CN101613591A - The mixing medium that a kind of heat pump is used - Google Patents
The mixing medium that a kind of heat pump is used Download PDFInfo
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- CN101613591A CN101613591A CN200810124052A CN200810124052A CN101613591A CN 101613591 A CN101613591 A CN 101613591A CN 200810124052 A CN200810124052 A CN 200810124052A CN 200810124052 A CN200810124052 A CN 200810124052A CN 101613591 A CN101613591 A CN 101613591A
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- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09K—MATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
- C09K5/00—Heat-transfer, heat-exchange or heat-storage materials, e.g. refrigerants; Materials for the production of heat or cold by chemical reactions other than by combustion
- C09K5/02—Materials undergoing a change of physical state when used
- C09K5/04—Materials undergoing a change of physical state when used the change of state being from liquid to vapour or vice versa
- C09K5/041—Materials undergoing a change of physical state when used the change of state being from liquid to vapour or vice versa for compression-type refrigeration systems
- C09K5/044—Materials undergoing a change of physical state when used the change of state being from liquid to vapour or vice versa for compression-type refrigeration systems comprising halogenated compounds
- C09K5/045—Materials undergoing a change of physical state when used the change of state being from liquid to vapour or vice versa for compression-type refrigeration systems comprising halogenated compounds containing only fluorine as halogen
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- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09K—MATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
- C09K2205/00—Aspects relating to compounds used in compression type refrigeration systems
- C09K2205/22—All components of a mixture being fluoro compounds
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- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09K—MATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
- C09K2205/00—Aspects relating to compounds used in compression type refrigeration systems
- C09K2205/34—The mixture being non-azeotropic
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Abstract
The present invention relates to the refrigerant mixture of the combination of two or three component, the binary non-azeotropic refrigerant by percentage to the quality, is made up of the material of following component: R125:1-80%, R152a:20-99%.Ternary non-azeotropic refrigerant by percentage to the quality, is made up of the material of following component: R125:2-50%, R152a:15-97%, R143a:1-35%.This refrigerant mixture carries out physical mixed at normal temperatures by the proportioning of formulating, and obtains corresponding mixing medium.This refrigeration agent ODP is zero, does not damage the ozone layer, and can reduce the Greenhouse effect influence, compliance with environmental protection requirements; Thermal parameter is suitable, and cycle performance is good.Can substitute the refrigerant mixture of Refrigerant 12 (CFC12) and difluorochloromethane (HCFC22) and the heat pump that is used in described refrigerant mixture.
Description
Technical field
The present invention relates to a kind of refrigerant mixture, especially be applied to the refrigerant mixture of heat pump, be used for substituting the heat pump that contains CFC12 or HCFC22 and be used in described refrigerant mixture.
Background technology
Since 1987, protection ozonosphere, superseded Ozone Depleting Substances reduce the whole world action of Greenhouse effect and just carry out according to " Montreal Agreement book " in countries in the world.China has begun actively to substitute work, and searching safety, alternative refrigerant efficient, environmental protection have become a urgent and important task.
Because CFC class refrigeration agent is by very high ozone depletion latent energy value (ODP), they are controlled by strict in the clause of Montreal and revision subsequently.HCFC class refrigeration agent, different with CFC, HCFC is that part hydrogen is former in being replaced by halogen atom, and the hydrogen atom that retains helps this chemical substance to divide decomposition at Middle Atmosmiddle stratosphere.Therefore also less relatively to the harm of ozonosphere generation.But, HCFC is listed in restricted substances in Copenhagen meeting in 1992, this has very big influence to refrigeration and air-conditioning industry, because the HCFC22 that still is widely used at present must be phased out, require developed country very to ban use of and to produce CFCs in 1996, the year two thousand twenty is abrogated HCFCs comprehensively; Developing country should stop production and consumption CFCs from 2010 comprehensively, and stops the use of HCFCs in the year two thousand thirty comprehensively.HFC has comprised R23, R32, R125, R134a and R152a etc.These hydrocarbon molecules comprise fluorine and do not comprise bromine.HFC class material is considered to substitute in the future the first-selected material of HCFCs because ozonosphere is not had destruction.But what HFC faced is their the stable problem of chemical property, and can assemble after discharging.This finally may quicken to cause Global warming.And the material that before half a century, has been replaced by CFC, as: ammonia (R717), water (R718), air (R729) and carbonic acid gas (R744) begin to become again available alternative working medium now.
