馏分油浆态床加氢处理研究: II FCC柴油加氢工艺条件及动力学研究

对FCC柴油在浆态床柴油加氢催化剂SP25上的加氢工艺条件进行了优化,并考察了加氢脱硫（HDS）和加氢脱氮（HDN）动力学。结果表明,提高反应温度、提高反应压力、增加催化剂的加入量、延长反应时间都能提高催化剂的加氢精制活性,最佳的FCC柴油浆态床加氢工艺条件为,温度350℃、压力6MPa、催化剂加入量6%、反应时间2h。催化剂循环使用性能的考察结果表明,SP25催化剂具有良好的活性稳定性。动力学研究结果表明,FCC柴油的加氢脱硫反应过程可以分为两个阶段。第一阶段为较易脱除的苯并噻吩类（BTs）硫化物的加氢脱硫反应,反应活化能为70.00kJ/mol;第二阶段为较难脱除的二苯并噻吩类（DBTs）硫化物的加氢脱硫反应,反应活化能为85.65kJ/mol。FCC柴油HDN反应的活化能为79.91kJ/mol。烷基取代的二苯并噻吩类硫化物（特别是DMDBTs）是加氢精制反应中最难脱除的含杂原子（S或N）烃类化合物。     

馏分油浆态床加氢处理研究：ⅡFCC柴油加氢工艺条件及动力学研究

对FCC柴油在浆态床柴油加氢催化剂SP25上的加氢工艺条件进行了优化,并考察了加氢脱硫（HDS）和加氢脱氮（HDN）动力学。结果表明,提高反应温度、提高反应压力、增加催化剂的加入量、延长反应时间都能提高催化剂的加氢精制活性,最佳的FCC柴油浆态床加氢工艺条件为,温度350℃、压力6MPa、催化剂加入量6％、反应时间2h。催化剂循环使用性能的考察结果表明,SP25催化剂具有良好的活性稳定性。动力学研究结果表明,FCC柴油的加氢脱硫反应过程可以分为两个阶段。第一阶段为较易脱除的苯并噻吩类（BTs）硫化物的加氢脱硫反应,反应活化能为70．00kJ／mol;第二阶段为较难脱除的二苯并噻吩类（DBTs）硫化物的加氢脱硫反应,反应活化能为85．65kJ／mol。FCC柴油HDN反应的活化能为79．91kJ／mol。烷基取代的二苯并噻吩类硫化物（特别是DMDBTs）是加氢精制反应中最难脱除的含杂原子（S或N）烃类化合物。     

加拿大合成原油减压馏分油及其催化裂化液体产物中含硫化合物分析

应用GC PFPD和GC MS技术对加拿大油砂合成原油（Synthetic Crude Oil，简称SCO）减压馏分油（350 ℃~500 ℃）中的含硫化合物进行定性定量分析。结果表明，所含硫化物主要是C3~7二苯并噻吩，而催化裂化反应后则以短侧链二苯并噻吩为主，还含少量烷基苯并噻吩和烷基噻吩，三者的质量分数分别为82.04%、13.42%和0.56%，均属于难以加氢脱除的含硫化合物。SCO减压馏分油和大港减压馏分油按不同比例混合后进行催化裂化反应，随着加拿大合成原油减压馏分油搀兑比增加，所得液相产物中烷基噻吩和烷基苯并噻吩质量分数逐渐降低，烷基二苯并噻吩相对质量分数增加，4-MDBT是丰度最高的含硫化合物，显示加氢油的特征。随掺兑比的提高，液相产物中总硫质量分数和柴油馏分中硫质量分数逐渐增高，而汽油馏分中硫质量分数逐渐降低。     

催化柴油中硫化物的气相-原子发射光谱分析方法及应用

 建立了催化柴油馏分中各种硫化物类型分布的气相 原子发射光谱分析方法,考察了条件对各种硫化物分离的影响,定性(或归类)了催化柴油中的130多个硫化物,计算了程序升温条件下各种硫化物的保留指数,为不同实验室的定性比较和方法的转让提供了依据。硫化物中的硫在2mg/L～1000mg/L时其质量浓度与峰面积呈较好的线性关系,相关系数达0 997。几种硫化物(苯并噻吩、4 甲基苯并噻吩、二苯并噻吩、4 甲基二苯并噻吩、4,6 二甲基二苯并噻吩)6次测定所得峰面积的相对标准偏差均小于5 0%。当信噪比(S/N)为3时,测得苯并噻吩硫的检出限为0 1mg/L。     

