Published February 2021 | Version v1
Journal article

Performance evaluation and multi-objective optimization of a low-temperature CO2 heat pump water heater based on artificial neural network and new economic analysis

  • 1. Engineering Research Center of Process Equipment and Remanufacturing, Ministry of Education, College of Mechanical Engineering, Zhejiang University of Technology, Hangzhou, 310014 (China)
  • 2. Zhejiang Zhenglishengneng Sci-Tech Ltd, Wenzhou, 325600 (China)
  • 3. Key Laboratory of Low-grade Energy Utilization Technologies and Systems, Chongqing University, Chongqing, 400044 (China)
  • 4. Key Laboratory of Refrigeration and Cryogenic Technology of Zhejiang Province, Institute of Refrigeration and Cryogenics, Zhejiang University, 310000, Hangzhou (China)

Description

Highlights: • Multi-optimization of low-temperature CO2 HPWH is done to raise performance using ANN. • Housing price and off-peak electric price is considered in new economic model for TAC. • CO2 emission and TAC for final solution are 8599.4 kg and 1626.9$/year, respectively. • As water demand grows, CO2 and TAC grow from 4.4 to 10.7ton and 866.7–2023.5$/year. • Cost of the space occupied by system is the fourth important factor in capital cost. For the advantages of high efficiency and low impact to the environment, CO2 air source heat pump water heater (ASHPWH) is applied to produce domestic water, which also reveals good potential in cold regions. In order to boost the system performance and practicability under low ambient temperature, optimization for CO2 ASHPWH is conducted using non-dominated sorting genetic algorithm (NSGA-II). A validated artificial neural network (ANN) predicts energy parameters for the optimization. And an economic model provides economic and environmental parameters, which considers the influence of housing price, tank volume, and on/off-peak electricity price, rarely taken into account in published studies. Then the optimizing progress is conducted under −20 °C ambient temperature and 9–65 °C water temperature, in which four optimized variables are selected: gas cooler outlet temperature (Tgc), heat rejection pressure (Pgc), compressor displacement (qvh) and water tank volume (Vwt). The final solution of Tgc = 15 °C, Pgc = 8294.1 kPa, Vwt = 0.3647 m3, qvh = 401.33 mL/s results in two objectives (CO2 emission and total annual cost) of 8599.4 kg and 1626.9 $/year, revealing advantages both in energy and economy. It is noteworthy that the cost of the space occupied by system is the fourth important factor in capital cost. These results lay solid foundation for further studies and system application.

Availability note (English)

Available from http://dx.doi.org/10.1016/j.energy.2020.119232

Additional details

Identifiers

DOI
10.1016/j.energy.2020.119232;
PII
S0360544220323392;

Publishing Information

Journal Title
Energy (Oxford)
Journal Volume
216
Journal Page Range
vp.
ISSN
0360-5442
CODEN
ENEYDS

Optional Information

Copyright
Copyright (c) 2020 Elsevier Ltd. All rights reserved.