EMIES/p-TsOH型低共熔溶剂的合成及其氧化脱硫性能的研究

通过1-乙基-3-甲基咪唑硫酸乙酯离子液体（EMIES）和对甲苯磺酸（p-TsOH）的混合物制备EMIES/p-TsOH型低共熔溶剂。其结构特征通过红外光谱、氢谱和热重技术进行了分析。并以EMIES/p-TsOH作为催化剂与萃取剂,H₂O₂作为氧化剂研究了其对模拟油中的硫化物的脱除性能。考察了反应温度、n（H₂O₂）/n（S）比、低共熔溶剂加入量及硫化物类型对脱硫效果的影响。在最佳的条件下,模拟油中二苯并噻吩（DBT）、4,6-二甲基二苯并噻吩（4,6-DMDBT）和苯并噻吩（BT）的脱除率分别为96.2%、92.2%和88.8%。经过五次循环使用后,DBT的脱除率仍达到93.6%。对该脱硫体系进行了动力学分析,其表观活化能为66.4kJ/mol。     

Sulfur-Selective Desulfurization of Dibenzothiophene and Diesel Oil by Newly Isolated Rhodococcus erythropolis NCC-1

A dibenzothiophene （DBT）-desulfurizing bacteria strain was isolated from oil-contaminated soils and identified as Rhodococcus erythropolis NCC-1. Strain NCC-1 was found to convert DBT to hydroxybiphenyl （2-HBP） via the 4S pathway and also be able to use organic sulfur compounds other than DBT as a sole sulfur source. The strain could desulfurize 4,6-dimethyldibenzothiophene （4,6-DMDBT）, which is one of the most recalcitrant dibenzothiophene derivatives to hydrodesulfurization. When two type of oils, a model oil [n-hexadecane （n-C16） containing DBT] and a hydrodesulfurized diesel oil with various organic sulfur compounds, were treated with Rhodococcus erythropolis NCC-1 cells, the total sulfur content significantly decreased, from 150 to 20 mg/L for n-C16 and from 554 to 274 mg/L for diesel oil. The newly isolated strain NCC-1 is considered to have good potential for application in the biodesulfurization of fossil fuels.     

利用两种微生物的协同作用进行柴油的深度脱硫

红串红球菌通过4S途径降解二苯并噻吩(DBT)产生 和2-羟基联苯(2-HBP). 和2-HBP的存在对红串红球菌的进一步脱硫有抑制作用, 加入脱 和2-HBP 的菌株可以解除 和2-HBP对红串红球菌脱硫反应的抑制, 使该反应继续向生成产物的方向移动, 从而提高其脱硫率. 在脱硫菌和专一性降解 的水解好氧菌(代号: PYS)的协同作用下可以使高浓度的DBT从1.142 mmol/L降到0.0468 mmol/L, 降解率达到95.9%, 比没有加PYS时提高32%的脱除率. 在油水比为1∶9的条件下, 可以将柴油中的硫从554 mg/mL降到306 mg/mL, 降解率达到44.8%.     

Desulfurization of dibenzothiophene, benzothiophene, and other thiophene analogs by a newly isolated bacterium, Gordonia alkanivorans strain 1B

A novel bacterium, Gordonia alkanivorans strain 1B, was isolated from hydrocarbon-contaminated soil. Assessment of the biodegradation of distinct organic sulfur-compounds, such as dibenzothiophene (DBT), benzothiophene (BT), DBT sulfone, and alkylated tiophenic compounds, as the sole source of sulfure was investigated. G. alkanivorans strain 1B was able to remove selectively the sulfur from DBT while keeping intact the remaining carbon-carbon structure. Orthophenyl phenol (2-hydroxybiphenyl) was the only detected metabolic product. The bacterial desulfurization activity was repressed by sulfate. G. alkanivorans straini 1B consumed 310 μM DBT after 120 h of cultivation, corresponding to a specific desulfurization rate of 1.03 μmol/(g of dry cells·h). When an equimolar mixture of DBT/BT was used as a source of sulfur in the growth medium, G. alkanivorans strain 1B assimilated both compounds in a sequential manner, with BT as the preferred source of sulfur. Only when BT concentration was decreased to a very low level was DBT utilized as the source of sulfur for bacterial growth. Thespecific desulfurization overall rates of BT and DBT obtained were 0.954 and 0.813 μmol/(g of dry cells·h), respectively. The newly isolated G. alkanivorans strain 1B has good potential for application in the biodesulfurization of fossil fuels.     

