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Contact Name
Himawan Tri Bayu Murti Petrus
Contact Email
jurnal.rekpros@ugm.ac.id
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Journal Mail Official
jurnal.rekpros@ugm.ac.id
Editorial Address
Jl. Grafika No. 2, Yogyakarta, Indonesia
Location
Kab. sleman,
Daerah istimewa yogyakarta
INDONESIA
Jurnal Rekayasa Proses
ISSN : 1978287X     EISSN : 25491490     DOI : -
Core Subject : Engineering,
Jurnal Rekayasa Proses is an open-access journal published by Chemical Engineering Department, Faculty of Engineering, Universitas Gadjah Mada as scientific journal to accommodate current topics related to chemical and biochemical process exploration and optimization which covers multi scale analysis from micro to macro and full plant size. Specialization topics covered by Jurnal Rekayasa Proses are: 1. Kinetics and Catalysis Includes simulations and experiments in reaction kinetics, catalyst synthesis and characterization, reactor design, process intensification, microreactor, multiphase reactors, multiscale phenomena, transfer phenomena in multiphase reactors. 2. Separation and Purification System Includes phase equilibrium, mass transfer, mixing and segregation, unit operation, distillation, absorption, extraction, membrane separation, adsorption, ion exchange, chromatography, crystallization and precipitation, supercritical fluids, bioprocess product purification. 3. Process System Engineering Includes simulation, analysis, optimization, and process control on chemical/biochemical processes based on mathematical modeling; multiscale modeling strategy (molecular level, phase level, unit level, and inter-unit integration); design of experiment (DoE); current methods on simulation for model parameter determination. 4. Oil, Gas, and Coal Technology Includes chemical engineering application on process optimization to achieve utmost efficiency in energy usage, natural gas purification, fractionation recovery, CO2 capture, coal liquefaction, enhanced oil recovery and current technology to deal with scarcity in fossil fuels and its environmental impacts. 5. Particle Technology Includes application of chemical engineering concepts on particulate system, which covers phenomenological study on nucleation, particle growth, breakage, and aggregation, particle population dynamic model, particulate fluid dynamic in chemical processes, characterization and engineering of particulate system. 6. Mineral Process Engineering Includes application of chemical engineering concepts in mineral ore processing, liberation techniques and purification, pyrometallurgy, hydrometallurgy, and energy efficiency in mineral processing industries. 7. Material and biomaterial Includes application of chemical engineering concepts in material synthesis, characterization, design and scale up of nano material synthesis, multiphase phenomena, material modifications (thin film, porous materials etc), contemporary synthesis techniques (such as chemical vapor deposition, hydrothermal synthesis, colloidal synthesis, nucleation mechanism and growth, nano particle dispersion stability, etc.). 8. Bioresource and Biomass Engineering Includes natural product processing to create higher economic value through purification and conversion techniques (such as natural dye, herbal supplements, dietary fibers, edible oils, etc), energy generation from biomass, life cycle and economic analysis on bioresource utilization. 9. Biochemistry and Bioprocess Engineering Includes biochemical reaction engineering, bioprocess optimization which includes microorganism selection and maintenance, bioprocess application for waste treatment, bioreactor modeling and optimization, downstream processing. 10. Biomedical Engineering Includes enhancement of cellular productions of enzymes, protein engineering, tissue engineering, materials for implants, and new materials to improve drug delivery system. 11. Energy, Water, Environment, and Sustainability Includes energy balances/audits in industries, energy conversion systems, energy storage and distribution system, water quality, water treatment, water quality analysis, green processes, waste minimization, environment remediation, and environment protection efforts (organic fertilizer production and application, biopesticides, etc.).
Articles 5 Documents
Search results for , issue "Vol 10 No 2 (2016): Volume 10, Number 2, 2016" : 5 Documents clear
Kinetika adsorpsi nikel (II) dalam larutan aqueous dengan karbon aktif arang tempurung kelapa Ardelita Adiningtyas; Panut Mulyono
Jurnal Rekayasa Proses Vol 10 No 2 (2016): Volume 10, Number 2, 2016
Publisher : Jurnal Rekayasa Proses

