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Contact Name
Himawan Tri Bayu Murti Petrus
Contact Email
jurnal.rekpros@ugm.ac.id
Phone
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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 6 Documents
Search results for , issue "Vol 1 No 1 (2007): Volume 1, Number 1, 2007" : 6 Documents clear
Simulation of hydrogen adsorption on modified carbon structures Chandra Wahyu Purnomo
Jurnal Rekayasa Proses Vol 1 No 1 (2007): Volume 1, Number 1, 2007
Publisher : Jurnal Rekayasa Proses

Show Abstract | Download Original | Original Source | Check in Google Scholar | DOI: 10.22146/jrekpros.jrp070304

Abstract

The adsorption simulation of hydrogen molecules onto modified carbon structures has been carried out. The modifications have been done by rearranging carbon nanotube structure and also by replacing carbon molecules by impurities i.e. boron and nitrogen atoms. The aims of this simulation isfinding an optimum adsorption delivery of each modified carbon structures leading to an effective gas storage system. The adsorption simulation has been carried by Grand Canonical Monte Carlo methods (GCMC). By this simulation, it wasfound that the optimum temperaturefor hydrogen adsorptiondelivery was still under room temperature.
Koefisien perpindahan panas volumetris dan kapasitas penyimpanan panas pada sistem penyimpan energi panas kontak langsung Panut Mulyono
Jurnal Rekayasa Proses Vol 1 No 1 (2007): Volume 1, Number 1, 2007
Publisher : Jurnal Rekayasa Proses

Show Abstract | Download Original | Original Source | Check in Google Scholar | DOI: 10.22146/jrekpros.jrp070305

Abstract

The volumetric coefficient of heat transfer and the energy storage capacity in a direct contact thermal energy storage system using Na2CO3.10H20 solution as a thermal energy storage medium have been investigated Hot kerosene was used as a heat transfer fluid The experiments were carried out by bubbling hot kerosene from the bottom of a column containing Na2CO3.10H2O solution. The column used in this experiment was made of glass of 3 mm in thickness with 7 cm of Inside diameter and 100 cm of height. A simple model to calculate the volumetric coefficient of heat transfer of the system has been developed The effects of kerosene flow rate and kerosene bubble diameter on the volumetric coefficient of heat transfer and the storing rate of energy were studied It was found that the volumetric coefficient of heat transfer was strongly affected by the flow rate of the kerosene and that the effect of the kerosene flow rate on the storing rate of energy was relatively high, while that of the effect of the bubble diameter was small. The relationship between the volumetric coefficient of heat transfer (in the form of the dimensionless group) and the kerosene bubble Reynolds number is Nu = 0.2362 Rei1.1475 with a mean relative error of 0.45% for the range of Reynolds number of 5 to 13.2.
Tinjauan parameter utama pada pressure swing distillation Arief Budiman; Sutijan
Jurnal Rekayasa Proses Vol 1 No 1 (2007): Volume 1, Number 1, 2007
Publisher : Jurnal Rekayasa Proses

Show Abstract | Download Original | Original Source | Check in Google Scholar | DOI: 10.22146/jrekpros.jrp070306

Abstract

Pemisahan komponen penyusun campuran azeotropik tidak dapat dilakukan dengan menggunakan kolom distilasi klasik. Salah satu cara untuk menjawab permasalahan ini adalah dengan menggunakan distilasi ayunan tekanan. Konfigurasi ini mengacu pada distilasi dua kolom yang beroperasi secara seri pada tekanan berbeda untuk memberikan kemampuan mengatasi penghalang azeotropik. Tujuan utama dari makalah ini adalah untuk mempelajari parameter utama pada kolom distilasi ayunan tekanan. Kondisi pengoperasian seperti jumlah pelat, pelat umpan, laju dasar, tekanan, dan laju daur ulang dipilih untuk dievaluasi.
Reaksi absorpsi gas CO2 dengan suspensi Ca(OH)2 Menjadi CaCO3 dalam reaktor slurry tangki berpengaduk Zahrul Mufrodi; Rochmadi Mufrodi; Hary Sulistyo
Jurnal Rekayasa Proses Vol 1 No 1 (2007): Volume 1, Number 1, 2007
Publisher : Jurnal Rekayasa Proses

