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All Journal Jurnal Bestari Reaktor International Journal of Science and Engineering (IJSE) International Journal of Renewable Energy Development TEKNIK METANA JURNAL KIMIA SAINS DAN APLIKASI Jurnal Ilmu Lingkungan JURNAL TEKNOLOGI KIMIA DAN INDUSTRI Prosiding Seminar Nasional Sains Dan Teknologi Fakultas Teknik Jurnal Bahan Alam Terbarukan Waste Technology Eksergi: Chemical Engineering Journal Techno: Jurnal Penelitian Journal of Engineering and Technological Sciences Majalah Ilmiah MOMENTUM ELKOMIKA: Jurnal Teknik Energi Elektrik, Teknik Telekomunikasi, & Teknik Elektronika International Journal of Artificial Intelligence Research Jurnal Ekonomi dan Bisnis Indonesian Journal of Chemistry Jurnal Aplikasi Teknologi Pangan Indonesia Journal of Halal PRoMEDIA Journal of Innovation in Business and Economics ULIN: Jurnal Hutan Tropis Andalas obstetrics and gynecology journal ASEAN Journal of Chemical Engineering Budimas : Jurnal Pengabdian Masyarakat Jurnal Teknik Kimia Indonesia Jurnal Pengabdian dan Peningkatan Mutu Masyarakat (JANAYU) Jurnal Ilmu Sosial Indonesia (JISI) Jurnal Energi Baru dan Terbarukan Journal of Bioresources and Environmental Sciences Jurnal Riptek Jurnal Profesi Insinyur Indonesia Journal of Bioresources and Environmental Sciences International Journal of Renewable Energy Development Bulletin of Chemical Reaction Engineering & Catalysis JURNAL REKAYASA KIMIA & LINGKUNGAN
. Widayat
Chemical Engineering Department, Faculty Of Engineering, Diponegoro University, Jl. Prof. Soedarto, SH, Tembalang, Semarang 50275
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Evaluation and Modification of Processes for Bioethanol Separation and Production P Sitompul, Johnner; Widayat, Widayat; H. Soerawidjaja, Tatang
International Journal of Renewable Energy Development Vol 1, No 1 (2012): February 2012
Publisher : Center of Biomass & Renewable Energy, Diponegoro University

Show Abstract | Download Original | Original Source | Check in Google Scholar | DOI: 10.14710/ijred.1.1.15-22

Abstract

This paper concerns on process evaluation and modification for bioethanol separation and production by applying pinch technology. Further, the paper is also focused on obtaining a most energy-efficient process among several processes. Three basic process configurations of bioethanol separation and production were selected for this study. The three separations and production systems are Othmer process, Barbet process and a separation process that operates under vacuum condition. Basically, each process is combination of Danish Distilleries process with a separation system yielding 95% (v/v) bioethanol. The production capacity of the plant is estimated about 4 x 107 litre of bioethanol 95% (v/v) per year. The result of the studies shows that the most energy efficient process among the three processes evaluated is the Othmer process, followed by the Barbet process and the process involving vacuum operation. The evaluation also shows that further energy saving can be carried for Barbet and Othmer process configuration when Tmin = 10oC for heat exchange possible.
Potency of Microalgae as Biodiesel Source in Indonesia Hadiyanto, Hadiyanto; Widayat, Widayat; Cahyo Kumoro, Andri
International Journal of Renewable Energy Development Vol 1, No 1 (2012): February 2012
Publisher : Center of Biomass & Renewable Energy, Diponegoro University

Show Abstract | Download Original | Original Source | Check in Google Scholar | DOI: 10.14710/ijred.1.1.23-27

Abstract

Within 20 years, Indonesia should find another energy alternative to substitutecurrent fossil oil. Current use of renewable energy is only 5% and need to be improved up to 17%of our energy mix program. Even though, most of the area in Indonesia is covered by sea, howeverthe utilization of microalgae as biofuel production is still limited. The biodiesel from currentsources (Jatropha, palm oil, and sorghum) is still not able to cover all the needs if the fossil oilcannot be explored anymore. In this paper, the potency of microalgae in Indonesia was analysed asthe new potential of energy (biodiesel) sources.
Ultrasound Assisted Esterification of Rubber Seed Oil for Biodiesel Production Widayat, Widayat; Fajar Tamtomo Kiono, Berkah
International Journal of Renewable Energy Development Vol 1, No 1 (2012): February 2012
Publisher : Center of Biomass & Renewable Energy, Diponegoro University

