mixture of non-flammable refrigerant, composition, process for producing refrigeration, method for r

专利摘要:
MIXTURE OF NONFLAMMABLE REFRIGERANT, COMPOSITIONS, PROCESS TO PRODUCE REFRIGERATION, METHOD FOR REPLACING A REFRIGERANT AND REFRIGERANT APPLIANCE. The present invention relates to the mixture of non-flammable refrigerant. The non-flammable refrigerant mixture consists essentially of (a) from 20% by weight to 25.5% by weight of HFO-1234yf, (b) from 20% by weight to 24.5% by weight of HFC-32, ( c) from 24.5% by weight to 30% by weight of HFC-125 (d) from 25.5% by weight to 30% by weight of HFC-134a, and (e) of about 0.0001% in 10% weight by weight of trans-HFO-1234ze. These coolant mixtures are useful as components of compositions that also contain non-coolant components (for example, lubricants), in processes for the production of refrigeration, in methods for replacing refrigerant R-404A, or R-507, and refrigeration appliances.
公开号:BR112014019964B1
申请号:R112014019964-7
申请日:2013-02-12
公开日:2021-02-09
发明作者:Barbara Haviland Minor
申请人:E.I. Du Pont De Nemours And Company；
IPC主号:

专利说明:

FIELD OF THE INVENTION
[001] The present invention relates to compositions for use in refrigeration systems. In particular, these compositions are useful in processes for the production of refrigeration, in methods for replacing refrigerants and in refrigeration devices. BACKGROUND OF THE INVENTION
[002] The refrigeration industry has been working in recent decades to find replacement refrigerants for chlorofluorocarbons (CFCs) and hydrochlorofluorocarbons (HCFCs) depleting the ozone layer, being eliminated as a result of the Montreal Protocol. The solution for most refrigeration producers was the commercialization of hydrofluorocarbon (HFC) refrigerants. The new HFC refrigerants, HFC-134a, being the most widely used at this time, have zero ozone depletion potential and are therefore not affected by the current phase-out regulation as a result of the Montreal Protocol.
[003] Other environmental regulations may ultimately lead to the elimination of certain HFC refrigerants. The industry is currently facing regulations regarding global warming potential (GWP) for refrigerants used in mobile air conditioning equipment. Should the regulation be more widely applied in the future, for example, for fixed air conditioning and refrigeration systems, an even greater need will be felt for refrigerants that can be used in all areas of the refrigeration and air conditioning industry. Uncertainty about current regulatory requirements in relation to GWP forces the industry to consider the various compounds and mixtures of candidates.
[004] The previously proposed replacement refrigerants for HFC refrigerants and refrigerant mixtures include HFC-152a, pure hydrocarbons, such as butane or propane, or "natural" refrigerants such as CO2. Each of these suggested replacements has problems, which include toxicity, flammability, low energy efficiency, or needs modifications to the design of the main equipment. New substitutions are also being proposed for HCFC-22, R-134a, R-404A, R-507, R-407C and R-410A, among others. The uncertainty as to which of the regulatory requirements in relation to GWP will finally be adopted forces the industry to consider the various compounds and mixtures of candidates that balance the need for low GWP, non-flammability, and the performance parameters of the current system. BRIEF DESCRIPTION OF THE INVENTION
[005] Certain compositions comprising tetrafluoropropene, difluoromethane, pentafluorethane and tetrafluorethane have been found to have suitable properties to allow their use as substitutes for the highest GWP refrigerants currently in use, in particular R-404A and R507.
[006] In accordance with the present invention, a mixture of non-flammable refrigerant is provided. The non-flammable refrigerant mixture consists essentially of (a) from 20% by weight to 25.5% by weight of HFO-1234yf, (b) from 20% by weight to 24.5% by weight of HFC-32, ( c) from 24.5% by weight to 30% by weight of HFC-125 (d) from 25.5% by weight to 30% by weight of HFC-134a, and (e) of about 0.0001% in 10% weight by weight of HFO-1234ze.
