A novel catalyst–sorbent system for an efficient H2 production with in-situ CO2 capture

2012 ◽  
Vol 37 (6) ◽  
pp. 4987-4996 ◽  
Author(s):  
M.H. Halabi ◽  
M.H.J.M. de Croon ◽  
J. van der Schaaf ◽  
P.D. Cobden ◽  
J.C. Schouten
2014 ◽  
Vol 63 ◽  
pp. 6815-6823 ◽  
Author(s):  
M.V. Gil ◽  
G. Esteban-Díez ◽  
C. Pevida ◽  
D. Chen ◽  
F. Rubiera

2019 ◽  
Vol 5 (2) ◽  
pp. 22 ◽  
Author(s):  
Zhengyang Zhao ◽  
Pei Yu ◽  
Bhuvana K. Shanbhag ◽  
Phillip Holt ◽  
Yu Lin Zhong ◽  
...  

Formic acid (FA) is a promising reservoir for hydrogen storage and distribution. Its dehydrogenation releases CO2 as a by-product, which limits its practical application. A proof of concept for a bio-catalytic system that simultaneously combines the dehydrogenation of formic acid for H2, in-situ capture of CO2 and its re-hydrogenation to reform formic acid is demonstrated. Enzymatic reactions catalyzed by carbonic anhydrase (CA) and formate dehydrogenase (FDH) under ambient condition are applied for in-situ CO2 capture and re-hydrogenation, respectively, to develop a sustainable system. Continuous production of FA from stripped CO2 was achieved at a rate of 40% using FDH combined with sustainable co-factor regeneration achieved by electrochemistry. In this study, the complete cycle of FA dehydrogenation, CO2 capture, and re-hydrogenation of CO2 to FA has been demonstrated in a single system. The proposed bio-catalytic system has the potential to reduce emissions of CO2 during H2 production from FA by effectively using it to recycle FA for continuous energy supply.


2013 ◽  
Author(s):  
Saeed Danaei Kenarsari ◽  
Yuan Zheng

A lab-scale CO2 capture system is designed, fabricated, and tested for performing CO2 capture via carbonation of very fine calcium oxide (CaO) with particle size in micrometers. This system includes a fixed-bed reactor made of stainless steel (12.7 mm in diameter and 76.2 mm long) packed with calcium oxide particles dispersed in sand particles; heated and maintained at a certain temperature (500–550°C) during each experiment. The pressure along the reactor can be kept constant using a back pressure regulator. The conditions of the tests are relevant to separation of CO2 from combustion/gasification flue gases and in-situ CO2 capture process. The inlet flow, 1% CO2 and 99% N2, goes through the reactor at the flow rate of 150 mL/min (at standard conditions). The CO2 percentage of the outlet gas is monitored and recorded by a portable CO2 analyzer. Using the outlet composition, the conversion of calcium oxide is figured and employed to develop the kinetics model. The results indicate that the rates of carbonation reactions considerably increase with raising the temperature from 500°C to 550°C. The conversion rates of CaO-carbonation are well fitted to a shrinking core model which combines chemical reaction controlled and diffusion controlled models.


2020 ◽  
Vol 59 (18) ◽  
pp. 8571-8580
Author(s):  
Joseph G. Yao ◽  
Matthew E. Boot-Handford ◽  
Zili Zhang ◽  
Geoffrey C. Maitland ◽  
Paul S. Fennell

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