Mohan Varkolu, Hari Babu Bathula, Young-Woong Suh, David Raju Burri, Seetha Rama Rao Kamaraju
{"title":"Ni/SBA-15催化剂上乙酰丙酸加氢反应的研究","authors":"Mohan Varkolu, Hari Babu Bathula, Young-Woong Suh, David Raju Burri, Seetha Rama Rao Kamaraju","doi":"10.1007/s13203-018-0203-z","DOIUrl":null,"url":null,"abstract":"<p>A series of Ni/SBA-15 catalysts were prepared by impregnation method for the hydrogenation of levulinic acid (LA) to γ-valerolactone in a fixed bed reactor at atmospheric pressure. The catalysts were characterized by XRD, TPR, AAS, Pulse chemisorption, SEM-EDAX, TEM, BET Surface area and XPS. The catalyst 30?wt% Ni/SBA-15 exhibited excellent catalytic performance (97% yield) at 250?°C due to the presence of superior number of active surface Ni species. While 30?wt% Ni/SiO<sub>2</sub> catalyst showed lower catalytic activity (87% yield) at about similar conversion. The co-feeding of formic acid (FA) and water (impurities) with levulinic acid was also evaluated over 30?wt% Ni/SBA-15 which yielded excellent levulinic acid conversion. The noteworthy results were obtained at a molar ratio of FA/LA?=?5. The constant catalytic activity during 10?h experiment with an external H<sub>2</sub> flow has showed the sturdiness of the Ni/SBA-15 catalyst.?On the other hand, a slight decrease in conversion as well as yield during the time-on-stream in the absence of external H<sub>2</sub> flow was attributed to the accumulation of carbon species on the catalyst surface.</p>","PeriodicalId":472,"journal":{"name":"Applied Petrochemical Research","volume":"8 3","pages":"153 - 162"},"PeriodicalIF":0.1250,"publicationDate":"2018-06-14","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"https://sci-hub-pdf.com/10.1007/s13203-018-0203-z","citationCount":"5","resultStr":"{\"title\":\"Hydrogenation of levulinic acid with and without external hydrogen over Ni/SBA-15 catalyst\",\"authors\":\"Mohan Varkolu, Hari Babu Bathula, Young-Woong Suh, David Raju Burri, Seetha Rama Rao Kamaraju\",\"doi\":\"10.1007/s13203-018-0203-z\",\"DOIUrl\":null,\"url\":null,\"abstract\":\"<p>A series of Ni/SBA-15 catalysts were prepared by impregnation method for the hydrogenation of levulinic acid (LA) to γ-valerolactone in a fixed bed reactor at atmospheric pressure. The catalysts were characterized by XRD, TPR, AAS, Pulse chemisorption, SEM-EDAX, TEM, BET Surface area and XPS. The catalyst 30?wt% Ni/SBA-15 exhibited excellent catalytic performance (97% yield) at 250?°C due to the presence of superior number of active surface Ni species. While 30?wt% Ni/SiO<sub>2</sub> catalyst showed lower catalytic activity (87% yield) at about similar conversion. The co-feeding of formic acid (FA) and water (impurities) with levulinic acid was also evaluated over 30?wt% Ni/SBA-15 which yielded excellent levulinic acid conversion. The noteworthy results were obtained at a molar ratio of FA/LA?=?5. The constant catalytic activity during 10?h experiment with an external H<sub>2</sub> flow has showed the sturdiness of the Ni/SBA-15 catalyst.?On the other hand, a slight decrease in conversion as well as yield during the time-on-stream in the absence of external H<sub>2</sub> flow was attributed to the accumulation of carbon species on the catalyst surface.</p>\",\"PeriodicalId\":472,\"journal\":{\"name\":\"Applied Petrochemical Research\",\"volume\":\"8 3\",\"pages\":\"153 - 162\"},\"PeriodicalIF\":0.1250,\"publicationDate\":\"2018-06-14\",\"publicationTypes\":\"Journal Article\",\"fieldsOfStudy\":null,\"isOpenAccess\":false,\"openAccessPdf\":\"https://sci-hub-pdf.com/10.1007/s13203-018-0203-z\",\"citationCount\":\"5\",\"resultStr\":null,\"platform\":\"Semanticscholar\",\"paperid\":null,\"PeriodicalName\":\"Applied Petrochemical Research\",\"FirstCategoryId\":\"1085\",\"ListUrlMain\":\"https://link.springer.com/article/10.1007/s13203-018-0203-z\",\"RegionNum\":0,\"RegionCategory\":null,\"ArticlePicture\":[],\"TitleCN\":null,\"AbstractTextCN\":null,\"PMCID\":null,\"EPubDate\":\"\",\"PubModel\":\"\",\"JCR\":\"\",\"JCRName\":\"\",\"Score\":null,\"Total\":0}","platform":"Semanticscholar","paperid":null,"PeriodicalName":"Applied Petrochemical Research","FirstCategoryId":"1085","ListUrlMain":"https://link.springer.com/article/10.1007/s13203-018-0203-z","RegionNum":0,"RegionCategory":null,"ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"","JCRName":"","Score":null,"Total":0}
Hydrogenation of levulinic acid with and without external hydrogen over Ni/SBA-15 catalyst
A series of Ni/SBA-15 catalysts were prepared by impregnation method for the hydrogenation of levulinic acid (LA) to γ-valerolactone in a fixed bed reactor at atmospheric pressure. The catalysts were characterized by XRD, TPR, AAS, Pulse chemisorption, SEM-EDAX, TEM, BET Surface area and XPS. The catalyst 30?wt% Ni/SBA-15 exhibited excellent catalytic performance (97% yield) at 250?°C due to the presence of superior number of active surface Ni species. While 30?wt% Ni/SiO2 catalyst showed lower catalytic activity (87% yield) at about similar conversion. The co-feeding of formic acid (FA) and water (impurities) with levulinic acid was also evaluated over 30?wt% Ni/SBA-15 which yielded excellent levulinic acid conversion. The noteworthy results were obtained at a molar ratio of FA/LA?=?5. The constant catalytic activity during 10?h experiment with an external H2 flow has showed the sturdiness of the Ni/SBA-15 catalyst.?On the other hand, a slight decrease in conversion as well as yield during the time-on-stream in the absence of external H2 flow was attributed to the accumulation of carbon species on the catalyst surface.
期刊介绍:
Applied Petrochemical Research is a quarterly Open Access journal supported by King Abdulaziz City for Science and Technology and all the manuscripts are single-blind peer-reviewed for scientific quality and acceptance. The article-processing charge (APC) for all authors is covered by KACST. Publication of original applied research on all aspects of the petrochemical industry focusing on new and smart technologies that allow the production of value-added end products in a cost-effective way. Topics of interest include: • Review of Petrochemical Processes • Reaction Engineering • Design • Catalysis • Pilot Plant and Production Studies • Synthesis As Applied to any of the following aspects of Petrochemical Research: -Feedstock Petrochemicals: Ethylene Production, Propylene Production, Butylene Production, Aromatics Production (Benzene, Toluene, Xylene etc...), Oxygenate Production (Methanol, Ethanol, Propanol etc…), Paraffins and Waxes. -Petrochemical Refining Processes: Cracking (Steam Cracking, Hydrocracking, Fluid Catalytic Cracking), Reforming and Aromatisation, Isomerisation Processes, Dimerization and Polymerization, Aromatic Alkylation, Oxidation Processes, Hydrogenation and Dehydrogenation. -Products: Polymers and Plastics, Lubricants, Speciality and Fine Chemicals (Adhesives, Fragrances, Flavours etc...), Fibres, Pharmaceuticals.