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常减压装置高硫油加工的腐蚀与防护 被引量:8
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作者 杨同莲 《化工设备与管道》 CAS 2005年第4期47-49,共3页
阐述了原油性质发生变化后,炼油厂常减压装置的腐蚀研究现状,介绍了主要设备腐蚀类型和防护措施,对其工艺防护和耐蚀材料的选择进行了评述,对现时使用的缓蚀剂进行了比较,并分析其腐蚀机理,提出了设备不同部位的材质选择建议。
关键词 常减压装置 高硫油加工 性质 腐蚀性 缓蚀剂 耐蚀材料
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南京扬子石化公司炼油厂做好加工高硫油防腐蚀安全技术准备
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作者 江镇海 《石油和化工设备》 CAS 2005年第3期40-40,共1页
关键词 南京扬子石化公司炼 高硫油 防腐蚀安全技术 设备腐蚀现象 腐蚀性能 生产装置
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高硫油清洁加工有系列化催化剂
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《气体净化》 2009年第3期31-32,共2页
在我国高硫原油进口和加工量大幅递增之际,中国石化抚顺石油化工研究院相继研发出一批催化裂化(FCC)原料加氢预处理催化剂并形成系列化,为我国炼油企业加工含硫原油、生产清洁燃料提供了技术支撑。
关键词 清洁加工 催化剂 高硫油 中国石化抚顺石化工研究院 加氢预处理 进口 催化裂化
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聚氨酯石墨抗静电防腐涂层在高硫原油中的耐蚀性研究
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作者 雷阿利 冯拉俊 +1 位作者 薛菁 杨士川 《西安石油大学学报(自然科学版)》 CAS 2007年第4期72-75,共4页
针对高硫油对原油储存设备腐蚀严重的实际,选用聚氨酯树脂为成膜物质,石墨为导电介质制备抗静电防腐涂层,采用失重法研究了石墨含量、硫浓度、温度对涂层耐蚀性的影响.结果表明:不舍石墨及ω(石墨)在25%时,涂层质量的增加主要... 针对高硫油对原油储存设备腐蚀严重的实际,选用聚氨酯树脂为成膜物质,石墨为导电介质制备抗静电防腐涂层,采用失重法研究了石墨含量、硫浓度、温度对涂层耐蚀性的影响.结果表明:不舍石墨及ω(石墨)在25%时,涂层质量的增加主要是由聚氨酯活性基团与介质中的硫反应引起,ω(石墨)在55%时涂层质量的增加主要是由渗透引起;不合石墨及ω(石墨)为25%时涂层增重较大,ω(石墨)为55%时涂层增重最大.硫含量增加使不含石墨的涂层质量增加,当ω(石墨)在25%~45%时,涂层质量增加与硫含量无关.温度升高使不含石墨的涂层质量增加,当ω(石墨)为25%~45%时,温度升高涂层质量变化较小.因此,聚氨酯石墨抗静电防腐涂层ω(石墨)为35%~45%时,其耐蚀性最好. 展开更多
关键词 高硫油 聚氨酯 石墨 防腐层 耐蚀性
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加氢裂化装置加工高硫原油存在问题及对策 被引量:1
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作者 胡瑾 陆新华 《河北化工》 2006年第5期36-37,41,共3页
通过对加工高硫油对反应系统、分馏系统、脱硫系统影响的分析,研究加工高硫原油中存在的问题,并针对现有问题对高硫油的加工提出了相应的对策。
关键词 高硫油 加氢裂化 装置 对策
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高硫高酸渣油对焦化装置的腐蚀及对策
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作者 高红利 曾懋辉 《广东化工》 CAS 2012年第15期39-39,50,共2页
近年来,随着炼厂加工高硫高酸劣质油比例的增加,设备腐蚀问题日益突出,给防腐工作提出了新的挑战,文章以焦化装置主要设备与管线的腐蚀情况出发,从多年的防腐工作实践中,总结出了一些宝贵的经验。
关键词 高硫油 延迟焦化装置 腐蚀
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燃油锅炉燃用高硫油的影响及对策 被引量:1
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作者 房鑫 《乡镇企业导报》 2021年第3期256-257,共2页
近年来,某炼化企业自备电厂转烧催化油浆,其硫含量居高不下,到第七年,甚至已经接近0.6%质量百分比.本文就燃用高硫油对锅炉影响表象进行分析,主要从高压蒸汽锅炉的高温过热器区(高温热偶、辐射受热面屏式过热器)的高温硫腐蚀、低温受热... 近年来,某炼化企业自备电厂转烧催化油浆,其硫含量居高不下,到第七年,甚至已经接近0.6%质量百分比.本文就燃用高硫油对锅炉影响表象进行分析,主要从高压蒸汽锅炉的高温过热器区(高温热偶、辐射受热面屏式过热器)的高温硫腐蚀、低温受热面(空气预热器)的露点腐蚀进行分析. 展开更多
关键词 腐蚀 高硫油 露点腐蚀 锅炉 压蒸汽锅炉
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裂解汽油加氢装置高硫含量石脑油开车优化 被引量:1
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作者 许宏伟 左永光 +2 位作者 周尖 张道君 薛新超 《乙烯工业》 CAS 2019年第3期22-25,I0001,共5页
独山子石化公司百万吨乙烯裂解汽油加氢装置引高硫石脑油开车,多次出现开车时产品中的硫含量长时间超标,大幅延长了开车时间。通过对系统操作和催化剂的性能及石脑油中含硫物料的比对分析,找到了问题的根本原因,并通过对改建后的裂解汽... 独山子石化公司百万吨乙烯裂解汽油加氢装置引高硫石脑油开车,多次出现开车时产品中的硫含量长时间超标,大幅延长了开车时间。通过对系统操作和催化剂的性能及石脑油中含硫物料的比对分析,找到了问题的根本原因,并通过对改建后的裂解汽油加氢装置进行优化操作,实现了缩短开车时间和降低能耗的目的。 展开更多
