Injectivity and Well Deliverability Test and Analysis in an Offshore Complex High CO2 Gas Carbonate Asset

2018 ◽  
Author(s):  
Rahim Masoudi ◽  
Muhammad Afiq Abd. Wahab ◽  
Eghbal Motaei ◽  
Abdolrahim Ataei
Keyword(s):  
Co2 Gas ◽  
1991 ◽  
Vol 28-29 (1) ◽  
pp. 877-886 ◽  
Author(s):  
Masaaki Negoro ◽  
Norio Shioji ◽  
Kazohisa Miyamoto ◽  
Yoshiharu Micira
Keyword(s):  
Co2 Gas ◽  

1976 ◽  
Vol 230 (3) ◽  
pp. 839-844 ◽  
Author(s):  
HR Weiss ◽  
JA Cohen ◽  
LA McPherson

The effects of inspiring low O2 or high CO2, or low-O2-high-CO2 gas mixtures on tissue perfusion and tissue Po2 of brain and muscle were studied in 76 anesthetized rats. Under control conditions, relative tissue Po2 of cerebral white matter measured polarographically averaged 16.4 mmHg and 18.7 mmHg in the biceps brachii. With low-O2 gas mixtures, tissue Po2 declined in both brain and muscle, but more in muscle. Tissue Po2 increased under high-CO2 conditions, with the brain increasing to a greater extent. Control cerebral cortex tissue perfusion averaged 23.5 ml/min per 100 g and muscle was 18.3 ml/min per 100 g measured by H2 clearance. Brain perfusion increased under all experimental conditions. Muscle perfusion did not change with low O2 alone, but increased with low-O2-high-CO2 or high-CO2 gas mixtures. Brain perfusion increased under all conditions significantly more than muscle. The brain appeared better protected compared to skeletal muscle in terms of tissue Po2 and perfusion under the stress of hypoxia and hypoxic-hypercapnia. The effects of hypercapnia are also greater on the brain.


2016 ◽  
Vol 6 (1) ◽  
pp. 52-56
Author(s):  
Harris Abd. Rahman Sabri ◽  
Abd. Rahman Abdul Rahim ◽  
Wong Kuan Yew ◽  
Syuhaida Ismail
Keyword(s):  
Co2 Gas ◽  

2018 ◽  
Author(s):  
H Mumtaz Lahuri ◽  
Akbar A Seman ◽  
N Hafizah Berahim ◽  
M Syazwan Onn ◽  
M Ghaddaffi M Nor

2021 ◽  
Author(s):  
M. Faizan Ahmad Zuhdi ◽  
F. Hadana Rahman ◽  
Hamid Shahjavan ◽  
M. Azlan Mas’od ◽  
R. Suhaib Salihuddin ◽  
...  

Abstract The CO2 capture technology is well understood in the oil and gas industry. However, to unlock the Hydrocarbon from an ultra-high CO2 offshore field (more than 70% mol), special attention is needed to capture CO2 for a field development to be economically attractive. Therefore, the current technology inventory needs to be studied to achieve project goals and at the same time achieving Carbon Capture and Storage (CCS) requirements. A hybrid of multiple carbon capture technology will help to improve the hydrocarbon (HC) loss, reduce both operational and capital cost and minimize overall auto consumption. The hybrid of cryogenic distillation (CryoD), membrane and supersonic gas separation (SGS) was studied to explore its feasibility. To enable ease of CO2 transport and handling, CO2 is preferred to be in liquid form. In order to achieve this, CryoD technology is the preferred solution for bulk removal. CryoD is also able to cater to the feed gas fluctuation and becomes a robust candidate for high variance feedstock. However, being dependant on sub zero working temperatures, the system will require larger equipment footprint and tonnage. The focus of the study is to evaluate the sensitivity impact of an operating condition on the Hybrid configuration of CryoD + membrane (CM) and CryoD + SGS (CS. Areas of focus will be equipment tonnage and footprint, power consumption and eventually cost (CAPEX & OPEX). The monetization of ultra-high CO2 gas field is then made feasible by using hybrid Acid Gas Removal Unit (AGRU) to meet sales gas specification. The CryoD + membrane technology is the preferred solution for offshore system.


2008 ◽  
Vol 63 (6) ◽  
pp. 681-684 ◽  
Author(s):  
Paul J. Dyson ◽  
Gábor Laurenczy

The viscosities of the ionic liquids [bmim][PF6] and [bmim][TF2N] (bmim = 1-methyl-3- butylimidazolium, TF2N = bis(trifluoromethylsulfonyl)imide) have been determined under CO2 pressure at 298 K. The viscosity decreases from 381 to 23 cP for [bmim][PF6] without CO2 and for 2.17 molal CO2 solutions (mole fraction XCO₂ = 0.381, 55 bar CO2), respectively. For [bmim][TF2N] the viscosity decreases from 54 cP for the ionic liquid to 21 cP for a 1.61 molal solution of CO2 (mole fraction XCO₂ = 0.403, 55 bar CO2).


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