核黄素光敏化氧化二苯并噻吩的研究

以二苯并噻吩(DBT)的正辛烷溶液模拟柴油、水为溶剂、空气中的O<,2>为氧化剂和核黄素(RF)为光敏剂,研究了DBT在15 W紫外杀菌灯照射下的光化学氧化.结果表明,反应的最佳条件为:核黄素浓度20mg/L,空气流速80-100 mL/min.在该反应条件下反应2 h后,DBT的脱硫率为60%.核黄素是通过O<,2>...     

DESs/SG催化剂的制备及其氧化脱硫性能

通过溶胶-凝胶法将脯氨酸基低共熔溶剂负载到硅胶上制得DESs/SG型催化剂。采用FT-IR、XRD、SEM/EDS及N_2吸附-脱附等手段对催化剂的结构进行表征。结果发现,低共熔溶剂可以成功负载到硅胶中,硅胶的比表面积和孔体积有所下降,而孔径增大。以DESs/SG为吸附剂和催化剂,H_2O_2为氧化剂,研究其对模拟油中的二苯并噻吩的脱除性能,考察了低共熔溶剂负载量、反应温度、n(H_2O_2)/n(S)比、催化剂用量、含硫化合物的类型以及催化剂循环使用次数对脱硫效率的影响。结果表明,在最优脱硫条件下,DESs/SG对二苯并噻吩、4,6-二甲基二苯并噻吩和苯并噻吩的脱硫率分别为97%、96. 5%和46. 4%;催化剂循环使用九次后,催化脱硫效率仍高达89. 4%。     

H2S对NiW/Al2O3和CoMo/Al2O3上二苯并噻吩和4,6-二甲基二苯并噻吩加氢脱硫反应的影响

 考察了H2S对NiW/Al2O3和CoMo/Al2O3上二苯并噻吩(DBT)和4,6-二甲基二苯并噻吩(DMDBT)加氢脱硫反应的影响. 结果表明,H2S同时抑制DBT和DMDBT两种硫化物的加氢脱硫反应,并且对DBT的抑制作用更为明显. 对于NiW/Al2O3和CoMo/Al2O3两种催化剂,H2S抑制了DBT和DMDBT的直接脱硫路径活性; 对于CoMo/Al2O3催化剂上DBT转化中的加氢反应也有抑制作用,但促进了DMDBT转化中加氢反应的进行. NiW/Al2O3催化剂更易受H2S的影响.     

Highly efficient extraction and oxidative desulfurization system using Na7H2LaW10O36⋅32 H2O in [bmim]BF4 at room temperature

Highly efficient, deep desulfurization of model oil containing dibenzothiophene (DBT), benzothiophene (BT), or 4,6-dimethyldibenzothiophene (4,6-DMDBT) has been achieved under mild conditions by using an extraction and catalytic oxidative desulfurization system (ECODS) in which a lanthanide-containing polyoxometalate Na(7)H(2)LnW(10)O(36)?32?H(2)O (LnW(10); Ln = Eu, La) acts as catalyst, [bmim]BF(4) (bmim = 1-butyl-3-methylimidazolium) as extractant, and H(2)O(2) as oxidant. Sulfur removal follows the order DBT>4,6-DMDBT>BT at 30?°C. DBT can be completely oxidized to the corresponding sulfone in 25?min under mild conditions, and the LaW(10)/[bmim]BF(4) system could be recycled for ten times with only slight decrease in activity. Thus, LaW(10) in [bmim]BF(4) is one of the most efficient systems for desulfurization using ionic liquids as extractant reported so far.     