Because it is limited to be fit to do the pure working medium of CFC surrogate, so mixing medium may be the effective way that addresses this problem.Mixing medium can obtain desired characteristic by the volumetric molar concentration proportioning that changes each component.In the past few years, people have proposed the substitute of multiple refrigerant mixture as CFC12 (also claiming R12), CFC502 (also claiming R502) and HCFC22 (also claiming R22), but some in them comprise HCFC as moiety, according to " Montreal Protocol ", its use is forbidden, therefore, in the long run, the refrigerant mixture of this HCFC of comprising is not suitable substituting refrigeration agent.What the present invention relates to comprises C2H4F2 C2H4F2 (HFC152a, also claim R152a), pentafluoride ethane (HFC125, also claim R125) and non-azeotropic mixed working medium boiling point difference under the equilibrium state of liquid and gas of Halothane (HFC143a also claims R143a) little, great development potentiality is arranged.
Heat pump fluid of the prior art is traditional R12, R22 and some alternative mixing mediums, as common R407c (R32/R125/R134a:23/25/52 massfraction), R417a (R125/R134a/R600:47/50/3 massfraction), R410a (R32/R125:50/50 massfraction) etc.Wherein R407C and R410a are the mixing mediums that very likely replaces R22 in the heat pump, generally can be raised to water temperature about 60 ℃ with the Teat pump boiler of these mixing mediums.Also the someone proposes the mixing medium that some are suitable for middle high temperature, high temperature heat pump, and be not described here.Also there is the scholar to mix surrogate with a certain amount of non-flammable R125 as R22 having flammable R152a.
Can be used as the substituting refrigeration agent that has refrigeration agent now in order to ensure predetermined substance, this material should have the coefficient of performance (COP) close with existing refrigeration agent.One of method that can solve this type of problem is to use refrigerant mixture.The advantage of refrigerant mixture is, regulates the composition of described refrigerant mixture by suitably making up various components, obtaining the coefficient of performance suitable with existing refrigeration agent and volume ability (VC) simultaneously, thereby makes and needn't do big transformation to compressor.
The R407C of DuPont company exploitation has traditional close refrigeration capacity of HCFC22 refrigeration agent, but its energy efficiency is relatively low, and its temperature glide difference is about 7 ℃, exhaust pressure and the R22 of R407C are close, efficiency approaches R22, its advantage is directly to charge (except that changing ester class oil), but its shortcoming is the decomposition that refrigeration agent may occur, cause leakage of refrigerant and miscellaneous part is produced detrimentally affect, when leaking appears in refrigeration agent in refrigeration system, with the isolating problem of the component that refrigeration agent occurs.In addition, when the slip temperature difference was excessive, changing mutually of refrigeration agent caused the pressure in vaporizer and condenser to change continuously, thereby causes the refrigeration system instability, finally makes the total system decrease in efficiency.This just means the new alternative working medium of needs searching.Allied Signal Inc. has developed and has sold R410a.R410a is a kind of nearly azeotropic mixture, and its temperature glide value is no more than 0.2 ℃.The exhaust pressure ratio R22 of R410a is high by 50～60%, and volume refrigerating capacity compressor is bigger, is about 1.4～1.5 times of R22, therefore can't directly charge, and must redesign compressor and major parts, and cost will be increased.Simultaneously, interchanger also need be optimized again to adapt to its lower volumetric flow rate.Therefore, although the Energy Efficiency Ratio R22 height of R410A, it only is applicable to newly-designed unit, can not be used for substituting the R22 of existing apparatus.
According to vapour pressure screening principle and the basic demand of working medium alternate, tentatively selected R152a and R125 constituent element as the binary mixing medium.The vapor-pressure curve of R152a and R125 and R22 is more approaching.The thermophysical property of these two kinds of constituent elements and alternative working medium relatively, the defective of R152a is to have combustibility, add a certain amount of non-flammable R125 and can suppress its combustibility, although the GWP value of R125 is higher, but when its proportion in mixture is significantly smaller than under the situation that the GWP value is about 0 R152a, the GWP value of mixture will reach satisfied degree.
The molten oiliness of R125 is relatively poor, but the intermiscibility of R152a and polyester lubricating oil is fine.So under the little situation of R125 content, the total molten oiliness of mixing medium can meet the demands.In addition, for R152a, R125, can also have polyoxyethylene glycol (PFPE) with the two lubricating oil that mixes simultaneously is oil and grease class.Significant be: the ODP value of R152a and R125 is 0, and this protection for ozonosphere is very important.And they all belong to the HFC class, have long-term alternate advantage.