Show Abstract | Download Original | Original Source | Check in Google Scholar | DOI: 10.14710/ijred.1.1.1-5

Abstract

Production of biodiesel is currently shifting from the first to the second generation inwhich the raw materials are mostly from non-edible type oils and fats. Biodiesel production iscommonly conducted under batch operation using mechanical agitation to accelerate masstransfers. The main drawback of oil esterification is the high content of free fatty acids (FFA) whichmay reduce the yield of biodiesel and prolong the production time (2-5 hours). Ultrasonificationhas been used in many applications such as component extraction due to its ability to producecavitation under certain frequency. This research is aimed to facilitate ultrasound system forimproving biodiesel production process particularly rubber seed oil. An ultrasound unit was usedunder constant temperature (40oC) and frequency of 40 Hz. The result showed that ultrasound canreduces the processing time and increases the biodiesel yield significantly. A model to describecorrelation of yield and its independent variables is yield (Y) = 43,4894 – 0,6926 X1 + 1,1807 X2 –7,1042 X3 + 2,6451 X1X2 – 1,6557 X1X3 + 5,7586 X2X3 - 10,5145 X1X2X3, where X1 is mesh sizes, X2ratio oil: methanol and X3 type of catalyst.
Multi-Feedstocks Biodiesel Production from Esterification of Calophyllum inophyllum Oil, Castor Oil, Palm Oil and Waste Cooking Oil Hadiyanto, H; Aini, Apsari Puspita; Widayat, Widayat; Kusmiyati, Kusmiyati; Budiman, Arief; Roesyadi, Achmad
International Journal of Renewable Energy Development Vol 9, No 1 (2020): February 2020
Publisher : Center of Biomass & Renewable Energy, Diponegoro University

Show Abstract | Download Original | Original Source | Check in Google Scholar | DOI: 10.14710/ijred.9.1.119-123

Abstract

Biodiesel can be produced from various vegetable oils and animal fat. Abundant sources of vegetable oil in Indonesia, such as Calophyllum inophyllum, Ricinus communis, palm oil, and waste cooking oil, were used as raw materials. Multi-feedstock biodiesel was used to increase the flexibility operation of biodiesel production. This study was conducted to determine the effect of a combination of vegetable oils on biodiesel characteristics. Degumming and two steps of esterification were applied for high free fatty acid feedstock before trans-esterification in combination with other vegetable oils. Potassium hydroxide was used as a homogenous catalyst and methanol as another raw material. The acid value of C. inophyllum decreased from 54 mg KOH/gr oil to 2.15 mg KOH/gr oil after two steps of esterification. Biodiesel yield from multi-feedstock was 87.926% with a methanol-to-oil molar ratio of 6:1, temperature of 60 ℃, and catalyst of 1%wt. ©2020. CBIORE-IJRED. All rights reserved
Biodiesel Production from Rubber Seed Oil via Esterification Process Widayat, Widayat; Suherman, S
International Journal of Renewable Energy Development Vol 1, No 2 (2012): July 2012
Publisher : Center of Biomass & Renewable Energy, Diponegoro University

Show Abstract | Download Original | Original Source | Check in Google Scholar | DOI: 10.14710/ijred.1.2.57-60

Abstract

One promise source of alternative energy is biodiesel from rubber seed oil, because the raw materials available in plentiful quantities and can be renewed. In addition, the rubber seed is still lack of utilization, and Indonesia is one of the largest rubbers producing country in the world. The objective of this research is to studied on biodiesel production by esterification process. Parameters used in this study are the ratio of catalyst and temperature and its influence on the characteristics of the resulting biodiesel product. Characterization of rubber seed include acid content number analysis, saponification numbers, density, viscosity, iodine number, type of free fatty acids and triglyceride oils. The results of analysis showed that rubber seed oil content obtained is 50.5%. The results of the GCMS analysis showed that a free fatty acid level in rubber seed is very high. Conversion into bio-diesel oil is obtained by at most 59.91% and lowest 48.24%.
Proses produksi triasetin dari gliserol dengan katalis asam sulfat W Widayat; Hantoro Satriado; A Abdullah; Ika Windrianto K. Handono
Jurnal Teknik Kimia Indonesia Vol 11, No 4 (2013)
Publisher : ASOSIASI PENDIDIKAN TINGGI TEKNIK KIMIA INDONESIA (APTEKIM)

