CN100347265C - Mixed heat pump work substance with zero ozone layer destroying potential - Google Patents
Mixed heat pump work substance with zero ozone layer destroying potential Download PDFInfo
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Abstract
臭氧破坏潜能为零的热泵混合工质,涉及一种中高温水源热泵机组使用的混合制冷工质。该工质含有1,1,1,2-四氟乙烷、1,1,1,2,3,3,3-七氟丙烷和1,1,1,2,3,3-六氟丙烷三种物质;也可在上述三种组分中加入丁烷后组成四元混合工质。其制备方法是将上述各种组分按其相应的配比在液相状态下进行物理混合。本发明不破坏臭氧层,符合环境保护要求;无毒、不可燃,其热工性能及热工参数均较好,可直接用于HFC-134a热泵机组中,压缩机与系统中的主要部件无需改动;应用该混合制冷工质的热泵机组可提供80℃左右的中高温热水。A heat pump mixed working fluid with zero ozone destruction potential relates to a mixed refrigeration working medium used in a medium-high temperature water source heat pump unit. The working fluid contains 1,1,1,2-tetrafluoroethane, 1,1,1,2,3,3,3-heptafluoropropane and 1,1,1,2,3,3-hexafluoropropane substances; butane can also be added to the above three components to form a quaternary mixed working medium. The preparation method is to physically mix the above-mentioned various components according to their corresponding proportions in a liquid state. The invention does not destroy the ozone layer and meets the requirements of environmental protection; it is non-toxic and non-flammable, has good thermal performance and thermal parameters, and can be directly used in HFC-134a heat pump units without modification of the main components of the compressor and the system ; The heat pump unit using the mixed refrigerant can provide medium and high temperature hot water at about 80°C.
Description
技术领域technical field
本发明涉及一种中高温水源热泵机组使用的混合制冷工质,特别涉及一种完全不破坏臭氧层(即臭氧破坏潜能ODP=0)的热泵工质。The invention relates to a mixed refrigeration working medium used in a medium-high temperature water source heat pump unit, in particular to a heat pump working medium which does not destroy the ozone layer at all (that is, the ozone destruction potential ODP=0).
背景技术Background technique
水源热泵技术是利用地热水、地下水、地表水(河水、湖水、海水)、工业废水等低温低位热能资源,并采用热泵原理,通过少量的电能输入使低位热能向高位热能转移,从而实现供热供冷的一种节能环保技术。水源热泵具有高效节能、运行稳定可靠、环境效益显著、一机多用等特点。由于水源热泵具有较高的效率、又几乎不受各个季节环境温度的影响、可以有效利用余热能源等特点,因此是目前制冷、空调行业的一个主要研究方向。Water source heat pump technology uses geothermal water, groundwater, surface water (river water, lake water, sea water), industrial waste water and other low-temperature and low-level thermal energy resources, and adopts the principle of heat pump to transfer low-level heat energy to high-level heat energy through a small amount of electric energy input, so as to realize power supply. An energy-saving and environmentally friendly technology for heating and cooling. The water source heat pump has the characteristics of high efficiency and energy saving, stable and reliable operation, remarkable environmental benefits, and one machine with multiple functions. Because water source heat pumps have high efficiency, are almost not affected by the ambient temperature in various seasons, and can effectively use waste heat energy, they are currently a major research direction in the refrigeration and air-conditioning industry.
以往通常用作水源热泵的中高温工质为CFC-11和CFC-114等。但由于CFC-11和CFC-114均属CFC类物质,其臭氧损耗潜值ODP分别为1.0和0.85,对大气臭氧层有严重的破坏作用,而且它们的温室效应影响也很大,其温室效应潜能值GWP分别为4600和9800,发达国家已于1996年禁用,而发展中国家也将于2010年禁用。所以,开发对环境友好的水源热泵中高温工质是十分必要的,特别是需要完全不破坏臭氧层(即ODP=0)的热泵工质。CFC-11 and CFC-114 are the medium and high temperature working fluids usually used in water source heat pumps in the past. However, since both CFC-11 and CFC-114 belong to CFC substances, their ozone depletion potential ODP is 1.0 and 0.85 respectively, which have serious damage to the atmospheric ozone layer, and their greenhouse effect is also very large, and their greenhouse effect potential The values of GWP are 4600 and 9800 respectively. Developed countries have banned it in 1996, while developing countries will also ban it in 2010. Therefore, it is very necessary to develop high-temperature working fluids in water source heat pumps that are environmentally friendly, especially heat pump working fluids that do not destroy the ozone layer (that is, ODP=0) at all.
