载铜5A分子筛在汽油模拟体系中脱硫性能的研究

近年,美国环保局计划将汽油中硫的质量分数从当前的300×10-6降到2006年的30×10-6,欧盟也已经通过了新的汽油硫质量分数标准为30×10-6~50×10-6,德国甚至提出计划使用无硫汽油[1]。中国汽油硫的质量分数高达800×10-6以上,与世界汽油品质距离甚远。因此汽油中硫化物的脱除成为当务之急。目前,脱硫技术主要有催化裂化脱硫、催化加氢脱硫、水蒸气脱硫、生物催化脱硫、吸附精制脱硫、氧化脱硫等[2~5]。吸附精制法具有净化度高、能耗低、易于操作等优点,高效的脱硫吸附剂制备是过程开发的关键。负载金属离子的活性纤维是脱除汽油中硫醇的一种…     

用[BMIM][Cu2Cl3]离子液体萃取脱除汽油中的硫化物

以不同的IL（ionic liquid）/油质量比,采用[BMIM][Cu2Cl3]（[BMIM]=1-butyl-3-methylimidazolium）对模型汽油和商品汽油进行单步和多步萃取脱硫实验;并合成几种具有不同阴离子和阳离子结构的离子液体,评价和比较了离子液体对商品汽油的萃取脱硫性能的影响。实验结果表明,具有较好的水稳定性和常温流动性的[BMIM] [Cu2Cl3]离子液体硫容较高,在IL/油质量比为1∶3时,经多步萃取后,油品中的硫质量分数降至20×10-6～30×10-6,累计脱硫率超过95%。汽油中其他组分对脱硫效果影响很小。[BMIM][Cu2Cl3]与汽油形成稳定的两相系统,分离方便。离子液体脱硫能力可以通过四氯化碳反萃取完全恢复。     

石油焦系活性炭的吸附脱硫

选取独山子石油焦为原料，以物理活化法制得比表面积达500m2/g～900m2/g的活性炭，进行吸附脱硫研究。采用酸氧化法对活性炭孔结构和微观孔径分布进行改性。酸氧化使活性炭表面酸性官能团含量明显增加，增加量约为原来的5倍。活性炭吸附脱硫性能随表面酸性官能团含量的增加而增大。理想的酸化条件是浓硝酸120℃氧化40min。通过静态吸附实验，活性炭吸附脱硫的最佳条件是，温度25℃，压力1.0MPa，静态吸附6h。最佳条件下吸附脱硫可使模型化合物硫的质量分数从137.9×10－6降至3.1×10－6。从活性炭孔径匹配考察可知，平均孔直径在0.8nm～2.1nm的活性炭对模型化合物硫的质量分数降低具有明显效果。     

裂解汽油中噻吩硫在Co-Mo/Al2O3上的催化加氢宏观动力学

采用绝热管式固定床积分反应器，在2.5MPa~3.9MPa、513K~655K、氢/裂解汽油摩尔比1.8~3.5和裂解汽油中噻吩、单甲基噻吩和双甲基噻吩质量分数为838×10－6、137×10－6~723×10－6和192×10－6~723×10－6下，对Co-Mo/Al2O3催化剂上裂解汽油催化加氢脱硫的宏观动力学进行了研究。以Powell优化法和Merson迭代法对动力学实验数据进行非线性参数估值，建立了良好吻合实验数据的、裂解汽油催化加氢脱硫的幂函数型宏观动力学模型。噻吩、单甲基噻吩和双甲基噻吩的反应级数分别为0.721、0.735和0.87，对应的加氢反应宏观活化能依次为70.0kJ·mol－1、67.9kJ·mol－1和59.9kJ·mol－1。各噻吩基硫的转化率均随反应压力的提高而增加，3.5MPa以上时，增加的趋势减缓；反应温度的提高有利于噻吩基硫转化率的增加；593K以上时，各硫化物的转化率随温度的增加呈现线性增加的趋势。     

功能化酸性离子液体催化柴油氧化脱硫的研究

以功能化酸性离子液体为催化剂,30%双氧水为氧化剂,将加氢柴油中的含硫化合物氧化为相应的砜类物质,并用N-甲基吡咯烷酮（NMP）萃取一次。同时考察了反应温度、反应时间和催化剂用量等因素对氧化脱硫反应的影响,得出最佳反应条件为,3mL油样（硫的质量分数为200×10-6）、1.5g酸性离子液体、 0.3mL H2O2、 25℃,3.5h、VNMP/Vdiesel=1∶1,脱硫率可达到86.7%,柴油硫的质量分数仅为25×10-6左右,反应结束后,可通过简单的倾倒将油样和催化剂分离,重复使用5次,其催化活性变化不大。     

