,采用吸附-沉淀法制备一系列Ru-Fe/Al2O3催化剂,并进行了H2-TPR、XRD及XPS表征。以马来酸二甲酯(DMM)催化加氢合成丁二酸二甲酯(DMS)为探针反应,考察了Fe的加入对Ru/Al2O3催化性能的影响。评价结果表明,当Fe/Ru原子比小于2时,催化剂活性变化不大;但Fe/Ru原子比大于或等于2时,催化剂活性明显增加;与Ru/Al2O3催化剂相比,Fe的加入改善了催化剂的高温氧化还原处理稳定性。以甲醇为溶剂,在70℃、1.0 MPa压力、600 r/min转速下,Ru-Fe/Al2O3催化DMM的转化率与生成DMS的选择性均接近100%。XPS和H2-TPR表征结果表明,Ru-Fe/Al2O3中Fe与Ru产生较强的相互作用,促进Ru的分散且调变了Ru的电子特性。     

新型高活性催化剂乙烯气相聚合的研究(Ⅵ)——锌化合物对催化剂及产物性能的影响

研究了新型高活性乙烯气相聚合催化剂TiCl₄、Ti(OBu)₄/MgCl₂、SiO₂和ZnCl₂/醇/AlR₃体系中ZnCl₂-AlEt₃/SiO₂重量比和锌化合物含量对气相均聚合的影响,比较了2种不同催化剂Cat# A和Cat# B的聚合反应动力学及性能差异.催化剂中锌化合物作为复合载体的重要组分,可显著改善产物分子量调节效果.通过比表面积、SEM、DSC以及FTIR对催化剂和聚合物的形态、结构及性能进行了分析和表征.结果表明,均聚产物与采用MgCl₂作载体的催化剂制备的产物相比,支化度较高,结晶度较低,熔融峰较宽.发现Cat#B制得的均聚产物具有新颖的熔融双峰.