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采用活性炭吸附法通过厌氧消化产生生物甲烷。

Bio-methane from an-aerobic digestion using activated carbon adsorption.

作者信息

Farooq Muhammad, Bell Alexandra H, Almustapha M N, Andresen John M

机构信息

Institute of Mechanical, Process & Energy Engineering, Heriot-Watt University, United Kingdom; Department of Mechanical Engineering, University of Engineering & Technology Lahore (KSK Campus), Pakistan.

Institute of Mechanical, Process & Energy Engineering, Heriot-Watt University, United Kingdom.

出版信息

Anaerobe. 2017 Aug;46:33-40. doi: 10.1016/j.anaerobe.2017.05.003. Epub 2017 May 5.

Abstract

There is an increasing global demand for carbon-neutral bio-methane from an-aerobic digestion (AD) to be injected into national gas grids. Bio-gas, a methane -rich energy gas, is produced by microbial decomposition of organic matter through an-aerobic conditions where the presence of carbon dioxide and hydrogen sulphide affects its performance. Although the microbiological process in the AD can be tailored to enhance the bio-gas composition, physical treatment is needed to convert the bio-gas into bio-methane. Water washing is the most common method for upgrading bio-gas for bio-methane production, but its large use of water is challenging towards industrial scale-up. Hence, the present study focuses on scale-up comparison of water washing with activated-carbon adsorption using HYSYS and Aspen Process Economic Analyzer. The models show that for plants processing less than 500 m/h water scrubbing was cost effective compared with activated carbon. However, against current fossil natural-gas cost of about 1 p/kWh in the UK both relied heavily on governmental subsidies to become economically feasible. For plants operating at 1000 m/hr, the treatment costs were reduced to below 1.5 p/kWh for water scrubbing and 0.9 p/kWh for activated carbon where the main benefits of activated carbon were lower capital and operating costs and virtually no water losses. It is envisioned that this method can significantly aid the production of sustainable bio-methane.

摘要

全球对通过厌氧消化(AD)产生的碳中和生物甲烷注入国家天然气网络的需求日益增加。沼气是一种富含甲烷的能源气体,它是通过有机物在厌氧条件下的微生物分解产生的,其中二氧化碳和硫化氢的存在会影响其性能。尽管可以调整AD中的微生物过程以提高沼气成分,但仍需要物理处理将沼气转化为生物甲烷。水洗是将沼气升级为生物甲烷生产最常用的方法,但其大量用水对工业规模扩大构成挑战。因此,本研究重点使用HYSYS和Aspen Process Economic Analyzer对水洗与活性炭吸附进行规模放大比较。模型表明,对于处理量小于500立方米/小时的工厂,与活性炭相比,水洗具有成本效益。然而,与目前英国约1便士/千瓦时的化石天然气成本相比,两者都严重依赖政府补贴才能在经济上可行。对于运行速度为1000立方米/小时的工厂,水洗的处理成本降至1.5便士/千瓦时以下,活性炭的处理成本降至0.9便士/千瓦时,其中活性炭的主要优点是资本和运营成本较低,几乎没有水损失。预计这种方法可以显著促进可持续生物甲烷的生产。

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