喷气燃料中抗氧剂2,6-二叔丁基对甲酚的高效液相分析

 采用高效液相法分析喷气燃料HDF 1中的抗氧化剂 2 ,6 二叔丁基对甲酚 (简称BHT)含量 ,研究了二元混合流动相中甲醇 乙酸缓冲液的比例对燃料主体和BHT分离效果的影响 ,选择了最佳分离条件 (甲醇所占体积分数为 85 % ,流速为 1mL/min) ,在此条件下 ,可测出质量分数为 1× 10 -5的BHT。用该喷气燃料配制了BHT质量分数在 2 0× 10 -6到 12 0× 10 -6之间的标准溶液 ,考察了BHT质量分数与峰面积之间的关系 ,结果表明线性关系良好。     

流化床快速制不定形活性焦脱除烟气中SO2的研究

利用大型流化床制得了适用于脱除烟道气中二氧化硫的不定形活性焦AC-A,并对其进行了特性分析,在固定床上考察了不同条件下脱除SO2的性能。与硫容相近的商业活性焦AC-B的脱硫性能对比,发现其脱硫性能较好。实验结果表明,在烟气中的二氧化硫的体积分数为0.05%~0.12%,反应温度为80 ℃～100 ℃,空速（GHSV）为1 200 h-1,O2的体积分数为6%,水蒸气为10%的情况下,活性焦AC-A保持SO2脱除率在90%以上达5 h。再生循环脱硫实验表明,活性焦AC-A具有良好的再生脱硫活性。     

汽油活性炭基脱硫吸附剂的制备与评价

以250℃温度下浓硫酸改性后的活性炭为载体,采用浸渍法制备了以MnO₂为活性组分的活性炭基的汽油脱硫吸附剂MnO₂/AC,考察了吸附剂的制备条件及脱硫条件对脱硫效果的影响。研究结果表明,适宜的吸附剂制备条件为,以Mn(NO₃)₂为活性组分前驱物,Mn(NO)₂浸渍液浓度0.15mol/L、常温下浸渍24h、焙烧温度350℃、焙烧时间2h。该吸附剂在静态吸附温度120℃、吸附时间2h、剂油质量比0.10的条件下可使原料油硫的质量分数从628.6×10^-6降至221.5×10^-6,脱硫率达到64.8%;在动态吸附温度60℃、空速1.76h^-1的条件下,初始流出汽油硫的质量分数降至21.8×10^-6,初始脱硫率达到96.5%。     

二次合成Y型杂原子分子筛的吸附脱硫研究

采用液-固相同晶取代反应制备骨架含Ga的Y型分子筛(AlY),研究其吸附脱除硫质量分数为500×10^-6模拟燃料中的硫化物。AlY处理含噻吩、四氢噻吩(THT)、4,6-二甲基二苯并噻吩(4,6-DMDBT)、二苯并噻吩(DBT)、苯并噻吩(BT)和4-甲基二苯并噻吩(4-MDBT)的模拟燃料时的吸附容量分别为7.0、17.4、14.5、16.9、6.9 和5.8mg(S)/g吸附剂。采用密度泛函理论(DFT)中的广义梯度近似方法(GGA)计算各分子中硫原子上的电荷数,噻吩、四氢噻吩、4,6-二甲基二苯并噻吩(4,6-DMDBT)、二苯并噻吩(DBT)、苯并噻吩(BT)和4-甲基二苯并噻吩(4-MDBT)中硫原子上电荷数分别为-0.159、-0.298、-0.214、-0.211、-0.193、-0.188。四氢噻吩和4,6-DMDBT中硫原子上的电子密度大于噻吩中硫原子上的电子密度,这就使得四氢噻吩和4,6-DMDBT中的硫原子与吸附位间的作用会明显大于噻吩中的硫原子与吸附位间的作用。采用AlY处理催化裂化汽油时的脱硫率可达68%。     

流动注射化学发光法测定硫离子

在0.06 mol.L-1硫酸介质中,溴酸钾氧化鲁米诺产生化学发光,硫离子对这一体系的化学发光具有增强作用。据此,结合流动注射技术,提出了一种测定硫离子的方法。线性范围为1.0×10-6～1.0×10-3g.L-1(分为3个浓度区间),检出限(3s/b)为8.0×10-7g.L-1。对1.0×10-4g.L-1硫离子标准溶液进行平行测定,其相对标准偏差(n=11)为3.4%。该方法用于水样中硫离子的测定,并以此样品为基体做回收试验,测得回收率在96.5%～105.0%之间。     

