cover
Contact Name
Himawan Tri Bayu Murti Petrus
Contact Email
jurnal.rekpros@ugm.ac.id
Phone
-
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 7 No 1 (2013): Volume 7, Number 1, 2013" : 5 Documents clear
Coating in primary reformer’s radiant section Baskara Aji Nugraha
Jurnal Rekayasa Proses Vol 7 No 1 (2013): Volume 7, Number 1, 2013
Publisher : Jurnal Rekayasa Proses

Show Abstract | Download Original | Original Source | Check in Google Scholar | DOI: 10.22146/jrekpros.4939

Abstract

Kaltim Parna Industri, (KPI), experienced severe fouling on the flue gas side of the coil heat exchangers. This happened on the outer tube side, which some were finned tubes. Although the cause had not clearly been identified, laboratory analysis indicated that the fouling had similar composition with the firebrick. Therefore, preliminary assumption of what causes the problem was firebrick erosion that was carried away by flue gas flow.In order to completely eliminate fouling source and hopefully to reduce cleaning frequency, we planned to coat combustion chamber with special high temperature resistance coating.The result was promising that the material was stable against high temperature and even further helped the operation.
Aplikasi analisis pinch untuk menurunkan konsumsi steam di bagian process house pabrik gula Daniyanto Daniyanto; Fathurrahman Rifai
Jurnal Rekayasa Proses Vol 7 No 1 (2013): Volume 7, Number 1, 2013
Publisher : Jurnal Rekayasa Proses

Show Abstract | Download Original | Original Source | Check in Google Scholar | DOI: 10.22146/jrekpros.4940

Abstract

The energy efficiency of sugar factory can be indicated by variable steam on cane (SOC). SOC is defined as weight of steam consumption per weight of crushed cane. The smaller the SOC, the energy efficiency of sugar mills is better. The main source of fuel in sugar mill is bagasse. The sugar factory will be efficient if SOC is less than 50%. If SOC value is more than 50%, it will cause additional fuel other than bagasse. If SOC is less than 40%, the cane sugar mill can do cogeneration and produce electricity for sale. This study aims to reduce SOC by reducing steam consumption in the process house through configuration process innovation with pinch analysis.The results showed that pinch analysis could be used to reduce steam consumption in sugar mill. Utilization of steam from evaporator could reduce steam consumption in the process house. The change in process configuration could provide SOC decrease by 8.8% from its former state. Steam produced by evaporator 2 could be used as heat source for heater 1 and heater 2, meanwhile steam produced by evaporator 1 as a heat source for vacuum pan. Exhaust steam could be used only for heater 3 and vacuum pan.
Modifikasi mekanisme koufopanos pada kinetika reaksi pirolisis ampas tebu (bagasse) Emi Erawati; Wahyudi Budi Sediawan; Panut Mulyono
Jurnal Rekayasa Proses Vol 7 No 1 (2013): Volume 7, Number 1, 2013
Publisher : Jurnal Rekayasa Proses

Show Abstract | Download Original | Original Source | Check in Google Scholar | DOI: 10.22146/jrekpros.4941

Abstract

Bagasse is a side product of sugar cane extraction. A sugar factory produces bagasse of about 13% from the total cane milled. According to the data from BPPS (1999-2007) the total bagasse produced is about two million tons. The aim of this study is to determine the value of activation energy and pre-exponential factor of pyrolysis kinetics of sugar cane bagasse. Pyrolysis had been carried out in a reactor made of steel pipe type 5737 with a dimension of 7.62 cm dia and of 37 cm long.The reactor was inserted into a furnace with a diameter of 15.24 cm and a length of 40 cm. One hundred and fifty grams of bagasse had been added into the reactor without the presence of oxygen at atmospheric pressure. Pyrolysis had been carried out at the particle size of (-20+25) mesh, (-25+30) mesh, (-30+35) mesh, (-35+40) mesh, and -40 mesh and heating rate of 100, 105, 115, and 120 volt.Modification of Koufopanos mechanism described four reaction steps, namely the reaction to produce intermediate product and further reaction in which intermediate product converted into gas, bio-oil, and char product was the most appropriate reaction model. From the modified model the activation energy E1, E2, E3, and E4 was 8,750.48; 2,350.7 ; 11,080.97 ; and 6,625.49 J/mol, respectively, while the pre-exponential factor A1, A2, A3, and A4 was 9.20x10-3 ; 2.13x10-2 ; 1.67 ; and 2.31 second, respectively for various size particles and heating rates.
Studi pemanfaatan condensate outlet steam trap sebagai air umpan boiler di Pabrik Amoniak Pusri-IB Alfa Widyawan; Ferlyn Fachlevie
Jurnal Rekayasa Proses Vol 7 No 1 (2013): Volume 7, Number 1, 2013
Publisher : Jurnal Rekayasa Proses

Show Abstract | Download Original | Original Source | Check in Google Scholar | DOI: 10.22146/jrekpros.4942