关键词 裂解汽加氢 石脑 开车优化
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裂解高硫石脑油对乙烯装置长周期运行的影响 被引量:2
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作者 王清江 窦洪春 《乙烯工业》 CAS 2011年第4期34-36,4-5,共3页
以高硫石脑油为裂解原料,加工过程中对装置影响较大,裂解气虽能满足工艺要求,但存在高硫石脑油硫含量不稳定、罐内油品不均匀等不确定因素,加之加工装置处理硫化物能力有限,无法满足加工高硫石脑油的要求。文中从高硫石脑油的储运条件... 以高硫石脑油为裂解原料,加工过程中对装置影响较大,裂解气虽能满足工艺要求,但存在高硫石脑油硫含量不稳定、罐内油品不均匀等不确定因素,加之加工装置处理硫化物能力有限,无法满足加工高硫石脑油的要求。文中从高硫石脑油的储运条件、加工工艺参数、工艺调整等方面进行分析,论述乙烯装置加工高硫石脑油实现长周期高负荷运行的方法。 展开更多
关键词 石脑 裂解 乙烯 长周期
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高硫焦代油工程电气调试中的问题及措施
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作者 战明雪 《齐鲁石油化工》 2007年第4期290-292,共3页
针对中国石化齐鲁分公司炼油厂高硫焦代油项目电气部分调试中遇到的问题.及时分析处理,为今后机组调试和机组运行中出现类似问题提供借鉴。
关键词 焦代 调试 电气
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铝钼共渗钢的耐蚀性能研究
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作者 刘文亮 严伟丽 李建留 《石油化工腐蚀与防护》 CAS 2005年第2期6-10,共5页
介绍了铝钼共渗钢及常用材料在加工进口含硫原油的中国石化镇海炼油化工股份有限公司,常减压蒸馏装置现场挂片腐蚀试验和工业应用情况。试验结果表明,高温部位常压塔的腐蚀情况比减压塔严重;在高温部位铝钼共渗钢耐蚀性能优于316L钢,渗... 介绍了铝钼共渗钢及常用材料在加工进口含硫原油的中国石化镇海炼油化工股份有限公司,常减压蒸馏装置现场挂片腐蚀试验和工业应用情况。试验结果表明,高温部位常压塔的腐蚀情况比减压塔严重;在高温部位铝钼共渗钢耐蚀性能优于316L钢,渗铝钢耐蚀性能优于1Cr18Ni9Ti钢而与316L钢相当。低温部位不锈钢材料要慎用。工业应用证明铝钼共渗钢耐蚀性能优良,这对加工进口高硫原油的炼油厂选材有一定的指导意义。 展开更多
关键词 高硫油 不锈钢 铝钼共渗钢 渗铝钢 腐蚀
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搪瓷管空气预热器的应用 被引量:6
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作者 顾雪梅 蔡昌忠 《发电设备》 2003年第4期54-57,共4页
该文针对高硫燃油对锅炉尾部受热面的腐蚀机理及腐蚀速率的影响,对各项防腐综合治理措施进行较为详尽的比较分析,重点介绍了搪瓷管防腐之关键所在———瓷釉配方的选择,并阐述了搪瓷管的制造技术指标和质量鉴定方法。
关键词 锅炉 空气预热器 高硫油 搪瓷管 防腐措施
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RS系列重整预加氢催化剂的开发和应用 被引量:8
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作者 何跃 高晓冬 《石化技术与应用》 CAS 2002年第5期317-318,共2页
介绍了中国石化石油化工科学研究院近年来开发的重整预加氢催化剂RS -1和RS-2 0的性能和工业应用结果。RS-1和RS-2 0具有高的脱硫活性 ,应用于高硫石脑油的加氢精制 ,可以使其在高空速条件下操作 ,性能优于国外同类型催化剂。由于RS催... 介绍了中国石化石油化工科学研究院近年来开发的重整预加氢催化剂RS -1和RS-2 0的性能和工业应用结果。RS-1和RS-2 0具有高的脱硫活性 ,应用于高硫石脑油的加氢精制 ,可以使其在高空速条件下操作 ,性能优于国外同类型催化剂。由于RS催化剂还具有较高的脱氮活性 ,因而还可应用于掺焦化汽油的石脑油的加氢精制。工业应用结果表明 ,RS -1、RS -2 0催化剂活性高、稳定性好 。 展开更多
关键词 催化重整 石脑 加氢精制
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Comprehensive Evaluation of Tahe Medium Gravity Crude 被引量:2
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作者 Li Li Zou Ying Weng Huixin 《China Petroleum Processing & Petrochemical Technology》 SCIE CAS 2008年第2期11-17,共7页
The comprehensive evaluation of Tahe medium gravity crude has demonstrated that this type of crude belongs to a intermediate base sour crude, featuring high vanadium content (103ppm), high carbon residue content, low ... The comprehensive evaluation of Tahe medium gravity crude has demonstrated that this type of crude belongs to a intermediate base sour crude, featuring high vanadium content (103ppm), high carbon residue content, low pour point, and low acid value. Based on the crude processing conditions at SINOPEC Luoyang