CeO2/NaY催化剂的氧合及其催化氧化脱硫性能

采用等体积浸渍法制备了一系列CeO₂/NaY催化剂,重点考察了焙烧温度和铈负载量对催化剂活性组分结构及性能的影响。通过拉曼（Raman）光谱、X射线衍射（XRD）、低温N₂吸附-脱附（BET）、高分辨透射电子显微镜（HR-TEM）以及氢气程序升温还原（H₂-TPR）等技术对催化剂的结构、形貌和化学性能进行了表征分析。结果表明,焙烧温度与铈负载量对于铈物种在分子筛载体表面及孔道内的分散形态和与载体的相互作用有着重要影响,进而影响催化剂中铈物种的氧合性能与氧化脱硫性能。在常温常压下的氧合性能测试,催化剂最大储氧量为每克催化剂1.44 mmol O₂。在反应温度100 ℃,催化剂用量0.20 g,以正辛烷为溶剂二苯并噻吩初始浓度为500 μg·g^-1的模拟油样20 mL,氧气流量为50 mL·min^-1的条件下,反应240 min二苯并噻吩转化率可达90.10%,二苯并噻吩被氧化为二苯并噻吩砜。因此,发展稀土改性分子筛催化剂,应用于以分子氧为氧化剂的油品氧化深度脱硫,对探究绿色高效的油品氧化脱硫技术具有积极意义。     

一步法制备含W介孔碳材料及其氧化脱硫性能研究

以钨酸钠为钨源,以乙二胺四乙酸二钠为碳源经过高温煅烧制备了含W的介孔碳材料,采用XRD、SEM、FT-IR、BET对含钨的介孔碳材料进行表征。结果表明,煅烧后介孔碳材料的表面形成了粒状含有结晶水的氧化钨(WO_3·H_2O)。相比于纯的介孔碳材料,含钨介孔碳材料的总比表面积减小。以含W介孔碳材料为催化剂,H_2O_2作为氧化剂,1-丁基-3-甲基咪唑氟硼酸盐([BMIM][BF_4])离子液体作为萃取剂,组成萃取-催化氧化脱硫体系(ECODS)并研究其对模拟油中二苯并噻吩脱除效果。考察了氧化钨负载量、反应温度、H_2O_2加入量、催化剂用量、离子液体用量以及不同类型硫化物对二苯并噻吩脱除的影响。在最佳反应条件下,催化剂对二苯并噻吩(DBT)、4,6-二甲基二苯并噻吩(4,6-DMDBT)、苯并噻吩(BT)、噻吩(TH)和真实汽油的脱除率分别达到98.6%、65.6%、61.2%、57.8%和64.3%。催化剂回收利用五次之后脱硫率略有降低,仍高达95.2%。     

NiY分子筛选择性吸附脱硫性能及作用机理

用液相离子交换法制备了NiY分子筛,并用XRD、TEM、ICP、N2吸附和吡啶吸附原位红外技术等表征手段对其进行了表征. 利用固定床、气相色谱-硫发光检测器（GC-SCD）及傅里叶红外光谱（FT-IR）等方法系统研究了NiY分子筛对噻吩、2-甲基噻吩、3-甲基噻吩、四氢噻吩、苯并噻吩、二苯并噻吩、4-甲基二苯并噻吩、4,6-二甲基二苯并噻吩8种有机硫化物的选择性吸附脱硫性能和吸附机理. 结果表明,NiY分子筛对硫化物的穿透吸附硫容量顺序为四氢噻吩﹥苯并噻吩≈二苯并噻吩≈4,6-二甲基二苯并噻吩﹥4-甲基二苯并噻吩﹥2-甲基噻吩≈3-甲基噻吩﹥噻吩,说明有机硫化物的空间位阻效应不是其在NiY分子筛上吸附的决定因素. 红外结果表明,不同硫化物与NiY分子筛的作用机理并不相同,但主要以硫原子与金属离子配位作用（S-M作用）为主. 噻吩及其烷基取代物在NiY吸附剂上表面酸性作用下发生催化反应,噻吩环的共轭体系遭到破坏形成硫化物大分子或聚合物,导致分子筛孔道的堵塞,严重影响吸附剂的吸附脱硫能力. NiY的选择性吸附脱硫性能是硫化物与吸附中心的作用模式及吸附剂表面酸性综合作用的结果.     

