稀土改质催化剂对废食用油制备燃料油的影响

利用浸渍法制备稀土改质催化剂,用于废食用油脂催化裂解的裂解气催化改质。考察了催化剂活性组分含量、硅铝比、焙烧温度、改质反应温度对产物组成、烯烃含量及收率的影响。得最佳条件:ZSM-5作为催化剂载体,催化剂活性组分镧稀土含量为6%,催化剂焙烧温度为550℃,改质反应温度为360℃。在最佳条件下催化改质,燃料油烯烃含量降低了34.3%,汽油含量提高了14.36%,轻柴油含量提高了1.67%,重柴油含量下降了6.72%,重油含量下降了2.2%,燃料油总收率提高了7.12%,油品质显著提高。     

在Ni-B非晶态催化剂作用下生物油水相加氢制备饱和醇

采用化学还原法制备了Ni-B和Ni-Co-B非晶态催化剂, 并采用X射线衍射(XRD)、BET比表面积、扫描电子显微镜(SEM)、透射电子显微镜(TEM)和电感耦合等离子体光谱(ICP)进行了结构表征. 结果表明, 在110 ℃及氢冷压4.0 MPa时, 在Ni-B或Ni-Co-B催化下, 丙酮、糠醛和苯酚的转化率和饱和醇的选择性分别达到99.99% 和95.00%以上. 对于Ni-B催化生物油真实体系, 在150 ℃及氢冷压4.0 MPa下, 饱和醇的收率达到47.54%. 温度过高易导致催化剂转晶从而降低反应活性. 为生物油的有效利用和饱和多元醇的制备提供了新思路.     

聚氯乙烯多乙烯多胺树脂催化合成正丁基苯基醚

研究了聚氯乙烯多乙烯多胺树脂催化合成正丁基苯基醚,考察了反应物摩尔比,反应温度,反应时间,催化剂用量等因素对产品收率的影响及催化剂的回收,套用性能,在本实验优化条件下,产品收率达９２％,催化剂回收和重复使用５次,重量未损失。活性未降低。     

改性Fe-Cu催化剂上由合成气合成酮和醇

 采用熔融法制备了三类改性催化剂FeCuVKMn,FeCuVKCe和FeCuVKCo,可用于有效地合成低级酮 和低碳醇. 在一定的温度范围内,CO转化率、C2+OH选择性及酮和醇的收率随反应温度的升高而升高; FeCuVKCo表现出比其他催化剂更宽的活性温度区间; 适量加入助剂可使Fe-Cu催化剂的催化性能显著改善. 催化剂活性及选择性的高低顺序是FeCuVKMn＞FeCuVKCo＞FeCuVKCe＞FeCuVK; 最高活性温度的高低顺序是FeCuVK=FeCuVKCe＞FeCuVKMn＞FeCuVKCo.     

微波条件下ZnCl2改性离子交换树脂催化改质生物油的研究

在微波加热条件下,以732型阳离子交换树脂和ZnCl2改性离子交换树脂为催化剂,添加乙醇为溶剂,对生物油进行催化酯化改质.比较研究了两种催化剂随催化剂用量、反应时间及反应温度改变对生物油改质效果的影响,同时考察了微波加热与传统水浴加热条件下催化剂的活性.结果表明,酯化过程中ZnC12改性离子交换树脂比732型树脂活性有...     

电石渣负载氟化钾的催化酯交换特性研究

通过浸渍法制备以氟化钾为活性体、电石渣为载体的负载型钙基酯交换催化剂,并在借助X射线荧光光谱仪、热分析天平、X射线衍射仪、氮气吸附-脱附仪、扫描电子显微镜以及哈米特指示剂法等手段对催化剂表征,以及气相色谱仪对原料油成分分析的基础上,通过间歇式酯交换实验系统,从催化剂添加量、醇油物质的量比、酯交换温度与时间等影响因素出发,研究了电石渣负载氟化钾催化花生油与甲醇酯交换的特性。电石渣负载氟化钾后,产生KCaF3、CaF2以及KF等新物相,并且在催化剂添加量为5%、反应温度为62℃、反应时间为2 h以及醇油物质的量比为15的酯交换条件下,能够取得91.58%的甘油收率,相比较氢氧化钙和未有活性体负载的电石渣,其催化酯交换性能得到提高。     