Petrochemical Branch Company, a proposal on the appropriate process flow scheme for processing Tahe crude oil has been raised with the main ideas presented as follows. The IBP-175 fraction is not an ideal feedstock for catalytic reforming; the 75-250 fraction is a qualified feedstock for zeolite de-waxing; the 140-230 fraction can be used to manufacture the No. 3 jet fuel through appropriate distillation range adjustment and product refining; the 175-350 fraction can be directly used to manufacture No.-10 diesel through proper refining; the atmospheric resid boiling over 350 is not suited to be used as the RFCC feedstock; the 350-520 vacuum distillate oil can be used as the FCC feedstock; and the vacuum residuum boiling over 520 is a good feedstock for manufacture of asphalt. 展开更多
关键词 medium gravity Tahe crude EVALUATION process scheme
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Development of Light Cycle Oil(LCO) Hydrocracking Technology over a Commercial W-Ni Based Catalyst 被引量:9
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作者 Peng Chong Yang Xuejing +4 位作者 Fang Xiangchen Huang Xinlu Cheng Zhenmin Zeng Ronghui Guo Rong 《China Petroleum Processing & Petrochemical Technology》 SCIE CAS 2015年第4期30-36,共7页
Because of its high density and low cetane number, the light cycle oil(LCO) containing heavy aromatics(60%—80%) can hardly be transformed through the conventional hydro-upgrading technology. In this report, a novel L... Because of its high density and low cetane number, the light cycle oil(LCO) containing heavy aromatics(60%—80%) can hardly be transformed through the conventional hydro-upgrading technology. In this report, a novel LCO hydrocracking technology(FD2G) was proposed for the utilization of LCO to manufacture high value-added products. Through the ingenious combination of hydroprocessing catalyst and the hydrocracking process, the high octane gasoline and the ultra-low sulfur diesel(ULSD) blendstocks were produced simultaneously. The influence of catalyst type, reaction temperature, pressure, respectively, on the research octane number(RON) of produced gasoline was studied in a fixed bed hydrogenation reactor. It indicated that high reaction temperature and medium pressure would favor the production of highoctane gasoline through the conversion of bi-aromatic and tri-aromatic hydrocarbons. The typical results of FD2 G technology on commercial units showed that it could produce clean diesel with a sulfur content of less than 10 μg/g and clean gasoline with a research octane number(RON) of up to 92. It would be contributed to the achievement of the maximum profit of a refinery, the FD2 G technology could provide a higher economic efficiency than the other diesel quality upgrading technology under the current gasoline and diesel price system. 展开更多
关键词 LCO hydrocracking high octane gasoline ULSD aromatics