Binary that R143a (HFC-143a) and R32, R134a, R125 form and tertiary mixture are considered to promise to be most the alternative thing that fills of widely used refrigeration agent R22 in air conditioning machinery and the heat pump set.In recent years, the relevant personnel have made lot of experiments to the thermodynamic properties of R143a both at home and abroad.
The ODP of the R125 that the present invention relates to, R143a and R152a (ODP) is 0.0, and their global warming potential (GWP) significantly is lower than other refrigeration agents.In view of this specific character, European Union (EU), Japan and most Asian countries have carried out a large amount of trials, they with the ODP value be 0.0 and the GWP refrigeration agent that is lower than traditional CFC or HFC refrigeration agent make up so that the thermodynamic behaviour that obtains expecting, raise the efficiency simultaneously and with the consistency of oil.In view of this, can think that propylene, propane, Trimethylmethane, DME and HFC152a can reach this purpose.But prior art is often regarded R125, R152a as a selecteed component, is combined into the beyond thought effect that mixing medium brings and ignored it.
Current, many countries have spent the alternative working medium that very big energy develops R22, and non-azeotropic mixed working medium that particularly those are existed in environment originally, safety, that purified refrigeration agent forms has caused special concern especially.In the cooling and warming circulation, refrigerating duty or heating capacity are the same important parameters with COP.Differ too big if substitute the refrigerating duty and the R22 of working medium, then compressor size must redesign, and cost is too high.Therefore, the refrigerating duty of alternative working medium must be similar with R22.
Refrigerant mixture involved in the present invention mainly comprises C2H4F2 C2H4F2 (R152a), pentafluoride ethane (R125) and Halothane (R143a).More particularly, the present invention also relates to refrigerant mixture that can replace Refrigerant 12 (R12) and difluorochloromethane (R22) and the refrigeration system that is used in described refrigerant mixture, described Refrigerant 12 now is widely used in home freezer and vehicle air conditioning, and described difluorochloromethane now is widely used in family expenses and business air conditioner.
Summary of the invention
The objective of the invention is to develop the New Refrigerating agent composition, this refrigerant mixture can use under the situation of not changing existing refrigeration system, it is selected from the refrigerant mixture by the combination of two or three component of C2H4F2 C2H4F2 (R152a), pentafluoride ethane (R125) and Halothane (R143a), its ODP (ODP) is 0.0, and their global warming potential (GWP) is also very low.Reach substantially and do not damage the ozone layer, can reduce the Greenhouse effect influence, compliance with environmental protection requirements; And nontoxic, low flammable, especially its thermal property and thermal parameter better performances can directly utilize R12 or R22 refrigeration system in heat pump, and the major parts in compressor and the system need not changed, and production line need not transformed, and is good with the miscible characteristic of lubricant.
Described refrigerant mixture of the present invention comprises: R152a and R125 refrigerant composition working medium, R152a, R125 and R143a refrigerant composition working medium; More particularly, the invention particularly relates to and be used for the pump type heat heat exchange system.The performance of same its low-temperature evaporation is also fabulous, has very high COP value in the serviceability below-5 ℃, the present invention also relates to refrigerant mixture that can replace Refrigerant 12 (R12) and difluorochloromethane (R22) and the heat pump that uses described refrigerant mixture, described Refrigerant 12 now is widely used in home freezer and vehicle air conditioning, and described difluorochloromethane now is widely used in family expenses and business air conditioner.
Prescription of the present invention mainly comprises: R125 and R152a refrigerant composition working medium, the ratio of the quality of R125 and R152a is: R125:1-80%, R152a:20-99%.
Binary non-azeotropic refrigerant composition working medium consists of: R125:2-50%, R152a:50-98%.
The binary non-azeotropic refrigerant consists of R125:5-14%, R152a:86-95%.
The binary non-azeotropic refrigerant consists of R125:35-65%, R152a:35-65%.
R125, R152a and R143a ternary non-azeotropic refrigerant composition working medium; R125, R152a and R143a mass percent are: R125:2-50%, R152a:15-97%, R143a:1-35%.
Ternary non-azeotropic refrigerant is R125:2-35%, R152a:64-97%R143a:1-10%.
Ternary non-azeotropic refrigerant is formed, R125:1-80%, R152a:20-97%, R143a:1-5%.
Ternary non-azeotropic refrigerant is formed, R125:5-15%, R152a:85-94%, R143a:1-5%
Ternary non-azeotropic refrigerant is formed, R125:35-64%, R152a:35-65%, R143a:1-5%
Above-mentioned mixing medium is applicable in heat pump and the extension product thereof.
Its preparation method is that said components is carried out physical mixed by its corresponding mixture ratio under liquid phase state.