[007] These coolant mixtures are useful as components in compositions that also contain non-coolant components (for example, lubricants), in processes for the production of refrigeration, in methods for replacing refrigerant R-404A, or R- 507, and in the refrigeration equipment. DETAILED DESCRIPTION OF THE INVENTION
[008] Before discussing details of the achievements described below, some terms are defined or clarified. DEFINITIONS
[009] As used herein, the term "heat transfer fluid" means a composition used to transport heat from a heat source to a heat sink.
[010] The term “heat source” is defined as any space, location, object or body from which it is convenient to add, transfer, move or remove heat. Examples of heat sources are spaces (open or closed) that require refrigeration or cooling, such as a refrigerator or freezer in a supermarket, building spaces that require air conditioning, industrial water coolers or the passenger compartment of a car that needs air conditioning. In some embodiments, the heat transfer composition may remain in a constant state throughout the transfer process (that is, it will not evaporate or condense). In other embodiments, evaporative cooling processes can also use heat transfer compositions.
[011] The term “heat sink” is defined as any space, location, object or body capable of absorbing heat. A vapor compression cooling system is an example of a heat sink.
[012] The term “refrigerant fluid” is defined as a heat transfer fluid, which is subjected to a phase change from liquid to gas and back again during the cycle used for heat transfer.
[013] A heat transfer system is the system (or appliance), used to produce a heating or cooling effect in a given space. A heat transfer system can be a mobile system or a stationary system.
[014] Examples of heat transfer systems are any type of refrigeration systems and air conditioning systems, which include, but are not limited to, air conditioners, freezers, refrigerators, heat pumps, water coolers, water coolers flooded evaporator, direct expansion coolers, commercial refrigerators, mobile refrigerators, mobile air conditioning units, mobile dehumidifiers, and combinations thereof.
[015] As used in the present, the mobile heat transfer system refers to any type of refrigeration, air conditioning, heating devices incorporated in a transport unit for road, rail, sea or air transport. In addition, mobile refrigeration or air conditioning units include those devices that are independent of any mobile vehicle and are known as “intermodal” systems. Such intermodal systems include “containers” (combined sea / land transport) as well as “exchange bodies” (combined road / rail transport).
[016] As used at present, stationary heat transfer systems are systems that are fixed during operation. A stationary heat transfer system can be associated with or connected to buildings of any variety, or they can be autonomously located externally devices, such as a beverage vending machine. These stationary applications can be air conditioning and stationary heat pumps, including, but not limited to, coolers, high temperature heat pumps, residential, commercial or industrial air conditioning systems (including residential heat pumps), and including terminals packed with window, without ducts, with ducts, and those external, but connected to the construction, such as ceiling systems. In stationary refrigeration applications, the compositions described can be useful in equipment, including commercial, industrial or residential refrigerators and freezers, ice machines, independent refrigerators and freezers, flooded evaporator coolers, direct expansion coolers, commercial refrigerators and freezers and refrigerator cabinet, and combined systems. In some embodiments, the described compositions can be used in supermarket refrigeration systems. In addition, stationary applications may use a secondary circuit system, which uses a primary refrigerant to produce cooling in a location that is transferred to a remote location through a secondary heat transfer fluid.
[017] Cooling capacity (also sometimes referred to as cooling capacity) is a term that defines the change in the enthalpy of a refrigerant (or mixture of refrigerant), in an evaporator per unit mass of circulated refrigerant (or mixture of refrigerant), or the heat removed by the refrigerant (or mixture of refrigerant) in the evaporator per unit volume of refrigerant vapor (or mixture of refrigerant) that leaves the evaporator (volumetric capacity). Refrigeration capacity is a measure of the ability of a refrigerant (or mixture of refrigerant) or the heat transfer composition to produce cold. Therefore, the greater the capacity, the greater the cooling produced. The cooling rate refers to the heat removed by the refrigerant (or mixture of refrigerant) in the evaporator per unit of time.
[018] The performance coefficient (COP) is the amount of heat removed in the evaporator divided by the energy consumption required to operate the cycle. The higher the COP, the greater the energy efficiency. COP is directly related to the energy efficiency index (EER), which is the efficiency index for refrigeration or air conditioning equipment at a specific set of internal and external temperatures.