Abstract

As ammonia and urea producer, PT. Pusri consumes a lot of steam, which is used as raw material in ammonia plant, as well as heating medium and turbine driving agent. Steam pressure used in the P-IB Ammonia plant varies from 3.5 to 123 kg/cm2gauge. Distribution system of steam piping to the equipments causes heat loss to the environment. This leads to the production of steam condensate flowing along the pipe. The steam condensate from the pipe (through the steam trap) is directly discharged into the sewer. The present study aimed to determine the rate of steam condensation and to elaborate an economic feasibility to utilize the condensate as boiler feed water in the Ammonia plant P-IB.Calculation of heat transfer in the pipes was based on the principles of conduction, convection and radiation. The rate of steam condensation was calculated with steam pressure variation from 3.5 to 123 kg/cm2gauge, pipe diameter from 4 to 20-inch and insulation thickness of 1 to 4 inches. The rate of condensation was expressed in a mathematical equation and was a function of insulation thickness and diameter of pipe.The results showed that the rate of steam condensation rised as steam pressure and pipe diameter increased and insulation thickness decreased. Operating cost reduced if the steam condensate was used as boiler feed water replacing demineralized water. This also caused reduction of fuel consumption and therefore resulted in simple payback period of 0.9 years.
Pengolahan gas CO2 hasil samping industri amoniak melalui gasifikasi batubara yang telah dipirolisis dengan menambahkan Ca(OH)2 Saripah sobah; Hary Sulistyo; Siti Syamsiah
Jurnal Rekayasa Proses Vol 7 No 1 (2013): Volume 7, Number 1, 2013
Publisher : Jurnal Rekayasa Proses

Show Abstract | Download Original | Original Source | Check in Google Scholar | DOI: 10.22146/jrekpros.4943

Abstract

CO2 is one of the greenhouse gases that is considered to cause global warming. Ammonia industry produces emission gas of CO2 in relatively great amount with an emission factor of 3.273 ton CO2/ton ammonia. One of the attempts to reduce CO2 gas emissions is by converting CO2 into syngas (CO) through gasification process. CO is one of the methanol feedstock. This research aimed to find out the amount of CO2 that can be reduced through charcoal gasification process. The reaction of carbon from coal can be reduced through the gasification process. Since the carbon reaction from coal with CO2 gas in the gasification process was an endothermic and occured very slowly at temperatures below 1000°C, Ca(OH) 2 was used as a catalyst. The coal gasification process was conducted in a fixed bed reactor. The experimental results showed that coal gasification with the use of Ca(OH) 2 in the pyrolysis process could reduce CO2 levels by 63.17%, meanwhile without Ca(OH) 2, the CO2 could be reduced only up to 35.2%.

Page 1 of 1 | Total Record : 5


Filter by Year

2013 2013


Filter By Issues
All Issue Vol 19 No 2 (2025): Volume 19, Number 2, 2025 Vol 19 No 1 (2025): Volume 19, Number 1, 2025 Vol 18 No 2 (2024): Volume 18, Number 2, 2024 Vol 18 No 1 (2024): Volume 18, Number 1, 2024 Vol 17 No 2 (2023): Volume 17, Number 2, 2023 Vol 17 No 1 (2023): Volume 17, Number 1, 2023 Vol 16 No 2 (2022): Volume 16, Number 2, 2022 Vol 16 No 1 (2022): Volume 16, Number 1, 2022 Vol 15 No 2 (2021): Volume 15, Number 2, 2021 Vol 15 No 1 (2021): Volume 15, Number 1, 2021 Vol 14 No 2 (2020): Volume 14, Number 2, 2020 Vol 14 No 1 (2020): Volume 14, Number 1, 2020 Vol 13 No 2 (2019): Volume 13, Number 2, 2019 Vol 13 No 1 (2019): Volume 13, Number 1, 2019 Vol 12 No 2 (2018): Volume 12, Number 2, 2018 Vol 12 No 1 (2018): Volume 12, Number 1, 2018 Vol 11 No 2 (2017): Volume 11, Number 2, 2017 Vol 11 No 1 (2017): Volume 11, Number 1, 2017 Vol 10 No 2 (2016): Volume 10, Number 2, 2016 Vol 10 No 1 (2016): Volume 10, Number 1, 2016 Vol 9 No 2 (2015): Volume 9, Number 2, 2015 Vol 9 No 1 (2015): Volume 9, Number 1, 2015 Vol 8 No 2 (2014): Volume 8, Number 2, 2014 Vol 8 No 1 (2014): Volume 8, Number 1, 2014 Vol 7 No 2 (2013): Volume 7, Number 2, 2013 Vol 7 No 1 (2013): Volume 7, Number 1, 2013 Vol 6 No 2 (2012): Volume 6, Number 2, 2012 Vol 6 No 1 (2012): Volume 6, Number 1, 2012 Vol 5 No 2 (2011): Volume 5, Number 2, 2011 Vol 5 No 1 (2011): Volume 5, Number 1, 2011 Vol 4 No 2 (2010): Volume 4, Number 2, 2010 Vol 4 No 1 (2010): Volume 4, Number 1, 2010 Vol 3 No 2 (2009): Volume 3, Number 2, 2009 Vol 3 No 1 (2009): Volume 3, Number 1, 2009 Vol 2 No 2 (2008): Volume 2, Number 2, 2008 Vol 2 No 1 (2008): Volume 2, Nomor 1, 2008 Vol 1 No 1 (2007): Volume 1, Number 1, 2007 More Issue