有机-无机杂多酸类离子液体催化汽油超声氧化脱硫

合成了一系列有机-无机杂多酸类离子液体, 并将其应用于超声作用下的催化模拟汽油氧化脱硫反应. 结果表明, 在超声波辅助下, 不仅反应时间大大缩短, 而且脱硫效率也大幅提高. 在合成的一系列催化剂中, Zr_0.25[BMIM]HPW₁₂O₄₀表现出最佳的催化活性. 考察了超声波功率、 超声/间隙时间、 催化剂用量、 H₂O₂用量、 反应温度及反应时间等因素对脱硫效果的影响. 以Zr_0.25[BMIM]HPW₁₂O₄₀为催化剂, 在优化的条件下[n(Cat.)=0.008 mmol, V(H₂O₂)=40 μL, V(模拟油)=10 mL, V(乙腈)=1 mL, 温度25 ℃, 时间10 min, 超声功率300 W, 超声时间2 s, 间隙时间1.5 s], 二苯并噻吩(DBT)的脱硫率达到97.8%; 该催化剂循环使用5次后, 脱硫率仍为81.9%; 其对不同硫化物的催化活性顺序为DBT>4,6-二甲基苯并噻吩(4,6-DMDBT)>乙硫醚>苯硫醚>正丁硫醇>甲基苯基硫醚>苯并噻吩(BT)>噻吩.     

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%。     

模拟轻质油品的氧化脱硫

以正庚烷为溶剂，苯并噻吩（BT）、二苯并噻吩（DBT）、4,6-二甲基二苯并噻吩（4,6-DMDBT）作为模型含硫化合物组成模拟轻质油品，在H2O2-HCOOH氧化体系中对模拟轻质油品氧化脱硫进行了研究。考察了氧化剂用量、氧化温度、氧化时间及芳烃、烯烃、含氮化合物的存在等因素对BT、DBT脱除的影响。实验结果表明：在反应温度60 ℃，H2O2∶S＝7∶1（mol/mol）,H2O2∶HCOOH＝1∶1（v/v）,反应时间在40 min的条件下，4,6-DMDBT能全部脱除, DBT、BT的脱除率分别为96% 、58%。向油品中添加芳烃、烯烃、含氮化合物等对BT、DBT的脱除均有不同程度的影响。     

直流电场对红串红球菌NCC-1脱硫效率的影响及电刺激机理的初探

研究了脱硫菌--红串红球菌NCC-1在直流电场作用下的生长及脱硫状况,以及实际柴油体系中的脱硫效率,并对外加弱电流加速脱硫菌生长的机理进行了初探。 实验表明,水相适宜范围的电流密度可以提高脱硫菌的脱硫效率,脱硫菌脱硫的最佳电流密度为0.72 A/m²,该条件下,铂电极培养体系菌体比不加电培养体系提前48 h完全降解0.2 mmol/L二苯并噻吩（DBT）。 比相同电流密度钛电极培养体系菌体提前24 h。 铂电极最佳电流密度下菌体对实际柴油的脱硫率可以达到67.4％,比钛电极培养体系菌体高11.7%,高于不加电24.6%。 经验证,发现引起这种变化的主要原因是水的阴极电解产物吸附氢和氢气的比例不同,其中氢气对摇瓶培养菌体促进作用显著。     

Deep extractive desulfurization of diesel fuels by FeCl3/ionic liquids

The extractive desulfurization of dibenzothiophene（DBT）,benzothiophene（BT）,and 4,6-dimethyldi-benzothiophene （4,6-DMDBT） in model oil was carried out using anhydrous FeCl₃ and 1-methyl-3-octylimidazolium chloride system（[Omim|Cl·2FeCl₃）.This new system exhibited high extractive efficiency and the sulfur removal of DBT in model oil(V_IL/V_oil=1/20) could reach 99.4%at room temperature for 30 min,which was obviously superior to single[Omim]Cl as extractant（22.9%）.When the[Omim|CI·2FeCl₃ was used,the S-removal of 4,6-DMDBT and BT could also be up to 99.3%and 96.2%, respectively.Moreover,the ionic liquid could be recycled five times without a significant decrease in extractive ability.     