Show Abstract | Download Original | Original Source | Check in Google Scholar | DOI: 10.5614/jtki.2013.12.1.3

Abstract

Triacetin production process from glycerol using sulfuric acid as catalyst.Glycerol can be produced from biodiesel production process with transesterification reaction. Glycerol of this reaction, not fully utilized as raw materials or as chemial products. Triacetate is a product of the esterification reaction of glycerol with acetic acid. Triacetate can be used for food and non-food. The objective of this study was to study the effect of temperature and the ratio of reactants on glycerol conversion on triacetate production process. The experiments were carried in batch process and total volume of glycerol and acetic acid 600 mL, stirring speed of 100 rpm and catalyst of sulphuric acid was 5 %-w glycerol based. The results of the qualitative analysis by means of FTIR confirmed there is Triacetate as product. Increasing of ratio molar of glycerol to acetic acid increased of glycerol conversion. The similar result obtained for temperature. The glycerol conversion was 67.6% and selectivity of triacetate 25%, where obtained using the reaction condition: mole ratio of glycerol to acetic acid 1:7, temperature 120 oC and 50 minutes.Keywords: glycerol, acetate acid, esterification, triacetin, glycerol conversion AbstrakGliserol dapat dihasilkan dari proses produksi biodiesel dari proses transesterifikasi. Gliserol dari proses ini, belum dimanfaatkan secara maksimal sebagai bahan baku maupun sebagai produk jadi. Triasetin atau gliserol triasetin merupakan produk reaksi esterifikasi gliserol dengan asam asetat. Kegunaan triasetin cukup banyak baik untuk keperluan bahan pangan maupun non pangan. Penelitian ini bertujuan untuk mempelajari pengaruh temperatur dan perbandingan reaktan terhadap konversi gliserol dalam proses produksi triasetin. Percobaan dilakukan dengan proses curah, dimana volume total gliserol dan asam asetat sebesar 600 mL, kecepatan pengadukan 100 rpm dan katalis asam sulfat adalah 5 %-b gliserol. Hasil analisis kualitatif dengan alat FTIR menunjukkan adanya produk triasetin, dimana kesesuaian dengan bahan standar triasetin cukup tinggi. Peningkatan perbandingan gliserol dengan asam asetat akan meningkatkan konversi gliserol. Demikian juga dengan peningkatan temperatur juga akan meningkatkan konversi gliserol. Hasil yang terbaik diperoleh pada perbandingan mol pereaksi gliserol dan asam asetat 1:7 temperatur 120 oC, waktu 50 menit dengan nilai konversi sebesar 67,6% dan selektivitas sebesar 25%. Kata kunci: gliserol, asam asetat, esterifikasi, triasetin, konversi gliserol
Kinetic study of the utilisation of different substrates to lactic acid using Lactobacillus delbrueckii A Abdullah; Hanapi bin Mat; W Widayat
Jurnal Teknik Kimia Indonesia Vol 4, No 1 (2005)
Publisher : ASOSIASI PENDIDIKAN TINGGI TEKNIK KIMIA INDONESIA (APTEKIM)

Show Abstract | Download Original | Original Source | Check in Google Scholar | DOI: 10.5614/jtki.2005.4.1.4