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Fluidized-bed pyrolysis of waste bamboo 被引量:3
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作者 XIAO Gang NI Ming-jiang +4 位作者 HUANG He CHI Yong XIAO Rui ZHONG Zhao-ping CEN Ke-fa 《Journal of Zhejiang University-Science A(Applied Physics & Engineering)》 SCIE EI CAS CSCD 2007年第9期1495-1499,共5页
Bamboo was a popular material substituting for wood, especially for one-off commodity in China. In order to recover energy and materials from waste bamboo, the basic characteristics of bamboo pyrolysis were studied by... Bamboo was a popular material substituting for wood, especially for one-off commodity in China. In order to recover energy and materials from waste bamboo, the basic characteristics of bamboo pyrolysis were studied by a thermogravimetric analyzer. It implied that the reaction began at 190-210℃, and the percentage of solid product deceased from about 25% to 17% when temperature ranged from 400℃ to 700℃. A lab-scale fluidized-bed furnace was setup to research the detailed properties of gaseous, liquid and solid products respectively. When temperature increased from 400℃ to 700℃, the mass percent of solid product decreased from 27% to 17% approximately, while that of syngas rose up from 19% to 35%. When temperature was about 500℃, the percentage of tar reached the top, about 31%. The mass balance of these experiments was about 93%-95%. It indicated that three reactions involved in the process: pyrolysis of exterior bamboo, pyrolysis of interior bamboo and secondary pyrolysis of heavy tar. 展开更多
关键词 BAMBOO PYROLYSIS Fluidized beds SYNGAS TAR
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Novel efficient procedure for biodiesel synthesis from waste oils with high acid value using 1-sulfobutyl-3-methylimidazolium hydrosulfate ionic liquid as the catalyst 被引量:1
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作者 Shuanglan Hu Ying Li Wenyong Lou 《Chinese Journal of Chemical Engineering》 SCIE EI CAS CSCD 2017年第10期1519-1523,共5页
Preparation of biodiesel from waste oils containing 72% of free fatty acids catalyzed by a novel Br?nsted acidic ionic liquid 1-sulfobutyl-3-methylimidazolium hydrosulfate([BHSO_3MIM][HSO_4]) was systematically invest... Preparation of biodiesel from waste oils containing 72% of free fatty acids catalyzed by a novel Br?nsted acidic ionic liquid 1-sulfobutyl-3-methylimidazolium hydrosulfate([BHSO_3MIM][HSO_4]) was systematically investigated.The optimum molar ratio of methanol to waste oils,catalyst amount,reaction temperature and reaction time were 8/1,10%(based on the mass of waste oils),140°C and 6 h,respectively,under which the obtained yield of biodiesel reached 94.9%.Also,[BHSO_3MIM][HSO_4] as a catalyst still retained around 97% of its original catalytic activity after successive re-use of 5 batches(6 h per batch),showing the excellent operational stability.Moreover,the acidic IL [BHSO_3MIM][HSO_4] was able to ef ficiently catalyze conversions of waste oils with different amounts of FFAs(free fatty acids) into biodiesel,and showed tremendous application potential.Therefore,an ef ficient and environmentally friendly catalyst is provided for the synthesis of biodiesel from waste oils with high acid value. 展开更多
