SCI和EI收录∣中国化工学会会刊

Chinese Journal of Chemical Engineering ›› 2024, Vol. 75 ›› Issue (11): 274-289.DOI: 10.1016/j.cjche.2024.06.020

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Energy, exergy, economic, and environmental compromising performance of dual-stage evaporation-ammonia hybrid compression–absorption refrigeration system for the cooling supply of keto-benzene dewaxing process

Shuaishuai Zhang, Yuanbo Liu, Tong Zheng, Da Ruan, Zhong Lan, Tingting Hao, Xuehu Ma   

  1. State Key Laboratory of Fine Chemicals, Liaoning Key Laboratory Clean Utilization of Chemical Resources, Institute of Chemical Engineering, Dalian University of Technology, Dalian 116024, China
  • Received:2024-03-19 Revised:2024-06-03 Accepted:2024-06-20 Online:2024-08-03 Published:2024-11-28
  • Contact: Xuehu Ma,E-mail:xuehuma@dlut.edu.cn
  • Supported by:
    The authors would like to acknowledge the financial support from the National Natural Science Foundation of China (51836002).

Energy, exergy, economic, and environmental compromising performance of dual-stage evaporation-ammonia hybrid compression–absorption refrigeration system for the cooling supply of keto-benzene dewaxing process

Shuaishuai Zhang, Yuanbo Liu, Tong Zheng, Da Ruan, Zhong Lan, Tingting Hao, Xuehu Ma   

  1. State Key Laboratory of Fine Chemicals, Liaoning Key Laboratory Clean Utilization of Chemical Resources, Institute of Chemical Engineering, Dalian University of Technology, Dalian 116024, China
  • 通讯作者: Xuehu Ma,E-mail:xuehuma@dlut.edu.cn
  • 基金资助:
    The authors would like to acknowledge the financial support from the National Natural Science Foundation of China (51836002).

Abstract: Absorption refrigeration systems driven by low-temperature waste heat is one way to achieve “carbon neutrality.” Meanwhile, the keto-benzene dewaxing equipment needs a cooling capacity of 5 MW, with refrigeration temperature of -10 ℃ and -25 ℃. This paper researches the feasibility of dual-stage evaporation-ammonia hybrid compression-absorption refrigeration system (DSE-AHCARS) replacing the vapor compression refrigeration system for keto-benzene dewaxing process based on energy, exergy, economic, and environmental (4E) analysis. At the primary- and secondary-stage evaporation temperature of 0 and -23 ℃, respectively, the coefficient of performance (COP) reaches the maximum value of 0.85; however, COP-electricity reaches the minimum value of 8.1. When the secondary-stage refrigeration temperature is -23 ℃, CO2 emission increases from 1150 t·a-1 to 3600 t·a-1, and life cycle climate performance increases from 3.29×104 to 7.7×104 t, with the primary-stage refrigeration temperature being -15-0 ℃, as well as matching three parameters to ensure the 4E compromising performance by the multi-objective optimization. To guarantee that the life cycle climate performance is less than 5.5×104 t, the payback period is <2 a, and COP is >0.6 at the optimal operation ranges, such that the refrigeration temperature difference between primary stage and secondary stage is within 20 ℃. The power of DSE-AHCARS was reduced by 77% compared with the vapor-compression refrigeration system. Therefore, the DSE-AHCARS can reduce CO2 emissions by about 6250 t·a-1 and save 1.2×105 t of CO2 in the life cycle climate performance term. This result shows that the DSE-AHCARS can completely replace the vapor-compression refrigeration system.

Key words: Evaporation, Optimal design, Thermodynamic process, Multi-objective optimization, Ammonia hybrid refrigeration

摘要: Absorption refrigeration systems driven by low-temperature waste heat is one way to achieve “carbon neutrality.” Meanwhile, the keto-benzene dewaxing equipment needs a cooling capacity of 5 MW, with refrigeration temperature of -10 ℃ and -25 ℃. This paper researches the feasibility of dual-stage evaporation-ammonia hybrid compression-absorption refrigeration system (DSE-AHCARS) replacing the vapor compression refrigeration system for keto-benzene dewaxing process based on energy, exergy, economic, and environmental (4E) analysis. At the primary- and secondary-stage evaporation temperature of 0 and -23 ℃, respectively, the coefficient of performance (COP) reaches the maximum value of 0.85; however, COP-electricity reaches the minimum value of 8.1. When the secondary-stage refrigeration temperature is -23 ℃, CO2 emission increases from 1150 t·a-1 to 3600 t·a-1, and life cycle climate performance increases from 3.29×104 to 7.7×104 t, with the primary-stage refrigeration temperature being -15-0 ℃, as well as matching three parameters to ensure the 4E compromising performance by the multi-objective optimization. To guarantee that the life cycle climate performance is less than 5.5×104 t, the payback period is <2 a, and COP is >0.6 at the optimal operation ranges, such that the refrigeration temperature difference between primary stage and secondary stage is within 20 ℃. The power of DSE-AHCARS was reduced by 77% compared with the vapor-compression refrigeration system. Therefore, the DSE-AHCARS can reduce CO2 emissions by about 6250 t·a-1 and save 1.2×105 t of CO2 in the life cycle climate performance term. This result shows that the DSE-AHCARS can completely replace the vapor-compression refrigeration system.

关键词: Evaporation, Optimal design, Thermodynamic process, Multi-objective optimization, Ammonia hybrid refrigeration