改性活性炭负载三聚磷酸二氢铝催化合成苯甲醛乙二醇缩醛

采用硝酸改性活性炭后负载三聚磷二氢铝用于催化合成苯甲醛乙二醇缩醛,通过单因素实验考察醇醛摩尔比、催化剂用量及反应时间等因素对产品收率的影响,并采用正交实验获取较佳工艺条件。 结果表明,该催化反应中,当反应温度为110 ℃时,各因素对收率的影响顺序为:醇醛比>反应时间>带水剂加入量>催化剂用量。 优化反应条件为:苯甲醛0.2 mol,醇醛摩尔比2.5,反应时间75 min,催化剂加入量4%(占反应物总质量),带水剂加入量25 mL,苯甲醛乙二醇缩醛收率86.5%,催化剂经5次重复使用后收率仍大于86.0%。     

负载型CaSO4/离子交换树脂催化合成单十二烷基磷酸酯

采用浸渍法制备了负载型金属盐离子交换树脂催化剂,考察了以磷酸与月桂醇为原料催化合成单十二烷基磷酸酯的催化性能.负载不同金属盐离子对单十二烷基磷酸酯的收率的影响表明,CaSO4负载离子交换树脂催化合成单十二烷基磷酸酯效果最好.研究发现,在CaSO4负载量1.2%,催化剂用量为总反应物质量的3%,反应温度90℃,反应12h工艺条件下,月桂醇的转化率为79.4%,单酯选择性为99.9%;加入环己烷作为带水剂,相同条件下,月桂醇转化率为92.3%,单酯选择性为99.9%,并且催化剂重复使用7次之后,催化性能仍保持不变.     

FCC汽油在Ni-Mo-P/USY催化剂上的降烯烃工艺研究

制备了Ni-Mo-P/USY催化剂,采用透射电镜(TEM)及选区电子衍射(SAED)等手段对催化剂进行表征,证实了Ni、Mo活性组分可以较好聚合于USY载体中,并以抚顺石油二厂FCC汽油为原料,考察在该催化剂上进行的烯烃异构化及芳构化反应,探讨了工艺条件对催化性能的影响,结果表明,P改性后的Ni-Mo-P/USY催化剂比改性前性能大为提高,在反应温度320℃、反应压力2.0MPa、质量空速(WHSV)4.0h-1、氢油比(VH2/VOil)400∶1的条件下,汽油烯烃转化率、液体收率、产品异构化选择性和芳构化选择性分别可以达到62.1%、78.4%、47.2%和14.1%.     

CaO-MgO@CoFe_2O_4磁性固体碱的制备及其大豆油酯交换反应催化性能

以草酸盐为前驱体采用两步法制备了一种以CaO-MgO作为活性组分,以CoFe_2O_4作为磁核的磁性固体碱催化剂,并用于大豆油与甲醇的酯交换反应合成生物柴油。对制备的磁性固体碱催化剂进行了磁滞回线、X-射线衍射(XRD)、CO_2-TPD及透射电镜(TEM)表征。考察了不同核壳物质的量比、焙烧温度、反应温度、反应时间、醇油物质的量比以及催化剂用量等因素对大豆油转化为生物柴油产率的影响。结果表明,采用核壳物质的量比为1∶6、焙烧温度为700℃所制备的CaO-MgO@CoFe_2O_4催化剂,当醇油物质的量比为12、催化剂用量为大豆油质量的1.0%时,在65℃下反应时间3 h,生物柴油收率高达97.1%。该催化剂具有较好的重复利用性能,重复利用四次后生物柴油的收率仍可达90%。     

醇酸树脂热炼过程中分子量分布的研究

<正> 涂料工业中醇酸树脂基料分子量分布的研究,通常采用萃取分级法和沉淀分级法,近年来发展了高速凝胶色谱法。我们曾报道了高效GPC法测定醇酸树脂的分子量分布的方法。本文就醇酸树脂热炼过程产物作了物性表征和研究。 实验所测试样系取自5吨反应釜热炼生产中酯化过程各阶段和反应终点的产物。各品种醇酸树脂的配方见表1。     

两相溶剂萃取黄连木籽油制备生物柴油

以黄连木籽为原料,采用乙醇/异己烷两相不互溶溶剂对其进行萃取处理.考察了乙醇／异己烷体积比、萃取温度和萃取时间对萃取过程的影响.通过实验确定最佳的萃取条件为,黄连木仁粉50 g,乙醇异己烷总体积300 mL,乙醇/异己烷体积比为50∶50,萃取温度40℃,萃取时间30 min.在此条件下,黄连木籽油出油率达到99.5％...     