柴油馏分中含硫化合物组成与分布特征

采用毛细管气相色谱/脉冲火焰光度检测器(GC/PFPD,Gas Chromatograph/ Pulsed Flame Photometric Detector)对新疆独山子石化公司炼油厂的五种柴油馏分中的硫化物进行了分析。结果表明,常一线馏分中所含的硫化物主要是C0~4苯并噻吩;常二线馏分中除含有C_1~4苯并噻吩外还含有大量的C_0~3二苯并噻吩及部分未知硫化物;焦化柴油中硫化物组成最为复杂,包含中间馏分油中所有常见的硫化物类型;而催化裂化柴油和加氢柴油中硫化物类型主要为烷基苯并噻吩和烷基二苯并噻吩,其中加氢柴油中的硫化物相对丰度比催化裂化柴油低的多。     

氧化-萃取脱除柴油中噻吩类硫化物研究进展

近年来针对柴油中噻吩类硫化物的脱除问题国内外进行了多种非加氢脱硫技术研究,其中氧化脱硫、萃取脱硫、氧化-萃取脱硫技术是研究较多、具有应用前景的脱硫方法。本文从柴油氧化-萃取脱除噻吩类硫化物的反应机理出发,重点概述了有机酸、酸酐催化体系、离子液体催化体系及分子筛催化体系氧化-萃取脱除噻吩类硫化物获得低硫柴油的最新研究成果,并提出了目前存在的问题及该领域未来的研究方向。     

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%。     

过氧化环己酮对二苯并噻吩的氧化脱硫研究

二苯并噻吩（dibenzothiophene DBT）及其衍生物是重油、减压馏分油及渣油中的主要硫化物。在通常的加氢脱硫中，二苯并噻吩系列是较难脱除的一类有机硫。近年来，以二苯并噻吩系列为模型的深度脱硫研究发展迅速。李建源等对二苯并噻吩及其衍生物为模型的氧化脱硫（Oxidative desulfurization ODS）、加氢脱硫、吸附脱硫及生物脱硫等作了较为详尽的报道。     

过氧化叔戊醇对二苯并噻吩的氧化脱硫研究

二苯并噻吩（DBT）及其衍生物是重油、减压馏分油及渣油中的主要硫化物。其性质稳定，在通常的加氢脱硫中，二苯并噻吩系列是较难脱除的一类有机硫。李建源等对二苯并噻吩及其衍生物为模型物的氧化脱硫（ODS）、加氢脱硫、吸附脱硫及生物脱硫等作了较为详细的综述。     

离子液体1-烷基-3-羧甲基苯并咪唑双三氟甲磺酰亚胺盐的合成及在油品中的脱硫应用

合成并表征了一类新型离子液体1-烷基-3-羧甲基苯并咪唑双三氟甲磺酰亚胺盐,将其与双氧水组合用于脱除模型油中的硫化物.结果表明,当模型油与萃取/催化剂1-辛基-3-羧甲基苯并咪唑双三氟甲磺酰亚胺盐([C_2O_2OBIM][Tf2N])的质量比为5∶1,H_2O_2/S摩尔比为5∶1,于75℃反应1 h后,模型油中二苯并噻吩(DBT)脱硫率为98.8%;脱硫过程符合一级动力学方程,5种硫化物的脱硫速率大小顺序为二苯并噻吩(DBT)4,6-二甲基二苯并噻吩(4,6-DMDBT)苯并噻吩(BT)2,5-二甲基噻吩(2,5-DMT)噻吩(T),其中脱除DBT和BT的反应表观活化能分别为44.16和52.10 k J/mol.该离子液体循环再生使用14次,脱硫率无明显下降.该深度脱硫方法具有操作简便及条件温和的特点.     