[019] The term "subcooling" refers to reducing the temperature of a liquid below the liquid's saturation point to a specified pressure. The saturation point is the temperature at which the vapor is completely condensed into a liquid, but subcooling continues to cool the liquid to a lower temperature at a given pressure. By cooling a coolant (or coolant mixture) below the saturation temperature (or bubble point temperature), the coolant liquid capacity can be increased. As a result, subcooling improves a system's cooling capacity and energy efficiency. The amount of subcooling is the amount of cooling below the saturation temperature (in degrees).
[020] Overheating is a term that defines how much above the saturation vapor temperature (the temperature at which, if the composition is cooled, the first liquid drop is formed, also referred to as a “dew point”), a composition of steam is heated.
[021] The temperature glide (sometimes simply referred to as “phase change”) is the absolute value of the difference between the initial and final temperatures of a phase change process by a refrigerant (or mixture refrigerant) within a component of a refrigerant system, exclusive of any subcooling or overheating. This term can be used to describe the condensation or evaporation of an almost azeotropic or non-azeotropic composition (or mixture of refrigerant). When referring to the temperature change temperature (temperature glide) of a refrigeration, air conditioning or heat pump system, it is common to provide the average temperature change temperature (glide) as the phase change temperature ( temperature glide) in the evaporator and the temperature change temperature (temperature glide) in the condenser.
[022] An azeotropic composition means a mixture of constant boiling point of two or more substances that behave as a single substance. One way of characterizing an azeotropic composition is that the vapor produced by partial evaporation or distillation of the liquid has the same composition as the liquid from which it is evaporated or distilled, that is, the mixture distills / reflows without changing the composition. Constant boiling point compositions are characterized as azeotropic since they exhibit a maximum or minimum boiling point, when compared to that of the non-azeotropic mixture of the same compounds. An azeotropic composition will not fractionate within a refrigeration or air conditioning system during operation. In addition, an azeotropic composition will not fractionate when leaking from a refrigeration or air conditioning system.
[023] An azeotrope-type composition (in general, also referred to as an "almost azeotropic composition") is a substantially constant boiling liquid mixture of two or more substances that essentially behave as a single substance. One way of characterizing an azeotrope-type composition is that the vapor produced by partial evaporation or distillation of the liquid substantially has the same composition as the liquid from which it is evaporated or distilled, that is, the distillate / reflux mixture, without substantial change in the composition. Another way of characterizing an azeotrope-type composition is that the vapor pressure of the bubble point and the vapor pressure of the dew point of the composition at a particular temperature are substantially the same. At present, a composition is of the azeotrope type if, after 50% by weight of the composition is removed, such as by evaporation or boiling, the difference in vapor pressure between the original composition and the remaining composition after 50% by weight of the original composition have been removed is less than about 10%.
[024] A non-azeotropic composition (also referred to as zeotropic) is a mixture of two or more substances that behaves as a simple mixture, rather than a single substance. One way of characterizing a non-azeotropic composition is that the vapor produced by partial evaporation or distillation of the liquid has a composition substantially different from the liquid from which it has been evaporated or distilled, that is, the distill / reflux mixture with substantial change in the composition. Another way of characterizing a non-azeotropic composition which is the vapor pressure of the bubble point and the vapor pressure of the dew point of the composition at a particular temperature are substantially different. At present, a composition is non-azeotropic if, after 50% by weight of the composition is removed, such as by evaporation or boiling, the difference in vapor pressure between the original composition and the remaining composition after 50% by weight of the original composition has removed is less than about 10%.
[025] As used herein, the term "lubricant" means any material added to a composition or a compressor (and in contact with any heat transfer composition in use within any heat transfer system), which provides lubrication compressor to help prevent parts from clogging.
[026] As used in the present, compatibilizers are compounds that improve the hydrofluorocarbon solubility of the compositions described in the lubricants of the heat transfer system. In some embodiments, the compatibilizers improve the return of the oil to the compressor. In some embodiments, the composition is used with a lubricating system to reduce the viscosity of the oil-rich phase.
