C1 Gas Refinery

Author(s):  
Ji Eun Woo ◽  
Seung Min Song ◽  
Sang Yup Lee ◽  
Yu-Sin Jang
Keyword(s):  
2015 ◽  
Vol 6 (1) ◽  
pp. 30-34 ◽  
Author(s):  
Iraj Mohammadfam ◽  
Susan Bastani ◽  
Mahbobeh Esaghi ◽  
Rostam Golmohamadi ◽  
Ali Saee

Author(s):  
Mohamad Mohamadi-Baghmolaei ◽  
Abdollah Hajizadeh ◽  
Sohrab Zendehboudi ◽  
Xili Duan ◽  
Hodjat Shiri ◽  
...  

2021 ◽  
Vol 18 (1) ◽  
pp. 285-301
Author(s):  
Fakhradin Ghasemi ◽  
Mohammad Kurdestani ◽  
Iraj MohammadFam ◽  
◽  
◽  
...  

2012 ◽  
Vol 4 ◽  
pp. 17-28 ◽  
Author(s):  
M.R. Rahimpour ◽  
Z. Jamshidnejad ◽  
S.M. Jokar ◽  
G. Karimi ◽  
A. Ghorbani ◽  
...  

2015 ◽  
Vol 77 (23) ◽  
Author(s):  
Mahidin Mahidin ◽  
Hamdani Hamdani ◽  
Jailani Ibrahim ◽  
Teuku Zubir ◽  
Agus Nur Yasin

Energy conservation is an important issue in all sectoral activities, especially in processing industries such as natural gas refinery and liquefaction plant, petrochemical and cement mill in which energy isused in large amount. This paper presents a discussion on the experience in establishment and implementation the energy conservation program, including the reduction of greenhouse gas (GHG) emission achieved in the last four years in Arun LNG Plant, a commercial natural gas liquefaction plant in Aceh, Indonesia with a capacity of 2.2 million ton LNG per year. In addition, an analysis on the specific energy consumption and CO2 reduction is provided. The Energy Management Matrix was adopted in assessment of the energy management implementation in theArun LNG Plant. It was found that the efficiency of the plant tended to decrease from year to year, which was represented by the specificity of fuel consumption (accounted based on the LNG product). In 2010 the specific fuel consumption was 0.0088 mmscf per m3 LNG product; it was up to 0.0234 in 2013. Fortunately, it was observed that the specific CO2 reduction (calculated on the LNG product basis) increased during tlast four years; in 2010 and 2013 the specific CO2 reduction was 0.195 and 0.518 ton per 105 m3 LNG produced, respectively.


Author(s):  
Neda Razi

Optimization of a large gas transmission pipeline results in reduced fuel consumption or higher capability and improves pipeline operation. In the current study, we have done an extensive research to optimize the operation of a huge NPS 56 pipeline system using gas cooling. This gas transmission line (the 4th major gas transmission pipeline of the National Iranian Gas Company, NIGC, or IGAT4) is designed to move over 110 MMSCMD (4.0 BCFD) of natural gas from the Assaluyeh Gas Refinery. This gas refinery which in turn receives gas from the huge gas reservoir of the South Pars Field (Iranian off-shore) is located in the south of Iran. The length of this system is over 800 kms (500 miles) with over 700 MW of compression power and aerial coolers at all compressor stations. This system passes through a very tortuous terrain with significant changes in elevation and ambient temperature which makes the optimization process even more challenging. The main objective of this project was to develop a customized tool to optimize the operation (energy consumption) of this gas transmission pipeline with all the existing system variables. The emphasis was on the impact of gas cooling (effective operation of aerial coolers) on the optimization process which in turn leads to the fuel minimization or higher capability. In this process, the impact of ambient temperature, soil temperature throughout the entire route of the pipeline, cost of electricity & fuel gas, heat transfer and Joule-Thompson effect were carefully considered. The tool was finally developed and was successfully tested on this gas transmission system which resulted in extremely accurate results. This tool could be further generalized to be used for other transmission systems.


2018 ◽  
Vol 67 ◽  
pp. 02039
Author(s):  
Mahmud Sudibandriyo ◽  
Melody Oratmangun

Hydrogen recovery from off gas of hydrocracking and hydrotreating unit is one of the crucial processes in an oil and gas refinery unit as this process helps in lowering the expenses for operations. This study aims to obtain activated carbon that is made from Betung bamboo which can be used as the adsorbent in this process. The activated agents used are H3PO4 and K2CO3, respectively. Each activation lasts for 30 minutes. The results of the characterization test shows that the Iodine number of the activated carbon produced reaches 916.4 mg/g with BET surface area of 465.2 m2/g. SEM-EDX analysis shows that the carbon content is 74.83%. The activated carbon obtained is used to separate Hydrogen and Methane from its mixture at 10, 20 and 30oC with pressure variations of 1 - 6 bar. The results indicate that the maximum number of moles adsorbed from CH4(21.5%)/H2 gas mixture is 0.247 mmol/g, that has been carried out at 6 bar with temperature of 10oC. Methane has 2.2 times higher adsorption capacity than hydrogen, therefore, the Betung bamboo based activated carbon produced from this research can be applied as the adsorbent in the separation process of CH4/H2 mixture and it fits the Langmuir model.


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