The invention has the beneficial effects as follows:
(1) temperature glide is little.
(2) environmental performance is good, and not only depletion potential ODP value is zero, and global warming potential is substantially less than R22 and existing main surrogate R407C, and compliance with environmental protection requirements becomes sharpest edges of the present invention.
(3) change with the mixing medium proportioning, its thermal parameter pests occurrence rule variation, thermal parameter such as operating pressure, pressure ratio can be close with R12, R22, can directly use the compressor of R12 or R22 correspondence, need not the specialized designs compressor separately into the present invention.Can directly charge when being used for substituting R12 or R22 refrigeration agent, and unit volume heating capacity and R12 or R22 are suitable, and can reduce filling quantity.Thermal property such as unit mass heating capacity are better than R12, R22, and exhaust temperature is also less than R22, and COP and R12, R22 are suitable, can be used as the long-term surrogate of R12, R22.
Embodiment
The present invention is intended to develop a kind of novel refrigerant that can be used for substituting R12 or R22, refrigeration agent newly developed is not only damaged the ozone layer, and Greenhouse effect is littler.Have in addition and R12 or suitable thermal parameter and the thermal property of R22, can be used as the direct surrogate of R12 or R22.
This novel refrigerant that can be used for substituting R12, R22 provided by the invention is characterized in that this refrigeration agent is selected from the refrigerant mixture of combination of two or three component of C2H4F2 C2H4F2 (R152a), pentafluoride ethane (R125) and Halothane (R143a).
Binary zeotrope R125 and R152a mass percent are: R125:1-80%, R152a:20-99%.Form the ternary non-azeotropic mixture after adding R143a, the mass ratio that R143a adds is 1-35%.R125, R152a and R143a tertiary mixture mass percent are:
R125：2-50％，R152a：35-97％，R143a：1-35％。
Refrigeration agent provided by the invention, its preparation method are that above-mentioned various components are carried out physical mixed according to its corresponding mixture ratio under liquid phase state.
The thermophysical property of table 1-1 R152a, R125 and R143a and R22 relatively
| Refrigeration agent | Molecular formula | Molecular weight | Normal boiling point (℃) | Zero pour (℃) | Emergent pressure (MPa) | Critical temperature (℃) | (* 10 for critical specific volume -3m 3/kg |
| ??HCFC22 | ??CHClF 2 | ??84.47 | ??-40.78 | ?-160 | ???4.988 | ???96.2 | ??1.905 |
| ??HFC152a | ??CHF 2CH 3 | ??66.05 | ??-24.4 | ?-177 | ???4.520 | ???113.3 | ??2.74 |
| ??HFC125 | ??CF 3CHF 2 | ??120.02 | ??-48.55 | ?-102.95 | ???3.631 | ???66.25 | ??1.748 |
| ??HFC143a | ??CH2FCF 3 | ??84.04 | ??-47.2 | ?-101 | ???3.784 | ???72.9 | ??2.31 |
The thermophysical property of table 1-2 R152a, R125 and R143a and R22, R407C relatively
| Refrigeration agent | Atmospheric lifetime (year) | The ODP value | The GWP value | Combustion range (%) | Level of security | Toxicity |
| ??HCFC22 | ??11.9 | ?0.034 | ?1700 | Do not fire | A1 | Low |
| ??R407C | ?0 | ?1526 | Do not fire | A1 | Do not have | |
| ??HFC152a | ??1.4 | ?0 | ?120 | ??4.8～17.3 | A2 | Low |
| ??HFC125 | ??29 | ?0 | ?3400 | Do not fire | A1 | Do not have |
| ??HFC143a | ??52 | ?0 | ?4300 | ??7.0～1?0.3 | A2 | Low |
-ODP is as benchmark value 1.0 with CFC-11.
-GWP is as benchmark value 1.0 with CO2 (100 year level).
The binary refrigeration agent composition performance analysis of R125 and R152a relatively.
Embodiment A 1: the mass percent by 5: 95 under liquid phase is carried out physical mixed with R125 and R152a.
Embodiment A 2: the mass percent by 10: 90 under liquid phase is carried out physical mixed with R125 and R152a.
Embodiment A 3: the mass percent by 14: 86 under liquid phase is carried out physical mixed with R125 and R152a.
Embodiment A 4: the mass percent by 20: 80 under liquid phase is carried out physical mixed with R125 and R1 52a.
Embodiment A 5: the mass percent by 28: 72 under liquid phase is carried out physical mixed with R125 and R1 52a.
