离子液体超酸清洁催化苯的烷基化反应

研究了在具有Lewis酸性的离子液体体系中进行的苯与烯烃及卤代烃的烷基化反应.以氯化1-甲基-3-乙基咪唑(MEIC)、氯化1-丁基吡啶(BPC)、氯化l-甲基-3-丁基咪唑(MBIC)及盐酸三甲胺(TMHC)季铵盐分别与AlCl3原位合成法制备离子液体催化体系.结果表明:以上各种离子液体均有很高的催化活性,反应转化率在较短的时间内达到100%.其中TMHC-A1Cl3离子液体单烷基化选择性达98.6%.与AlCl3相比,催化活性显著提高,生成烷基化产物不溶于离子液体,因而易于分离,催化剂可重复使用.     

二苯醚烷基化反应中酸性离子液体的循环使用

使用酸性离子液体催化二苯醚与十二烯烷基化反应,考察了离子液体的失活原因,提出了循环使用离子液体的解决办法.在二苯醚与十二烯烷基化反应中, Lewis酸性离子液体不能多次循环使用的原因是离子液体与二苯醚相互作用导致具有催化活性的Al2Cl72－分解、流失.改变离子液体的阳离子不能从本质上解决其与二苯醚间的相互作用.适时补加损失量的AlCl3使离子液体的Lewis酸性得以恢复,可以解决体系中酸性离子液体循环使用问题,循环使用8次后产物产率仍保持90％左右.     

Cu对离子液体异丁烷/丁烯烷基化反应选择性的影响研究

合成并表征了[BMIm]Cl-1.8AlCl3-0.5CuCl、[Et3NH]Cl-1.8AlCl3/CuAlCl4等离子液体,考察了含Cu离子液体等酸性催化剂中的异丁烷/丁烯烷基化反应,研究了Cu对离子液体烷基化选择性的影响。结果表明,Cu的引入对离子液体酸性的影响较小,不是反应选择性提高的主要原因,而烷基化过程中CuAlCl5-/CuAlCl4等配合物的存在,以及它们对2-丁烯的络合吸附是改善离子液体催化选择性的关键因素。相同反应条件下,[Et3NH]Cl-1.8AlCl3/CuAlCl4、[BMIm]Cl-1.8AlCl3/CuAlCl4等催化剂的三甲基戊烷选择性最高可达87.5%(质量分数),产物辛烷值100.5,明显优于硫酸、常规氯铝酸离子液体和复合离子液体等烷基化汽油辛烷值。     

离子液体对稠油的改质降黏作用影响因素研究

合成了烷基咪唑型离子液体\[BMIM\]\[AlCl₄\],研究了稠油含硫量、含水量、过渡金属盐、温度等对离子液体进行稠油改质降黏作用的影响。实验结果表明,稠油含一定硫量是进行稠油改质降黏的必要条件。用\[BMIM\]\[AlCl₄\]离子液体对稠油进行有效的改质降黏时,稠油含水量应小于10%。环烷酸镍(NiNaph）与离子液体复配使用对稠油改质降黏具有增效作用。用质量分数为5%的\[BMIM\]\[AlCl₄\]离子液体在一定条件下处理新疆稠油,可使稠油降黏率达到60%,沥青质降低78%。用\[BMIM\]\[AlCl₄\] 离子液体对新疆稠油进行改质降黏的最佳温度为65℃~85℃。     

离子液体的酸性测定及其催化的二苯醚／十二烯烷基化反应

 采用乙腈探针红外光谱法测定了［bmim］Cl／AlCl3类离子液体的酸性．结果表明，乙腈可以区分离子液体的酸类型（Bronsted酸或Lewis酸），同时可以指示离子液体的Lewis酸强度．使用［bmim］Cl／AlCl3类离子液体催化二苯醚与十二烯的烷基化反应，研究了离子液体的酸强度、反应温度和醚烯比对反应的影响，并与AlCl3催化体系进行对比．结果发现，该离子液体对二苯醚与十二烯烷基化反应的催化活性明显高于AlCl3．使用离子液体作催化剂显著提高了烷基化反应的产率，简化了产物的分离与提纯，且对环境友好．当控制反应温度为80℃，原料醚烯摩尔比为7，并采用酸强度适中的离子液体时，目标产物单十二烷基二苯醚的产率接近90％．     

