Abstract

Flue gas contains high amount of low-grade heat and water vapor that are attractive for recovery. This study assesses performance of a hybrid of water scrubber and membrane distillation (MD) to recover both heat and water from a simulated flue gas. The former help to condense the water vapor to form a hot liquid flow which later used as the feed for the MD unit. The system simultaneously recovers water and heat through the MD permeate. Results show that the system performance is dictated by the MD performance since most heat and water can be recovered by the scrubber unit. The scrubber achieved nearly complete water and heat recovery because the flue gas flows were supersaturated with steam condensed in the water scrubber unit. The recovered water and heat in the scrubber contains in the hot liquid used as the feed for the MD unit. The MD performance is affected by both the temperature and the flow rate of the flue gas. The MD fluxes increases at higher flue gas temperatures and higher flow rates because of higher enthalpy of the flue gas inputs. The maximum obtained water and heat fluxes of 12 kg m−2 h−1 and 2505 kJm−2 h−1 respectively, obtained at flue gas temperature of 99 °C and at flow rate of 5.56 L min−1. The MD flux was also found stable over the testing period at this optimum condition. Further study on assessing a more realistic flue gas composition is required to capture complexity of the process, particularly to address the impacts of particulates and acid gases.

Highlights

  • Alternative energy sources are required to fulfil the growing demands of energy utilizations.Despite the dominance of the fosil based fuels to serve those demands, they are depleting and their utilizations cause detrimental impacts to the environmental [1]

  • The decrease in flue gas temperature at high flue gas flow rates is attributed the lower enthalpy of the flue gas flow due to lesser water vapour fraction generated a

  • Experimental results show that membrane distillation (MD) performances decrease with the rise in gas flow rates

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Summary

Introduction

Alternative energy sources are required to fulfil the growing demands of energy utilizations. Despite the dominance of the fosil based fuels (crude oil, natural gas and coal) to serve those demands, they are depleting and their utilizations cause detrimental impacts to the environmental [1] This is one of the major reasons why some countries attempt to explore renewable energy sources that are more benigh to the environment [2] through utilization of the solar energy [3] or the biomass-based fuel to power the transportation sector. The flue gas temperature is relatively low making heat recovery a great challenge [14] because of the large surface area required for energy harvesting. Flue gas from coal-fired power plant generally has temperature below 130 ◦ C, and it contains 10–16% (v/v) water vapour [15] To handle such condition, combined cycle for heat recovery or implementation of heat cascade may be necessary [16].

Experimental Set Up of Hybrid MD-Wet Scrubber
Membrane Characteristics
Scrubber Unit Installation
Membrane Distillation Cell Assembly
Fluxes and Recovery Determination
Hybrid System Operation Assessment
Performance
Effect of Temperature
Effect of Flue Gas Flow Rate
Water and Heat Flux Evolution
Practical Consideration
Conclusions
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