Nonisothermal catalytic liquefaction of corn stalk in subcritical and supercritical water

Nonisothermal catalytic liquefaction of corn stalk in subcritical and supercritical water
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DOI:
10.1021/ef0300141
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发表时间:
2004
期刊:
影响因子:
5.3
通讯作者:
C. Song;Haoquan Hu;Shengwei Zhu;Gang Wang;Guohua Chen
C. Song;Haoquan Hu;Shengwei Zhu;Gang Wang;Guohua Chen
中科院分区:
工程技术3区
文献类型:
--
作者:
C. Song;Haoquan Hu;Shengwei Zhu;Gang Wang;Guohua Chen

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采用热重法(TG)对玉米秸秆进行热解,在碳酸钠(na2co3)和碳酸钠(na2co3)催化和不催化条件下,采用非等温流体萃取技术对玉米秸秆进行半连续液化研究。结果表明,在DTG曲线上,玉米秸秆的主要热解区域为~ 500 ~ 650 K,最大热解速率出现在~ 600 K。催化剂的存在对热解有明显的影响,特别是在550-650 K的温度范围内。当催化剂的添加量大于1.0 wt %时,催化剂的DTG曲线从双峰变为单峰,对半纤维素的影响大于对纤维素和木质素的影响。动力学分析表明,催化剂添加量不同,主要热解范围(10 ~ 70 wt %)的活化能也不同。以3ml /min的水为溶剂,在25mpa压力下,添加或不添加1.0 wt %的na2co3,玉米秸秆的液化转化率分别可达95.7%和95.4%。催化剂的主要作用是提高生物油的收率,从没有催化剂的33.4%提高到1.0 wt % na2co3的47.2%。催化剂对较高温度下的液化有积极作用,可以提高液产物收率,改善液产物质量。与不使用催化剂相比,使用催化剂可以获得更多的生物油和更少的生物气。在实验条件下,玉米秸秆的热解和液化都可能发生两段主反应。
The pyrolysis of corn stalk was performed with thermogravimetry (TG), and its liquefaction was investigated in a semicontinuous apparatus with a nonisothermal fluid extraction technique, both with and without sodium carbonate (Na 2 CO 3 ) as a catalyst. The results indicated that the main pyrolysis region of corn stalk is ∼500-650 K and the maximum rate occurs at ∼600 K on the differential thermogravimetry (DTG) curve. The presence of a catalyst has an obvious effect on the pyrolysis, especially in the temperature range of 550-650 K. When more than 1.0 wt % of catalyst was added, the DTG curve is altered greatly, from two peaks to one, for the catalyst, which has a greater effect on hemicellulose than on cellulose and lignin. Kinetic analysis shows that the activation energy in the main pyrolysis range (10-70 wt %) varies with different amounts of catalyst addition. The liquefaction conversion of corn stalk with 3 mL/min of water as a solvent at a pressure of 25 MPa, with or without the addition of 1.0 wt % of Na 2 CO 3 , is up to 95.7 and 95.4 wt %, respectively. The catalyst mainly improved the yield of bio-oil, from 33.4% without a catalyst, increasing to 47.2% with 1.0 wt % of Na 2 CO 3 . The catalyst has a positive effect on the liquefaction at relatively higher temperatures and can increase the yield of liquid product, as well as improve the quality of liquid product. More bio-oil and less gas can be obtained with a catalyst than that without a catalyst. A two-stage main reaction may occur for both the pyrolysis and liquefaction of corn stalk under the experimental conditions.