Embodiment A 6: the mass percent by 35: 65 under liquid phase is carried out physical mixed with R125 and R152a.
Embodiment A 7: the mass percent by 40: 60 under liquid phase is carried out physical mixed with R125 and R152a.
Embodiment A 8: R125 and R152a are carried out physical mixed by 50: 50 mass percents under liquid phase.
Embodiment A 9: the mass percent by 65: 35 under liquid phase is carried out physical mixed with R125 and R152a.
Embodiment A 10:R125 and the R152a mass percent by 80: 20 under liquid phase is carried out physical mixed.
The ternary refrigerant mixtures performance analysis of R125, R152a and R143a relatively.
Embodiment B 1: R125, R152a and R143a mass percent by 2: 97: 1 under liquid phase are carried out physical mixed.
Embodiment B 2: R125, R152a and R143a mass percent by 10: 89: 1 under liquid phase are carried out physical mixed.
Embodiment B 3: R125, R152a and R143a mass percent by 20: 75: 5 under liquid phase are carried out physical mixed.
Embodiment B 4: R125, R152a and R143a mass percent by 35: 64: 1 under liquid phase are carried out physical mixed.
Embodiment B 5: R125, R152a and R143a mass percent by 35: 60: 5 under liquid phase are carried out physical mixed.
Embodiment B 6: R125, R152a and R143a mass percent by 40: 52: 8 under liquid phase are carried out physical mixed.
Embodiment B 7: with R125, R152a and R143a under liquid phase by 45: 45: 10 mass percent physical mixed.
Embodiment B 8: with R125, R152a and R143a under liquid phase by 41: 41: 18 mass percent physical mixed.
Embodiment B 9: with R125, R152a and R143a under liquid phase by 35: 40: 25 mass percent physical mixed.
Embodiment B 10: R125, R152a and R143a mass percent by 45: 25: 30 under liquid phase are carried out physical mixed.
Embodiment B 11: R125, R152a and R143a mass percent by 30: 35: 35 under liquid phase are carried out physical mixed.
Embodiment B 12: R125, R152a and R143a mass percent by 50: 15: 35 under liquid phase are carried out physical mixed.
Now the performance of the foregoing description and R12, R22 and main surrogate R407C thereof are compared, characteristics of the present invention and effect are described.
The comparison of table 2 temperature glide (unit: ℃)
| Bubble point temperature | Dew-point temperature | Temperature glide | Bubble point temperature | Dew-point temperature | Temperature glide | ||
| Embodiment A 1 | -25.59 | -24.50 | ?1.09 | Embodiment B 3 | -31.56 | -26.95 | ?4.61 |
| Embodiment A 2 | -27.10 | -25.00 | ?2.10 | Embodiment B 4 | -34.14 | -28.34 | ?5.80 |
| Embodiment A 3 | -28.56 | -25.55 | ?3.01 | Embodiment B 5 | -35.18 | ?-29.12 | ?6.06 |
| Embodiment A 4 | -29.96 | -26.13 | ?3.83 | Embodiment B 6 | -37.02 | -30.63 | ?6.39 |
| Embodiment A 5 | -32.10 | -27.15 | ?4.95 | Embodiment B 7 | -38.51 | -32.09 | ?6.42 |
| Embodiment A 6 | -33.87 | -28.15 | ?5.72 | Embodiment B 8 | -39.37 | -33.23 | ?6.14 |
| Embodiment A 7 | -35.09 | -28.94 | ?6.15 | Embodiment B 9 | -39.65 | -33.68 | ?5.97 |
| Embodiment A 8 | -37.41 | -30.72 | ?6.69 | Embodiment B 10 | -42.39 | -37.74 | ?4.65 |
| Embodiment A 9 | -40.68 | -34.11 | ?6.57 | Embodiment B 11 | -40.71 | -35.16 | ?5.55 |
| Embodiment A 10 | -43.81 | -38.8 | ?5.10 | Embodiment B 12 | -44.15 | -41.1 | ?3.05 |
| Embodiment B 1 | -25.08 | -24.34 | ?0.74 | ?R407C | -43.63 | -36.63 | ?7.00 |
| Embodiment B 2 | -27.48 | -25.15 | ?2.33 |
Annotate: bubble point temperature in the table and dew-point temperature all are the temperature of saturation when standard atmospheric pressure 101.325kPa.
As can be seen from the table, the temperature glide of all embodiment is all less than R407C, and commercial use is no problem fully.
Environmental performance
Following table compared the environmental performance of the foregoing description and R22, R407C, wherein the ODP value as benchmark value 1.0, the GWP value is with CO with CFC-11
2As benchmark value 1.0 (100 years).