溴加成脱烯反应用于含烯汽油单体烃及族组成的分析

 提出了一种用于汽油组成分析的新方法 ,该方法采用溴加成选择性地转化并检测烯烃 ,解决了单体烃分析中的烷烯混峰问题 ,简化了识谱过程 ,由此通过一个包含极性预柱与非极性分析柱的简单二维体系或者与气相仪 (GC)联用的原子发射光谱检测器 (AED)两种途径均可进行准确度高的单体烃分析。在所选溴加成条件下 ,汽油中烯烃溴化率为 10 0 % ,而烷烃和芳烃保持惰性。处理全过程仅需 12 0s～ 15 0s ,操作简单且重复性好。该处理适用于含烯量为 0～ 10 0 % (体积分数 )的汽油 ,且主要针对含烯较高的催化裂化汽油。     

Synthesis and Characterisation of Hierarchically Structured Titanium Silicalite-1 Zeolites with Large Intracrystalline Macropores

The successful synthesis of hierarchically structured titanium silicalite-1 (TS-1) with large intracrystalline macropores by steam-assisted crystallisation of mesoporous silica particles is reported. The macropore topology was imaged in 3D by using electron tomography and synchrotron radiation-based ptychographic X-ray computed tomography, revealing interconnected macropores within the crystals accounting for about 30 % of the particle volume. The study of the macropore formation mechanism revealed that the mesoporous silica particles act as a sacrificial macropore template during the synthesis. Silicon-to-titanium ratio of the macroporous TS-1 samples was successfully tuned from 100 to 44. The hierarchically structured TS-1 exhibited high activity in the liquid phase epoxidation of 2-octene with hydrogen peroxide. The hierarchically structured TS-1 surpassed a conventional nano-sized TS-1 sample in terms of alkene conversion and showed comparable selectivity to the epoxide. The flexible synthesis route described here can be used to prepare hierarchical zeolites with improved mass transport properties for other selective oxidation reactions.     

干胶法制备钛硅沸石及其催化性能

以四丙基溴化铵为模板剂,以乙二胺(EDA)为碱源,采用干胶法制备了TS-1,并在此基础上引入介孔/大孔模板剂蔗糖而制备出多级孔道TS-1.采用X射线衍射、紫外-可见光谱及N2物理吸附-脱附等手段对所得样品进行了表征,并考察了它们催化噻吩(Th)及苯并噻吩(BT)氧化反应的性能.结果表明,随着釜底部n(EDA)/n(H2O)比的降低,TS-1结晶度、骨架Ti含量及其在Th氧化反应中的催化活性均升高.而当以乙胺和正丁胺为碱源时,TS-1难以晶化.所制备的多级孔道TS-1样品具有介孔/大孔孔道,在Th氧化反应中的催化活性高于TS-1;对于BT的氧化,当n(sucrose)/n(SiO2)为0.35时,制备的多级孔道TS-1样品的催化活性最高,BT脱除率可达100%,而TS-1则无催化活性.     

Selective oxidation of propylene over gold deposited on titanium-based oxides

Gold supported on titanium-based metal oxides can assist the selective partial oxidation of propylene at temperatures from 313 K to 573 K in a gas containing both H₂ and O₂. The preparation method was found to be crucial in controlling the selectivities. In general, impregnation and chemical vapor deposition methods do not produce selective catalysts. Only the deposition-precipitation method makes gold selective to propylene oxide or propanal, suggesting that a strong contact between the gold particles and the titanium ion sites on the support is important. The effect of changing the support was also dramatic; the use of the anatase form of TiO₂ and Ti-MCM-41 results in propylene oxide production, while the rutile structure of TiO₂ caused complete oxidation to CO₂. Microporous crystalline titanium silicates such as TS-1, TS-2, and Ti-β zeolite make gold relatively selective to propanal and of the three TS-1 gives the highest selectivity. These results indicate that the oxidation of propylene in the copresence of H₂ must involve the surface of the supports and that the reaction takes place at the interface perimeter around the gold particles.     

