CN101864277A - Refrigerant composition with low GWP (Global Warming Potential) value - Google Patents
Refrigerant composition with low GWP (Global Warming Potential) value Download PDFInfo
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- CN101864277A CN101864277A CN201010196224A CN201010196224A CN101864277A CN 101864277 A CN101864277 A CN 101864277A CN 201010196224 A CN201010196224 A CN 201010196224A CN 201010196224 A CN201010196224 A CN 201010196224A CN 101864277 A CN101864277 A CN 101864277A
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Abstract
The invention discloses a refrigerant composition with a low GWP value. The composition consists of 2,3,3,3-tetrafluoropropene(HFO-1234yf), 1,1-difluoroethane (HFC-152a) and dimethyl ether (DME). The preparation method comprises the step of physically mixing the above components at normal temperature in corresponding proportion. The refrigerant composition has zero Ozone-Depletion Potential (ODP), and very low global warming potential (GWP), meets the requirement of environmental protection, has physical property equivalent to HFC-134a, and can be directly used in the traditional HFC-134a system without redesigning a compressor.
Description
Technical field
The present invention relates to a kind of refrigerant composition of low GWP value, relate in particular to a kind of refrigerant composition that substitutes HFC-134a in refrigeration, air-conditioning or the heat-pump apparatus that uses HFC-134a that is applied to have now.
Background technology
With HCFC-22, CFC-12, CFC-11 is that the freonll-11 of representative has good thermodynamic cycle performance, is widely used in industries such as refrigeration, air-conditioning.But this type of material has higher ozone depletion potential (ODP), and atmospheric residence time is very long, and global warming potential (GWP) is also very high, is one of main chemical substance of destroying atmospheric ozone layer, generation Greenhouse effect.Deleterious ultraviolet radiation can directly arrive earth surface after ozonosphere went to pot, and the plant plankton in farm crop and the ocean is produced severe impairment, but also can influence the immunity system of human body, the sickness rate of increase skin carcinoma, cataract etc.Global warming is another severe environmental problem that the mankind face, and brings serious consequence to ecotope, and thousands of times of GWP values have also played the effect of adding fuel to the flames to a large amount of dischargings of the refrigeration agent of carbonic acid gas.Montreal protocol and amendment thereof are forbidden CFC class material substantially, and regulation is progressively cut down to finally banning use of HCFC-22.In recent years, the exploitation about the refrigeration agent substitute products is one of important topic of organic fluorine chemical industry and association area research always.
The refrigeration agent substitute products that use mainly are HFC-134a, R410A and R407C etc. at present.But these refrigeration agents respectively have relative merits, still are not very desirable.Wherein, the thermal conduction of R407C is relatively poor, and volume refrigerating capacity compressor under the identical operating mode and COP value in order to reach the refrigerating duty identical with HCFC-22, need the heat-transfer effect of enhanced heat exchange device all less than HCFC-22, and manufacturing cost will increase.The volume refrigerating capacity compressor of R410A is big more a lot of than HCFC-22, but its evaporating pressure, condensing pressure are also high a lot of than HCFC-22, can not directly be used for substituting HCFC-22, need to redesign compressor, interchanger, pipeline and system in use, and, these two kinds of mix refrigerants all have higher GWP value, and a large amount of dischargings can the aggravation global warming.HFC-134a has good thermomechanical property and good safety in utilization, has become the refrigeration agent of widespread use in the domestic and international refrigerating and air conditioning industry, and its ODP is zero, but GWP is still higher, and a large amount of uses can cause global warming equally.Fluorine-containing greenhouse gases (F-gas) the control laws and regulations requirement that European Union in 2004 passes through, from on January 1st, 2011, European Union will forbid that the automative air conditioning of new production uses the GWP value greater than 150 refrigeration agent, and from January 1st, 2017, forbid that all automative air conditionings use GWP greater than 150 refrigeration agent, therefore, study refrigeration agent that hangs down GWP and the trend that matching system becomes refrigeration, air-conditioning and heat pump industry development thereof and inevitable.
Summary of the invention
The objective of the invention is to research and develop a kind of refrigerant composition of low GWP value, to make refrigeration agent ODP newly developed be zero and can suppress global warming, especially research and develop a kind of cycle performance and HFC-134a quite, can directly be used in the refrigeration agent that has the HFC-134a system now and can be used as the long-term surrogate of HFC-134a.
The present invention is a kind of refrigerant composition of low GWP value, and it is by 2,3,3,3-tetrafluoeopropene (HFO-1234yf), 1, and 1-C2H4F2 C2H4F2 (HFC-152a) and dme (DME) are formed, and the mass percent of each component is:
2,3,3,3-tetrafluoeopropene (HFO-1234yf): 50%~90%;
1,1-C2H4F2 C2H4F2 (HFC-152a): 5%~30%;
Dme (DME): 5%~30%.
The preparation method of refrigerant composition provided by the invention is with 2,3,3,3-tetrafluoeopropene HFO-1234yf, 1, and 1-C2H4F2 C2H4F2 HFC-152a and dme (DME) carry out physical mixed at normal temperatures by its specified quality proportioning.