The comparison of table 3 environmental performance
| Refrigeration agent | ?OD | ?GWP | Refrigeration agent | ?ODP | ?GWP |
| Embodiment A 1 | ?0 | ?289 | Embodiment B 4 | ?0 | ?1310 |
| Embodiment A 2 | ?0 | ?448 | Embodiment B 5 | ?0 | ?1482 |
| Embodiment A 3 | ?0 | ?612 | Embodiment B 6 | ?0 | ?1766 |
| Embodiment A 4 | ?0 | ?776 | Embodiment B 7 | ?0 | ?2014 |
| Embodiment A 5 | ?0 | ?1038 | Embodiment B 8 | ?0 | ?2268 |
| Embodiment A 6 | ?0 | ?1268 | Embodiment B 9 | ?0 | ?2313 |
| Embodiment A 7 | ?0 | ?1432 | Embodiment B 10 | ?0 | ?2850 |
| Embodiment A 8 | ?0 | ?1760 | Embodiment B 11 | ?0 | ?2567 |
| Embodiment A 9 | ?0 | ?2252 | Embodiment B 12 | ?0 | ?3385 |
| Embodiment A 10 | ?0 | ?2748 | ?R12 | ?0.82 | ?8100 |
| Embodiment B 1 | ?0 | ?227 | ?R22 | ?0.034 | ?1700 |
| Embodiment B 2 | ?0 | ?490 | ?R407C | ?0 | ?1526 |
| Embodiment B 3 | ?0 | ?985 |
As can be seen from the table, it is zero that the ozonosphere of the foregoing description consumes potential (ODP) value, and atmospheric ozone layer is not had destruction, and this point is better than R12 and R22.
Moreover, the global warming potential of above-mentioned enforcement A1-A7 (GWP) is worth less than R22, has only 17%～84% of R22.Be 19%～93% of R407CGWP value, more meet current protection ozonosphere, reduce the environmental protection requirement of Global warming effect.
Moreover, the global warming potential of the foregoing description B1-B8 (GWP) value and R22 are suitable with R407C, meet current protection ozonosphere, reduce the environmental protection requirement of Global warming effect.
Thermal parameter and thermal performance
The present invention has obtained the thermal physical property parameter of the mixture of different proportionings by using Calculation of Physical Properties computed in software commonly used in the world, and Theoretical Calculation uses the performance of the heat pump thermodynamic cycle of different proportioning mixtures when having contrasted 5 ℃ of average vaporization temperatures, shown in table 4-1.
Performance between table 4-1 R12, R22 and the substituting refrigerant mixture relatively
| Parameter and performance | Condensing pressure MPa | Evaporating pressure MPa | Pressure ratio | Unit mass heating capacity kJ/kg | Compressor wasted work kJ/kg | ?CO ?P |
| Embodiment A 1 | 1.2218 | 0.3212 | 3.8039 | 289.54 | 62.07 | ?4.67 |
| Embodiment A 2 | 1.2676 | 0.3281 | 3.8634 | 280.83 | 61.18 | ?4.59 |
| Embodiment A 3 | 1.3149 | 0.3357 | 3.9169 | 272.04 | 60.19 | ?4.52 |
| Embodiment A 4 | 1.3636 | 0.3440 | 3.9639 | 263.10 | 59.06 | ?4.46 |
| Embodiment A 5 | 1.4449 | 0.3591 | 4.0236 | 248.53 | 56.97 | ?4.36 |
| Embodiment A 6 | 1.5199 | 0.3744 | 4.0596 | 235.56 | 54.93 | ?4.29 |
| Embodiment A 7 | 1.5759 | 0.3869 | 4.0731 | 226.15 | 53.32 | ?4.24 |
| Embodiment A 8 | 1.6948 | 0.4166 | 4.0682 | 206.97 | 49.76 | ?4.16 |
| Embodiment A 9 | 1.8945 | 0.4781 | 3.9626 | 177.24 | 43.53 | ?4.07 |
| Embodiment A 10 | 2.1301 | 0.5726 | 3.7201 | 146.27 | 36.24 | ?4.04 |
| Embodiment B 1 | 1.2060 | 0.3190 | 3.7806 | 293.52 | 62.54 | ?4.69 |
| Embodiment B 2 | 1.2788 | 0.3301 | 3.8740 | 279.65 | 61.15 | ?4.57 |
| Embodiment B 3 | 1.4201 | 0.3557 | 3.9924 | 256.71 | 58.42 | ?4.39 |
| Embodiment B 4 | 1.5316 | 0.3773 | 4.0594 | 234.24 | 54.75 | ?4.28 |
