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Cracking of a Used Lubricant Oil Using NiMo/MCM-41 and the Mixture of Ni/MCM-41 and H-MCM-41 Catalysts
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作者 Falah lip Izul Armunanto Ria Pratama Aristo Tyas 《Journal of Chemistry and Chemical Engineering》 2013年第2期95-101,共7页
Catalytic activities of NiMo/MCM-41 and the mixture of Ni/MCM-41 with H-MCM-41 in cracking used ULO (lubricant oil) have been studied. This work was started by synthesis of aluminosilicate (MCM-41) at ratio of Si/... Catalytic activities of NiMo/MCM-41 and the mixture of Ni/MCM-41 with H-MCM-41 in cracking used ULO (lubricant oil) have been studied. This work was started by synthesis of aluminosilicate (MCM-41) at ratio of Si/AI = 50, using CTAB (cetyltrimethylammonium bromide) as a template, and TMAOH (tetramethylammonium hydroxide) as co-surfactant, where a hydrothermal process at 100 ℃ was conducted for 12 h. Organic compounds were then burned out from the dry solid material by calcination at 540 ℃. Ni/MCM-41 and H-MCM-41 were produced by ion exchange method, followed by reduction and calcination treatments, respectively, while NiMo/MCM-41 was produced by impregnation method followed by calcination. Product of MCM-41 was characterized by XRD (X-ray Diffraction), Fourier FTIR (transform infra red spectrophotometric), TEM (transmission electron microscopic) and BET (brunauer-emmet-teller) methods. Performance of the catalytic activities were shown by both of NiMo/MCM-41 and the mixture of 1:1 of H-MCM-41 and Ni/MCM-41 were mixed with the ULO at ratio of 1:200 (w/v) in a stainless steel reactor, then they were heated at 420 ℃. The products of cracking were analyzed using GC-MS (gas chromatography-mass spectrometry). Results of the work showed that the MCM-41 was successfully synthesized. Using mixture of Ni/MCM-41 and H-MCM-41 catalysts, 56.6% of ULO could be converted to OLP (organic liquid product). However, using NiMo/MCM-41 catalyst only 28.5% OLP could be produced. GC-MS analyses showed that cracking of the ULO at 420 ~C using NiMo/MCM-41 catalyst gave conversion 4.3% and 8.8% to gasoline like and diesel like fractions, respectively, while using mixture of Ni/MCM-41 and H-MCM-41 catalysts, conversion of 12.2% and 14.8% respectively to gasoline like and diesel like fractions were obtained. 展开更多
关键词 NiMo/mcm-41 Ni/mcm-41 h-mcm-41 catalyst cracking.
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铝镧修饰MCM-41介孔分子筛的合成、表征及在乙氧基化反应中的催化性能 被引量:2
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作者 邓启刚 周德瑞 宋伟明 《分子催化》 EI CAS CSCD 北大核心 2006年第2期114-118,共5页
以十六烷基三甲基溴化铵(CTAB)为模板剂,正硅酸乙酯(TEOS)为硅源,乙二胺为碱性介质,水热法合成了硅铝、硅镧及硅(铝+镧)摩尔比为30的Al-MCM-41、La-MCM-41和Al-La-MCM-41介孔分子筛,通过XRD、IR、NH3-TPD吸附脱附、BET、热分析及CCl4吸... 以十六烷基三甲基溴化铵(CTAB)为模板剂,正硅酸乙酯(TEOS)为硅源,乙二胺为碱性介质,水热法合成了硅铝、硅镧及硅(铝+镧)摩尔比为30的Al-MCM-41、La-MCM-41和Al-La-MCM-41介孔分子筛,通过XRD、IR、NH3-TPD吸附脱附、BET、热分析及CCl4吸附等方法对分子筛的晶体结构和表面物性进行了研究,XRD及BET研究结果表明,所合成的分子筛具有典型的六方介孔结构特征及较大的比表面积.NH3-TPD结果表明所合成的介孔分子筛均达到中强酸酸度.将Al-MCM-41、La-MCM-41和Al-La-MCM-41分别用于催化乙氧基化反应,研究结果表明Al-La-MCM-41具有更高的催化活性,Al-La-MCM-41为正辛醇质量的5%,反应温度为120℃,反应压力0.2MPa,n(醇)∶n(环氧乙烷)=1∶3时,正辛醇聚氧乙烯醚产品的收率达92%. 展开更多
关键词 Al-h-mcm-41 乙氧基化反应 介孔分子筛 催化
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SO_3H-MCM-41对丙烯酸和异丁烯加成反应的催化性能 被引量:1
