Microalgae-based coproduction of ammonia and power employing chemical looping process

被引:23
|
作者
Nurdiawati, Anissa [1 ]
Zaini, Ilman Nuran [2 ]
Amin, Mohamad [3 ]
Sasongko, Dwiwahju [4 ]
Aziz, Muhammad [5 ]
机构
[1] Tokyo Inst Technol, Dept Transdisciplinary Sci & Engn, Meguro Ku, 2-12-1 Ookayama, Tokyo 1528550, Japan
[2] Royal Inst Technol KTH, Dept Mat Sci & Engn, Brinellvagen 23, S-10044 Stockholm, Sweden
[3] State Univ Malang, Dept Biol Educ, Semarang St 5, East Java 65145, Indonesia
[4] ITB, Dept Chem Engn, Ganesha 10, Bandung 40132, Indonesia
[5] Tokyo Inst Technol, Inst Innovat Res, Meguro Ku, 2-12-1 Ookayama, Tokyo 1528550, Japan
来源
CHEMICAL ENGINEERING RESEARCH & DESIGN | 2019年 / 146卷
关键词
Hydrogen production; Ammonia synthesis; Chemical looping; Gasification; System integration; Energy efficiency; FLUIDIZED-BED REACTOR; HYDROGEN-PRODUCTION; STEAM GASIFICATION; BIOMASS; ENERGY; COMBUSTION; OXIDE; COGENERATION; GENERATION; FUEL;
D O I
10.1016/j.cherd.2019.04.013
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Hydrogen (H-2) production and storage technologies are the main challenges in the realization of H-2 utilization in which the goal is to achieve high conversion efficiencies and a high storage density. In this study, microalgae gasification and ammonia (NH3) production are proposed to efficiently convert microalgae to NH3 for efficient H-2 storage. The integrated system comprises drying, gasification, syngas chemical looping (SCL), NH3 synthesis, and power generation. Microalgae are converted to syngas in the gasification module and then introduced into the SCL module to produce high-purity H-2 and a separated carbon dioxide (CO2) stream. SCL is also employed to produce a nitrogen (N-2)-rich stream, which can replace a conventional air separation unit (ASU) system. The three operating parameters that are evaluated in this study include the steam to biomass (S/B) ratio during gasification, reducer operating temperature during chemical looping, and recycle to feed streams ratio. An increase in the S/B ratio has a negative effect on the total energy efficiency because the efficiency decreases owing to the reduced production of H-2 in the oxidizer. To maximize the efficiency of NH3 production, a higher recycle ratio is favorable. The proposed integrated system can obtain high total energy efficiency of up to 64.3%, comprising 63.8% NH3 production efficiency and 0.05% power generation efficiency. (C) 2019 Institution of Chemical Engineers. Published by Elsevier B.V. All rights reserved.
引用
收藏
页码:311 / 323
页数:13
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