为了满足暖气片供暖和防止病菌(如军团菌等)在生活热水中滋生,往往需要提供80℃左右的热水。In order to meet the needs of radiator heating and prevent bacteria (such as Legionella, etc.) from breeding in domestic hot water, it is often necessary to provide hot water at about 80°C.
目前现有的热泵工质,或出水温度过低(氟里昂-22和1,1,1,2-四氟乙烷),或对大气臭氧层有破坏作用(即ODP不为零),或出水温度过高,以至于使原有压缩机无法正常工作。所以,急需完全不破坏臭氧层并能够使用现有压缩机提供80℃左右热水的热泵工质。At present, the existing heat pump working fluid, or the outlet water temperature is too low (Freon-22 and 1,1,1,2-tetrafluoroethane), or has a destructive effect on the atmospheric ozone layer (that is, the ODP is not zero), or the outlet water The temperature is so high that the original compressor cannot work properly. Therefore, there is an urgent need for a heat pump working fluid that does not destroy the ozone layer at all and can use the existing compressor to provide hot water at about 80°C.
发明内容Contents of the invention
本发明旨在研究开发适用于中高温水源热泵机组的混合新工质,使其既能不破坏臭氧层,且满足减少温室效应的环保要求;又具有较好的热工参数和热工性能,安全、可靠;并与现有的HFC-134a冷水机组设备和冷冻油相容,可接充灌,在接利用中常温水源(40℃左右)条件下,可提供80℃左右的中高温热水。The invention aims at researching and developing a new mixed working medium suitable for medium and high temperature water source heat pump units, so that it can not only not destroy the ozone layer, but also meet the environmental protection requirements of reducing the greenhouse effect; it also has better thermal parameters and thermal performance, and is safe. , reliable; and compatible with the existing HFC-134a chiller equipment and refrigeration oil, can be directly charged, and can provide medium-high temperature heat of about 80°C under the condition of direct use of medium-temperature water source (about 40°C) water.
本发明的技术方案如下:Technical scheme of the present invention is as follows:
本发明提供的一种臭氧破坏潜能为零的热泵混合工质,其特征在于:该混合工质合1,1,1,2-四氟乙烷、1,1,1,2,3,3,3-七氟丙烷和1,1,1,2,3,3-六氟丙烷三种物质,各组分的质量百分此含量分别为:A heat pump mixed working fluid with zero ozone depletion potential provided by the present invention is characterized in that: the mixed working medium contains 1,1,1,2-tetrafluoroethane, 1,1,1,2,3,3 , 3-heptafluoropropane and 1,1,1,2,3,3-hexafluoropropane, the mass percentages of each component are as follows:
1,1,1,2-四氟乙烷 10~80%1,1,1,2-Tetrafluoroethane 10~80%
1,1,1,2,3,3,3-七氟丙烷 5~80%1,1,1,2,3,3,3-Heptafluoropropane 5~80%
1,1,1,2,3,3-六氟丙烷 15~80%。1,1,1,2,3,3-hexafluoropropane 15-80%.
还可以在上述三种组分中加入丁烷,其组分的质量百分比含量分别为:Butane can also be added in the above three components, and the mass percent content of its components is respectively:
1,1,1,2-四氟乙烷 10~80%1,1,1,2-Tetrafluoroethane 10~80%
1,1,1,2,3,3,3-七氟丙烷 5~80%1,1,1,2,3,3,3-Heptafluoropropane 5~80%
1,1,1,2,3,3-六氟丙烷 13~80%1,1,1,2,3,3-Hexafluoropropane 13~80%
丁烷 2~10%Butane 2~10%
本发明提供的制冷工质,其制备方法是将上述各种组分按其相应的配比在液相状态下进行物理混合即可。The refrigeration working fluid provided by the invention can be prepared by physically mixing the above-mentioned various components according to their corresponding proportions in a liquid state.