氨基酸辅助合成高活性六配位钛物种的TS-1分子筛

TS-1分子筛是以TO4(T=Si,Ti)四面体为基本单元,通过氧桥连接而形成的具有MFI拓扑结构的微孔晶体材料,其在催化烯烃环氧化、酮类氨肟化、氧化脱硫及芳香烃羟基化等氧化反应中表现出较好的催化活性.目前,提高TS-1分子筛催化性能的方法主要包括:(1)制备纳米和多级孔TS-1分子筛,以提高其扩散传质性能;(2)提高TS-1分子筛的钛含量并抑制锐钛矿相的产生,以增加其催化活性位点.最新研究表明,相比于传统四配位钛物种(TiO4)作为催化活性中心,六配位(TiO6)钛物种在烯烃环氧化反应中具有更高的催化活性,可进一步降低反应活化能,最终实现高效催化转化.然而,TiO6物种结构中的Ti-OH组分,易导致开环反应发生,从而降低环氧化产物的选择性.因此,构筑高活性TiO6物种及调变TiO4/TiO6比例,对提高烯烃转化率及环氧产物选择性具有重要意义.当前,高活性钛物种的结构表征及其构筑已成为研究热点且仍面临挑战.本文协同采用氨基酸辅助合成策略和两步晶化方法,成功地制备出具有TiO4和TiO6物种且无锐钛矿相的多级孔TS-1分子筛.在该协同策略中,两步晶化过程有利于抑制锐钛矿相的形成,而氨基酸的引入对高活性TiO6物种的构筑具有重要作用.氨基酸分子可与钛原料形成螯合物,为TS-1分子筛晶化提供"养料",并有效平衡晶体成核与生长速率及稳定TiO6物种,最终实现制备富含TiO6物种的多级孔TS-1分子筛.相比于传统TiO4物种作为催化活性中心(1-己烯的转化率<25％,环氧化产物选择性>95％),本文所制备的TS-1分子筛(Si/Ti=36.9)因其兼具TiO4和TiO6物种,在1-己烯环氧化反应中表现出更好的催化性能(1-己烯的转化率33％,环氧化产物选择性95％).这是由于TiO4物种不会导致开环反应的发生,因此可以保证较高的环氧产物选择性,而TiO6物种经H2O2活化后,可形成具有更高活性及更小位阻效应的催化中心,极大提高了1-己烯转化率.综上,本文合成策略为构筑具有高活性钛物种及多级孔结构的钛硅分子筛提供了指导作用,为调控硅铝酸盐及硅取代磷酸铝分子筛材料活性位点的含量和分布提供了新思路.     

A rational approach in the design of selective mesoporous adsorbents

Two MCM-41 derived adsorbents have been tailor-made for the separation of silver and copper ions using the hard-soft, acid-base (HSAB) principle as the design guideline. NH2-MCM-41 containing "hard" Lewis base adsorption sites (i.e., RNH2) was prepared for the adsorption of the "hard" Lewis acid, Cu2+, and SH-MCM-41 with a grafted "soft" thiolpropyl base was prepared for the selective removal of Ag+, a "soft" Lewis acid. Single- and binary-component adsorption studies were conducted at different metal concentrations, solution compositions, and pH values. The experimental results showed that SH-MCM-41 has excellent affinity and capacity for silver adsorption and adsorbed only the silver ions with copper remaining in the solution. The selectivity was not affected by the metal concentration and composition, anion, and pH. Under similar experimental conditions, NH2-MCM-41 selectively adsorbed copper from the binary solution. The selectivity of NH2-MCM-41 remained for the copper at different pH values, although the adsorption capacity diminished at lower pH values. The type of anions used affected copper adsorption on NH2-MCM-41 with an increased copper uptake in the presence of the sulfate ions. A simple Freundlich adsorption model was sufficient to describe metal adsorption on SH-MCM-41 and NH2-MCM-41, and the LeVan and Vermeulen model was successfully used to predict the adsorption capacity and selectivity for binary-component adsorptions.     

Monte Carlo模拟预测汽油组分与聚酰亚胺相容性

利用Monte Carlo模拟研究了不同结构的聚酰亚胺与典型汽油组分的相容性.结果表明,3,3′,4,4′-二苯甲酮四羧酸二酐-2,4,6-三甲基对苯二胺( BTDA-3 MPDA)与典型汽油组分的相容性较高,且对噻吩的选择性高于其他结构的聚酰亚胺.在300～500 K温度范围内,BTDA-3MPDA与五种典型汽油组分...     

