Hydrogen production by catalytic gasification of coal in supercritical water with alkaline catalysts.pdf
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journal homepage: www.elsevier .com/locate/heHydrogen production by catalytic gasification of
coal in supercritical water with alkaline catalysts:
Explore the way to complete gasification of coalZhiwei Ge, Hui Jin, Liejin Guo*
State Key Laboratory of Multiphase Flow in Power Engineering, Xian Jiaotong University, Xian 710049, Chinaa r t i c l e i n f o
Article history:
Received 17 April 2014
Received in revised form
17 September 2014
Accepted 22 September 2014
Available online 12 October 2014
Keywords:
Supercritical water
Coal
Gasification
Hydrogen
Catalyst* Corresponding author. Tel.: t86 29 8266 38
E-mail address: lj-guo@ (
/10.1016/j.ijhydene.2014.09.1
0360-3199/Copyright ? 2014, Hydrogen Enera b s t r a c t
Supercritical water gasification (SCWG) of coal is a promising technology for clean coal
utilization. In this paper, hydrogen production by catalytic gasification of coal in super-
critical water (SCW) was carried out in a micro batch reactor with various alkaline cata-
lysts: Na2CO3, K2CO3, Ca(OH)2, NaOH and KOH. H2 yield in relation to the alkaline catalyst
was in the following order: K2CO3 z KOH z NaOH Na2CO3 Ca(OH)2. Then, hydrogen
production by catalytic gasification of coal with K2CO3 was systematically investigated in
supercritical water. The influences of the main operating parameters including feed con-
centration, catalyst loading and reaction temperature on the gasification characteristics of
coal were investigated. The experimental results showed that carbon gasification efficiency
(CE, mass of carbon in gaseous product/mass of carbon in coal 100%) and H2 yield
increased with increasing catalyst loading, increasing temperature, and decreasing coal
concentration. In particular, coal was completely gasified at 700 C when the weight ratio of
K2CO3 to coal was 1, and it was encouraging that raw coal was con
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