Preparation of cerium-loaded Y-zeolites for removal of organic sulfur compounds from hydrodesulfurizated gasoline and diesel oil

Ce(IV)-loaded Y-zeolites (CeY) were prepared for selective removal of the trace amount of organic sulfur compounds from hydrodesulfurization (HDS)-treated diesel oil. The CeY samples can be obtained from NH4-Y-zeolite (NH4Y) using liquid-phase ion-exchange and solid-state ion-exchange methods. The ion-exchange reactions, structures, and selective adsorptions of organic sulfur compounds of the CeY samples were investigated using XRD, IR, XPS, TEM, and GC sulfur analyzer. The organic sulfur compound uptakes strongly depend on the amount and the valency of Ce in the zeolite structure. Ce(IV) shows much higher adsorptive ability than Ce(III). A CeY-S sample prepared by solid-state ion-exchange reaction of NH4Y and Ce(NO3)3 with Ce/NH4 mole ratio of 0.63 at 250 degrees C showed a maximum sulfur uptake from a model solution of HDS-treated gasoline containing thiophene [S = 5 ppm (ppm = mg/L)]. A desulfurization from a HDS-treated diesel oil containing organic sulfur compounds (S = 1.87 ppm) and H2S (S = 0.73 ppm) was investigated with a combination of the CeY-S and a CuO adsorbent for removal of H2S by a batch method. The sulfur content was reduced to below 0.01 ppm for the first time. This method provides a promising desulfurization process to prepare a clean fuel for fuel cells.     

SK Hydrodesulfurization (HDS) Pretreatment Technology for Ultralow Sulfur Diesel (ULSD) Production

SK Corporation of Korea has developed a unique process, SK hydrodesulfurization (HDS) pretreatment technology, to produce ultralow sulfur diesel (ULSD) with pretreatment of the middle-distillate-range petroleum fractions. This technology has been successfully demonstrated through a 1000 barrel/day (B/D) demonstration plant, which has been running since May 2002. This technology is based on the adsorptive removal of a small amount of nitrogen-based natural polar compounds (NPC). Dramatic improvement in deep HDS efficiency is observed with the removal of NPC from the feedstock.SK HDS pretreatment process consists of multiple adsorbers, two stripping columns for desorbent recovery, associated pumps, and overhead system. Middle distillate feed is pretreated prior to HDS process in the adsorbent vessels followed by stripping to remove a small amount of desorbent. The pretreated is then sent to the downstream HDS unit for sulfur removal. The rejected stream with high nitrogen content, about 2vol%, can be either used as a blending stock for heavy petroleum products or processed in other refining units.This paper describes the fundamental principle of the process, discusses the case study results with various feedstocks and operation conditions in pilot plant and demonstration plant, and provides economic assessment data.     

Desulfurization of model and real fuels by extraction and oxidation processes using an indenylmolybdenum tricarbonyl pre-catalyst

Regulations on the permissible levels of sulfur in transportation fuels are becoming ever more strict, with a global shift towards “zero sulfur” fuels, and the revamp of existing hydrodesulfurization (HDS) facilities to meet these lower caps is cost-prohibitive. Metal-catalyzed sulfoxidation chemistry is viewed as an economically viable desulfurization strategy that could complement conventional HDS technology. In the present work, the complex [η⁵-IndMo(CO)₃Me] ( 1 ) (Ind = indenyl) was employed in the catalytic oxidative desulfurization (CODS) of model and real liquid fuels, using aqueous hydrogen peroxide (H₂O₂) as oxidant. After optimization of the CODS reaction parameters (diesel/H₂O₂ ratio, catalyst amount, temperature), a high-sulfur (2000 ppm) model diesel containing benzothiophene, dibenzothiophene, 4-methyldibenzothiophene and 4,6-dimethyldibenzothiophene could be completely desulfurized within 2 hr under solvent-free conditions or in the presence of the ionic liquid 1-butyl-3-methylimidazolium hexafluorophosphate ([BMIM]PF₆) as extraction solvent. The catalyst formed under solvent-free conditions could be recycled without a significant decrease in desulfurization activity. The high performance of the CODS system was verified in the sulfur removal from a commercial untreated diesel fuel with a sulfur content of 2300 ppm, and a jet fuel with a sulfur content of 1100 ppm. Solvent-free CODS in combination with initial/final extraction gave desulfurization efficiencies of 70% for the diesel fuel and 55% for the jet fuel. CODS with [BMIM]PF₆ in combination with initial/final extraction led to a sulfur removal of 95.9% for the diesel fuel, which is one of the best results yet reported for ODS of commercial diesels.     

