BibTex Citation Data :
@article{Reaktor4801, author = {Widayat Widayat and Achmad Roesyadi and Muhammad Rachimoellah}, title = {KINETIKA REAKSI PADA PROSES PRODUKSI DIETIL ETER DARI ETANOL DENGAN KATALIS H-ZEOLIT}, journal = {Reaktor}, volume = {14}, number = {2}, year = {2012}, keywords = {DiEtil Eter; konversi etanol; kinetika reaksi; katalis zeolit}, abstract = { DiEtil Eter diprod uksi dari etanol dengan proses dehidrasi. Penelitian ini bertujuan untuk mempelajari kinetika reaksi proses dehidrasi etanol dengan katalis H-zeolit. Katalis H-zeolit disintesis dengan proses dealuminasi dan kalsinasi dan impregnasi dengan logam Al dan proses reduksi dan kalsinasi. Proses produksi DiEtil Eter dilaksanakan dengan proses adsorpsi dan reaksi katalitik sedangkan proses studi kinetika reaksi menggunakan pendekatan Langmuir-Hinshelwood. Proses analisis kinetika reaksi menggunakan perangkat lunak MATLAB. Model kinetika reaksi proses dehidrasi etanol menjadi DiEtil Eter dan etilen dengan katalis H-zeolit pada konsentrasi umpan etanol 85-95% dan rentang temperatur 140-240oC, dimana reaksi permukaan yang mengontrol reaksi global adalah DiEthyl Ether is produced by using ethanol dehydration process. The objective of this research was to study the reaction kinetic of ethanol dehydration process by H-zeolite catalyst from natural zeolite. The H-zeolite catalyst was prepared by dealumination, calcination, impregnation with Al and reduction processes. DiEthyl Ether production was produced by using adsorption-catalytic reaction. The kinetic study was did with MATLAB software. Kinetic model of ethanol dehydration processes into DiEthyl Ether and ethylene with Hzeolite catalyst and ethanol feed concentration among 85-95% and temperature between 140-240oC under surface reaction is shown by }, issn = {2407-5973}, pages = {101--108} doi = {10.14710/reaktor.14.2.101-108}, url = {https://ejournal.undip.ac.id/index.php/reaktor/article/view/4801} }
Refworks Citation Data :
DiEtil Eter diprod
uksi dari etanol dengan proses dehidrasi. Penelitian ini bertujuan untukmempelajari kinetika reaksi proses dehidrasi etanol dengan katalis H-zeolit. Katalis H-zeolitdisintesis dengan proses dealuminasi dan kalsinasi dan impregnasi dengan logam Al dan prosesreduksi dan kalsinasi. Proses produksi DiEtil Eter dilaksanakan dengan proses adsorpsi dan reaksikatalitik sedangkan proses studi kinetika reaksi menggunakan pendekatan Langmuir-Hinshelwood.Proses analisis kinetika reaksi menggunakan perangkat lunak MATLAB. Model kinetika reaksi prosesdehidrasi etanol menjadi DiEtil Eter dan etilen dengan katalis H-zeolit pada konsentrasi umpanetanol 85-95% dan rentang temperatur 140-240oC, dimana reaksi permukaan yang mengontrol reaksiglobal adalah
DiEthyl Ether is produced by using ethanol dehydrationprocess. The objective of this research was to study the reaction kinetic of ethanol dehydrationprocess by H-zeolite catalyst from natural zeolite. The H-zeolite catalyst was prepared bydealumination, calcination, impregnation with Al and reduction processes. DiEthyl Ether productionwas produced by using adsorption-catalytic reaction. The kinetic study was did with MATLABsoftware. Kinetic model of ethanol dehydration processes into DiEthyl Ether and ethylene with Hzeolitecatalyst and ethanol feed concentration among 85-95% and temperature between 140-240oCunder surface reaction is shown by
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JURNAL REAKTOR (p-ISSN: 0852-0798; e-ISSN: 2407-5973)
Published by Departement of Chemical Engineering, Diponegoro University
