1 Introduction
2 Heat pumps’ research and applications
Fig. 1 Sketch of heat pump |
Table 1 Performance Indicators and their explanations of the heat pump |
Performance Indicator | Explanation |
---|---|
QH = QL + W | QH is the heat transferred to heat sink with high temperature (TH), QL is the heat collected from heat source with low temperature (TL), while W is electricity (for compression type) or heat (for absorption type) input. |
COP=QHW=1+QLW>1 | The coefficient of performance (COP) is the ratio between heat supply to work. Higher COPs equate to higher efficiency, lower energy (power) consumption, thus lower operating costs. The COP is always over 1 in heat pumps, because it pumps “free” heat from heat source to heat sink. |
COPmax=THTH−TL | Maximum theoretical COPmax (Carnot COP) of heat pump operating between specific heat source TL and heat sink temperature TH. |
εHP=COPCOPmax | Thermodynamic perfectness εHP is the ratio between heat pump COP and the maximum theoretical COPmax, which could never reach 100%. |
ΔTlift = TH − TL | Temperature lift ΔTlift is the temperature difference between the high-temperature heat sink and the low-temperature heat source. |
2.1 Building applications
Fig. 2 Multiple buildings’ heating modes |
Table 2 Temperature range of buildings’ heat demands |
Heating mode | Temperature needed |
---|---|
Radiator heater | 80 °C (inlet water temperature) |
60 °C (return water temperature) | |
Hot water | 40 ~ 50 °C |
Floor heating | 35 °C-40 °C |
Fan coil unit | 35 ~ 45 °C |
Fig. 3 Waste-heat-based heat pumps for district heating. a Absorption heat pump in Lanzhou, 290 MW scale. b Centrifugal compression heat pump, 10 MW scale |
Fig. 4 Pilot research for thermal comfort and high efficiency heating and cooling. a Different terminal heating modes. b Desiccant coated heat pumps |
2.2 Industrial applications
Fig. 5 The temperature range of heating demands in buildings and different industrial processes |
Fig. 6 Air source heat pump for steam generation [13] |
3 Data and methodology
3.1 Emission intensity assessment
3.1.1 China’ heating sector GHG emission
Table 3 GHG emission intensities and market shares of different heating technologies in China |
China | GHG direct | GHG indirect | Proportion (%) |
---|---|---|---|
Heating type | gCO2/kWh | gCO2/kWh | 2020 |
Oil | 356 | 100 | 9.91 |
Oil Advanced | 310 | 87 | 0.33 |
Gas | 269 | 62 | 11.4 |
Gas Advanced | 224 | 52 | 1.24 |
Biomass | 0 | 390 | 27.05 |
Biomass Advanced | 0 | 69 | 2.28 |
Coal | 472 | 30 | 12.96 |
District | 472 | 30 | 12.95 |
Electric | 717 | 0 | 5.74 |
Heat pump - Ground source | 239 | 0 | 1.67 |
Heat pump - Air-Water | 239 | 0 | 1.66 |
Heat pump - Air-Air | 239 | 0 | 1.71 |
Solar Thermal | 0 | 0 | 11.09 |
3.1.2 Emission intensity of heating facilities
3.2 Heat pumps’ market share in China assessment
Table 4 The heat demands in some industrial processes [9] |
Industrial process | Use | Heat-carrying form | Temperature |
---|---|---|---|
Food | Rinse | Air | 80-150 °C |
Concentrate | Steam | 130-190 °C | |
Drying | Steam (air) | 130-240 °C | |
Plastic | Initiation | Steam | 130-150 °C |
Rapid Separation | Steam | 150 °C | |
Extrusion | Steam | 150 °C | |
Drying | Steam (air) | 180 °C | |
Blend | Steam | 150 °C | |
Glass | Flatten | Air | 110-150 °C |
Dry fibers | Air | 130-180 °C | |
Chemical industry | Heating dipping | Steam (air) | 150-180 °C |
Drying | Steam (air) | 150-180 °C | |
Paper-making | Kraft bleaching | Steam | 150-180 °C |
Drying | Steam | 150 °C | |
Woodworking | Drying in cellar | Air | 80-120 °C |
Preparation of plywood | Steam | 120-180 °C | |
