期刊
JOURNAL OF CLEANER PRODUCTION
卷 178, 期 -, 页码 325-342出版社
ELSEVIER SCI LTD
DOI: 10.1016/j.jclepro.2017.12.279
关键词
Ammonia; Hydrogen; Process optimization; Solar energy; Water; Wind energy
资金
- TCUE fellowship from Fundacion Universidad - Empresa USAL
- MINECO [DPI2015-67341-C2-1-R]
- FPU grant from MECD
In this work a production facility of ammonia has been evaluated using air and water as raw materials. Nitrogen is obtained from air separation using a Linde's double column. Hydrogen is produced from water splitting. Next, hydrogen and oxygen are purified to remove water and traces of chemicals. Finally, ammonia is synthesized in a three bed packed reactor. Two cooling designs were considered, indirect and direct cooling. The ammonia is recovered by condensation using the cold air. Power for compression and electrolysis is obtained from renewable sources either solar, photovoltaic, or wind energy. The process is simulated developing surrogate models for each of the units involved with special attention to the electrolyzer, Linde's column, synthesis reactor and ammonia recovery. In particular, the multibed reactor is modeled rigorously off line to validate the conversions and its operation. The full process is formulated as an MINLP problem. Solar energy and indirect cooling are selected for the production of ammonia. However, the high cost of panels results in high investment capital, over 1500 M(sic), but promising production cost of ammonia, 1.35(sic)/kg. (C) 2018 Elsevier Ltd. All rights reserved.
作者
我是这篇论文的作者
点击您的名字以认领此论文并将其添加到您的个人资料中。
推荐
暂无数据