Study on Cooling Heat Transfer of Supercritical Carbon Dioxide Applied to Transcritical Carbon Dioxide Heat Pump

Study on Cooling Heat Transfer of Supercritical Carbon Dioxide Applied to Transcritical Carbon Dioxide Heat Pump

Chaobin Dang (University of Tokyo, Japan) and Eiji Hihara (The University of Tokyo, Japan)
Copyright: © 2017 |Pages: 43
DOI: 10.4018/978-1-5225-2047-4.ch010
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Abstract

Understanding the heat transfer characteristics of supercritical fluids is of fundamental importance in many industrial processes such as transcritical heat pump system, supercritical water-cooled reactor, supercritical separation and supercritical extraction processes. This paper addresses recent experimental, theoretical and numerical studies on cooling heat transfer of supercritical CO2. A systematic study on heat transfer coefficient and pressure drop of supercritical CO2 was carried out at wide ranges of tube diameter, mass flux, heat flux, temperature and pressure. Based on the understanding of temperature and velocity distributions at cross-sectional direction provided by the numerical simulation, a new prediction model was proposed, which agreed well with the experimental results. In addition, the effect of lubricating oil was also discussed with the focus on the change in flow pattern and heat transfer performance of oil and supercritical CO2.
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Introduction

Re-Discovering of Carbon Dioxide Refrigerant

Carbon dioxide, hereafter CO2, was initially applied as a refrigerant in late 1800s because it was proven safe and highly efficient. It was commonly used on board ship till it was substituted by CFCs (chlorofluorocarbons) in 1930s because the latter was operated at lower system pressures. Things have changed since 1990s. Due to two treatments on environmental protection, i.e. the Montreal Protocol and Kyoto Protocol, carbon dioxide has been re-discovered and is expected to be a promising refrigerant in applications such as hot water heater, automotive A/C, and low temperature refrigerators.

Lorentzen (1995) compared several common alternative refrigerants. In contrast with CFCs and HCFCs, the alternatives, such as ammonia, hydrocarbons, and CO2, have an ODP (Ozone Depletion Potential) of zero and a negligible GWP (Global Warming Potential). As for HFC134a, although its ODP is zero, it has a GWP as high as 1200 (100 year) or 3100 (20 year). With respect to the safety of “old” refrigerants, only CO2 can compete with the non-flammable HFCs. Although CO2 is also listed as a greenhouse gas, it is because of the large amounts emitted from many industrial applications. In comparison with HFCs, the GWP of CO2 is negligible when CO2 is used as a refrigerant. Therefore, the use of CO2 as a refrigerant has major benefits of being environmentally benign and safety.

When CO2 is applied to conventional vapor compression cycle, it shows significantly different characteristics comparing with other refrigerants. Due to its low critical temperature (Tcp = 31.1ºC, Pcp = 7.38 MPa), the CO2 heat pump cycle has to be operated trans-critically when the ambient temperature is near or higher than the critical temperature. In this case, the heat absorbing process takes place at subcritical pressure whereas the heat rejection takes place at supercritical state. This kind of trans-critical cycle is initially proposed by Lorentzen and his coworkers for automotive air conditioning and hot water heat pump systems (Figure 1).

Figure 1.

Temperature-entropy chart for a trans-critical process of hot water heat pump

Lorentzen, 1995.

Due to the temperature glide in the gas cooler at supercritical pressure, the temperature profiles of the CO2 and the secondary fluid can be advantageously adapted in order to minimize heat transfer loss and hence improve energy efficiency. In addition, high discharge temperature of coolant about 90ºC-100ºC can be obtained without increasing the refrigerant side pressure and temperature so much. Thus an obvious preferable application of CO2 heat pump could be hot air or water production.

Although the high vapor pressure requires the redesign for more durable compressor and other parts, the high pressure and low viscosity of CO2 may lead to a small pressure loss. Furthermore, the pressure ratio of CO2 heat pump is quite low, only 2-3, compared to the value of 4-5 in conventional vapor compression cycle. Higher compressor efficiency can be achieved for the CO2 trans-critical cycle.

In Japan, since the commercialization of the “Eco Cute” in 2001, the production of CO2 heat pump water heaters has increased steadily. According to JRAIA (The Japan Refrigeration and Air Conditioning Industry Association), the total installations in Japan achieved 5 million units by March 2016. The coefficient of performance (COP) of the heat pump unit increased from 3.46 in its first generation units to 4.90 in those produced toward the end of 2007. See Figure 2.

Figure 2.

Shipment of Eco cute in Japan and the transition of COP: (a) shipment in Japan; (b) COP variations

In conclusion, the CO2 technology is very attractive as it is environmentally benign and safe. Properly designed systems for such applications as hot water supplier and automotive A/C have been proved competitive to the former CFC-based and ozone depleting system. Main difficulty of design and optimization of CO2 heat pump is related to the lack of information about the flow and heat transfer at supercritical pressure in cooling process, this paper addresses recent experimental, theoretical and numerical studies on cooling heat transfer of the supercritical CO2, including the effect of lubricating oil with the focus on the change in flow pattern and heat transfer performance of oil and supercritical CO2 at different operation conditions.

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