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咖啡渣成型制备生物质炭及其CH4/N2分离性能

高雨舟 徐爽 王成通 张雪洁 刘汝帅 陆安慧

高雨舟, 徐爽, 王成通, 张雪洁, 刘汝帅, 陆安慧. 咖啡渣成型制备生物质炭及其CH4/N2分离性能. 新型炭材料(中英文), 2022, 37(6): 1145-1153. doi: 10.1016/S1872-5805(22)60626-7
引用本文: 高雨舟, 徐爽, 王成通, 张雪洁, 刘汝帅, 陆安慧. 咖啡渣成型制备生物质炭及其CH4/N2分离性能. 新型炭材料(中英文), 2022, 37(6): 1145-1153. doi: 10.1016/S1872-5805(22)60626-7
GAO Yu-zhou, Xu Shuang, WANG Cheng-tong, ZHANG Xue-jie, LIU Ru-shuai, LU An-Hui. Preparation of molded biomass carbon from coffee grounds and its CH4/N2 separation performance. New Carbon Mater., 2022, 37(6): 1145-1153. doi: 10.1016/S1872-5805(22)60626-7
Citation: GAO Yu-zhou, Xu Shuang, WANG Cheng-tong, ZHANG Xue-jie, LIU Ru-shuai, LU An-Hui. Preparation of molded biomass carbon from coffee grounds and its CH4/N2 separation performance. New Carbon Mater., 2022, 37(6): 1145-1153. doi: 10.1016/S1872-5805(22)60626-7

咖啡渣成型制备生物质炭及其CH4/N2分离性能

doi: 10.1016/S1872-5805(22)60626-7
基金项目: 中石化大连院项目(HX20200500),辽宁省高等学校创新团队支持计划(LT2016001),中央高校基本科研业务费资助(DUT20GJ215)。
详细信息
    作者简介:

    高雨舟,硕士研究生. E-mail:gyz961210@qq.com

    通讯作者:

    陆安慧,博士,教授. E-mail:anhuilu@dlut.edu.cn

  • 中图分类号: TQ028.2

Preparation of molded biomass carbon from coffee grounds and its CH4/N2 separation performance

Funds: Projects of Sinopec Dalian Institute (HX20200500), Program for Liaoning Innovative Research Team in University (LT2016001), Fundamental Research Funds for the Central Universities (DUT20GJ215).
More Information
  • 摘要: 本文以咖啡渣为原料,硅酸钠为黏结剂和造孔剂,通过挤条成型技术制备柱状炭前驱体,经高温炭化活化和碱洗除硅,获得高强度柱状多孔炭吸附剂(CGCs),研究其CH4/N2的吸附分离性能。红外光谱分析结果显示9wt%硅酸钠溶液与原料质量比为1.5的样品CGC-1.5含有丰富的含氧官能团。CGCs的比表面积和孔容积随着前驱体中硅酸钠含量的增加而增大,其中CGC-1.5的比表面积为527 m2·g−1,总孔容为0.33 cm3·g−1。氮吸附等温线和CO2吸附等温线分析结果表明CGCs含有丰富的微孔、介孔以及大孔(个别样品),微孔主要集中在0.48 nm左右。在298 K和0.1 MPa条件下CGC-1.5对CH4的平衡吸附量为0.87 mmol·g−1,CH4/N2 (3/7)的IAST分离选择性达到10.3,优于多数生物质基多孔炭固体吸附剂和晶态材料。双组份动态穿透测试结果证实该材料在常压和加压条件均具有优异的CH4/N2动态分离性能,298 K时0.11 MPa和0.5 MPa条件下的动态选择性分别达到10.4和17.9,经10次吸-脱附循环测试,吸附量保持不变。CGC-1.5的机械强度高达123 N·cm−1,具有潜在的工业应用前景。
  • FIG. 1962.  FIG. 1962.

    FIG. 1962..  FIG. 1962.

    图  1  样品微观形貌的SEM照片:(a, b) CGC-0, (c, d) CGC-1.5除硅前, (e, f) CGC-1.5除硅后

    Figure  1.  SEM images of (a, b) CGC-0, (c, d) CGC-1.5 before removal of the silica, (e, f) CGC-1.5 after removal of the silica

    图  2  (a) 除硅前后CGCs的XRD谱图与(b) GCCs的红外光谱图

    Figure  2.  (a) XRD patterns of CGCs before and after removal of the silica and (b) FT-IR spectra of CGCs

    图  3  除硅前后CGCs样品的(a) 77 K N2吸脱附等温线和 (b) 孔径分布图(DFT方法), CGCs样品的 (c) 273 K CO2吸脱附等温线和(d) 微孔孔径分布图和累计孔容(DFT方法)