| Embodiment B 5 | 1.5784 | 0.3895 | 4.0524 | 228.80 | 53.86 | ?4.25 |
| Embodiment B 6 | 1.6710 | 0.4142 | 4.0343 | 215.10 | 51.35 | ?4.19 |
| Embodiment B 7 | 1.7552 | 0.4393 | 3.9954 | 202.51 | 48.79 | ?4.15 |
| Embodiment B 8 | 1.8036 | 0.4589 | 3.9303 | 198.88 | 47.96 | ?4.15 |
| Embodiment B 9 | 1.8155 | 0.4663 | 3.8934 | 200.56 | 48.24 | ?4.16 |
| Embodiment B 10 | 2.0064 | 0.5431 | 3.6943 | 173.09 | 41.82 | ?4.14 |
| Embodiment B 11 | 1.8760 | 0.4926 | 3.8084 | 196.33 | 47.08 | ?4.17 |
| Embodiment B 12 | 2.1451 | 0.6102 | 3.5154 | 155.46 | 37.47 | ?4.15 |
| R22 | 1.9427 | 0.5841 | 3.3260 | 197.24 | 42.89 | ?4.60 |
| R12 | 1.2166 | 0.3620 | 3.3608 | 144.7 | 30.89 | ?4.68 |
| R407C | 2.2160 | 0.3853 | 5.7514 | 217.06 | 64.86 | ?3.35 |
For the performance under the envrionment temperature in the winter time of heat pump relatively, average vaporization temperature has been done Theoretical Calculation equally for-5 ℃ of performances down, as showing shown in the 4-2.
Performance between table 4-2 R12, R22 and the substituting refrigerant mixture relatively
| Parameter and performance | Condensing pressure MPa | Evaporating pressure MPa | Pressure ratio | Unit mass heating capacity kJ/kg | Compressor wasted work kJ/kg | ?COP |
| Embodiment A 1 | 1.0775 | 0.2243 | ?4.8038 | ?302.87 | ?73.07 | ?4.15 |
| Embodiment A 2 | 1.1192 | 0.2293 | ?4.8809 | ?293.91 | ?71.96 | ?4.08 |
| Embodiment A 3 | 1.1623 | 0.2347 | ?4.9523 | ?284.81 | ?70.71 | ?4.03 |
| Embodiment A 4 | 1.2066 | 0.2406 | ?5.0150 | ?275.62 | ?69.36 | ?3.97 |
| Embodiment A 5 | 1.2806 | 0.2513 | ?5.0959 | ?260.59 | ?66.86 | ?3.90 |
| Embodiment A 6 | 1.3487 | 0.2623 | ?5.1418 | ?247.23 | ?64.46 | ?3.84 |
| Embodiment A 7 | 1.3994 | 0.2713 | ?5.1581 | ?237.50 | ?62.56 | ?3.80 |
| Embodiment A 8 | 1.5070 | 0.2927 | ?5.1486 | ?217.70 | ?58.40 | ?3.73 |
| Embodiment A 9 | 1.6871 | 0.3378 | ?4.9944 | ?193.02 | ?52.63 | ?3.67 |
| Embodiment A 10 | 1.8986 | 0.4082 | ?4.6512 | ?155.11 | ?42.83 | ?3.62 |
| Embodiment B 1 | 1.0630 | 0.2228 | ?4.7711 | ?307.00 | ?73.65 | ?4.17 |
| Embodiment B 2 | 1.1294 | 0.2307 | ?4.8955 | ?292.71 | ?71.92 | ?4.07 |
| Embodiment B 3 | 1.2581 | 0.2490 | ?5.0526 | ?269.12 | ?68.58 | ?3.92 |
| Embodiment B 4 | 1.3593 | 0.2644 | ?5.1411 | ?245.88 | ?64.24 | ?3.83 |
| Embodiment B 5 | 1.4017 | 0.2733 | ?5.1288 | ?240.36 | ?63.24 | ?3.80 |
| Embodiment B 6 | 1.4855 | 0.2912 | ?5.1013 | ?226.25 | ?60.29 | ?3.75 |
| Embodiment B 7 | 1.5615 | 0.3095 | ?5.0452 | ?213.27 | ?57.33 | ?3.72 |
| Embodiment B 8 | 1.6051 | 0.3241 | ?4.9825 | ?209.64 | ?56.39 | ?3.72 |
| Embodiment B 9 | 1.6159 | 0.3297 | ?4.9011 | ?211.57 | ?56.82 | ?3.72 |
| Embodiment B 10 | 1.7873 | 0.3873 | ?4.6148 | ?183.26 | ?49.42 | ?3.71 |
| Embodiment B 11 | 1.6705 | 0.3495 | ?4.7797 | ?206.91 | ?55.54 | ?3.73 |
| Embodiment B 12 | 1.9115 | 0.4386 | ?4.3582 | ?165.09 | ?44.36 | ?3.72 |
| R22 | 1.7292 | 0.4218 | ?4.0996 | ?207.87 | ?50.73 | ?4.10 |
| R12 | 1.0821 | 0.2606 | ?4.1523 | ?150.68 | ?36.25 | ?4.16 |
| R407C | 1.9723 | 0.3853 | ?5.1189 | ?208.61 | ?57.25 | ?3.64 |
As seen, the foregoing description A1-A7 is along with the raising of R125 content from table 4, and the COP of mixture reduces slip temperature difference increase simultaneously, and is simultaneously as shown in table 2, increases mixture slip temperature difference with R125 content and obviously increases.