Show Abstract | Download Original | Original Source | Check in Google Scholar | DOI: 10.22146/jrekpros.33335

Abstract

The adsorption kinetics of nickel (II) in aqueous solution with activated carbon from coconut shell was studied by measuring the nickel concentration in the solution (C) as a function of time (t). The parameters studied in this study were adsorption temperature (T), particle diameter of activated carbon (d), and mass ratio of activated carbon to aqueous solution (r). It was found that the adsorption rate increased with the increase of the adsorption temperature and the mass ratio of activated carbon to aqueous solution. On the contrary, it was found that the rate of adsorption decreased with increasing the particle diameter of the activated carbon.
Pengaruh variasi organic loading rate sampah buah jeruk terhadap produksi biohidrogen pada reaktor kontinu Baruna Sakti Wicaksono Bonanza; Sarto Sarto
Jurnal Rekayasa Proses Vol 10 No 2 (2016): Volume 10, Number 2, 2016
Publisher : Jurnal Rekayasa Proses

Show Abstract | Download Original | Original Source | Check in Google Scholar | DOI: 10.22146/jrekpros.33336

Abstract

Biohydrogen is a potential alternative energy generated through the process of dark fermentation of organic waste. This research aims to determine the effect of organic loading rate (OLR) variations of orange waste on biohydrogen production. This research dealt with the production of biohydrogen in the continuous system. The reactor was equipped with circulation and operated anaerobically. The inoculum was taken from the sludge of the biogas installation in Gemah Ripah Fruit Market. Orange waste was used in three variations of organic loading rate (OLR) at 2.2, 2.5, and 3.1 L/day. The results revealed that the daily productions of gas for those OLR are about 15, 35, and 26 L/day respectively. Futhermore, for OLR of 2.5 L/day the total solid decreased from about 8 to 5%.
Pengaruh waktu dan konsentrasi NaOH pada proses delignifikasi wheat bran Devi Sepmita Wulansari; Supranto Supranto
Jurnal Rekayasa Proses Vol 10 No 2 (2016): Volume 10, Number 2, 2016
Publisher : Jurnal Rekayasa Proses

Show Abstract | Download Original | Original Source | Check in Google Scholar | DOI: 10.22146/jrekpros.33337

Abstract

There are approximately 14.5% of whole wheat which belongs to bran and contains cellulose (33.7-40%), hemicellulose (21-26%), lignin (11–22.9%) and the other components. Cellulose is polysaccharide which is composed of 2000-3000 unit of glucose. Cellulose purification from the wheat bran can be done by the hydrolysis, followed by the processes of delignification and bleaching. The experiments were perfomed first by hydrolizing 20 grams of wheat bran using 250 mL of 2.5 N HCl solution for 2 hours at temperature of 80oC. The next process was delignification using 400 mL of NaOH solution and was conducted by varying the time in 1 hour, 1,5 hours, 2 hours, and 2.5 hours and the concentration of NaOH solution in 0.5 N; 1 N; 1.5 N; 2 N. For the last process, bleaching was performed by using 300 mL of H2O2 10% solution in temperature of 80 oC for 1 hour. The sample was then dried in order to remove water content by getting the sample in the oven for 1 hour at temperature of 40 oC. The goals of the experiments were to find the correlation between the variation of time and NaOH concentration to the cellulose quality in terms of the color and the structure of cellulose sample and and to the quantitative measure which was the yield of the sample. The best product was obtained at the optimum operation of 2.5 hours delignification and 1.55 N of NaOH concentration.
Produksi organic preservative dan solid biofuel dari hydrothermal treatment tongkol jagung dengan variasi temperatur Haidar Ali; Ahmad Tawfiequrrahman Yuliansyah
Jurnal Rekayasa Proses Vol 10 No 2 (2016): Volume 10, Number 2, 2016
Publisher : Jurnal Rekayasa Proses