Abstract

AbstractLactic acid fermentation includes several reactions in association with the microorganism growth. A kinetic study was performed of the utilisation of multiple substrates to lactic acid using Lactobacillus  delbrueckii. Batch fermentation was performed to study effect of different substrates such as glucose, fructose and sucrose. The objective of this research is to study kinetics grow microbial. An anaerobic fermentation were studied in 3 litres stirred fermentor (Biostat B Model) with working volume of 1 liter: temperature = 40ºC, pH=6.0, inoculums size= 5%, sugar concentration= 20 g/L. During the first hours of fermentation, glucose and fructose accumulated in the medium and the rate of hydrolysis of sucrose to glucose and fructose was faster than conversion of these substrate. The maximum concentration of glucose and fructose was 5.82 and 5.14 g/L respectively. The sucrose, glucose, and fructose consumption completely utilized at 56, 68, and 104 hours, respectively. Kinetic parameter for maximum specific growth rate in glucose, fructose and sucrose is 0.083, 0.024, and 0.024 (h-1), respectively. The saturation constant is 4.64, 3.41, and 1.36 g/L.Keywords: Kinetic Study, Sugars, Lactic Acid, Maximum Specific Growth Rate, Saturation Constant AbstrakFermentasi asam laktat melibatkan banyak reaksi dalam pertumbuhan mikroorganisme. Studi kinetika reaksi tentang kinerja penggunaan berbagai subtrat untuk memproduksi asam laktat dengan Lactobacillus delbrueckii.Subtrat yang digunakan adalah glukosa, fruktosa, dan sukrosa, dengan proses fermentasi curah. Penelitian ini bertujuan memepelajari kinetika pertumbuhan mikroba. Fermentasi anaerobik dilakukan dalam fermentor 3 liter (Biostat B Model) dengan volume total 1 liter, temperatur = 40ºC, pH= 6.0, konsentrasi inokulum = 5%, konsentrasi gula = 20 g/L. Selama satu jam pertama fermentasi, glukosa dan fruktosa diakumulasi dalam medium dan laju reaksi hidrolisis sukrosa menjadi glukosa dan fruktosa sangat cepat dibandingkan dengan konversi substrat ini. Konsentrasi glukosa dan fruktosa adalah 5.82 dan 5.14 g/L. Waktu yang dibutuhkan sukrosa, glukosa dan fruktosa masing-masing adalah 56, 68, dan 104 jam. Parameter kinetika untuk laju pertumbuhan spesifik maksimum dalam medium glukosa, fruktosa, dan sukrosa masing-masing adalah 0.083, 0.024, dan 0.024 (h-1). Konstanta saturasi adalah 4.64, 3.41, dan 1.36.Kata Kunci:  Kinetika Reaksi, Gula, Asam Laktat, Laju Pertumbuhan Spesifik Maksimum, Konstanta Saturasi
Kinetic Study on Ultrasound Assisted Biodiesel Production from Waste Cooking Oil Widayat Widayat; Haris Nu'man Aulia; H Hadiyanto; Setia Budi Sasongko
Journal of Engineering and Technological Sciences Vol. 47 No. 4 (2015)
Publisher : Institute for Research and Community Services, Institut Teknologi Bandung

Show Abstract | Download Original | Original Source | Check in Google Scholar | DOI: 10.5614/j.eng.technol.sci.2015.47.4.3