The condensing pressure of the foregoing description A1-A3, evaporating pressure, pressure ratio and R12 are close, and be in allowed band, in addition, their unit volume heating capacity and R12 are suitable, this means that embodiment can directly use the compressor of R12, need not specialized designs compressor separately into the present invention.Can directly charge when being used for substituting the R12 refrigeration agent.The condensing pressure of embodiment A 7-A9, evaporating pressure, pressure ratio and R12 are close, and are in allowed band, but the unit volume heating capacity less than R22, the COP value of all embodiment is all greater than the surrogate R407C of R22, and is suitable with R12, R22.
The condensing pressure of the foregoing description B1-B4, evaporating pressure, pressure ratio and R12 are close, and are in allowed band, can directly charge when being used for substituting the R12 refrigeration agent.
Claims (10)
1. the binary non-azeotropic refrigerant is characterized in that by percentage to the quality, is made up of the material of following component: R125:1-80%, R152a:20-99%.
2, binary non-azeotropic refrigerant according to claim 1 is characterized in that consisting of R125:2-50%, R152a:50-98%.
3, binary non-azeotropic refrigerant according to claim 1 is characterized in that consisting of R125:5-14%, R152a:86-95%.
4, binary non-azeotropic refrigerant according to claim 1 is characterized in that consisting of R125:35-65%, R152a:35-65%.
5, ternary non-azeotropic refrigerant is characterized in that by percentage to the quality, is made up of the material of following component: R125:2-50%, R152a:15-97%, R143a:1-35%.
6, ternary non-azeotropic refrigerant according to claim 5 is characterized in that R125:2-35%, R152a:64-97%; R143a:1-10%.
7, ternary non-azeotropic refrigerant according to claim 5 is characterized in that R125:1-80%, R152a:20-97%, R143a:1-5%.
8, ternary non-azeotropic refrigerant according to claim 5 is characterized in that R125:5-15%, R152a:85-94%, R143a:1-5%.
9, ternary non-azeotropic refrigerant according to claim 5 is characterized in that R125:35-64%, R152a:35-65%, R143a:1-5%.
10, the mixing medium of one of claim 1-9 is applicable in heat pump and the extension product thereof.
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| CN200810124052A CN101613591A (en) | 2008-06-23 | 2008-06-23 | The mixing medium that a kind of heat pump is used |
| AU2009264496A AU2009264496B2 (en) | 2008-06-23 | 2009-06-04 | A mixed working fluid for heat pumps |
| PCT/CN2009/072121 WO2009155822A1 (en) | 2008-06-23 | 2009-06-04 | A mixed working fluid for heat pumps |
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| CN 201110066189 Division CN102181269B (en) | 2008-06-23 | 2008-06-23 | Mixed working medium for heat pump system |
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| CN102261775A (en) * | 2011-06-27 | 2011-11-30 | 浙江盾安人工环境股份有限公司 | Thermal expansion valve of R290 refrigerant air-conditioning system |
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| JPH03170583A (en) * | 1989-11-30 | 1991-07-24 | Matsushita Electric Ind Co Ltd | Working fluid |
| JPH08231945A (en) * | 1995-02-27 | 1996-09-10 | Sanyo Electric Co Ltd | Working fluid |
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| CN102261775A (en) * | 2011-06-27 | 2011-11-30 | 浙江盾安人工环境股份有限公司 | Thermal expansion valve of R290 refrigerant air-conditioning system |
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| AU2009264496A1 (en) | 2009-12-30 |
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