Show Abstract | Download Original | Original Source | Check in Google Scholar | DOI: 10.22146/jrekpros.jrp070301

Abstract

Sistem reaksi padat, cair, dan gas banyak digunakan dalam industri kimia. Pembuatan CaCO3 salah satu contohnya, dimana CaCO3 banyak digunakan pada berbagai industri seperti industri kosmetik, bahan apigment inacrylic, industri pulp dan karet. Percobaan ini mempelajari reaksi pembuatan CaCO3 dari penyerapan gas CO2 dalam suspensi Ca(OH). Reaksi ini dilakukan dalam reaktor slurry dengan agitasi. Pertama, reaktor dipanaskan sampai suhu reaksi yang diinginkan tercapai. Setelah itu padatan kalsium karbonat disuspensikan dalam reaktor. Gas CO2 (pada suhu yang sama) dialirkan ke dalam reaktor dengan kecepatan volumetrik tertentu menggunakan gas spurge. Sampel diambil setiap I menit hingga seluruh Ca(OH)2 bereaksi. Variabel yang diteliti dalam penelitian ini adalah kecepatan putaran agitator {5.667 -I 1.067 rps dan laju volumetrik gas C02 (34.0127- 60.5503 ggl). Koefisien perpindahan massa dan koefisien laju reaksi dihitung menggunakan SSE minimum. Berdasarkan teori dua film pada perpindahan massa gas-cair dan teori film tunggal pada kelarutan Ca(OH)2. model matematika yang diusulkan cocok dengan data. Selain itu berdasarkan indeks Reynolds pada berbagai kecepatan putaran agitator dan laju volumetrik gas CO2. akhirnya disimpulkan bahwa rezim dinamis datar mempengaruhi eksperimen ini.
Absorption characteristics of solvents for carbon dioxide capture Sholeh Ma' mun; Hallvard Svendsen; Olav Julissen
Jurnal Rekayasa Proses Vol 1 No 1 (2007): Volume 1, Number 1, 2007
Publisher : Jurnal Rekayasa Proses

Show Abstract | Download Original | Original Source | Check in Google Scholar | DOI: 10.22146/jrekpros.jrp070302

Abstract

This study focuses on the absorption characteristics of solvents for CO2 capture. The objective is to develop new and more efficient solvents or solvent mixtures with higher absorption rates and loading capacities than existing ones. CO2 absorption was investigated at 40°C using both alkanolamine-based and non-alkanolamine-based solvents. The absorption characteristics, crucial for CO2 removal, depend on the absorption rate and capacity of the solvents. All absorbents are compared to the commercially used MEA. Experimental results reveal that most tested absorbents exhibit poorer performance than MEA. However, a 30-wt% AEEA in aqueous solution emerges as a potential contender, demonstrating superior absorption characteristics. In comparison to 30-wt% MEA, the 30-wt%- AEEA shows a higher absorption rate from a loading of 0.35 and increased absorption capacity (0.82 mol CO2/mol AEEA and 0.47 mol CO2/mol MEA at 9.5 kPa CO2 partial pressure).
CO oxidation over copper-chromium catalyst supported by indonesian zeolite Suryo Purwono
Jurnal Rekayasa Proses Vol 1 No 1 (2007): Volume 1, Number 1, 2007
Publisher : Jurnal Rekayasa Proses

Show Abstract | Download Original | Original Source | Check in Google Scholar | DOI: 10.22146/jrekpros.jrp070303

Abstract

The objectives of this paper are to oxidize CO on metal catalyst supported by natural zeolite and to find model for kinetic of CO oxidation that will accurately predict oxidation raJe under different temperatures and feed concentrations. The results shows that using Impregnation method, copper and chromium metals active components of the catalyst can be dispersed on the natural zeolite as catalyst support. The reaction rate measurements of catalytic oxidation of CO were done in the temperature range between 300 and 520oC using a differential micro-reactor. 'J1!e results show that the reaction rate depends strongly on the bed temperature and feed concentration and is not controlled by bulk phase mass transfer and pore diffusion.

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