Abstract

The objective of this research was to study  a kinetic model of biodiesel production from waste cooking oil assisted by ultrasound power. The model considered the biodiesel production process as a 2nd order reversible reaction, while its kinetic parameters were estimated using MATLAB, based on data extracted from Hingu, et al. [1]. The data represented experiments under low-frequency ultrasonic wave (20 kHz) and variations of temperature, power, catalyst concentration, and alcohol-oil molar ratio. Statistical analysis showed that the proposed model fits well to the experimental data with a determination coefficient (R2) higher than 0.9.
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
Co-Authors A Abdullah A Abdurrakhman Abdullah Abdullah Achmad Roesyadi Achmad Roesyadi Achmad Wildan ADE ARTA, MOCHAMAD ZAINUDIN Adi Darmawan Adit Rizky Wicaksono Afriani, Nurfika Agus Suprihanto Ahmad Juanda Ahmad Ni’matullah, Albaari Aini, Apsari Puspita Aji Baharsyah Aji Prasetyaningrum Aji, Satriyo Akbar Asfar, A.M. Iqbal Al-Baari, Ahmad N Al-Baarri, Ahmad Ni'matullah Al-Baarri, Ahmad Ni’matullah Alfareza, Muhammad Ircham Almaas Salwa, Diah Ayu Andi Friadi Andika Pradifan Andrew Bryano Kermite, Andrew Bryano Andri Cahyo Kumoro Andri Cahyo Kumoro Andrianto, Novian Andry Anggoro Arahim Anggra Widhi Anggra Widhi Anik Sarminingsih, Anik Annisa Metantya Maharani Ari Eko Prasetyo Ari Eko Prasetyo Ariadi, Ariadi Arianti Nuur Annisa Arief Budiman Aris Triwiyatno Arwan, Berriandi Aulia, Haris Nu’man B Budiyono Bacthiar, Hafni Bagus Agang Sudrajat Bakti Jos Bambang Cahyono Banowati, Tria Nita Berkah Fajar Tamtomo kiono Bernike Vemmialia Jonfita Budi Warsito Budianto, Irawan Arief Catur Pramono D. Ingrid A D. Soetrisnanto Dani Puji Utomo Danny Soetrisnanto DENNY SANJAYA Devina Ingrid A. Dita Ayu Sofiati Driastuti, Faradilla Dyah Hesti Wardhani Edward, Leonardo Ela, Hulasoh Elijah Syarief Elysia, Alvina Enda Merizki br Ginting Fauzandy Husna Setyanto Ferdy D, Erbert H Hadiyanto H M Rachimoellah H Satriadi H. Satriadi H. Satriadi Hadiyanto Hadiyanto Hanapi bin Mat Hanapi bin Mat Handung Nuryadi Hanifa Zakiyatul Urbach Hantoro Satriadi Hantoro Satriadi Hantoro Satriado Haris Nu'man Aulia Haris Nu’man Aulia Hasanah, Alfi Hendra Try Ardianto Hendro, Andika Heru Susanto Hesti Rahayu I. Hartati Ika Windrianto K. Handono Indah Hartati Iqbal Mubarak Irawan Arif Budianto Irayani, Indah Jafron Wasiq Hidayat Johnner P Sitompul Khoirun Nisa Kurdianto Kurdianto Kurnia, Atik Kusdiantini, Endang Kusmiyati, K Lukman Hakim Firdaus Luqman Buchori Luqman Buchori M. Djaeni M. Hadi M. Hadi M. Hadi Makrufah Hidayah I Marcelinus Christwardana Maria Siahaan Marta Chandra Anikke Putri Masyhad Masyhad Meiny Suzery Melati, Emilla Mhd. Adithia Perdana Arman Mochamad Arief Budihardjo MSK. Tony Suryo Utomo Muchammad Muchammad Muhammad Farizan Praevia Muhammad Hilmazar Hawari Muhammad Rachimoellah Muhammad Rachimoellah Muhammad Syukri Hasan Muhammad Syukri Hasan Nabilla Salma Listyawijayanti Nasir, Yahya Ndaru Okvitarini Ngadiwiyana M.Si. S.Si. Ngurah Widiantara Ni'matuzahroh Ni'matuzahroh Novianti, Khusnul Rofida Noviyanto, Sigit Nur Rokhati Nurjannah, Rifa Nurul Yaqin Pandapotan, Boris Poltak Prakoso, Satrio Budi Prasetyo, Ahmad Wisnu Pratomo, Shendy Eko Priyosetyoko Priyosetyoko, Priyosetyoko Puja Chrisdianto Manapa Putri, Sylvia Rahmi Rahmania, Yusi Luluk Ratnawati Ratnawati Razak, Habibie Riky Yonas Riky Yonas Riva Amrulloh Roz, Kenny S Suherman S Supriyandi Samudra, Makitta Widi Saudale, Jeanette Mutiara Paula Sekarningtyas, Nazifa Seno, Abdi Setia Budi Sasongko Setia Budi Sasongko Setiadi, Muhammad Irfan Sianturi, Aurelia Genesya Silviana Silviana Silviana, S Siti Nur Khairunisa Aroli Sri Nastiti Andharini Sri Puji Lestari Sri Widodo Agung Suedi Sriatun Sriatun Striadi, H. Sugiyanto - Sulardjaka Sulardjaka Sulardjaka Sulardjaka Sulardjaka, S Sulastri, Cucu Sumiati Sumiati Suroso Agus Saputro Sussatrio, Hardito Syafrudin Syafrudin Syaiful . Sylvia Rahmi Putri Tatang H. Soerawidjaja Taufiq, Akbar Teguh Purnomo, Teguh Tri Winarni Agustini Tri Winarni, Agustini Tutuk Djoko Kusworo Uray Irzandi Uray Irzandi Utama, Bobby Indra Vicky Ramadhani, Vicky widodo, anton sri Wira Pinem Yanuar Rifianto YS Darmanto Yudhy Dharmawan Yuliani, Kristina Wulan Yulita Arni Priastiwi Yuliyandjaja, John Philia Yusi Luluk, Rahmania