FCC汽油降烯烃助剂的研究

中国车用汽油的突出问题之一是烯烃过高,汽油中烯烃过高将在发动机中产生沉积物,增加发动机有害物排放。催化裂化汽油的烯烃体积分数高以及催化裂化汽油在汽油调和组分中占有过高的比例,是中国目前成品汽油中烯烃体积分数过高的主要原因。国内汽油总量中FCC汽油占80％以上,而FCC汽油的烯烃体积分数为40％～55％。因此降低FCC汽油烯烃体积分数具有重要意义。     

酸性离子液体催化的异丁烷/丁烯烷基化反应研究

以一系列酸性离子液体作为催化剂,考察了异丁烷/丁烯在不同离子液体中催化异丁烷与丁烯的烷基化反应,研究了离子液体在进行酸性和阴阳离子调整后对烷基化反应的影响.其中[MBSIM]OTf类离子液体催化所得目的产物三甲基戊烷含量最高可达69.8%,该类催化体系重复使用8次,催化性能没有明显下降.     

离子液体的酸性测定及其催化的异丁烷／丁烯烷基化反应

 初次采用吡啶红外光谱探针法测定了离子液体的酸性．该方法能鉴别离子液体的Br¨onsted／Lewis酸类型，并可以粗略指示离子液体的Lewis酸强度．将［bmim］Cl／AlCl3类离子液体用于催化异丁烷与丁烯的烷基化反应，考察了酸强度、反应温度、压力和时间对产物分布的影响，并在最优操作条件下与传统的H2SO4催化剂进行了比较．结果表明，离子液体对烷基化反应的催化活性和选择性与H2SO4可比，而且它更容易与产物分离，不经任何处理可循环利用10次．     

USY分子筛催化FCC汽油的烷基化脱硫反应研究

以USY分子筛催化FCC汽油中噻吩类硫化物与烯烃的烷基化反应,采用DL-2B-EE微库仑仪测定反应前后硫分布的变化,考察了USY分子筛的制备条件和烷基化反应温度对其催化性能的影响.实验结果表明,水蒸汽处理温度350℃、水蒸汽处理时间5h,反应温度120℃时,USY分子筛催化剂的比表面积为613m2/g,催化活性最佳,使得FCC汽油中<100℃馏分的硫含量减少至16.92mg/L.水蒸汽流速对USY分子筛催化烷基化反应影响不大.不同处理方法所得USY分子筛的吡啶吸附红外光谱结果表明,具有较多的酸中心的USY分子筛更有利于催化FCC汽油的烷基化脱硫反应.     

复合离子液体碳四烷基化技术开发与应用

碳四烷基化油是车用汽油的理想调和组分,其在汽油中的调和比例伴随汽油质量标准的升级而不断提升.中国石油大学(北京)从2000年开始选定氯铝酸离子液体碳四烷基化研究方向,逐步完成了催化剂研发、离子液体碳四烷基化技术开发与工业示范.研究了氯铝酸离子液体的组成、结构及其催化性能之间的关系,设计合成了兼具高活性和高选择性的复合离子液体催化剂.研究了复合离子液体催化剂的失活机理,开发了催化剂再生方案以及氯铝酸离子液体Lewis酸活性的监控方法,在中试装置上进行了2个月的长周期运行试验,初步完成了复合离子液体碳四烷基化技术的工艺开发.研发了新型的静态混合反应器与旋液分离器,设计建成了包含原料处理、烷基化反应、催化剂再生、产品分离与精制4个系统的工业装置,并获得了优异的工业运行结果.复合离子液体碳四烷基化技术实现了产品和工艺的双绿色化,有着良好的应用前景和推广价值.     

Al2O3孔结构对纳米HZSM-5基催化剂改质FCC汽油性能的影响

采用NH₃-TPD、FT-IR、N₂吸附-脱附等手段对两种不同来源的氧化铝样品进行了表征。结果表明,两种Al₂O₃的总酸量及酸强度没有明显差别,酸类型均以Lewis酸为主,其中,Al₂O₃ (b)的平均孔径及孔体积较大。在固定床微型反应装置上考察了以两种Al₂O₃为载体制备的纳米HZSM-5基催化剂改质全馏分FCC汽油的性能。实验结果表明,以大孔Al₂O₃为载体的HZSM-5基催化剂具有较好的降烯烃、芳构化、异构化活性及稳定性。改性纳米HZSM-5负载的LaNiMo催化剂对FCC汽油的300 h评价结果表明,烯烃饱和率为83%,脱硫率为87%,同时维持了油品的辛烷值。     

Development in the green synthesis of cyclic carbonate from carbon dioxide using ionic liquids

