KINETIKA REAKSI PADA PROSES PRODUKSI DIETIL ETER DARI ETANOL DENGAN KATALIS H-ZEOLIT

Widayat Widayat; Achmad Roesyadi; Muhammad Rachimoellah

doi:10.14710/reaktor.14.2.101-108

DOI: https://doi.org/10.14710/reaktor.14.2.101-108

KINETIKA REAKSI PADA PROSES PRODUKSI DIETIL ETER DARI ETANOL DENGAN KATALIS H-ZEOLIT

*Widayat Widayat - Jurusan Teknik Kimia Fakultas Teknik Universitas Diponegoro Semarang, Indonesia

Achmad Roesyadi - Jurusan Teknik Kimia Fakultas Teknologi Industri Institut Teknologi Sepuluh Nopember, Indonesia

Muhammad Rachimoellah - Jurusan Teknik Kimia Fakultas Teknologi Industri Institut Teknologi Sepuluh Nopember, Indonesia

Published: 3 Sep 2012.

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}
}

Citation Format:

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

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Keywords: DiEtil Eter; konversi etanol; kinetika reaksi; katalis zeolit

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Article Info

Section: Research Article

Language : EN

In Volume 14, Nomor 2, Oktober 2012

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