Hot-pressed fiberboard | Steam | 200 °C | |
Synthetic rubber | Initiation | Steam | 130 °C |
Monomer recovery | Steam | 130 °C | |
Drying | Steam (air) | 130 °C | |
Textile industry | Rinse | Water | 80-100 °C |
Handle | Steam | 80-130 °C | |
Drying | Steam (air) | 80-140 °C | |
Road construction | Melting asphalt | Steam | 120-180 °C |
Tobacco industry | Silk making | Steam | 150-200 °C |
Fig. 7 Heating energy consumption fractions in EU industries divided by temperature [57] |
3.3 Decarbonization potential assessment
3.3.1 Prediction of the end-use energy consumption variation by sectors and time
Table 5 End-use energy demand by sector |
End-use energy demand by sector | 2020 | 2030 | 2040 | 2050 | 2060 | |||||
---|---|---|---|---|---|---|---|---|---|---|
Amount | Share | Amount | Share | Amount | Share | Amount | Share | Amount | Share | |
Industry | 21.1 | 60% | 19.3 | 49% | 14.6 | 40% | 12 | 36% | 10.7 | 35% |
Building | 8.1 | 23% | 11.3 | 28% | 12.2 | 33% | 11.6 | 34% | 11.5 | 37% |
Transportation | 5 | 14% | 7.9 | 20% | 8.8 | 24% | 9.2 | 27% | 7.8 | 25% |
Other | 0.9 | 3% | 1.2 | 3% | 1.1 | 3% | 1 | 3% | 0.9 | 3% |
Note: The energy unit is 109 tons of standard coal |
3.3.2 Basic assumptions on heat pump
3.3.3 Heat pump decarbonization potential assessment
Fig. 8 Flow chart of the quantification of the heating decarbonization potential by heat pump |
3.4 LCOH assessment
Table 6 The key assumptions for LCOH calculating |
Parameters | Buildings’ sector | Industrial sector | ||||
---|---|---|---|---|---|---|
Type | Heat pump | Natural gas | Electrical resistance | Heat pump | Natural gas | Electrical resistance |
Capital cost CNY·kW−1 | 971 | 261 | 162 | 1714 | 143 | 169 |
Annual operation hours | 4000 | 4000 | 4000 | 6000 | 6000 | 6000 |
Lifetime years | 15 | 15 | 15 | 15 | 15 | 15 |
Efficiency/COP | ~ 3-4 | 95% | 95% | 2 | 95% | 95% |
Maintain cost factor | 1.5% | 1.5% | 1.5% | 1.5% | 1.5% | 1.5% |
Note: The typical lifetime years, maintain cost factor, COP value are determined by some references [4,59] and our investigation, while capital cost is based on our investigation on the market available products on average, while 20 kW heater for building sector with and 350 kW steam boiler for industrial sector. The calculation model does not consider financing or inflation, nor the degradation of collector efficiency or any residual value of the asset |
4 Assessment on heat pumps and other heating facilities
4.1 CO2 emission evaluation
Fig. 9 CO2 emission evaluation on heat pumps compared with other heating modes. a Different heating modes’ CO2 emission intensity based on current power structure. b CO2 emission of heat pumps under current and future scenarios |
4.2 Heat pumps’ decarbonization potential
Fig. 10 Decarbonization potential of heat pump in 2060 with increasing share for industrial and buildings’ sector |
4.3 Economic evaluation
Fig. 11 Techno-economics comparison between heat pump (HP), electrical resistance heating (ER) and natural gas heating (NG) among different provinces in China’s Mainland based on the current situation. a LCOH for buildings’ sector (HP-NG). b LCOH for buildings’ sector (HP- ER). c LCOH for industrial sector (HP- NG). d LCOH for industrial sector (HP-ER) |
5 Discussion and future prospects
Fig. 12 Technology roadmap for heat pump development in China 2060 carbon-neutrality. Shown in the box is a proposed technology roadmap for heat pump decarbonization. Government, Manufacturer, and users could work together to create a development roadmap for heat pump market penetration in near-term, middle-term, and long-term |