The present invention has the following advantages and beneficial effect:
1, ODP value of the present invention is zero, and GWP very low (less than 150) meets environmental protection requirement.Table 1 has been listed the basic parameter of each component of the present invention.
2, thermal parameter and HFC-134a are very approaching, the present invention directly can be charged in refrigeration, air-conditioning or the heat pump set of the existing HFC-134a of use, need not to be specialized designs compressor of the present invention and system thereof.
3, cycle performance is good.COP value of the present invention is suitable with HFC-134a, and volume refrigerating capacity compressor is also very approaching with HFC-134a, need not the parts and the pipeline of the system that changes when substituting HFC-134a, meets HFC-134a alternate long term growth requirement.
In a word; refrigerant composition provided by the invention is to develop with substituting of refrigeration agent for satisfying refrigeration, air-conditioning or heat pump, especially can be used for existing HFC-134a system and substitute HFC-134a; thermal property is suitable in HFC-134a, meets requirement on environmental protection.
The basic parameter of the contained component of table 1 environment friendly refrigerating fluid
Component | Title | Molecular weight | Normal boiling point ℃ | Critical temperature ℃ | Emergent pressure MPa | ??ODP | ??GWP |
??HFO-1234yf | 2,3,3, the 3-tetrafluoeopropene | ??114.04 | ??-29.45 | ??94.7 | ??3.382 | ??0 | ??4 |
??HFC-152a | 1, the 1-C2H4F2 C2H4F2 | ??66.05 | ??-24.02 | ??113.26 | ??4.517 | ??0 | ??120 |
??DME | Dme | ??46.07 | ??-24.81 | ??127.15 | ??5.341 | ??0 | ??0 |
The present invention is further illustrated below in conjunction with specific embodiment.
Embodiment
The present invention is a kind of refrigerant composition of low GWP value, and it is by 2,3,3,3-tetrafluoeopropene (HFO-1234yf), 1, and 1-C2H4F2 C2H4F2 (HFC-152a) and dme (DME) are formed, and the mass percent of each component is:
Embodiment 1: get 50% HFO-1234yf, 20% HFC-152a, 30% DME, carry out at normal temperatures after the physical mixed as refrigeration agent.
Embodiment 2: get 50% HFO-1234yf, 30% HFC-152a, 20% DME, carry out at normal temperatures after the physical mixed as refrigeration agent.
Embodiment 3: get 50% HFO-1234yf, 25% HFC-152a, 25% DME, carry out at normal temperatures after the physical mixed as refrigeration agent.
Embodiment 4: get 60% HFO-1234yf, 20% HFC-152a, 20% DME, carry out at normal temperatures after the physical mixed as refrigeration agent.
Embodiment 5: get 67% HFO-1234yf, 18% HFC-152a, 15% DME, carry out at normal temperatures after the physical mixed as refrigeration agent.
Embodiment 6: get 70% HFO-1234yf, 15% HFC-152a, 15% DME, carry out at normal temperatures after the physical mixed as refrigeration agent.
Embodiment 7: get 90% HFO-1234yf, 5% HFC-152a, 5% DME, carry out at normal temperatures after the physical mixed as refrigeration agent.
The design conditions of refrigeration system are taken as: average vaporization temperature is 2 ℃, and average condensing temperature is 60 ℃, and superheating temperature is 5 ℃, and condensate depression is 5 ℃, according to cycle calculations, the foregoing description have related parameter and cycle performance index as shown in table 2.
Table 2 embodiment of the invention performance
Parameter and performance | Embodiment 1 | Embodiment 2 | Embodiment 3 | Embodiment 4 | Embodiment 5 | Embodiment 6 | Embodiment 7 | ??HFC-1??34a |
Evaporating pressure MPa | ??0.327 | ??0.334 | ??0.331 | ??0.335 | ??0.339 | ??0.339 | ??0.342 | ??0.315 |
Condensing pressure MPa | ??1.616 | ??1.651 | ??1.635 | ??1.649 | ??1.664 | ??1.658 | ??1.661 | ??1.682 |
Pressure ratio | ??4.94 | ??4.94 | ??4.94 | ??4.91 | ??4.90 | ??4.89 | ??4.86 | ??5.35 |
System amount refrigerating duty KJ/kg | ??174.40 | ??164.31 | ??169.59 | ??152.20 | ??139.27 | ??136.39 | ??105.75 | ??125.2??3 |
Volume refrigerating capacity compressor KJ/m3 | ??1925 | ??1947 | ??1939 | ??1913 | ??1894 | ??1878 | ??1763 | ??1884 |
??COP | ??3.57 | ??3.55 | ??3.56 | ??3.51 | ??3.46 | ??3.45 | ??3.30 | ??3.49 |
??ODP | ??0 | ??0 | ??0 | ??0 | ??0 | ??0 | ??0 | ??0 |
??GWP | ??26 | ??38 | ??32 | ??26.4 | ??24.28 | ??20.8 | ??9.6 | ??1300 |
As can be seen from Table 2, every performance and the parameter of the present invention and HFC-134a are more approaching, and ozone layer destroying potential of the present invention (ODP) is zero, can not destroy atmospheric ozone layer, and Greenhouse effect potential (GWP) is very low, meets requirement on environmental protection.
