The Experts below are selected from a list of 3 Experts worldwide ranked by ideXlab platform
Ying Chen - One of the best experts on this subject based on the ideXlab platform.
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Synthesis and simultaneous MINLP optimization of heat exchanger network, steam Rankine cycle, and organic Rankine cycle
Energy, 2020Co-Authors: Xiaojian Huang, Pei Lu, Jianyong Chen, Zhi Yang, Yingzong Liang, Chao Wang, Ying ChenAbstract:Process plants are typically energy intensive plants and pollutant emission contributors. Energy integration in Process plants effectively reduces energy consumption and pollutant emission. In a traditional energy integration concept, a heat exchanger network (HEN) is typically constructed for heat recovery between Process Streams. However, a large amount of medium-to-low-temperature surplus heat usually occurs in Hot Streams, where further internal heat integration is impossible, and is inevitably cooled by external cold source. Integrating organic Rankine cycle (ORC) into the Process HEN is an effect way in further enhancing the energy recovery. However, the HEN, utility plant, and ORC are traditionally designed and optimized separately or sequentially, resulting in local energy integration or optimization. In the present study, ORC is integrated into a HEN to generate power energy from surplus heat. An improved superstructure is constructed and a mixed integer non-linear programming model is developed for the synthesis and simultaneous optimization of the integration system containing Process-Process HEN, Hot utility-cold Stream HEN, Process Hot Stream-ORC HEN, steam utility plant, and cold utility plant. Two case studies of different scale in complexity are elaborated to validate the proposed methodology. Sensitivity analysis of carbon tax and fuel price are finally conducted.
Xiaojian Huang - One of the best experts on this subject based on the ideXlab platform.
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Synthesis and simultaneous MINLP optimization of heat exchanger network, steam Rankine cycle, and organic Rankine cycle
Energy, 2020Co-Authors: Xiaojian Huang, Pei Lu, Jianyong Chen, Zhi Yang, Yingzong Liang, Chao Wang, Ying ChenAbstract:Process plants are typically energy intensive plants and pollutant emission contributors. Energy integration in Process plants effectively reduces energy consumption and pollutant emission. In a traditional energy integration concept, a heat exchanger network (HEN) is typically constructed for heat recovery between Process Streams. However, a large amount of medium-to-low-temperature surplus heat usually occurs in Hot Streams, where further internal heat integration is impossible, and is inevitably cooled by external cold source. Integrating organic Rankine cycle (ORC) into the Process HEN is an effect way in further enhancing the energy recovery. However, the HEN, utility plant, and ORC are traditionally designed and optimized separately or sequentially, resulting in local energy integration or optimization. In the present study, ORC is integrated into a HEN to generate power energy from surplus heat. An improved superstructure is constructed and a mixed integer non-linear programming model is developed for the synthesis and simultaneous optimization of the integration system containing Process-Process HEN, Hot utility-cold Stream HEN, Process Hot Stream-ORC HEN, steam utility plant, and cold utility plant. Two case studies of different scale in complexity are elaborated to validate the proposed methodology. Sensitivity analysis of carbon tax and fuel price are finally conducted.
Pei Lu - One of the best experts on this subject based on the ideXlab platform.
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Synthesis and simultaneous MINLP optimization of heat exchanger network, steam Rankine cycle, and organic Rankine cycle
Energy, 2020Co-Authors: Xiaojian Huang, Pei Lu, Jianyong Chen, Zhi Yang, Yingzong Liang, Chao Wang, Ying ChenAbstract:Process plants are typically energy intensive plants and pollutant emission contributors. Energy integration in Process plants effectively reduces energy consumption and pollutant emission. In a traditional energy integration concept, a heat exchanger network (HEN) is typically constructed for heat recovery between Process Streams. However, a large amount of medium-to-low-temperature surplus heat usually occurs in Hot Streams, where further internal heat integration is impossible, and is inevitably cooled by external cold source. Integrating organic Rankine cycle (ORC) into the Process HEN is an effect way in further enhancing the energy recovery. However, the HEN, utility plant, and ORC are traditionally designed and optimized separately or sequentially, resulting in local energy integration or optimization. In the present study, ORC is integrated into a HEN to generate power energy from surplus heat. An improved superstructure is constructed and a mixed integer non-linear programming model is developed for the synthesis and simultaneous optimization of the integration system containing Process-Process HEN, Hot utility-cold Stream HEN, Process Hot Stream-ORC HEN, steam utility plant, and cold utility plant. Two case studies of different scale in complexity are elaborated to validate the proposed methodology. Sensitivity analysis of carbon tax and fuel price are finally conducted.
Jianyong Chen - One of the best experts on this subject based on the ideXlab platform.
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Synthesis and simultaneous MINLP optimization of heat exchanger network, steam Rankine cycle, and organic Rankine cycle
Energy, 2020Co-Authors: Xiaojian Huang, Pei Lu, Jianyong Chen, Zhi Yang, Yingzong Liang, Chao Wang, Ying ChenAbstract:Process plants are typically energy intensive plants and pollutant emission contributors. Energy integration in Process plants effectively reduces energy consumption and pollutant emission. In a traditional energy integration concept, a heat exchanger network (HEN) is typically constructed for heat recovery between Process Streams. However, a large amount of medium-to-low-temperature surplus heat usually occurs in Hot Streams, where further internal heat integration is impossible, and is inevitably cooled by external cold source. Integrating organic Rankine cycle (ORC) into the Process HEN is an effect way in further enhancing the energy recovery. However, the HEN, utility plant, and ORC are traditionally designed and optimized separately or sequentially, resulting in local energy integration or optimization. In the present study, ORC is integrated into a HEN to generate power energy from surplus heat. An improved superstructure is constructed and a mixed integer non-linear programming model is developed for the synthesis and simultaneous optimization of the integration system containing Process-Process HEN, Hot utility-cold Stream HEN, Process Hot Stream-ORC HEN, steam utility plant, and cold utility plant. Two case studies of different scale in complexity are elaborated to validate the proposed methodology. Sensitivity analysis of carbon tax and fuel price are finally conducted.
Zhi Yang - One of the best experts on this subject based on the ideXlab platform.
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Synthesis and simultaneous MINLP optimization of heat exchanger network, steam Rankine cycle, and organic Rankine cycle
Energy, 2020Co-Authors: Xiaojian Huang, Pei Lu, Jianyong Chen, Zhi Yang, Yingzong Liang, Chao Wang, Ying ChenAbstract:Process plants are typically energy intensive plants and pollutant emission contributors. Energy integration in Process plants effectively reduces energy consumption and pollutant emission. In a traditional energy integration concept, a heat exchanger network (HEN) is typically constructed for heat recovery between Process Streams. However, a large amount of medium-to-low-temperature surplus heat usually occurs in Hot Streams, where further internal heat integration is impossible, and is inevitably cooled by external cold source. Integrating organic Rankine cycle (ORC) into the Process HEN is an effect way in further enhancing the energy recovery. However, the HEN, utility plant, and ORC are traditionally designed and optimized separately or sequentially, resulting in local energy integration or optimization. In the present study, ORC is integrated into a HEN to generate power energy from surplus heat. An improved superstructure is constructed and a mixed integer non-linear programming model is developed for the synthesis and simultaneous optimization of the integration system containing Process-Process HEN, Hot utility-cold Stream HEN, Process Hot Stream-ORC HEN, steam utility plant, and cold utility plant. Two case studies of different scale in complexity are elaborated to validate the proposed methodology. Sensitivity analysis of carbon tax and fuel price are finally conducted.