Organic municipal solid waste derived hydrogen production through supercritical water gasification process configured with K2CO3/SiO2: Performance study

被引:6
|
作者
Soudagar, Manzoore Elahi M. [1 ,2 ,3 ]
Upadhyay, Viyat Varun [4 ]
Bhooshanam, N. Naga [5 ]
Singh, Ravindra Pratap [4 ]
Rabadiya, Dhaval [6 ]
Venkatesh, R. [7 ]
Mohanavel, Vinayagam [8 ,9 ,10 ]
Alotaibi, Majed A. [11 ]
Seikh, A. H. [12 ]
机构
[1] Lishui Univ, Coll Engn, Lishui 323000, Zhejiang, Peoples R China
[2] Lishui Univ, Lishui Ind Technol Res Inst, Lishui 323000, Peoples R China
[3] Chitkara Univ, Ctr Res Impact & Outcome, Rajpura 140417, Punjab, India
[4] GLA Univ, Dept Mech Engn, Mathura 281406, Uttar Pradesh, India
[5] Aditya Univ, Dept Mech Engn, Surampalem 533437, Andhra Pradesh, India
[6] Parul Univ, Fac Management Studies, PO Limda, Vadodara 391760, Gujarat, India
[7] Saveetha Univ, Saveetha Inst Med & Tech Sci SIMATS, Saveetha Sch Engn, Dept Mech Engn, Chennai 602105, Tamilnadu, India
[8] Bharath Inst Higher Educ & Res, Ctr Mat Engn & Regenerat Med, Chennai 600073, Tamil Nadu, India
[9] Graphic Era Hill Univ, Dept Mech Engn, Dehra Dun 248002, Uttarakhand, India
[10] Graphic Era Univ, Dept Mech Engn, Dehra Dun 248002, Uttarakhand, India
[11] King Saud Univ, Coll Engn, Dept Elect Engn, POB 2455, Riyadh 11451, Saudi Arabia
[12] King Saud Univ, Coll Engn, Dept Mech Engn, Riyadh 11421, Saudi Arabia
来源
BIOMASS & BIOENERGY | 2024年 / 190卷
关键词
Gasification; Hydrogen; K (2) CO (3) /SiO 2 Catalyst; Processing time; Temperature; Properties; SEWAGE-SLUDGE; CHEMICAL ACTIVATION; PURIFICATION; PARAMETERS; PYROLYSIS; CARBON; MODEL;
D O I
10.1016/j.biombioe.2024.107379
中图分类号
S2 [农业工程];
学科分类号
0828 ;
摘要
Cities worldwide face a significant public health and environmental challenge in handling municipal solid waste (MSW). This research exposed an effective utilization of MSW as the source for hydrogen production via a supercritical water gasification process under 450-650 degrees C at 15-45 min processing time. The impacts of gasification temperature and processing time on the functional properties of hydrogen production are studied. Its results are compared to identify the optimum processing temperature and processing time to adopt the system. Integrating 3 wt% silicon dioxide (SiO2) nanoparticles/3 wt% of potassium carbonate (K2CO3) enhances hydrogen production by increasing the catalyst's surface area and improving the stability of active sites, leading to more efficient gasification reactions. Increasing the gasification temperature from 450 to 650 degrees C significantly raises the hydrogen molar fraction and gas yield with peak gasification efficiency (GE) and hydrogen efficiency (HE) values. The gasifier functioned with catalyst (3 wt% K2CO3/SiO2) under 650 degrees C gasification temperature and 45min gasification time influenced better output responses like improved hydrogen gas yield of 63.7 mol/kg, higher gasification efficiency of 59.8 %, better hydrogen efficiency (63.4 %) and increased carbon conversion efficiency of 63.4 and 42.5 % respectively.
引用
收藏
页数:9
相关论文
共 42 条
  • [21] Experimental study on steam co-gasification of biomass/municipal solid waste (MSW) for H2-rich gas production
    Tian, Ye
    Liu, Wenze
    Zeng, Chongzhe
    Zhou, Xiong
    Du, Shihan
    Wang, Yihao
    Li, Heng
    JOURNAL OF THE ENERGY INSTITUTE, 2025, 118
  • [22] K2CO3-catalyzed gasification of coal of different ranks in supercritical water for hydrogen production: A general kinetic model with good coal adaptability
    Ou, Guobiao
    Ren, Yifei
    Jin, Hui
    Guo, Liejin
    INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2023, 48 (75) : 29082 - 29096
  • [23] Catalytic steam reforming of biomass-derived tar for hydrogen production with K2CO3/NiO/γ-Al2O3 catalyst
    Kuchonthara, Prapan
    Puttasawat, Buppha
    Piumsomboon, Pornpote
    Mekasut, Lursuang
    Vitidsant, Tharapong
    KOREAN JOURNAL OF CHEMICAL ENGINEERING, 2012, 29 (11) : 1525 - 1530
  • [24] Catalytic steam reforming of biomass-derived tar for hydrogen production with K2CO3/NiO/γ-Al2O3 catalyst
    Prapan Kuchonthara
    Buppha Puttasawat
    Pornpote Piumsomboon
    Lursuang Mekasut
    Tharapong Vitidsant
    Korean Journal of Chemical Engineering, 2012, 29 : 1525 - 1530
  • [25] Increased hydrogen production in co-gasification of sewage sludge and municipal solid waste through two-stage fluidized bed gasification process over metal-coated activated carbon
    Lin, Chiou-Liang
    Yang, Hui-Hsuan
    Su, En-Chin
    FUEL, 2024, 371
  • [26] HYDROGEN-PRODUCTION FROM WATER BY IN2O3 AND K2CO3 USING GRAPHITE, ACTIVE-CARBON AND BIOMASS AS REDUCTANTS
    OTSUKA, K
    TAKIZAWA, Y
    SHIBUYA, S
    MORIKAWA, A
    CHEMISTRY LETTERS, 1981, (03) : 347 - 350
  • [27] Co-production of high strength extruded activated carbon and hydrogen-rich syngas via K2CO3 catalytic incomplete gasification of coal
    Liu P.
    Wang J.
    Yao M.
    Song X.
    Lü P.
    Bai Y.
    Yu G.
    Meitan Xuebao/Journal of the China Coal Society, 2023, 48 : 728 - 739
  • [28] Molecular dynamics study on thermophysical properties of K2CO3 molten salt-based SiO2 nanofluids using Buckingham potential framework
    Ji, Chang
    Yang, Xueming
    Ma, Yongfu
    Chi, He
    Xie, Jianfei
    JOURNAL OF MOLECULAR LIQUIDS, 2024, 407
  • [29] Study on the suppression of hydrogen-air explosions by ultrafine water mist containing KCl, K2CO3, or NaCl
    Zhao, Xiangdi
    Zhao, Jiangyue
    Zhu, Xiaolong
    Xu, Wei
    Zhang, Guangwen
    Wang, Chun
    Wang, Xishi
    FIRE SAFETY JOURNAL, 2025, 153
  • [30] Computational fluid dynamics study of sequential hydrothermal carbonization and CO2-gasification of municipal solid waste-coconut husk-derived hydrochar for tunable syngas production
    Mateo, Rainier Sam G.
    Mosqueda, Alexander O.
    Kuttin, Kannie Winston
    Yu, Haowen
    Pico, Alec Paolo V. Dy
    Abesamis, Mariane Fe A.
    Ding, Lu
    Yu, Guangsuo
    FUEL, 2025, 388