3,4-Dichlorotoluene Ammoxidation to 3,4-Dichlorobenzonitrile over VPO/SiO2 Catalyst

Ammoxidation of 3,4-dichlorotoluene(DCT) to prepare 3,4-dichlorobenzonitrile (DCBN) over silica supported vanadium phosphorus oxide catalysts has been studied. On the VPO/SiO2 catalyst, the influence of the reaction temperature, the molar ratio of air/DCT, the molar ratio of NH3/DCT in the feed gas and the space velocity (vs) on the conversion, yield and selectivity was observed. The most appropriate reaction condition is: reaction T=673 K, n(DCT)∶n(NH3)∶n(air)=1∶7∶30 and vs=250 h-1. At this optimum reaction condition, the conversion of DCT is 97.8%; the molar yield of DCBN is 67.4%. It was found that the addition of element phosphorus can improve the yield of DCBN compared with VO/SiO2 catalyst.     

Preparation and luminescence characteristics of Sr3SiO5：Eu^2＋ phosphor for white LED

The Sr3SiO5：Eu^2＋ phosphor was synthesized by high temperature solid-state reaction. The emission spectrum of Sr3SiO5：Eu^2＋ shows two bands centered at 487 and 575 nm, which well agree with the theoretic values of emission spectrum. The excitation spectrum for 575 nm emission center has several excitation bands at 365, 418, 458 and 473 nm. And the results show that the emission spectrum of Sr3SiO5：Eu^2＋ is influenced by the Eu^2＋ concentration. The relative emission spectra of the white-emitting InGaN-based YAG：Ce^3＋ LED and Sr3SiO5：Eu^2＋ LED were investigated. The results show that the color development of InGaN-based Sr3SiO5：Eu^2＋ is better than that of InGaN-based YAG：Ce^3＋, and the CIE chromaticity of InGaN-based Sr3SiO5：Eu^2＋ is （x=0.348, y=0.326）.     

Reaction condition optimization and kinetic investigation of roasting zinc oxide ore using (NH<Subscript>4</Subscript>)<Subscript>2</Subscript>SO<Subscript>4</Subscript>

An orthogonal test was used to optimize the reaction conditions of roasting zinc oxide ore using (NH₄)₂SO₄. The optimized reaction conditions are defined as an (NH₄)₂SO₄/zinc molar ratio of 1.4:1, a roasting temperature of 440°C, and a thermostatic time of 60 min. The molar ratio of (NH₄)₂SO₄/zinc is the most predominant factor and the roasting temperature is the second significant factor that governs the zinc extraction. Thermogravimetric–differential thermal analysis was used for (NH₄)₂SO₄ and zinc mixed in a molar ratio of 1.4:1 at the heating rates of 5, 10, 15, and 20 K·min-1. Two strong endothermic peaks indicate that the complex chemical reactions occur at approximately 290°C and 400°C. XRD analysis was employed to examine the transformations of mineral phases during roasting process. Kinetic parameters, including reaction apparent activation energy, reaction order, and frequency factor, were calculated by the Doyle–Ozawa and Kissinger methods. Corresponding to the two endothermic peaks, the kinetic equations were obtained.     

由呋喃制备吡咯的催化剂研究

使用SiO2-Al2O3催化剂,以呋喃和氨水为反应物,通过芳香环上杂原子取代的气固相催化反应制备吡咯.确定了催化剂的最佳制备条件:灼烧温度600℃,Al质量分数10%～25%,反应的pH值2.5～3.2.在催化反应温度(420±1)℃范围内,反应物的摩尔比呋喃∶氨∶水为1∶8∶37,液时空速0.27h-1,该催化剂表现出改善的稳定性和良好的催化活性及反应选择性.     

