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All Journal Reaktor Indonesian Journal of Chemistry
Muhammad Rachimoellah
Jurusan Teknik Kimia Fakultas Teknologi Industri Institut Teknologi Sepuluh Nopember Surabaya Jl. Arief Rahman Hakim Kampus Sukolilo Surabaya
Chemical Engineering, Chemistry & Bioengineering Chemistry Control & Systems Engineering Energy Materials Science & Nanotechnology

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PENGARUH WAKTU DEALUMINASI DAN JENIS SUMBER ZEOLIT ALAM TERHADAP KINERJA H-ZEOLIT UNTUK PROSES DEHIDRASI ETANOL Widayat Widayat; Achmad Roesyadi; Muhammad Rachimoellah
Reaktor Volume 13, Nomor 1, Juni 2010
Publisher : Dept. of Chemical Engineering, Diponegoro University

Show Abstract | Download Original | Original Source | Check in Google Scholar | Full PDF (593.546 KB) | DOI: 10.14710/reaktor.13.1.51-57

Abstract

Katalis H-zeolit telah disintesa dari zeolit alam. Proses pembuatan katalis meliputi tahap proses pelakuan kimia, penyaringan dan pencucian, pengeringan dan proses kalsinasi. Penelitian ini bertujuan mempelajari waktu dan sumber bahan baku terhadap karakteristik katalis yang meliputi perbandingan Si/Al, X ray Diffraction (XRD) dan luas permukaan. Hasil penelitian menunjukkan bahwa perlakuan kimia menyebabkan penurunan kadar CaO, MgO dan Na2O karena melarut dalam asam klorida. Perbandingan Si/Al juga menurun dengan meningkatnya waktu operasi dan nilai Si/Al tertinggi pada waktu perlakuan kimia 7 jam. Hasil analisa XRD dari produk katalis tidak dipengaruhi oleh waktu. Luas permukaan spesifik dan volume total pori bernilai tertinggi pada waktu operasi 10 jam sebesar 184,52 m2/gram dan volume total pori 108,243 x 10-3 cc/gram. Hasil uji katalitik menunjukkan bahwa katalis KZ A dan KZ B dapat digunakan untuk proses dehidrasi etanol, yang ditunjukkan adanya produk DiEtil Eter pada proses dehidrasi. Yield DiEtil Eter terbaik diperoleh untuk katalis zeolit KZ A 10 yaitu sebesar 1,78% dan KZ B 15 sebesar 0,28%.
KINETIKA REAKSI PADA PROSES PRODUKSI DIETIL ETER DARI ETANOL DENGAN KATALIS H-ZEOLIT Widayat Widayat; Achmad Roesyadi; Muhammad Rachimoellah
Reaktor Volume 14, Nomor 2, Oktober 2012
Publisher : Dept. of Chemical Engineering, Diponegoro University

Show Abstract | Download Original | Original Source | Check in Google Scholar | Full PDF (151.162 KB) | DOI: 10.14710/reaktor.14.2.101-108

Abstract

DiEtil Eter diproduksi 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 adalahDiEthyl 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
Purification of Curcuminoids from Natural Deep Eutectic Solvents (NADES) Matrices Using Chromatography-Based Separation Methods Orchidea Rachmaniah; Muhammad Rifqy Muhsin; Angga Widya Putra; Muhammad Rachimoellah
Indonesian Journal of Chemistry Vol 21, No 4 (2021)
Publisher : Universitas Gadjah Mada

Show Abstract | Download Original | Original Source | Check in Google Scholar | DOI: 10.22146/ijc.58935

Abstract

Curcuminoids can be successfully extracted from Curcuma zedoaria using natural deep eutectic solvents (NADES) as extraction solvents. However, a mixture of extracted curcuminoids, NADES, and impurities from C. zedoaria was obtained as a slurry at the end of the extraction process. Therefore, further separation and purification were required to obtain the extracted compound in high purity. Herein, two purification methods based on classical column chromatography (CCC) and solid-phase extraction (SPE), were evaluated for the purification of curcuminoids from NADES matrices after extraction. Choline chloride–malic acid–water (CCMA–H2O) and choline chloride–citric acid–water (CCCA–H2O) in the molar ratio of 1:1:18 were selected as NADES matrices due to their high solubility and stabilization capability for curcuminoids. Ethanol-conditioned silica gel (60–200 µm) was applied as the bed resin for CCC, and a C18 cartridge was used for SPE. Acetonitrile/0.1% acetic acid, water/0.1% acetic acid, and iso-propanol/0.1% acetic acid were used as mobile phases for CCC. For SPE, methanol/0.05% acetic acid and water/0.05% acetic acid were applied in the conditioning step, water/0.05% acetic acid in the washing step, and methanol/acetonitrile (1:1) in the eluting step. The SPE method produced higher recovery of curcuminoids from the CCCA–H2O and CCMA–H2O matrices (75.27% and 73.40%, respectively) compared to CCC (51.9% and 61.0%, respectively). After removing the NADES constituents from the crude extract of curcuminoids, recrystallization was attempted.
Co-Authors . Widayat Achmad Roesyadi Angga Widya Putra Muhammad Rifqy Muhsin Rachmaniah, Orchidea