Hydrogen Production by Catalytic Supercritical Water Gasification of Black Liquor-Based Wastewater

被引:10
|
作者
Demey, Hary [1 ]
Ratel, Gilles [1 ]
Lacaze, Bruno [1 ]
Delattre, Olivier [1 ]
Haarlemmer, Geert [1 ]
Roubaud, Anne [1 ]
机构
[1] Univ Grenoble Alpes, CEA, LITEN, DTCH,Lab Reacteurs & Procedes LRP, F-38000 Grenoble, France
基金
欧盟地平线“2020”;
关键词
black liquor; catalyst; supercritical water gasification (SCWG); wastewater treatment; hydrogen production; SEWAGE-SLUDGE; GLUCOSE; BIOMASS; ENERGY; PULP;
D O I
10.3390/en16083343
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
In this work, the wastewater obtained from the hydrothermal liquefaction of black liquor was treated and valorized for hydrogen production by supercritical water gasification (SCWG). The influence of the main process parameters on the conversion yield was studied. The experiments were conducted at three different temperatures (below and above the critical point of water): 350 degrees C, 450 degrees C and 600 degrees C. The results showed that by increasing the temperature from 350 degrees C to 600 degrees C, the total gas yield was highly improved (from 1.9 mol gas/kg of dried feedstock to 13.1 mol gas/kg of dried feedstock). The H-2 composition was higher than that of CH4 and CO2 at 600 degrees C, and the HHV of the obtained gas was 61.2 MJ/kg. The total organic carbon (TOC) removal efficiency was also improved by increasing the temperature, indicating that the SCWG process could be used for both applications: (i) for wastewater treatment; (ii) for producing a high calorific gas. The experiments with the Raney-nickel catalyst were performed in order to study the catalyst's influence on the conversion yield. The results indicated that the catalyst enhances carbon conversion and gas production from mild to higher temperatures. The maximum total gas yield obtained with this catalyst was 32.4 mol gas/kg of dried feedstock at 600 degrees C, which is 2.5 times higher than that obtained at the same operating conditions without a catalyst. The H-2 yield and the HHV of the obtained gas with the catalyst were 20.98 mol gas/kg dried feedstock and 80.2 MJ/kg, respectively. However, the major contribution of the catalytic SCWG process was the improvement of the total gas yield at mild operating temperatures (450 degrees C), and the obtained performance was even higher than that obtained at 600 degrees C without catalyst (17.81 mol gas/kg dried feedstock and 13.1 mol gas/kg dried feedstock, respectively). This is a sustainable approach for treating wastewater at mild temperatures by catalytic SCWG.
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页数:13
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