Utilisation of Carbon Dioxide for Electro-Carburisation of Mild Steel in Molten Carbonate Salts

2011 ◽  
Vol 158 (11) ◽  
pp. H1117 ◽  
Author(s):  
Nancy J. Siambun ◽  
Harimi Mohamed ◽  
Di Hu ◽  
Daniel Jewell ◽  
Yeo K. Beng ◽  
...  
Carbon ◽  
2016 ◽  
Vol 106 ◽  
pp. 208-217 ◽  
Author(s):  
Hongjun Wu ◽  
Zhida Li ◽  
Deqiang Ji ◽  
Yue Liu ◽  
Lili Li ◽  
...  

Energy ◽  
2005 ◽  
Vol 30 (7) ◽  
pp. 1192-1203 ◽  
Author(s):  
Gong Jin ◽  
Hiroyuki Iwaki ◽  
Norio Arai ◽  
Kuniyuki Kitagawa

RSC Advances ◽  
2014 ◽  
Vol 4 (67) ◽  
pp. 35808-35817 ◽  
Author(s):  
Happiness V. Ijije ◽  
Richard C. Lawrence ◽  
George Z. Chen

Carbon dioxide can be electrochemically reduced to carbon in molten carbonate salts, promising affordable energy, materials and environmental explorations.


Author(s):  
Hiroyuki Iwaki ◽  
Gong Jin ◽  
Tomohiko Furuhata ◽  
Norio Arai

In this paper, wastepaper gasification with steam and carbon dioxide was tested in the presence of molten carbonate salt catalysts. Reactions with steam or carbon dioxide were first compared. Hydrogen was mainly produced by gasification with steam, but no carbon monoxide was generated. For the case where carbon dioxide was used as a reactant instead of steam, generation of carbon monoxide greatly increased via the Boudouard reaction. Different ratios of mixtures of lithium, sodium and potassium carbonates were examined. Lithium was found to play a critical role in the various catalyst combinations. The reaction rate with respect to carbon conversion was approximately first order for low carbon conversions. The rate constants were investigated at different temperatures (923–1023K) and the activation energies were determined. In addition, the flexibility of this technique was examined with three different types of wastepaper. These results suggest the applicability of this process for the effective use of wastepaper and recovery of carbon dioxide.


Author(s):  
Ji Ho Ahn ◽  
Tong Seop Kim

Owing to the increasing consumption of fossil fuels and emission of greenhouse gases, interests in highly efficient and low carbon emitting power systems are growing fast. Several research groups have been suggesting advanced systems based on fuel cells and have also been applying carbon capture and storage technology to satisfy the demand for clean energy. In this study, the performance of a hybrid system, which is a combination of a molten carbonate fuel cell (MCFC) with oxy-combustion carbon capture and an indirectly fired micro gas turbine (MGT) was predicted. A 2.5MW MCFC system that is used in commercial applications was used as the reference system so that the results of the study could be applicable to practical situations. The ambient pressure type hybrid system was modeled by referring to the design parameters of an MGT that is currently being developed. A semi-closed type design characterized by flow recirculation was adopted for this hybrid system. A part of the recirculating gas is converted into liquefied carbon dioxide and captured for storage at the carbon separation unit. Almost 100% carbon dioxide capture is possible with this system. In these systems, the output power of the fuel cell is larger than in the normal hybrid system without carbon capture because the partial pressure of carbon dioxide increases. The increased cell power partially compensates for the power loss due to the carbon capture and MGT power reduction. The dependence of net system efficiency of the oxy-hybrid on compressor pressure ratio is marginal, especially beyond an optimal value.


1998 ◽  
Vol 66 (6) ◽  
pp. 635-640 ◽  
Author(s):  
Hidekazu KASAI ◽  
Takahiro MATSUO ◽  
Minoru HOSAKA ◽  
Naobumi MOTOHIRA ◽  
Nobuyuki KAMIYA ◽  
...  

Author(s):  
Ji Ho Ahn ◽  
Tong Seop Kim

Owing to the increasing consumption of fossil fuels and emission of greenhouse gases, interests in highly efficient and low carbon emitting power systems are growing fast. Several research groups have been suggesting advanced systems based on fuel cells and have also been applying carbon capture and storage technology to satisfy the demand for clean energy. In this study, the performance of a hybrid system, which is a combination of a molten carbonate fuel cell (MCFC) with oxy-combustion carbon capture and an indirectly fired micro gas turbine (MGT), was predicted. A 2.5 MW MCFC system that is used in commercial applications was used as the reference system so that the results of the study could be applied to practical situations. The ambient pressure type hybrid system was modeled by referring to the design parameters of an MGT that is currently being developed. A semi-closed type design characterized by flow recirculation was adopted for this hybrid system. A part of the recirculating gas is converted into liquefied carbon dioxide and captured for storage at the carbon separation unit (CSU). Almost 100% carbon dioxide capture is possible with this system. In these systems, the output power of the fuel cell is larger than in the normal hybrid system without carbon capture because the partial pressure of carbon dioxide increases. The increased cell power partially compensates for the power loss due to the carbon capture and MGT power reduction. The dependence of net system efficiency of the oxy-hybrid on compressor pressure ratio is marginal, especially beyond an optimal value.


2020 ◽  
Vol 56 (73) ◽  
pp. 10762-10765
Author(s):  
Yasuhiro Sato ◽  
Yoshihito Kayaki ◽  
Takao Ikariya

Metal–NH cooperative Ir complexes having a C–N chelate effectively promoted the reduction of bicarbonate and half-carbonate salts formed from CO2 in 2-propanol under mild conditions to produce formate salts with a maximum turnover number of 3200.


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