The preparation method:
The preparation method of refrigerant composition provided by the invention is with 2,3,3,3-tetrafluoeopropene HFO-1234yf, 1, and 1-C2H4F2 C2H4F2 HFC-152a and dme (DME) carry out physical mixed at normal temperatures by its specified quality proportioning.
Claims (1)
1. the refrigerant composition of a low GWP value is characterized in that: it is by 2,3,3,3-tetrafluoeopropene (HFO-1234yf), 1, and 1-C2H4F2 C2H4F2 (HFC-152a) and dme (DME) are formed, and the mass percent of each component is:
2,3,3,3-tetrafluoeopropene (HFO-1234yf): 50%~90%;
1,1-C2H4F2 C2H4F2 (HFC-152a): 5%~30%;
Dme (DME): 5%~30%.
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Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103289648A (en) * | 2013-05-06 | 2013-09-11 | 陈振乐 | Environmentally-friendly energy-saving refrigerant capable of substituting R134a |
WO2014202017A1 (en) | 2013-06-21 | 2014-12-24 | 浙江蓝天环保高科技股份有限公司 | Mixed refrigerant |
WO2015000367A1 (en) | 2013-07-05 | 2015-01-08 | 浙江蓝天环保高科技股份有限公司 | Environment-friendly near-azeotropic mixed refrigerant |
WO2018120257A1 (en) | 2016-12-26 | 2018-07-05 | 浙江衢化氟化学有限公司 | Refrigerant composition containing hydrofluoroolefin |
WO2021062963A1 (en) | 2019-09-30 | 2021-04-08 | 浙江衢化氟化学有限公司 | Composition of fluoroolefin and fluoroalkane |
WO2022017109A1 (en) | 2020-07-21 | 2022-01-27 | 浙江衢化氟化学有限公司 | Composition containing fluorohydrocarbon and preparation method therefor |
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WO2008009923A2 (en) * | 2006-07-17 | 2008-01-24 | Ineos Fluor Holdings Limited | Heat transfer compositions |
CN101297016A (en) * | 2005-03-04 | 2008-10-29 | 纳幕尔杜邦公司 | Compositions comprising a fluoroolefin |
CN101346450A (en) * | 2005-11-01 | 2009-01-14 | 纳幕尔杜邦公司 | Compositions comprising fluoroolefins and uses thereof |
JP2009155463A (en) * | 2007-12-26 | 2009-07-16 | Nippon Oil Corp | Refrigerating machine oil and hydraulic fluid composition for refrigerating machine |
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2010
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CN101297016A (en) * | 2005-03-04 | 2008-10-29 | 纳幕尔杜邦公司 | Compositions comprising a fluoroolefin |
CN101346450A (en) * | 2005-11-01 | 2009-01-14 | 纳幕尔杜邦公司 | Compositions comprising fluoroolefins and uses thereof |
WO2008009923A2 (en) * | 2006-07-17 | 2008-01-24 | Ineos Fluor Holdings Limited | Heat transfer compositions |
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Cited By (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103289648A (en) * | 2013-05-06 | 2013-09-11 | 陈振乐 | Environmentally-friendly energy-saving refrigerant capable of substituting R134a |
WO2014202017A1 (en) | 2013-06-21 | 2014-12-24 | 浙江蓝天环保高科技股份有限公司 | Mixed refrigerant |
WO2015000367A1 (en) | 2013-07-05 | 2015-01-08 | 浙江蓝天环保高科技股份有限公司 | Environment-friendly near-azeotropic mixed refrigerant |
US10752819B2 (en) | 2013-07-05 | 2020-08-25 | Zhejiang Lantian Environmental Protection Hi-Tech Co., Ltd. | Environmentally friendly near-azeotropic mixed refrigerant |
US11136483B2 (en) | 2013-07-05 | 2021-10-05 | Zhejiang Lantian Environmental Protection Hi-Tech Co., Ltd. | Environmentally friendly near-azeotropic mixed refrigerant |
US11549042B2 (en) | 2013-07-05 | 2023-01-10 | Zhejiang Lantian Environmental Protection Hi-Tech Co., Ltd. | Environmentally friendly near-azeotropic mixed refrigerant |
WO2018120257A1 (en) | 2016-12-26 | 2018-07-05 | 浙江衢化氟化学有限公司 | Refrigerant composition containing hydrofluoroolefin |
US11104833B2 (en) | 2016-12-26 | 2021-08-31 | Zhejiang Quhua Fluor-Chemistry Co Ltd | Hydrofluoroolefins-containing refrigerant composition |
WO2021062963A1 (en) | 2019-09-30 | 2021-04-08 | 浙江衢化氟化学有限公司 | Composition of fluoroolefin and fluoroalkane |
WO2022017109A1 (en) | 2020-07-21 | 2022-01-27 | 浙江衢化氟化学有限公司 | Composition containing fluorohydrocarbon and preparation method therefor |
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Application publication date: 20101020 |