甲基丙烯酸十二酯精制及其树脂性能研究

对工业级甲基丙烯酸十二酯单体进行了精制提纯,采用悬浮聚合法合成了甲基丙烯酸十二酯树脂。利用傅立叶变换红外光谱(FTIR)对精制前后单体以及树脂的结构进行了表征、利用热分析仪(TG)和差式扫描量热仪(DSC)对树脂的热性能进行了分析,同时研究了精制时碱液浓度对树脂饱和吸油率、吸油速率以及充分溶胀后树脂剩余率的影响。结果表明,精制后单体合成的树脂耐热性能有了明显改善,热降解温度大大提高;精制前后单体合成的树脂,由于杂质存在的缘故,其低温玻璃化转变类型明显不同;经6wt%碱液和8wt%碱液精制后单体的纯度有了明显提高,由其合成的树脂饱和吸油率,吸油速率都有较大提高,甚至接近化学纯单体合成树脂的饱和吸油率。     

Kinetics of the production of chain-end groups and methanol from the depolymerization of cellulose during the ageing of paper/oil systems. Part 1: Standard wood kraft insulation

Recently, the existence of a relation between the rupture of 1,4-β-glycosidic bonds in the cellulose during thermal-ageing of paper/oil systems and the detection of methanol in the oil has been reported for the first time in this journal (Jalbert et al. 2007). The present study addresses the rate constants of the reaction for standard wood kraft papers, two immersed in inhibited naphthenic oil under air (paper/oil weight–volume ratio of 1:18) and one in non-inhibited paraffinic oil under nitrogen (paper/oil weight–volume ratio of 1:30). The isotherms in the range of 60–130 °C show that the initial rate of methanol production markedly increases with temperature and to a lesser extent with the moisture of the specimens (initially between 0.5 and 2.25% (w/w)), similarly to what is noted for the depolymerization through the Ekenstam’s pseudo-zero order model. The Arrhenius expression of the rate constants reveals linear relationships that confirm the dominance of a given mechanism in both cases. A very good agreement is also noted for the activation energy over the entirely paper/oil systems studied (106.9 ± 4.3 and 103.5 ± 3.7 kJ mol^?1 for methanol and scissions, respectively). Furthermore, a comparison of the rate constants $ \left( {k_{{{\text{CH}}_{ 3} {\text{OH}}}} /k_{\text{scissions}} } \right) Recently, the existence of a relation between the rupture of 1,4-β-glycosidic bonds in the cellulose during thermal-ageing of paper/oil systems and the detection of methanol in the oil has been reported for the first time in this journal (Jalbert et al. 2007). The present study addresses the rate constants of the reaction for standard wood kraft papers, two immersed in inhibited naphthenic oil under air (paper/oil weight–volume ratio of 1:18) and one in non-inhibited paraffinic oil under nitrogen (paper/oil weight–volume ratio of 1:30). The isotherms in the range of 60–130 °C show that the initial rate of methanol production markedly increases with temperature and to a lesser extent with the moisture of the specimens (initially between 0.5 and 2.25% (w/w)), similarly to what is noted for the depolymerization through the Ekenstam’s pseudo-zero order model. The Arrhenius expression of the rate constants reveals linear relationships that confirm the dominance of a given mechanism in both cases. A very good agreement is also noted for the activation energy over the entirely paper/oil systems studied (106.9 ± 4.3 and 103.5 ± 3.7 kJ mol⁻¹ for methanol and scissions, respectively). Furthermore, a comparison of the rate constants shows approximately constant values indicating an apparent yield for the methanol of about one-third molecule per every scission for the tests under air (0.27 ± 0.04 for Clupak HD75 and 0.37 ± 0.14 for Munksj? TH70) and even lower for the ones under N₂ (0.12 ± 0.03 for Munksj? E.G.). As expected from a pseudo-zero order model, these values were shown to be consistent with a similar comparison of the amount of CH₃OH and chain-end groups produced under specific time–temperature ageing conditions (168 h at 120 °C). Finally, an additional test carried out with unaged cellulose in contact with a fresh solution of methanol in oil (cellulose/oil weight–volume ratio of 1:18) shows that at equilibrium, over 58% of the species is lost from the solution due to penetration into the fibres. Such results reveal the importance of the species partitioning in establishing the true correspondence between the molecules of CH₃OH produced and the scissions.     

