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基于炭气原位耦合重整的秸秆热解设备研制

秦超 孟海波 李庆达 叶炳南 于炳驰 丛宏斌

秦超,孟海波,李庆达,等.基于炭气原位耦合重整的秸秆热解设备研制[J].农业工程,2022,12(5):30-35. doi: 10.19998/j.cnki.2095-1795.2022.05.007
引用本文: 秦超,孟海波,李庆达,等.基于炭气原位耦合重整的秸秆热解设备研制[J].农业工程,2022,12(5):30-35. doi: 10.19998/j.cnki.2095-1795.2022.05.007
QIN Chao,MENG Haibo,LI Qingda,et al.Development of straw pyrolysis equipment based on biochar syngas coupling reforming[J].Agricultural Engineering,2022,12(5):30-35. doi: 10.19998/j.cnki.2095-1795.2022.05.007
Citation: QIN Chao,MENG Haibo,LI Qingda,et al.Development of straw pyrolysis equipment based on biochar syngas coupling reforming[J].Agricultural Engineering,2022,12(5):30-35. doi: 10.19998/j.cnki.2095-1795.2022.05.007

基于炭气原位耦合重整的秸秆热解设备研制

doi: 10.19998/j.cnki.2095-1795.2022.05.007
基金项目: 国家重点研发计划项目(2019YFD1100501);黑龙江八一农垦大学“三纵”科研支持计划重点专项(ZDZX202102)
详细信息
    作者简介:

    秦超,硕士生,主要从事农业工程与信息技术研究 E-mail:790647098@qq.com

    李庆达,博士,教授,主要从事农业工程与信息技术研究 E-mail:liqingda23@126.com

  • 中图分类号: S216.2

Development of Straw Pyrolysis Equipment Based on Biochar Syngas Coupling Reforming

  • 摘要:

    针对当前生物质热解炭化设备存在产物质量较差、能量损耗严重等问题,采用多级布风搅拌和气体回流重整等方法,提出生物质炭气原位耦合重整工艺路线,并对炉体、压实机构和多级布风搅拌出料机构进行设计,研发立式移动床生物质炭化设备。以花生壳为原料开展热解炭化试验,结果表明,原料处理能力1312 kg/h,生物炭得率27.8%,热解气热值6.3 MJ/m3,焦油转化率71.3%,各项性能指标均达到设计要求。

     

  • 图 1  生物质内加热炭化生产工艺流程

    Figure 1.  Biomass internal heating charring production process

    图 2  秸秆内加热移动床热解设备

    1. 进料斗 2. 上料输送带 3. 热解炉 4. 鼓风机 5. 引风机6. 气体采样口 7. 燃烧器 8. 三联冷凝器 9. 炭箱10. 生物炭输送带 11. 出炭螺旋 12. 多联出炭通路

    Figure 2.  Straw internal heating moving bed pyrolysis equipment

    图 3  炉体结构

    1. 进料口 2. 热解气上出口 3. 热解气下出口 4. 上空气入口5. 下空气入口 6. 热解气回流口 7. 出炭口 8. 点火口9. 下料位计 10. 上料位计

    Figure 3.  Structure of furnace body

    图 4  压实器结构

    1. 压实板 2. 稳压排气口 3. 压实器电机 4. 进料口 5. 压实器传动轴

    Figure 4.  Structure of compactor

    图 5  多级搅拌出料机构结构

    1. 搅拌杆 2. 布风板 3. 出料杆 4. 驱动电机

    Figure 5.  Structure of multistage mixing discharge mechanism

    图 6  出料机构运动分析

    Figure 6.  Motion analysis of discharge mechanism

    图 7  设备实物

    Figure 7.  Physical map of equipment

    表  1  立式移动床热解反应器主要技术参数

    Table  1.   Main technical parameters of vertical moving bed pyrolysis reactor

    指标参数
    炉体高度/mm3 500
    炉体直径/mm1 200
    配套动力/kW21.3
    加热方式内加热
    设计原料处理能力/(kg·h−11 300
    出炭口数量4
    布风方式环状多级布风
    下载: 导出CSV

    表  2  试验结果

    Table  2.   Test result

    测试指标测得值
    原料处理量/(kg·h−11312
    生物炭得率/%27.8
    出炭温度/°C462
    热解气热值/(MJ·m−36.3
    焦油转化率/%71.3
    下载: 导出CSV
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  • 收稿日期:  2022-01-04
  • 修回日期:  2022-02-21
  • 出版日期:  2022-05-20

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