Dissolution of Al<Subscript>2</Subscript>TiO<Subscript>5</Subscript> inclusions in CaO-SiO<Subscript>2</Subscript>-Al<Subscript>2</Subscript>O<Subscript>3</Subscript> slags at 1823 K

Al-Ti-O inclusions always clog submerged nozzles in Ti-bearing Al-killed steel. A typical synthesized Al₂TiO₅ inclusion was immersed in a CaO-SiO₂-Al₂O₃ molten slag for different durations at 1823 K. The Al₂TiO₅ dissolution paths and mechanism were revealed by scanning electron microscopy (SEM) and energy dispersive spectroscopy (EDS). Decreased amounts of Ti and Al and increased amounts of Si and Ca at the dissolution boundary prove that inclusion dissolution and slag penetration simultaneously occur. SiO₂ diffuses or penetrates the inclusion more quickly than CaO, as indicated by the w(CaO)/w(SiO₂) value in the reaction region. A liquid product (containing 0.7–1.2 w(CaO)/w(SiO₂), 15wt%–20wt% Al₂O₃, and 5wt%–15wt% TiO₂) forms on the inclusion surface when Al₂TiO₅ is dissolved in the slag. Al₂TiO₅ initially dissolves faster than the diffusion rate of the liquid product toward the bulk slag. With increasing reaction time, the boundary reaches its largest distance, the Al₂TiO₅ dissolution rate equals the liquid product diffusion rate, and the dissolution process remains stable until the inclusion is completely dissolved.     

2,2,6,6-四羟甲基环己醇五烯丙基醚的合成

以环己酮、甲醛为原料在碱催化下经羟醛缩合,康尼扎罗两步反应制得中间体2,2,6,6-四羟甲基环己醇。此化合物在季铵盐相转移催化下与氯丙烯反应生成2,2,6,6-四羟甲基环己醇五烯丙基醚。用红外光谱、¹³C和¹H核磁共振谱对2,2,6,6-四羟甲基环己醇和2,2,6,6-四羟甲基环己醇五烯丙基醚进行了表征。探讨了反应温度,催化剂用量,物料物质的量比等对2,2,6,6-四羟甲基环己醇和2,2,6,6-四羟甲基环己醇五烯丙基醚产率的影响。结果表明,合成2,2,6,6-四羟甲基环己醇的适宜条件为：n（碱）∶n（甲醛）∶n（环己酮）＝1.25∶5.5∶1,羟醛缩合反应温度和反应时间分别为10℃和1h,康尼扎罗反应温度和时间分别为40℃和1.5h;合成2,2,6,6-四羟甲基环己醇五烯丙基醚的适宜条件为：n（氢氧化钠）∶n（氯丙烯）∶n（2,2,6,6-四羟甲基环己醇）=9∶10∶1,相转移剂用量为10%（以2,2,6,6-四羟甲基环己醇质量为基准）,反应温度和时间分别为80℃和120h,2,2,6,6-四羟甲基环己醇五烯丙基醚产率为58.3%。     

Immobilization of 12-phosphotungstic heteropolyacid on amine-functionalized SiO<Subscript>2</Subscript> for tetrahydrofuran polymerization

The 12-phosphotungstic heteropolyacid (HPW) was immobilized on the surface of a silica carrier modified by the amine groups of organosilane γ-aminopropyl triethoxysilane (APTES), and its catalytic performance was investigated for tetrahydrofuran (THF) ring-opening polymerization. This amine-functionalized catalyst exhibited better activity, and the polytetramethylene ether glycol (PTMG) yield was 63.7%. The 12-phosphotungstic heteropolyacid supported on aminopropyl-functionalized SiO₂ support (HPW/SiO₂-APTES) was reused four times and showed a good maintenance of activity which was better than that of the conven-tional catalyst HPW supported on SiO₂ (HPW/SiO₂). These results were obtained using infrared spectroscopy, nuclear magnetic resonance spectroscopy, nitrogen adsorption and X-ray diffraction. HPW on the HPW/SiO₂-APTES catalyst exhibited higher dispersed state and maintained a more stable structure than that of the HPW/SiO₂ sample.     