造纸白泥催化花生油与甲醇酯交换的特性研究

从催化剂用量、酯交换温度及时间、醇油物质的量比等影响因素出发,并借助热重、X射线荧光光谱、X射线衍射、氮气吸附与哈米特指示剂等催化剂表征手段,研究造纸白泥催化花生油与甲醇的酯交换特性.造纸白泥通过800 ℃煅烧-常温水合-600 ℃活化处理后,成分以CaO为主、比表面积为7.28 m²/g、碱性强度为9.8相似文献   

THE MECHANISM OF CURE REACTION OF 4,4''''-DIAMINODIPHENYL METHANE WITH TETRAGLYCIDYL 4,4''''-DIAMINODIPHENYL METHANE EPOXY

The cure reaction of tetraglycidyl 4,4'-diaminodiphenyl methane (TGDDM) epoxy resin with 4,4'-diaminodiphenyl methane (DDM) has been studied by using DSC. Instead of one exothermic peak, two exothermic peaks, indicative of a complex reaction mechanism, are shown in the DSC curve of TGDDM-DDM mixtures in nonisothermal cure experiments when the content of DDM is lower than stoichiometric ratio. The result of the kinetic analysis of the cure reaction shows that the activation energy of the lower temperature exotherm peak is about 56 kJ/mol and that of the higher temperature exotherm peak is about 136 kJ/mol. The lower temperature cure reaction peak can be attributed to the primary amine-epoxide and secondary amine-epoxide reactions, and the higher temperature cure reaction peak can be attributed to the epoxide-hydroxy reaction under catalysis of tertiary amine in the TGDDM epoxy resin. Because the network density of the cured epoxy resin is determined by these two reactions, the content of DDM has little effect on the glass transition temperature of cured epoxy resin.     

Rink Amide树脂结构对多肽合成的影响研究

研究了Rink Amide树脂取代度、溶胀度及肽链的长度不同对肽合成收率的影响,并对影响Rink Amide树脂溶胀度的因素进行了研究,结果表明,合成长肽时低取代度、高溶胀度的Rink Amide树脂能获得较好的肽收率。     

单一化学交联与物理化学复合交联高吸油树脂的比较

提出在单一化学交联吸油树脂中引入物理交联的设想，并采用悬浮聚合法了单一化学交联和物理－化学复合交联的聚丙烯酸酯系高吸油树脂，对两种不同树脂的吸油速率，低亲油性单体树脂的吸油性能，最佳单体配比以及化学交联剂含量的影响进行了比较，结果表明物理交联的引入加快了树脂的吸油速率，提高低亲油性单体树脂的吸油能力，并且还使最佳单体配比中低亲油性单体含量增加，同时表明部分物理交联吸油树脂有一最佳化学交联剂含量区。     

采用Pd／树脂催化剂的轻汽油临氢醚化反应研究

研究了催化裂化轻汽油临氢醚化工艺,以降低催化裂化汽油的烯烃含量并提高辛烷值,制备了Pd负载D005阳离子交换树脂催化剂,该催化剂具有同时催化二烯烃选择性加氢和步碳烃与甲醇醚化的功能。考察了遗金属负载量和反应择醚收率的影响,在反应温度343K、压力1．5Mpa,n（甲醇）/ n(叔碳烯烃）比＝1．1、n（氢）／n（二烯）比＝2、液时空速3/h的条件下,醚收率达55．32％。2016h的寿命试验表明,该催化剂活性稳定,可以长周期使用。     

脂肪酸在超临界甲醇中的酯化反应研究

超临界甲醇中的酯化和酯交换反应是利用植物油、动物油或废油脂制备生物柴油的新工艺.它的最大特点是不需要添加催化剂,超临界甲醇既是反应媒介,又是反应物.