T. Matsuda, Jinichi Ogawa, H. Kawashima, Motomu Ojima
{"title":"Catalytic Hydroboration in Gas Phase","authors":"T. Matsuda, Jinichi Ogawa, H. Kawashima, Motomu Ojima","doi":"10.1627/JPI1959.18.67","DOIUrl":null,"url":null,"abstract":"A new catalytic hydroboration of olefins in the gas phase has been proposed. The kinetics of the reaction of diborane with ethylene or propylene in the presence of a Pd-carbon catalyst was investigated at 30°C to 50°C The initial rate of the reaction, ri, was expressed by ri=kp1/2BPO, where PB and PO denote the initial partial pressures of diborane and ethylene or propylene, respectively, and k the rate constant. The activation energy was 6 and 1.5kcal/mol for ethylene and propylene, respectively. These activation energies were much smaller than those for noncatalytic hydroboration found in literature. The reaction mechanism was interpreted in terms of the rate-determining step which is the attack of the olefin on the dissociated diborane on the catalyst. The reaction mechanism was further confirmed by the adsorptions of diborane, ethylene and propylene.","PeriodicalId":9596,"journal":{"name":"Bulletin of The Japan Petroleum Institute","volume":"74 1","pages":"67-72"},"PeriodicalIF":0.0000,"publicationDate":"1976-05-25","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"1","resultStr":null,"platform":"Semanticscholar","paperid":null,"PeriodicalName":"Bulletin of The Japan Petroleum Institute","FirstCategoryId":"1085","ListUrlMain":"https://doi.org/10.1627/JPI1959.18.67","RegionNum":0,"RegionCategory":null,"ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"","JCRName":"","Score":null,"Total":0}
引用次数: 1
Abstract
A new catalytic hydroboration of olefins in the gas phase has been proposed. The kinetics of the reaction of diborane with ethylene or propylene in the presence of a Pd-carbon catalyst was investigated at 30°C to 50°C The initial rate of the reaction, ri, was expressed by ri=kp1/2BPO, where PB and PO denote the initial partial pressures of diborane and ethylene or propylene, respectively, and k the rate constant. The activation energy was 6 and 1.5kcal/mol for ethylene and propylene, respectively. These activation energies were much smaller than those for noncatalytic hydroboration found in literature. The reaction mechanism was interpreted in terms of the rate-determining step which is the attack of the olefin on the dissociated diborane on the catalyst. The reaction mechanism was further confirmed by the adsorptions of diborane, ethylene and propylene.