Show Abstract | Download Original | Original Source | Check in Google Scholar | DOI: 10.22146/jrekpros.33338

Abstract

Corn is one of staple food and influential commodity driving Indonesia’s economy. Indonesia currently produces as high as 19 million tons of corn which contains 50% of biomass in the form of cob. Waste from harvesting and consumption of corn, namely, corn cob (CC) is left as waste. This CC is actually a sustainable, easily accessible, and renewable biomass energy source as an alternative to Indonesia’s depleting fossil fuel reserves. Hydrothermal treatment is a conversion method that has some consequential advantages compared to other methods; e.g. the ability to treat high-moisture biomass like CC and the possibility to use lower temperature. This research aims to produce and characterize liquid and solid fuel subsequent to hydrothermal treatment of CC obtained from Sleman, Yogyakarta. After size reduction, fine particles were mixed with water to form slurry. Slurry was heated in an autoclave for hydrothermal treatment at initial pressure of 2.0 MPa and was held for 200 °C, 240 °C, and 270 °C in 30 minutes. The solid and liquid products were then separated. Liquid was analyzed using GC-MS and solid by using AAS. The result showed that, in comparison to raw material, solid product had higher carbon content which resulted in the increase of calorific value of the solid biofuel. The calorific value of solid product ranged from 19,59 -22,02 MJ/kg or 20,93-35,87% higher than raw materials and 4-17% higher than average coal used in Indonesia. Major component in liquid product are N, N-dimethyl formamide, furfural, and phenolic compound, with benzoic acid present as minor component. The potential of liquid products as organic preservatives are examined by testing the tenacity of wood against termite according to ASTM D3345-74 standard method. Result showed that liquid product were effective in exhibiting termiticidal activity and temperature 200 °C showed the optimum condition.
Pengaruh suhu pada esterifikasi amil alkohol dengan asam asetat menggunakan asam sulfat sebagai katalisator Muhammad Naufal Fakhry; Suprihastuti Sri Rahayu
Jurnal Rekayasa Proses Vol 10 No 2 (2016): Volume 10, Number 2, 2016
Publisher : Jurnal Rekayasa Proses

Show Abstract | Download Original | Original Source | Check in Google Scholar | DOI: 10.22146/jrekpros.33339

Abstract

Ester compounds are widely used as solvents, artificial aroma materials, and precursors of pharmaceutical ingredients. One of the ester compounds widely used in the chemical industry is amyl acetate. Amyl acetate can be synthesized by esterification of amyl alcohol and acetic acid, which is a liquid-liquid heterogeneous reaction. This study aims to study the kinetics of this particular reaction focusing on the effect of temperature. The catalyst used in this study was sulfuric acid. The mole ratio of acetic acid to amyl alcohol used was 2: 5. Reaction was run at constant temperature in a three-neck flask as a batch reactor. The acetic acid and sulfuric acid were first put into the reactor and heated while stirring. After reaching a certain temperature, the preheated amyl alcohol was added into the reactor. During reaction, the temperature was maintained at the desired temperature. The reactants and products involved in this reaction were immiscible. The product phases were separated and then the remaining acetic acid content in the water-soluble phase was analyzed by volumetric method. The study was carried out in 4 variations of temperature i.e. 70, 80, 90, and 100 oC. The results of experimental data analysis showed that the reaction will be faster when the temperature is higher. The mass transfer from the acetic acid phase to the amyl alcohol phase increased with the increase of temperature. The value of the reaction rate constant, the overall mass transfer coefficient, and the Henry’s constant were evaluated by the parameter fitting method using the MATLAB program. Based on the evaluation at the highest reaction temperature 100 oC, the rate constant was 0.0134 mL.mole-2s-1, the mass transfer coefficient was 0.3180 L s-1, and the Henry’s constant was 0.0174 (mole/L)A in phase II/(mole/L)A in phase I.

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