4.7 Article

Improving inter-plant integration of syngas production technologies by the recycling of CO2 and by-product of the Fischer-Tropsch process

Journal

INTERNATIONAL JOURNAL OF HYDROGEN ENERGY
Volume 47, Issue 74, Pages 31755-31772

Publisher

PERGAMON-ELSEVIER SCIENCE LTD
DOI: 10.1016/j.ijhydene.2021.12.184

Keywords

Pinch analysis; Inter-plant integration; Heat exchanger network; High-temperature Co-electrolysis; Energy saving; CO2 reduction

Funding

  1. Republic of Kazakhstan [AP09260365]

Ask authors/readers for more resources

The paper focuses on reducing emissions in synthesis-gas production through better integration and increased energy efficiency. The study investigates the use of Fischer-Tropsch by-products and carbon dioxide for synthesis gas production. By adjusting process stream temperatures, optimizing heat exchanger networks, and utilizing secondary energy resources, the proposed approach maximizes economic and environmental benefits. Results show that using natural gas as a fuel source has the lowest carbon footprint, while coal has higher CO2 emissions, making it suitable as a feedstock for high-temperature co-electrolysis.
This paper deals with the emission reduction in synthesis-gas production by better inte-gration and increasing the energy efficiency of a high-temperature co-electrolysis unit combined with the Fischer-Tropsch process. The investigated process utilises the by-product of Fischer-Tropsch, as an energy source and carbon dioxide as a feedstock for synthesis gas production. The proposed approach is based on adjusting process streams temperatures with the further synthesis of a new heat exchangers network and optimisation of the utility system. The potential of secondary energy resources was determined using plus/minus principles and simulation of a high-temperature co-electrolysis unit. The proposed technique maximises the economic and environmental benefits of inter-unit integration. Two scenarios were considered for sharing the high-temperature co-electrolysis and the Fischer-Tropsch process. In the first scenario, by-products from the Fischer-Tropsch process were used as fuel for a high-temperature co-electrolysis. Optimisation of secondary energy sources and the synthesis of a new heat exchanger network reduce fuel consumption by 47% and electricity by 11%. An additional environmental benefit is reflected in emission reduction by 25,145 tCO(2)/y. The second scenario uses fossil fuel as a primary energy source. The new exchanger network for the high-temperature co -electrolysis was built for different energy sources. The use of natural gas resulted in total annual costs of the heat exchanger network to 1,388,034 USD/y, which is 1%, 14%, 116% less than for coal, fuel oil and LPG, respectively. The use of natural gas as a fuel has the lowest carbon footprint of 7288 tCO(2)/y. On the other hand, coal as an energy source has commensurable economic indicators that produce 2 times more CO2, which can be used as a feedstock for a high-temperature co-electrolysis. This work shows how in-depth preliminary analysis can optimise the use of primary and secondary energy resources during inter-plant integration. (C) 2021 Hydrogen Energy Publications LLC. Published by Elsevier Ltd. All rights reserved.

Authors

I am an author on this paper
Click your name to claim this paper and add it to your profile.

Reviews

Primary Rating

4.7
Not enough ratings

Secondary Ratings

Novelty
-
Significance
-
Scientific rigor
-
Rate this paper

Recommended

No Data Available
No Data Available