Thermodynamics and phase transformations in the recovery of zinc from willemite

Willemite is a common component of zinc and lead metallurgical slags that, in the absence of effective utilization methods, cause serious environmental problems. To solve this problem and increase zinc recovery, we proposed a novel extraction method of zinc from willemite by calcified roasting followed by leaching in NH₄Cl-NH₃·H₂O solution. The thermodynamics and phase conversion of Zn₂SiO₄ to zinc oxide (ZnO) during calcified roasting with CaO were investigated. The mechanism of mineralogical phase conversion and the effects of the CaO-to-Zn₂SiO₄ mole ratio (n(CaO)/n(Zn₂SiO₄)), roasting temperature, and the roasting time on zinc-bearing phase conversion were experimentally investigated. The results show that Zn₂SiO₄ was first converted to Ca₂ZnSi₂O₇ and then to ZnO. The critical step in extracting zinc from willemite is the conversion of Zn₂SiO₄ to ZnO. The zinc percent leached in the ammonia leaching system rapidly increased because of the gradual complete phase conversion from willemite to ZnO via the calcified roasting process.     

气固相催化合成吡咯的催化剂的研究

以ZSM-5、SiO₂-Al₂O₃和Al₂O₃为催化剂,在连续流动固定床反应器中,氨与呋喃催化合成吡咯。用程序升温氨脱附法（NH₃-TPD）测定了催化剂表面相对酸强度及酸量分布,筛选出了催化活性好和选择性高的SiO₂-Al₂O₃-d硅酸铝催化剂,并对金属氧化物进行了改性。在反应温度为425～435℃、n (AM)：n (FN)为10：1以及催化剂负荷（以呋喃计）为16.6 mmol /(h•g)的条件下,吡咯的收率可达90％以上。     

Synthesis, Characterization and Calorimetry of Ni（C4H8N2O3）2Cl2

A coordination complex was synthesized from NiCl2 and dipeptide glycylglycine（GG）. It was characterized by element analysis, NMR and TG methods, and then was determined to be Ni（C4HsN2O3）2Cl2. Using an isoperibolic reaction calorimeter, the standard molar enthalpy of formation of Ni（GG）2Cl2（solid） has been determined to be -（1 674.66±2.02） kJ · mol^-1 at 298.15 K.     

无机-有机杂化材料催化合成乙酸异戊酯及动力学研究

以甘氨酸(Gly)和磷钨酸为原料合成的一系列无机有机杂化材料为催化剂,考察各因素对其催化合成乙酸异戊酯的影响,并利用响应面分析法优化乙酸异戊酯合成工艺。研究表明,[GlyH]_(1.0)-H_(2.0)PW_(12)O_(40)催化剂具有最高的催化酯化反应活性和重复使用性能。响应面分析法优化乙酸异戊酯合成的最佳条件为:醇酸摩尔数比为1.05∶1,催化剂用量为酸质量的4.5%,反应时间2.0h,带水剂量10mL,该条件下,乙酸异戊酯产率为98.5%,结果与模型预测值基本相符。优化条件下[GlyH]_(1.0)-H_(2.0)PW_(12)O_(40)催化酯化反应表观活化能为79.73kJ/mol。     

三组分高效合成吡唑并[3,4-b]吡啶衍生物

以氨基吡唑、芳酮醛水合物和丙二腈为原料,醋酸为溶剂,在100℃微波辐射下高效制备一系列吡唑并[3,4-b]吡啶衍生物。此制备方式具有反应快(反应时间为20~30 min)、操作简单、选择性高和环境友好等优点。产物的结构可通过高分辨质谱、红外光谱、核磁共振氢谱和碳谱进行表征;其中化合物6-氨基-4-(4-氯苯甲酰基)-1,3-二甲基-1H-吡唑[3,4-b]吡啶-5-腈4a的结构经由X射线单晶衍射进一步确认。     

Decay dynamics of excited CS<Subscript>2</Subscript> and NH<Subscript>3</Subscript> investigated by femtosecond laser

By using the home-made femtosecond laser system and the time-of-flightmass spectrometer, the decay dynamics of excited carbon disulfide (CS2) and ammonia (NH3) are investigated in real time by pump-probe multiphoton ionization detection. The estimated lifetime constant of the NH3 state (514 fs) agreed quite well with the literature report. For the first time, the decay lifetime constants of the NH3 ′1A′1 state (93793 fs), the CS2 state (153 ± 10 fs), and the CS2 Rydberg state[2-3]6sσg(3Ⅱg)(948 ± 23 fs) are obtained.     