This brief review presents the recent development in the synthesis of cyclic carbonate from carbon dioxide (CO₂) using ionic liquids as catalyst and/or reaction medium. The synthesis of cyclic carbonate includes three aspects: catalytic reaction of CO₂ and epoxide, electrochemical reaction of CO₂ and epoxide, and oxidative carboxylation of olefin. Some ionic liquids are suitable catalysts and/or solvents to the CO₂ fixation to produce cyclic carbonate. The activity of ionic liquid is greatly enhanced by the addition of Lewis acidic compounds of metal halides or metal complexes that have no or low activity by themselves. Using ionic liquids for the electrochemical synthesis of the cyclic carbonate can avoid harmful organic solvents, supporting electrolytes and catalysts, which are necessary for conventional electrochemical reaction systems. Although the ionic liquid is better for the oxidative carboxylation of olefin than the ordinary catalysts reported previously, this reaction system is at a preliminary stage. Using the ionic liquids, the synthesis process will become greener and simpler because of easy product separation and catalyst recycling and unnecessary use of volatile and harmful organic solvents.     

吡啶离子液体催化作用下的FCC汽油烷基化脱硫

合成一种Brønsted酸性离子液体[BPY]HSO₄,采用红外光谱和核磁共振对其进行表征。以[BPY]HSO₄为催化剂,对FCC汽油进行烷基化脱硫,考察反应温度、反应时间和剂油质量比对脱硫效果的影响及脱硫前后FCC汽油性质的变化,并对[BPY]HSO₄进行了再生。结果表明,在反应温度为65 ℃、反应时间为90 min和剂油质量比为0.09的条件下,FCC汽油的硫含量从580.0 μg/g降至6.4 μg/g,脱硫率为98.90%,满足中国国Ⅴ车用汽油硫含量标准(<10 μg/g);脱硫前后硫分布变化表明,在[BPY]HSO₄的催化作用下,前170 ℃馏分油中硫化物大部分转移到后170 ℃重馏分中,重馏分中硫化物可采用加氢方法进行脱除;PONA组成变化表明,烷基化脱硫过程对FCC汽油的烃类组成影响较小,且脱硫前后辛烷值变化不大;[BPY]HSO₄经萃取再生后可循环使用。     

氯铝酸离子液体酸性的吡啶探针红外光谱研究

利用吡啶探针红外光谱法研究了氯铝酸离子液体的酸性,发现当氯铝酸离子液体A lC l3的摩尔分数x为0.4~0.5时,离子液体表现出弱Lew is酸的红外特性。对吡啶探针吸附Lew is酸位A l2C l7-、A lC l4-、A l2C l6和A lC l3的各振动模式红外特征峰峰位进行了归属,通过红外特征峰峰位置和峰面积可以指示离子液体的酸强度。利用吡啶探针递增吸附法考察了吡啶递增吸附对氯铝酸离子液体酸性位的影响。研究发现,当吡啶量增加到一定程度时,Py-A l2C l7-配位络合物容易与吡啶发生反应生成Py-A lC l4-和Py-A lC l3配位络合物,从而导致离子液体的吡啶吸附红外特征峰发生变化。     

Cr改性USY分子筛提高裂化催化剂的异构化性能

在催化裂化过程中,烷烃分子在酸性催化剂表面进行一系列的反应,其中氢转移反应能导致汽油中的烯烃质量分数降低,而异构化、环化、芳构化反应则改善裂化产品的分布,对提高裂化汽油的辛烷值有明显的效果。为了解决我国裂化汽油中烯烃质量分数过高的问题,目前大多数催化裂化装置都采用了降烯烃裂化催化剂,以氢转移反应活性高的REUSY分子筛作为裂化催化剂的活性组分。但由于REUSY分子筛的异构化活性较低,因此裂化汽油的辛烷值有所下降,需要对裂化汽油进行加氢异构化处理。若直接对裂化催化剂进行改性,提高其异构化反应活性,     

Efficient Lewis acid ionic liquid-catalyzed synthesis of the key intermediate of coenzyme Q10 under microwave irradiation

An efficient synthesis of a valuable intermediate of coenzyme Q(10) by microwave-assisted Lewis acidic ionic liquid (IL)-catalyzed Friedel-Crafts alkylation is reported. The acidity of six [Etpy]BF(4)-based ionic liquids was characterized by means of the FT-IR technique using acetonitrile as a molecular probe. The catalytic activities of these ionic liquids were correlated with their Lewis acidity. With increasing Lewis acid strength of the ionic liquids, their catalytic activity in the Friedel-Crafts reaction increased, except for [Etpy]BF(4)-AlCl(3). The effects of the reaction system, the molar fraction of Lewis acid in the Lewis acid ILs and heating techniques were also investigated. Among the six Lewis acid ionic liquids tested [Etpy]BF(4)-ZnCl(2) showed the best catalytic activity, with a yield of 89% after a very short reaction time (150 seconds). This procedure has the advantages of higher efficiency, better reusability of ILs, energy conservation and eco-friendliness. The method has practical value for preparation of CoQ(10) on an industrial scale.     