上述组分中的1,1,1,2-四氟乙烷(HFC-134a),其分子式为CH2FCF3,摩尔质量为102.03,正常沸点为-26.1℃,临界温度为101.1℃,临界压力为4.06MPa。Among the above components, 1,1,1,2-tetrafluoroethane (HFC-134a) has a molecular formula of CH 2 FCF 3 , a molar mass of 102.03, a normal boiling point of -26.1°C, and a critical temperature of 101.1°C. The pressure is 4.06MPa.
1,1,1,2,3,3,3-七氟丙烷(HFC-227ea),其分子式为CF3CHFCF3,摩尔质量为170.03,正常沸点为-15.6℃,临界温度为102.8℃,临界压力为2.98MPa。1,1,1,2,3,3,3-Heptafluoropropane (HFC-227ea), its molecular formula is CF 3 CHFCF 3 , its molar mass is 170.03, its normal boiling point is -15.6°C, its critical temperature is 102.8°C, and its critical pressure is 2.98MPa.
1,1,1,2,3,3-六氟丙烷(HFC-236ea),其分子式为CHF2CHFCF3,摩尔质量为152.04,正常沸点为6.2℃,临界温度为139.3℃,临界压力为3.50MPa。1,1,1,2,3,3-hexafluoropropane (HFC-236ea), its molecular formula is CHF 2 CHFCF 3 , its molar mass is 152.04, its normal boiling point is 6.2°C, its critical temperature is 139.3°C, and its critical pressure is 3.50 MPa.
丁烷(HC-600),其分子式为CH3CH2CH2CH3,摩尔质量为58.12,正常沸点为-0.5℃,临界温度为152.0℃,临界压力为3.80MPa。Butane (HC-600), its molecular formula is CH 3 CH 2 CH 2 CH 3 , its molar mass is 58.12, its normal boiling point is -0.5°C, its critical temperature is 152.0°C, and its critical pressure is 3.80MPa.
本发明具有以下优点及有益效果:The present invention has the following advantages and beneficial effects:
a.环境性能:a.Environmental performance:
本发明的制冷剂其臭氧破坏潜能(ODP)均为零,其温室效应系数(GWP)也较低,近似HFC-134a。本发明完全符合保护臭氧层,减少温室效应的环境保护要求。The refrigerant of the present invention has zero ozone destruction potential (ODP) and low greenhouse effect coefficient (GWP), which is similar to HFC-134a. The invention fully complies with the environmental protection requirements of protecting the ozone layer and reducing the greenhouse effect.
b.热工参数:b. Thermal parameters:
HFC-134a制冷剂在常温热泵工况(蒸发温度27℃、冷凝温度71℃、过冷温度5℃和过热温度5℃)下,蒸发压力为706.2MPa、冷凝压力为2168.3MPa、压缩比为3.07、排气温度为87.9℃。而本发明用于中高温设计工况(蒸发温度40℃、冷凝温度83℃、过冷温度2℃和过热温度10℃)时,蒸发压力和冷凝压力均与HFC-134a在中常温热泵工况下的相近。说明了本发明可接充灌于原HFC-134a的系统,而不需改动其它部件,就可提供较高的出水温度(80℃左右)。HFC-134a refrigerant under normal temperature heat pump conditions (evaporating temperature 27°C, condensing temperature 71°C, subcooling temperature 5°C and superheating temperature 5°C), the evaporation pressure is 706.2MPa, the condensation pressure is 2168.3MPa, and the compression ratio is 3.07 , The exhaust temperature is 87.9°C. And when the present invention is used in medium and high temperature design conditions (evaporating temperature 40°C, condensation temperature 83°C, supercooling temperature 2°C and superheating temperature 10°C), the evaporation pressure and condensation pressure are all the same as those of HFC-134a in medium and normal temperature heat pump conditions The next one is similar. It shows that the present invention can be directly filled in the original HFC-134a system without changing other components, and can provide a higher outlet water temperature (about 80°C).
c.热工性能:c. Thermal performance:
本发明在上述设计工况下的供热COP为4.8左右、容积供热量为5100kJ/m3左右,热工性能较好。The heating COP of the present invention is about 4.8 and the volumetric heat supply is about 5100kJ/ m3 under the above design working conditions, and the thermal performance is better.
