Thermodynamic Simulations of Hydrate-Based Removal of Carbon Dioxide and Hydrogen Sulfide from Low-Quality Natural Gas

2013 ◽  
Vol 52 (43) ◽  
pp. 15165-15176 ◽  
Author(s):  
Satoru Akatsu ◽  
Shuhei Tomita ◽  
Yasuhiko H. Mori ◽  
Ryo Ohmura
2019 ◽  
Vol 9 (17) ◽  
pp. 4573-4580 ◽  
Author(s):  
Adam A. Arvidsson ◽  
William Taifan ◽  
Anders Hellman ◽  
Jonas Baltrusaitis

A large fraction of the global natural gas reserves is in the form of sour gas, i.e. contains hydrogen sulfide (H2S) and carbon dioxide (CO2), and needs to be sweetened before utilization.


2021 ◽  
Vol 288 ◽  
pp. 125689
Author(s):  
Xuewen Cao ◽  
Dan Guo ◽  
Wenjuan Sun ◽  
Pan Zhang ◽  
Gaoya Ding ◽  
...  

KnE Energy ◽  
2015 ◽  
Vol 2 (2) ◽  
pp. 126 ◽  
Author(s):  
Mufidatul Islamiyah ◽  
Totok Soehartanto ◽  
Ridho Hantoro ◽  
Arif Abdurrahman

<p>Purifying biogas from CO2 (carbon dioxide) and H2S (hydrogen sulfide) needs to be done to improve the quality of the biogas in the fuel. The presence of H2S in biogas can cause corrosive to the equipment, in addition to this, H2S is also dangerous for human and animal health. CO2 contained in Biogas is also an impurity that can cause corrosive beside H2S so the contained in biogas is also an impurity that can cause corrosive, so the purification process needs to be done in order to qualify biogas as natural gas which environmentally friendly and safe for health. The basic ingredient of biogas purification using water scrubbers base ingredients are water, which flowed pressurized biogas purification column from the bottom, of the column in order to reduce CO2 and H2S gases. The result of purification by using this method was that the levels of H2S in biogas reduced by 32.8 % while the CO2 content decreased by 21.2 %. It can be concluded that the H2S gas more soluble in the water compared with CO2, as H2S gas has higher efficiency removal from CO2. </p><p><strong>Keywords</strong>: biogas; carbon dioxide; hydrogen sulfide, waters scrubber</p>


2020 ◽  
Vol 12 (42) ◽  
pp. 47984-47992
Author(s):  
Mahmoud M. Abdelnaby ◽  
Kyle E. Cordova ◽  
Ismail Abdulazeez ◽  
Ahmed M. Alloush ◽  
Bassem A. Al-Maythalony ◽  
...  

2011 ◽  
Vol 108 ◽  
pp. 308-313 ◽  
Author(s):  
Shan Fa Tang ◽  
Xue Yang ◽  
Da Wei Wu

Natural gas of Tazhong-1 gas field contains 7.7% carbon dioxide and 2.31% hydrogen sulfide, and produced water salinity is up to 140000mg/L,the well-bore tube has seriously potential corrosion destructive with natural gas being exploited. Based on the corrosion type partition of down-hole tube for eighteen production wells of Tazhong-1 gas field, P110,P110S and P110SS corrosion behavior were investigated under the conditions of simulated formation water containing carbon dioxide or hydrogen sulfide/carbon dioxide, and corrosion inhibitors were chosen to meet need of anticorrosion of Tazhong-1 gas field. The results show that fifteen wells in eighteen production wells belong to hydrogen sulfide corrosion of both hydrogen sulfide and carbon dioxide influence. Other wells are singular carbon dioxide corrosion. The most severe corrosion of three types of down-hole tubes all occurs at 90°C in both corrosion media, and their corrosion resistance order is respectively P110>P110S>P110SS and P110S>P110SS>P110 under the conditions of simulated formation water containing carbon dioxide or hydrogen sulfide and carbon dioxide. The selected anti-temperature corrosion inhibitors (YU-1、YU-4) can control the corrosion rate of three types of down-hole tubular goods within 0.076mm/a in simulated formation water media with carbon dioxide (PCO2=0.08~4.64MPa) or hydrogen sulfide and carbon dioxide (PH2S/Pco2=1.3/4.64Mpa) while added amount of the inhibitor is 120~300mg/L or 200mg/L. All of these provide technical support for safe and fast development of Tazhong-1 gas field.


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