超声波下酸化碘酸钾和亚硫酸钠反应的反应速率研究

分别测定在有超声波作用和在无超声波作用条件下 ,酸化碘酸钾 (KIO3 )和亚硫酸钠 (Na2 SO3 )反应的反应速率方程式及活化能 ,从而研究该反应的机理以及超声波在该反应中的作用 ,并确定反应的最佳条件。实验得出 ,超声波对该反应有一定的促进作用 ,但是这种促进作用只提高反应的速率常数和降低反应的活化能 ,并没有改变反应机理。在超声波功率为 30 0W时 ,反应的速率方程表示式为 :v =k·c1 0 9(KIO3 ) ·c1 0 0 (Na2 SO3 )·c1 0 8(H+ ) ,其中 :k =95 0 (mol-1·L) 2 ·s-1,活化能为 17 35kJ·mol-1。实验还得出 ,在温度为2 98K时 ,当KIO3 与Na2 SO3 的初始浓度比为 2∶5 ,H+ 的初始浓度为 0 0 4 2 8mol·L-1,超声功率为 30 0W时 ,反应速率为最快 ,即v =4 31× 10 -4mol·L-1·s-1)。     

3,4-二芳基吡咯的合成

卟啉化合物及其金属配合物是一类极具潜力、环境友好的光电转换材料而成为国际上人们研究的热点,3,4-二芳基吡咯作为构建该卟啉类化合物的中心体,其合成方法的研究很少。本文以亚氨基二乙酸为原料,经酯化和酰基化2步反应得到N-乙酰基-亚胺基二乙酸二甲酯,再将得到反应物在甲醇钠溶液中与二芳基乙二酮发生缩合反应得到3,4-二芳基吡咯-2,5-二甲酸,最后将3,4-二芳基吡咯-2,5-二甲酸在乙醇胺中回流脱羧制得3,4-二芳基吡咯,其结构经1H NMR、13C NMR和元素分析得以确证。该合成方法具有反应条件温和、反应速度快、产率较高、操作简单等优点。     

α-(2,5-二甲基-3,4-二乙酰基吡咯基)萘的合成和晶体结构

 在酸性介质中,3,4-二乙酰基-2,5-己二酮与萘胺作用,合成得到了α-(2,5-二甲基-3,4-二乙酰基吡咯基)萘,用IR,1H-NMR,MS,HRMS对其进行了表征,并用X射线衍射测定了α-(2,5-二甲基-3,4-二乙酰基吡咯基)萘的晶体结构.该晶体属三斜晶系,P1空间群,晶体学数据为:a是0.8045(1)nm,b是1.0018(1)nm,c是2.0757(2)nm,α是80.09(1)°,β是82.66(1)°,γ是83.81(1)°,V是1.6281(3)nm³,Z是4,M_r是305.36,D_c是1.246×10³kg/m³,μ(M_oK_α)是0.080mm^-1,F(000)是648,在I>2σ(I)的独立可观测衍射点为3669个,最终偏差因子R是0.0406,W_R是0.0962.     

Catalytic oxidation of phenol in wastewater-A new application of the amorphous Fe78Si9B13 alloy