Kinetics and Mechanism of the Photo-oxidation of Thiophene by O2 Adsorbed on Molecular Sieves

Photochemical oxidation of thiophene in n-octane/water extraction system using O2 as oxidant was studied. The reaction mechanism ofthiophene oxidation was proposed. Results obtained here can be used as the reference for the oxidative desulfurization of gasoline because thiophene is one of the main components containing sulfur in fluid catalytic cracking gasoline. Thiophene dissolved in n-octane was photodecomposed and removed into the water phase at ambient temperature and atmospheric pressure. A 500 W high-pressure mercury lamp （main wave length 365 nm, 0.22 kW/m） was used as light source for irradiation, and air was introduced by a gas pump to supply O2. Thiophene can be photo-oxidized to sulfone, oxalic acid, SO4^2-, and CO2. The desulfurization yield of thiophene in n-octane is 58.9% under photo-irradiation for 5 h under the conditions of air flow at 150 mL/min and V（water）：V（n-octane）=1：1. It can be improved to 92.3% by adding 0.15 g zeoliteartificial into 100 mL reaction system, which is the adsorbent for O2 and thiophene. And under such conditions, the photo-oxidation kinetics of thiophene with O2/zeoliteartificial is first-order with an apparent rate constant of 0.5047 h^-1 and a half-time of 1.37 h. The sulfur content can be depressed from 800 μL/L to less than 62 μL/L.     

The study of thiophene adsorption onto La(III)-exchanged zeolite NaY by FT-IR spectroscopy

Zeolites NaY and LaNaY (ion-exchanged with aqueous lanthanum nitrate solution) were used as adsorbents for removing organic sulfur compounds from model gasoline solutions (without and with toluene) and fluid catalytic cracked gasoline in fixed-bed adsorption equipment at room temperature and atmosphere pressure. The adsorptive selectivity for organic sulfur compounds was significantly increased when Na(+) ions in zeolite NaY were exchanged with lanthanum ions. IR spectra of thiophene adsorption indicate that thiophene is adsorbed onto La(3+) ions via direct S-La(3+) interaction and Na(+) ions via pi-electronic interaction for La(3+)-exchanged zeolite NaY, but only via pi-electronic interaction with Na(+) ions for NaY. The amount of adsorbed thiophene on La(3+)-exchanged zeolite Y was slightly decreased by coadsorption of benzene, but greatly reduced on NaY. The adsorption of thiophene via interaction with La(3+) on La(3+)-exchanged zeolite Y is hardly replaced by benzene coadsorption. The direct S-La(3+) interaction might be the essential reason for the evidently improved adsorptive selectivity of LaNaY for removing organic sulfur compounds from solutions containing large amount of aromatics.     

多酸结构对纳米钛硅TS-1沸石催化氧化脱硫性能的影响

采用浸渍法合成了纳米钛硅TS-1沸石负载的钼系列多金属氧酸盐(POM)复合催化剂,采用扫描电子显微镜(SEM)、傅里叶红外光谱(FT-IR)、固体紫外漫反射(UV-Vis)、X-ray粉末衍射(XRD)、氮气吸附脱附(BET)、³¹P和²⁹Si魔角核磁共振(MAS-NMR)等对催化剂的结构进行表征。 研究结果表明,在低温焙烧或烘干条件下,负载后催化剂多酸的结构保持,钼酸铵高温(550 ℃)焙烧后转变为三氧化钼。 以有机硫化物噻吩(TH)、苯并噻吩(BT)和二苯并噻吩(DBT)的正辛烷溶液为模拟油品评价了催化剂的氧化脱硫性能。 实验结果表明,纳米TS-1沸石载体上不同结构多酸作为脱硫催化剂对硫化物的脱除活性顺序为:Keggin型Mo-POM＞Anderson型Mo-POM＞Dawson型Mo-POM＞Mo-金属氧化物。以上述负载的多酸为催化剂,在反应条件为:V(模拟油)=V(乙醇)=10.0 mL,m(催化剂)=0.2 g,n(H₂O₂)∶n(S)=10∶1,温度60 ℃,硫化物按照由易到难的脱除顺序为TH＞DBT＞BT,与常规的TS-1沸石或者多酸催化剂的脱除顺序存在明显差异。 这是纳米TS-1沸石对于有机硫分子氧化反应的择形效应和POM催化氧化脱硫的电子云密度影响综合作用的结果。 Keggin型Mo-POM催化剂具有良好的循环使用性能,是一类制备方法简单、催化活性高且稳定性好的绿色环保型催化剂。