Process development and performance assessment of flexible calcium looping biomass gasification for production of renewable gas with adjustable composition

被引:6
|
作者
Zalec, Domen [1 ]
Hanak, Dawid P. [2 ]
Moze, Matic [1 ]
Golobic, Iztok [1 ]
机构
[1] Univ Ljubljana, Fac Mech Engn, Askerceva 6, SI-1000 Ljubljana, Slovenia
[2] Cranfield Univ, Sch Water Energy & Environm, Energy & Power, Cranfield, Beds, England
基金
英国工程与自然科学研究理事会;
关键词
biomethane; calcium looping; hydrogen; process design; simulation; sorption enhanced gasification; SORPTION ENHANCED GASIFICATION; SITU CO2 CAPTURE; BUBBLING FLUIDIZED-BED; SER STEAM GASIFICATION; HYDROGEN-PRODUCTION; ATMOSPHERIC-PRESSURE; COAL/CAO REACTION; SYNGAS PRODUCTION; HYPR-RING; TEMPERATURE;
D O I
10.1002/er.7558
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 recent years, the field of biomass gasification as a method of transforming biomass into a more useable gaseous fuel experienced expedited development since it represents a prominent way to achieve sustainability goals and targets set by the Paris accord and, more recently, the European Green Deal. The use of natural gas is projected to reduce with the transition toward exploitation of renewable gas, while a new area of hydrogen applications is also emerging. However, with uncertain production of current processes, and consumption patterns seen on the market, an opportunity for a new flexible process exists. This article investigates a concept process design of sorption-enhanced gasification (SEG) based on calcium looping. Aspen Plus simulation software was used to develop and simulate the process models for flexible production of bio-SNG or bio-H-2. The process parameters can be manipulated to either achieve a high-purity bio-H-2 (>96 mol%) or high-purity bio-SNG (>95 mol%), as well as any other combination of the two main products. The concept process is based on a low-pressure, low-temperature dual-fluidized bed reactor with steam as a gasifying agent and an additional downstream Sabatier process reactor to achieve high CH4 contents. The simulated process achieves process efficiency of up to 62.2%(LHV) and 78.0%(LHV) for H-2 and CH4 production, respectively, with production yields reaching 0.112 kg H-2/kg BM and 0.23 kg CH4/kg BM. These values were validated and benchmarked against comparable process designs, and the performance of the proposed process was found to be on par or superior. Overall, the proposed process design exhibits clear benefits of calcium looping gasification, with high process efficiency, negligible NOx, SO2, and H2S content, and high flexibility. Therefore, the proposed process addressed and successfully solved some of the key challenges of achieving viability of a gasification plant on a commercial scale.
引用
收藏
页码:6197 / 6215
页数:19
相关论文
共 50 条
  • [21] Flexible sorption enhanced gasification (SEG) of biomass for the production of synthetic natural gas (SNG) and liquid biofuels: Process assessment of stand-alone and power-to-gas plant schemes for SNG production
    Martinez, I.
    Romano, M. C.
    ENERGY, 2016, 113 : 615 - 630
  • [22] Parametric modeling and performance assessment of a novel cogeneration system of biomass chemical looping gasification driven by solar energy
    Mu, Lin
    Xie, Pengwei
    Hu, Tiancai
    Shang, Yan
    Pu, Hang
    Dong, Ming
    Huo, Zhaoyi
    BIOMASS CONVERSION AND BIOREFINERY, 2024, 15 (6) : 9531 - 9552
  • [23] Feasibility analysis of H2 production by calcium looping process based on coal gasification in a transport reactor
    Wang, Xun
    Gao, Jun
    Jiang, Liaxia
    INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2016, 41 (28) : 12000 - 12018
  • [24] Optimizing performance of iron-rich sludge ash as cost-effective oxygen carrier by calcium-based additive for syngas production from biomass chemical-looping gasification
    Fang, Hua
    Yi, Fan
    Sun, Meng
    Gao, Haojie
    Dai, Ying
    Wang, Xiaoyuan
    Wang, Yinfeng
    Guo, Kai
    Chen, Jianbiao
    Zhu, Yuezhao
    BIORESOURCE TECHNOLOGY, 2023, 385
  • [25] Performance Analysis of a New Integrated Gasification Technology Driven by Biomass for Hydrogen and Electricity Cogeneration with a Dual Chemical Looping Process
    Zhu, Lin
    Chen, Hu
    Zhang, Zheng
    ENERGY TECHNOLOGY, 2016, 4 (10) : 1274 - 1285
  • [26] Hydrogen production via integrated configuration of steam gasification process of biomass and water-gas shift reaction: Process simulation and optimization
    Babatabar, Mokhtar Akhond
    Saidi, Majid
    INTERNATIONAL JOURNAL OF ENERGY RESEARCH, 2021, 45 (13) : 19378 - 19394
  • [27] Performance assessment of hydrogen production from a solar-assisted biomass gasification system
    Kalinci, Yildiz
    Hepbasli, Arif
    Dincer, Ibrahim
    INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2013, 38 (14) : 6120 - 6129
  • [28] A two-stage circulated fluidized bed process to minimize tar generation of biomass gasification for fuel gas production
    Wang, Chao
    Zhu, Lianfeng
    Zhang, Mengjuan
    Han, Zhennan
    Jia, Xin
    Bai, Dingrong
    Duo, Wenli
    Bi, Xiaotao
    Abudula, Abuliti
    Guan, Guoqing
    Xu, Guangwen
    APPLIED ENERGY, 2022, 323
  • [29] Biomass Gasification Integrated with Chemical Looping System for Hydrogen and Power. Coproduction Process - Thermodynamic and Techno-Economic Assessment
    Jiang, Peng
    Berrouk, Abdallah S.
    Dara, Satyadileep
    CHEMICAL ENGINEERING & TECHNOLOGY, 2019, 42 (05) : 1153 - 1168
  • [30] Negative emissions power plant based on flexible calcium-looping process integrated with renewables and methane production
    Ortiz, C.
    Garcia-Luna, S.
    Carro, A.
    Chacartegui, R.
    Perez-Maqueda, L.
    RENEWABLE & SUSTAINABLE ENERGY REVIEWS, 2023, 185