Highly efficient synthesis of dicoumarols and xanthene derivatives in presence of Brønsted–Lewis acidic ionic liquids catalyst

A series of metal chloride-based acidic ionic liquids have been prepared and used as an efficient catalyst in one-pot multicomponent synthesis of biscoumarins and substituted xanthenes derivatives under solvent-free conditions. Among the acidic ionic liquids, N-methylpyrrolidonium zinc chloride (Hnmp/ZnCl₃)-based Brønsted–Lewis acidic ionic liquids were found to be an effective and recyclable catalyst for a one-pot synthesis of biscoumarins through the domino Knoevenagel–Michael reaction of a variety of aldehydes with 4-hydroxycoumarin in short reaction times. The reactions which occur under relatively mild conditions afforded the biscoumarin derivatives employing a very low loading of catalyst in satisfactory isolated yields and high purity after simple work-up. The Brønsted–Lewis acidic ionic liquid catalyst was reused four times without any variation in yield.     

Thermal degradation of polyethylene and polystyrene from the packaging industry over different catalysts into fuel-like feed stocks

Thermal degradation of waste polymers was carried out as a suitable technique for converting plastic polymers into liquid hydrocarbons, which could be used as feed stock materials. The catalytic degradation of waste plastics (polyethylene and polystyrene) was investigated in a batch reactor over different catalysts (FCC, ZSM-5 and clinoptillolite). The effects of catalysts and their average grain size on the properties of main degradation products (gases, gasoline, diesel oil) are discussed. The temperature range of 410-450 °C was used in the process. Both equilibrium FCC catalyst and natural clinoptilolite zeolite catalyst had good catalytic activity to produce light hydrocarbon liquids, and ZSM-5 catalyst produced the highest amount of gaseous products. Gases and liquids formed in cracking reactions were analyzed by gas chromatography. The liquid products consisted of a wide spectrum of hydrocarbons distributed within the C₅-C₂₈ carbon number range depending on the cracking parameters. The composition of hydrocarbons had linear non-branched structure in case of polyethylene, while from polystyrene more aromatics (ethyl-benzene, styrene, toluene, and benzene) were produced. The yields of volatile products increased with increasing degradation temperature. The olefin content of liquids was measured with an infrared technique and an olefin concentration of 50-60% was observed. The concentration of unsaturated compounds increased with decreasing temperature, and in the presence of catalysts. The activation energies were calculated on the basis of the composition of volatile products. The apparent activation energies were decreased by catalysts and catalyst caused both carbon-chain and double bond isomerisation.     

烯烃在催化裂化催化剂上反应机理的初步研究

在自制的微反-色谱装置上,进行了单体烯烃和催化裂化汽油在不同条件下的催化裂化反应实验。对单体烯烃的裂化反应规律和汽油中的烯烃在半再生催化剂和待生催化剂上的催化裂化反应规律进行对比分析。结果表明,单体烯烃反应中,C6及C6以下的烯烃主要发生骨架异构和双键异构反应,氢转移和直接裂化反应发生的较少。C7以上的烯烃95%以上发生转化,高温下直接裂化生成C3、C4,氢转移和异构化比率较大。汽油中的烯烃转化主要集中在C7以上,烯烃之间存在一定的交互作用,单体烯烃的催化裂化反应规律可以初步预测汽油中烯烃的转化。催化剂上的结焦类型对汽油中的烯烃的转化方式没有影响。     

离子液体的结构及其汽油萃取脱硫性能

用不同金属氯化物与氯代甲基咪唑合成离子液体,采用快原子轰击谱测定了这些离子液体的结构,并评价了这些离子液体对汽油萃取脱硫的能力.实验结果表明,由CuCl合成的离子液体中存在稳定的CuCl-2 ,Cu2Cl-3 和Cu3Cl-4 阴离子.这些阴离子可能通过Cu(I)与S的π络合作用而使离子液体具有较高的萃取脱硫效率.经六次萃取后,汽油中的硫含量可以从 650 μg·g-1降至 20~30μg·g-1.