介孔硅胶在柴油氧化-吸附组合脱硫中的应用研究

以硅胶(SG)为吸附剂,采用自制的双亲催化剂与H₂O₂组成的催化氧化体系将柴油进行氧化,利用固定床动态吸附法考察了硅胶性质、氧化过程及吸附条件等对硅胶吸附脱硫性能的影响,并对硅胶进行了表征。小角XRD和氮气吸脱附结果表明,实验所用硅胶具有介孔结构。吸附脱硫实验结果表明,在油剂比(柴油与吸附剂的体积比)相同时,氧化-吸附脱硫过程脱硫率明显高于吸附脱硫过程脱硫率;选用硅胶作吸附剂,吸附温度为40℃,吸附空速为6.0 h^-1时脱硫效果较好,当油剂比为1时,脱硫率高达94.57%,且该介孔硅胶具有较大的吸附硫容,随油剂比增大下降缓慢,当油剂比增大到15时,脱硫率仍达85.89%。     

Ultra Deep Hydrodesulfurization of Gas Oils Over Sulfide and/or Noble Metal Catalysts

Deep hydrodesulfurization (HDS) of sterically hindered sulfur compounds in gas oils will require enhanced hydrogenation activity to hydrogenate the aromatic rings of the sulfur compounds. Although H₂S is known to inhibit the direct HDS route for most of the sulfided catalysts, its promotion to the hydrogenation and subsequent HDS was newly observed for unsupported MoS₂. This promotion suggests that ultra deep HDS over sulfide catalysts can be achieved along with high metal loading, minimal support-metal interactions and optimal dependence on the Ni species. On the other hand, the strong hydrogenation activity of sulfur-tolerant noble metal catalysts suggests that ultra deep HDS as well as deep aromatics saturation can be achieved. This paper discusses recent catalytic approaches for ultra deep HDS using conventional sulfide catalysts and/or noble metal catalysts, such as the newly developed Pd-Pt/Yb-USY zeolite catalyst.     

柴油非加氢脱硫技术研究中样品的选择

利用气相色谱/原子发射光谱检测器（GC/AED），对小型加氢装置的加氢脱硫柴油样品及氧化/萃取前后样品油中含硫化合物进行了分析，对色谱图中出现的几个可疑峰进行了分析和推测，表明这几个峰是由元素硫产生的，并通过无硫油样中加入硫磺和对样品进行汞洗等实验进行了验证。此外，对于加氢柴油中元素硫产生原因以及对硫质量分数测定和对实验分析的影响，在氧化脱硫等非加氢脱硫实验中样品的选择等问题进行了讨论。     

柴油馏分加氢脱硫动力学及反应器研究进展

当前各国环保法规对柴油中硫的质量分数的限制越来越严格。催化加氢脱硫是实现柴油低硫化的重要途径，动力学和新反应器的研究受到了研究者的广泛关注。本文介绍了柴油馏分中两种典型的难脱除含硫化合物二苯并噻吩和4,6-二甲基二苯并噻吩在各类催化剂上加氢脱硫的反应路径，比较了这两种模型含硫化合物的直接脱硫（DDS）和先加氢再脱硫（HYD）路径相对快慢的影响因素。详细综述了假1级、假2级、快慢1级、n级、L-H以及抑制剂H2S存在下的动力学模型在描述二苯并噻吩类模型化合物及真实油品的加氢脱硫过程中的研究现状，介绍了神经网络在柴油加氢动力学和脱硫率预测方面的研究进展。还对催化精馏、并流-逆流滴流床、两相床反应器等新型加氢脱硫反应器的最新发展作了综述，展望了加氢脱硫动力学及反应器的研究方向和面临的挑战。     

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.