综上所述,本发明不破坏臭氧层,可降低温室效应影响,符合环保要求;且无毒、不可燃,热工性能及热工参数均较好,可接利用HFC-134a热泵系统提供中高温热水(80℃左右),压缩机与系统中的主要部件不需改动,生产线不需改造。In summary, the present invention does not destroy the ozone layer, can reduce the impact of the greenhouse effect, and meets environmental protection requirements; it is non-toxic, non-flammable, has good thermal performance and thermal parameters, and can directly use the HFC-134a heat pump system to provide High-temperature hot water (about 80°C), the main components in the compressor and the system do not need to be changed, and the production line does not need to be modified.
具体实施方式Detailed ways
实施例1:将10%的HFC-134a、10%的HFC-227ea与80%的HFC-236ea在液相下进行物理混合。Example 1: 10% of HFC-134a, 10% of HFC-227ea and 80% of HFC-236ea were physically mixed in liquid phase.
实施例2:将45%的HFC-134a、25%的HFC-227ea与30%的HFC-236ea在液相下进行物理混合。Example 2: 45% of HFC-134a, 25% of HFC-227ea and 30% of HFC-236ea were physically mixed in liquid phase.
实施例3:将80%的HFC-134a、5%的HFC-227ea与15%的HFC-236ea在液相下进行物理混合。Example 3: 80% of HFC-134a, 5% of HFC-227ea and 15% of HFC-236ea were physically mixed in liquid phase.
实施例4:将10%的HFC-134a、5%的HFC-227ea、80%的HFC-236ea与5%的HC-600在液相下进行物理混合。Example 4: 10% of HFC-134a, 5% of HFC-227ea, 80% of HFC-236ea and 5% of HC-600 were physically mixed in liquid phase.
实施例5:将53%的HFC-134a、20%的HFC-227ea、20%的HFC-236ea与7%的HC-600在液相下进行物理混合。Example 5: 53% of HFC-134a, 20% of HFC-227ea, 20% of HFC-236ea and 7% of HC-600 were physically mixed in liquid phase.
实施例6:将80%的HFC-134a、5%的HFC-227ea、13%的HFC-236ea与2%的HC-600在液相下进行物理混合。Example 6: 80% of HFC-134a, 5% of HFC-227ea, 13% of HFC-236ea and 2% of HC-600 were physically mixed in liquid phase.
在设计工况下,即蒸发温度40℃、冷凝温度83℃、过冷温度2℃和过热温度10℃下,将上述实施例制冷工质的热工性能列于表1中。表1中还列出了HFC-134a的参数,以兹此较。Under the design working conditions, that is, the evaporation temperature is 40°C, the condensation temperature is 83°C, the subcooling temperature is 2°C, and the superheating temperature is 10°C, the thermal properties of the refrigerants in the above examples are listed in Table 1. Table 1 also lists the parameters of HFC-134a for comparison.
由表1可见,与HFC-134a相此,冷凝压力低,排气温度相当,供热工况下的COP和供热量相当,说明完全可以利用现有的HFC-134a热泵压缩机组成热泵机组,在中常温水源条件下(40℃左右)可以提供80℃左右的热水。此外,从表1还可看出,本发明的制冷剂的ODP值全部为零,GWP低于或近似HFC-134a。值得注意的是,由于加入了HC-600,本专利中提出的四元制冷工质的GWP值比相应的三元制冷工质小。因此,综合环境性能较好。It can be seen from Table 1 that, compared with HFC-134a, the condensing pressure is low, the exhaust temperature is equivalent, and the COP and heat supply under heating conditions are equivalent, indicating that the existing HFC-134a heat pump compressor can be used to form a heat pump unit , Under the condition of medium and normal temperature water source (about 40 ℃), it can provide hot water at about 80 ℃. In addition, it can also be seen from Table 1 that the ODP values of the refrigerants of the present invention are all zero, and the GWP is lower than or similar to HFC-134a. It is worth noting that due to the addition of HC-600, the GWP value of the quaternary refrigerant proposed in this patent is smaller than that of the corresponding ternary refrigerant. Therefore, the overall environmental performance is better.
表1 实施例热工性能和环境性质
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