3.8 Article

Prospect of Direct Dimethyl Ether Production from CO2: Reactor Design Development

Journal

Publisher

PENERBIT UTM PRESS
DOI: 10.11113/mjfas.v19n2.2841

Keywords

Dimethyl ether; syngas; reactor design; fixed bed reactor; fluidized bed reactor; membrane reactor; process intensification

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The increasing emissions of carbon dioxide (CO2) and volatile hydrocarbons from burning fossil fuels have led to significant global warming and air pollution. To mitigate the environmental impact of fossil fuels, there has been a growing interest in utilizing CO2 generated through new technologies to produce alternative fuels. Dimethyl ether (DME) is one such clean alternative fuel that has been investigated for a more sustainable and greener environment. This paper discusses the direct synthesis of DME from CO2 through dehydrogenation and dehydration reactions, highlighting the challenges and difficulties associated with reactor development and proposing future directions.
The increasing emissions of carbon dioxide (CO2) , volatile hydrocarbons via burning of fossil fuels result in a significant amount of global warming and air pollution. With the concern over the impact of fossil fuel to the environment, the interest in alternative fuel production from the CO2 generated through utilization of new technologies has risen rapidly. Several clean alternative fuels, including dimethyl ether (DME) have been investigated for a more sustainable and greener environment. DME has a high cetane number but produces much lower NOx emission upon combustion. DME is typically synthesized using syngas based on conventional indirect DME route, where the process begins with conversion of syngas into methanol and subsequently dehydrated to DME in separate units. Recently, a direct single-step route to produce DME through dehydrogenation of CO2 and dehydration of methanol by utilising a novel bifunctional catalyst has been investigated. In direct DME, the dehydrogenation and dehydration occur simultaneously in a single reactor, which eliminate the need for a methanol production plant. However, the use of conventional fixed-bed reactor (FBR) for the direct DME synthesis causes many challenges including catalyst deactivation, where water appears in the reaction area, limiting the conversion of CO2 reactants into DME and consequently, the DME yield. It is also essential to manage the exothermic heat generated from the catalyst for better DME yield. In order to overcome these hurdles, several types of reactors have been proposed such as fluidized bed reactor, slurry reactor, microreactor and catalytic membrane reactor. In this paper, different types of reactors are first discussed and its applications related to the direct DME production from CO2 are highlighted. Finally, the challenges and difficulties of reactor development are addressed and future direction is outlined.

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