MoO3/介孔Al2O3催化氧化脱除模拟油中的硫

以环己烷为溶剂,二苯并噻吩（DBT）、苯并噻吩（BT）、4,6-二甲基二苯并噻吩（4,6-DMDBT）、噻吩（Th）作为模型含硫化合物配制成模拟油,在MoO3/介孔Al2O3-H2O2体系中对模拟油催化氧化脱硫进行了研究. 考察了MoO3负载量、氧化剂用量、催化剂用量、氧化反应温度及反应时间对DBT脱除效果的影响. 实验结果表明：在MoO3负载量为20%,催化剂用量为1.5%,氧化剂H2O2与模拟油中硫的摩尔比为4,反应温度为60℃,反应时间为40分钟时DBT脱除率最高,达99.4%,几乎可以被完全脱除;在此条件下模型化合物的氧化反应活性顺序为：DBT > 4,6-DMDBT >BT>Th.     

Preparation of Partially Hydrogenated 4,6‐Dimethyldibenzothiophenes

The synthesis of three key intermediates of the hydrogenation pathway in the hydrodesulfurization of 4,6‐dimethyldibenzothiophene (4,6‐DM‐DBT; 1 ) is described. The hydrogenated derivatives 1,2,3,4‐tetrahydro‐4,6‐dimethyldibenzothiophene (= 4,6‐dimethyl‐1,2,3,4‐tetrahydrodibenzothiophene; 4,6‐DM‐TH‐DBT; 2 ), 1,2,3,4,4a,9b‐hexahydro‐4,6‐dimethyldibenzothiophene (= 4,6‐dimethyl‐1,2,3,4,4a,9b‐hexahydrodibenzothiophene; 4,6‐DM‐HH‐DBT; 3 ), and dodecahydro‐4,6‐dimethyldibenzothiophene (= 4,6‐dimethylperhydrodibenzothiophene; 4,6‐DM‐PH‐DBT; 4 ) were prepared by direct hydrogenation of 1 . The reactions were carried out in continuous and batch reactors by using metal sulfide as well as noble‐metal catalysts. The influence of the reaction conditions on the formation of the products and the distribution of their stereoisomers was studied in detail. The isomers of the main products were isolated and characterized by NMR, GC/MS/MS, and X‐ray crystal‐structure diffractometry.     

Ti-MWW分子筛催化叔丁基过氧化氢氧化脱硫

以Ti-MWW为催化剂,考察了不同氧化剂对分别含有苯并噻吩、二苯并噻吩和4,6-二甲基二苯并噻吩等有机硫化物模拟油品氧化反应的影响,结果表明,叔丁基过氧化氢对有机含硫化合物的氧化活性明显高于过氧化氢水溶液。以叔丁基过氧化氢为氧化剂,三种噻吩类含硫化合物氧化的难易顺序为二苯并噻吩> 4, 6-二甲基二苯并噻吩> 苯并噻吩,其氧化活性顺序与含硫化合物中硫原子的电子云密度和空间位阻有关。考察了Ti-MWW/叔丁基过氧化氢催化氧化体系对成品柴油的催化氧化脱硫,结果表明,成品柴油中的含硫化合物可被有效地氧化脱除,在优化的反应条件下,经过两次氧化、萃取后,成品柴油中的总硫含量从1015μg/mL降低至11μg/mL,总脱硫率达到99%。     

Effect of the nature of sulfur compounds on their reactivity in the oxidative desulfurization of hydrocarbon fuels with oxygen over a modified CuZnAlO catalyst

The reactivity of thiophene, dibenzothiophene (DBT), and 4,6-dimethyldibenzothiophene (4,6-DMDBT), which are the representatives of the main classes of sulfur compounds that are the constituents of diesel fractions, was studied in the course of their oxidative desulfurization with oxygen on a CuO/ZnO/Al₂O₃ catalyst modified with boron and molybdenum additives. At T ≥ 375°C, the reactivity increased in the order thiophene < DBT < 4,6-DMDBT. The degree of sulfur removal in the form of SO₂ from hydrocarbon fuel, which was simulated by a solution of 4,6-DMDBT in toluene, was 80%. Under the assumption of a first order reaction with respect to sulfur compound and oxygen, the apparent activation energies of the test processes were calculated. An attempt was made to reveal the role of the adsorption of sulfur compounds in the overall process of oxidative desulfurization with the use of X-ray diffraction analysis, X-ray photoelectron spectroscopy, and differential thermal and thermogravimetric analysis with the massspectrometric monitoring of gas phase composition.