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作者 周峰 汤吉海 +3 位作者 陈献 费兆阳 崔咪芬 乔旭 《石油学报(石油加工)》 EI CAS CSCD 北大核心 2014年第4期629-637,共9页
采用一步水热共缩合法制备了表面磺酸嫁接的介孔分子筛SO3H-MCM-41,采用XRD、N2吸附-脱附、红外吸收光谱、吡啶吸附红外光谱、酸碱滴定等手段对其物理化学性质进行了表征,考察了SO3H-MCM-41对丙烯酸与异丁烯直接加成反应合成丙烯酸叔丁... 采用一步水热共缩合法制备了表面磺酸嫁接的介孔分子筛SO3H-MCM-41,采用XRD、N2吸附-脱附、红外吸收光谱、吡啶吸附红外光谱、酸碱滴定等手段对其物理化学性质进行了表征,考察了SO3H-MCM-41对丙烯酸与异丁烯直接加成反应合成丙烯酸叔丁酯的催化性能,在n(i-Butene)/n(Acrylic acid)=1时,探讨了催化剂制备条件n(Sulfonic acid)/n(Silica),丙烯酸与异丁烯加成反应条件m(t-Butanol)/m(Acrylic acid)、m(Catalyst)/m(Acrylic acid)和反应温度对反应转化率及产物选择性的影响。结果表明,SO3H-MCM-41表面成功嫁接了磺酸基团,嫁接后的分子筛具有纯硅MCM-41分子筛的晶体结构。提高n(i-Butene)/n(Acrylic acid)可以显著提高丙烯酸转化率,而丙烯酸叔丁酯选择性基本保持不变;采用n(Sulfonic acid)/n(Silica)=0.3制备的SO3H-MCM-41催化剂,在反应时间6h、、反应温度50℃、n(i-Butene)/n(Acrylic acid)=2、m(Catalyst)/m(Acrylic acid)=0.01和m(t-Butanol)/m(Acrylic acid)=0.04的条件下,丙烯酸转化率为90.0%,丙烯酸叔丁酯选择性为92.8%,二异丁烯选择性为4.8%。SO3H-MCM-41催化剂重复使用5次其催化活性保持稳定。在工业生产过程中,提高丙烯酸转化率有利于降低丙烯酸与丙烯酸叔丁酯的分离能耗。 展开更多
关键词 SO3h-mcm-41 丙烯酸 异丁烯 丙烯酸叔丁酯 加成反应
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Hβ/MCM-41复合分子筛催化剂上苯甲醚与乙酸酐酰化反应研究 被引量:6
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作者 吉向飞 秦张峰 +2 位作者 董梅 王国富 王建国 《燃料化学学报》 EI CAS CSCD 北大核心 2008年第5期621-624,共4页
以β沸石为硅源,制备了不同硅铝比的Hβ/MCM-41复合分子筛,考察了该复合分子筛对苯甲醚与乙酸酐酰化反应的催化效果,并与介孔MCM-41、微孔Hβ分子筛的催化效果进行了比较,研究了分子筛硅铝比、酸性及孔道结构对酰化反应催化性能的影响... 以β沸石为硅源,制备了不同硅铝比的Hβ/MCM-41复合分子筛,考察了该复合分子筛对苯甲醚与乙酸酐酰化反应的催化效果,并与介孔MCM-41、微孔Hβ分子筛的催化效果进行了比较,研究了分子筛硅铝比、酸性及孔道结构对酰化反应催化性能的影响。结果表明,对于苯甲醚和乙酸酐酰化反应,Hβ/MCM-41复合分子筛具有较好的催化稳定性,反应过程中的积炭量较少,积炭的碳氢比较低。该复合分子筛不仅具有微孔沸石的强酸性,而且具有较大孔径的介孔,产物分子能及时从孔道中扩散出来,催化活性位不易中毒失活。 展开更多
关键词 复合分子筛 hβ/mcm--41 酰化 苯甲醚 乙酸酐
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介孔复合材料C_2H_5-MCM-41的制备及在水样痕量芘测定中的作用 被引量:2
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作者 刘妍 杨富巍 +2 位作者 赵素瑞 白冰峰 王小芳 《化学研究与应用》 CAS CSCD 北大核心 2008年第2期188-192,共5页
The composite mesoporous materials C2H5-MCM-41 are synthesized by multistep method,and its structure is characerized and evaluated.A solid-phase microextraction(SPME) method coupled to HPLC is proposed for the determi... The composite mesoporous materials C2H5-MCM-41 are synthesized by multistep method,and its structure is characerized and evaluated.A solid-phase microextraction(SPME) method coupled to HPLC is proposed for the determination of trace pyrene with C2H5-MCM-41 mesporous materials as the coating of extractor.Extraction time,extraction temperation,stirring rate,ionic strength,and desorption time had been optimized.The liner range is 0.15~150μg·L-1,detection limit is 0.062μg.L-1(S/N=3),whereas the RSD(n=5) range is 0.035%,which suggests that the sample pretreatment method of SPME is fast,convenient,recise,sensitive and solvent-free. 展开更多
关键词 介孔材料 C2h5-mcm-41 固相微萃 高效液相色谱
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有机弱碱体系中氢型硅铝MCM-41介孔分子筛的合成及表征 被引量:25
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作者 林文勇 庞文琴 +2 位作者 魏长平 李冬妹 甄开吉 《高等学校化学学报》 SCIE EI CAS CSCD 北大核心 1999年第10期1495-1498,共4页
以有机胺为碱源合成出硅铝介孔分子筛MCM-41, 并将合成产物的性能与采用传统方法(以氢氧化钠为碱源)合成的产物进行了对比. 所合成产物经焙烧脱除有机表面活性剂后即为氢型. XRD和TEM 结果表明, 所合成的产物骨架具... 以有机胺为碱源合成出硅铝介孔分子筛MCM-41, 并将合成产物的性能与采用传统方法(以氢氧化钠为碱源)合成的产物进行了对比. 所合成产物经焙烧脱除有机表面活性剂后即为氢型. XRD和TEM 结果表明, 所合成的产物骨架具有很高的有序度. 固体核磁共振结果显示, 铝原子以四配位的形式存在于样品的原粉中. 经过高温焙烧, 有少量骨架铝脱出骨架, 转变成六配位形式. 展开更多
关键词 氢型 mcm-41 合成 分子筛 催化剂 介孔
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