The amorphous Fe78Si9B13 alloy was used as a heterogeneous Fenton catalyst in the process of phenol degradation.The influences of main operating parameters such as reaction temperature,catalyst amount,hydrogen peroxide dosage and initial pH of solution on phenol degradation rate were investigated.The maximum mineralization of phenol was achieved at 60°C,6 g/L Fe78Si9B13, 0.31 mol/L hydrogen peroxide,with an initial pH of 2.5.More than 99%of phenol was completely removed under the optimum conditions within 10 min for a solution containing 1000 mg/L of phenol.Batch experiments for solutions containing phenol con- centrations ranging from 50 to 2000 mg/L were investigated under the above conditions and the same excellent degradation rate was obtained.The Fe78Si9B13 showed better catalytic activity than iron powder and Fe 2+ .Addition of n-butannol(hydroxyl radical scavenger)decreased the degradation rate of phenol,which demonstrates that hydroxyl radicals were mainly responsible for the removal of phenol.We demonstrated that phenol may be degraded by hydroxyl radicals decomposed by hydrogen peroxide on the surface of Fe78Si9B13 and illustrated the reaction mechanism for this process.This amorphous alloy exhibited high stability in recycling experiments and showed excellent reuse performance even after continuous operations of 8 cycles.     

In situ time-resolved FTIR investigation on the reaction mechanism of partial oxidation of methane to syngas over supported Rh and Ru catalysts

In situ time-resolved FTIR spectroscopy was used to study the reaction mechanism of partial oxidation of methane (POM) to synthesis gas and the reaction of CH₄/O₂/He (2/1/45, molar ratio) gas mixture with adsorbed CO species over Rh/SiO₂, Ru/γ-Al₂O₃ and Ru/SiO₂ catalysts at 500—600℃. It was found that CO is the primary product of POM reaction over reduced and working state Rh/SiO₂ catalysts. Direct oxidation of CH₄ is the main pathway of synthesis gas formation over Rh/SiO₂ catalyst. CO₂ is the primary product of POM over Ru/γ-Al₂O₃ and Ru/SiO₂ catalysts. The dominant reaction pathway for synthesis gas formation over Ru/γ-Al₂O₃ catalyst is via the reforming reactions of CH₄ with CO₂ and H₂O. For the POM reaction over Rh/SiO₂ and Ru/γ-Al₂O₃ catalysts, consecutive oxidation of surface CO species is an important pathway of CO₂ formation.     

Investigation of the cross-reaction mechanism of C<Subscript>6</Subscript>H<Subscript>5</Subscript>F-HNO<Subscript>2</Subscript> aqueous solution irradiated at 355 nm by transient absorbance spectrum technique

The transient absorption spectrum technique was employed to investigate the cross-reaction mechanism of C6H5F-HNO2 aqueous solution irradiated at 355 nm. The characteristic and the kinetic parameters of transient species were also detected. Hydroxyl radical derived from the photolysis of HNO2 was added to monofluorobenzene with a second-order rate constant of （5.83±0.17）×10^9 L·mol^-1·s^-1 to form an adduct, C6H5F…OH, which was able to react with HNO2 as the main reaction pathway with a rate constant of （8.3±0.1）×10^7 L·mol^-1·s^-1. The C6F6…OH adduct can also be decayed by elimination of H2O to yield monofluorophenyl radical C6H4F-. By GC-MS technique, the final products were identified to be monofluorophenol, nitro-monofluorobenzene, nitro-monofluorophenol and para-fluorobiphenyl.     

Kinetic studies of the decomposition reaction of adducts of dinuclear Fe(Ⅱ)/O2

Kinetic studies of the decomposition reaction of dinuclear Fe(Ⅱ) adducts [Fe₂(N-Et-HPTB){O₂P(OPh)₂}](Cl- O₄)₂ (1) and [Fe₂(N-Et-HPTB) {O₂P(Ph)₂}] (ClO₄)₂ (2) with O₂ have been carried out at low temperature using UV-vis spectra. The decomposition reaction of Fe(Ⅱ)/O₂ adducts was first-order in the experimental conditions, and the activation parameters were obtained. ?H^¹ = 85.62 kJ·mol^-1, ?S¹ = 19.43 J·mol^-1·K^-1 for compound (1) and ?H^¹ = 97.97 kJ·mol^-1, ?S^¹ = 55.68 J·mol^-1·K^-1 for compound (2). These results are similar to those of dioxygen adducts of other metals complexes and natural enzymes such as methane mono- oxygenase (MMOH).