    Figure  3.  (a) N2 adsorption isotherms at 77 K of CGCs before and after removal of silica and (b) pore size distributions (DFT model) from N2 adsorption at 77 K, (c) CO2 adsorption isotherms at 273 K of CGCs,(d) micropore size distributions and cumulative pore volumes(DFT model) from CO2 adsorption at 273 K

    图  4  CGCs在(a) 273 K和 (b) 298 K下的CH4和N2静态吸附曲线, (c) CGCs对CH4/N2的IAST吸附选择性(CH4∶N2=3∶7), (d) CGC-1.5与文献报道的部分吸附剂在CH4吸附容量与CH4/N2吸附选择性方面的对比(CH4∶N2=3∶7, 298 K, 0.1 MPa)[5-7, 10, 12, 15, 20, 21, 27, 30]

    Figure  4.  CH4 and N2 adsorption isotherms of CGCs at (a) 273 K and (b) 298 K, (c) IAST-predicted selectivities of CGCs at 298 K (CH4/N2=3∶7), (d) the comparison between CGC-1.5 and other adsorbents on CH4/N2(3∶7) selectivity and CH4 uptake at 0.1 MPa and 298 K [5-7, 10, 12 , 15, 20, 21, 27, 30]

    图  5  CGC-1.5在不同测试条件下CH4、N2混合气动态穿透曲线 (a) 298 K和0.11 MPa, (b) CGC-1.5和CGC-0动态穿透曲线对比图,(c) 298 K和0.5 MPa, (d)水汽条件下动态穿透曲线

    Figure  5.  Breakthrough curves for CH4/N2 mixture of CGC-1.5 at different test conditions (a) 298 K and 0.11 MPa, (b) comparison of breakthrough curves between CGC-1.5 and CGC-0, (c) 298 K and 0.5 MPa, (d) breakthrough curve tested in humid condition

    图  6  在298 K和0.11 MPa条件下CGC-1.5的(a) 吸-脱附循环测试, (b) 10次循环测试CH4动态吸附量, (c) CGCs的机械强度

    Figure  6.  (a) Cycle test of CH4 adsorption-desorption on CGC-1.5 at 298 K and 0.11 MPa, followed a regeneration by Ar flow at 298 K, (b) CH4 uptakes on CGC-1.5 at 298 K in 10 times adsorption-desorption cycles, (c) mechanical strength of CGCs

    表  1  CGCs的孔结构参数

    Table  1.   Structural parameters of CGCs

    SampleSBET
    (m2·g−1)
    Smic
    (m2·g−1)
    Vtotal
    (cm3·g−1)
    Vmic
    (cm3·g−1)
    CGC-04473710.190.14
    CGC-1.12421770.160.07
    CGC-1.1
    (with SiO2)
    2411930.110.07
    CGC-1.33352280.230.09
    CGC-1.55273710.330.15
    下载: 导出CSV

    表  2  CGCs在298 K和0.1 MPa条件对CH4、N2的吸附容量及IAST选择性(CH4∶N2=3∶7)

    Table  2.   CH4 and N2 adsorption capacities of CGCs at 298 K, 0.1 MPa and the IAST selectivities of CGCs (CH4∶N2=3∶7)

    SampleCH4 adsorption capacity (mmol·g−1)N2 adsorption capacity (mmol·g−1)IAST Selectivity
    CGC-1.10.700.207.8
    CGC-1.30.730.196.6
    CGC-1.50.870.2010.3
    下载: 导出CSV

    表  3  CGCs在298 K下对CH4和N2的Langmuir-Freundlich拟合参数

    Table  3.   Langmuir-Freundlich fitting parameters of CH4 and N2 on CGCs at 298 K

    SampleQs
    (mmol·g−1
    K*10−3
    (kpa)
    mR2
    N2CGC-1.10.408.801.060.99997
    CGC-1.30.379.841.070.99996
    CGC-1.50.3710.351.080.99993
    CH4CGC-1.11.478.570.900.99995
    CGC-1.31.508.791.000.99979
    CGC-1.51.967.290.890.99997
    下载: 导出CSV

    表  4  在298 K, 1.1 bar条件下CGCs的CH4、N2动态吸附数据

    Table  4.   Dynamic adsorption capacity of CH4 and N2 on CGCs at 298 K and 1.1 bar

    SampleCH4 dynamic adsorption capacity
    (mmol·g−1)
    N2 dynamic adsorption capacity
    (mmol·g−1)
    Separation time
    (min)
    SCH4/N2
    CGC-1.50.250.0561510.4
    CGC-00.310.50701.4
    下载: 导出CSV
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出版历程
  • 收稿日期:  2022-04-24
  • 修回日期:  2022-06-14
  • 网络出版日期:  2022-06-29
  • 刊出日期:  2022-11-28

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