关键词 1-Sulfobutyl-3-methylimidazolium hydrosulfate Biodiesel Waste oils with high acid value Catalyst
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数据分析
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作者 嵇丽 魏慧琼 《证券导刊》 2005年第14期80-90,共11页
关键词 数据分析 盈利预测 景气周期 加工量 石化产品 石化行业 分析师 高硫油 扬子石化 齐鲁石化
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Identification and formation of sulfur-containing steroids in sulfur-rich heavy oils in the Jinxian Sag,Bohai Bay Basin,North China 被引量:1
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作者 LU Hong WANG QingTao +4 位作者 JIANG LinXiang ZHANG Hui LIU JinZhong SHENG GuoYing PENG PingAn 《Science China Earth Sciences》 SCIE EI CAS 2013年第11期1953-1961,共9页
High abundant sulfur-containing steroids were identified and detected in saturate hydrocarbon fractions of heavy oil with a high sulfur content in the Jinxian Sag,Bohai Bay Basin,North China.These sulfur-containing st... High abundant sulfur-containing steroids were identified and detected in saturate hydrocarbon fractions of heavy oil with a high sulfur content in the Jinxian Sag,Bohai Bay Basin,North China.These sulfur-containing steroids were structurally merged into the D-ring of steroid nucleus with thiophene ring and/or combined into the C-22 in the side-chain.Based on the previous reports of sulfur-containing steroids with methylthio-steroids and intra-molecular form,four formation mechanisms of sulfur-containing steroids and diagenetic pathway of steroids under S-rich conditions were proposed in this paper according to the double bond positions in the sterene compounds.Hydrogenation and sulfurization both occurred in the diagenetic processes of olefinic bond in the side-chain of steroids:abiogenic chemical hydrogenation of H2S and HS-leads to the formation of regular steranes;a successful sulfurization process leads to the formation of the side-chain sulfur-containing steroids whereas unsuccessful cyclization and/or sulfurization result in the generation of short-chain steranes.This kind of mechanism of hydrogenation/sulfurization of side-chain olefinic bond provides a potential genesis clue for the occurrence of high abundance of short-chain steranes(higher than the common regular steroids,phytane and n-alkanes)in S-rich heavy oils and source rocks in the Jinxian Sag,Bohai Bay Basin,North China. 展开更多
关键词 sulfur-containing steroids short-chain steranes SULFURIZATION hydrogenation C-S bond H2S Jinxian Sag
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