[027] As used in the present, the oil return refers to the ability of a heat transfer composition to transport the lubricant through a heat transfer system and returned to the compressor. That is, in use, it is not uncommon for a part of the compressor lubricant to be carried by the heat transfer composition from the compressor to the other parts of the system. In such systems, if the lubricant is not efficiently returned to the compressor, the compressor will eventually fail due to lack of lubrication.
[028] As used herein, the “ultraviolet” dye is defined as a fluorescent or phosphorescent UV composition that absorbs light in the ultraviolet region or “near” the ultraviolet of the electromagnetic spectrum. The fluorescence produced by the fluorescent UV dye under illumination by a UV light that emits at least some radiation with a wavelength in the range of about 10 nm to about 775 nm can be detected.
[029] Flammability is a term used to designate a composition's ability to ignite and / or propagate a flame. For refrigerants and other heat transfer compositions, the lowest flammability limit (“LFL”) is the minimum concentration of the heat transfer composition in the air that is capable of propagating a flame through a homogeneous mixture of the composition and the air under the test conditions specified in the ASTM (American Society of Testing and Materials) standard E681. The upper flammability limit ("UFL") is the maximum concentration of the heat transfer composition in the air that is capable of propagating a flame through a homogeneous mixture of the composition and the air under the same test conditions. To be classified by the ASHRAE (American Society of Heating, Refrigerating and Air Conditioning Engineers) as non-flammable, a refrigerant must be non-flammable under the conditions of the ASTM E681 standard, as formulated in the liquid and gaseous phase, as well as non-flammable in the liquid and gas phases. gases that result in leakage scenarios.
[030] Global warming potential (GWP) is an index for calculating the contribution to global warming, due to the atmospheric emission of one kilogram of a specific greenhouse gas compared to the emission of one kilogram of carbon dioxide. GWP can be calculated for different time horizons showing the effect of the atmospheric life span of a given gas. The GWP for the 100-year time horizon is commonly the referenced value. In the case of mixtures, a weighted average can be calculated based on the individual GWP values for each component of the mix.
[031] The ozone depletion potential (ODP) is a number that refers to the amount of ozone depletion caused by a substance. ODP is the proportion of the impact on ozone of a chemical compared to the impact of a similar mass of CFC-11 (fluorotrichloromethane). Therefore, the CFC-11 ODP is set to 1.0. Other CFCs and HCFCs have ODPs that range from 0.01 to 1.0. HFCs have zero ODP since they do not contain chlorine.
[032] As used herein, the terms "comprises", "comprising", "includes", "including", "owns", "owning" or any other amendment thereto, are intended to cover non-exclusive inclusion. For example, a composition, process, method, article or device that includes a list of elements is not necessarily limited to just those elements, but may include other elements not expressly listed or inherent in such a composition, process, method, article or device. In addition, unless expressly stated to the contrary, "or" refers to an inclusive or not to an exclusive or exclusive. For example, a condition A or B is satisfied by any of the following characteristics: A is true (or present) and B is false (or not present), A is false (or not present) and B is true (or present) and both A and B are true (or present).
[033] The transition phrase “which consists of” excludes any unspecified element, step or ingredient. If it is in the claim this will restrict the claim to the inclusion of materials in addition to those cited, except for the normally associated impurities. When the phrase “consists of” appears in a clause in the body of a claim, instead of immediately after the preamble, it limits only the element presented in that clause; the other elements are not excluded from the claim as a whole.
[034] The transition phrase “which essentially consists of” is used to define the composition, method or apparatus that includes the materials, stages, characteristics, components or elements, in addition to those described literally, provided that these materials, stages, resources, additional components or elements included do not materially affect the basic and innovative feature (s) of the claimed invention. The term "which essentially consists of" occupies a middle ground between "comprises" and "consists". Typically, the components of the refrigerant mixtures and the refrigerant mixtures themselves may contain small amounts (for example, less than about 0.5 % by weight in total) of impurities and / or derived products (for example, from the manufacture of refrigerant components or the recovery of refrigerant components from other systems) that do not materially affect the innovative and basic characteristics of the refrigerant mixture. For example, HFC-134a may contain minor amounts of HFC-134 as a by-product of the manufacture of HFC-134a, of specific interest in connection with the present invention is HFO-1234ze, which may be a by-product of certain processes for the production of HFO-1234yf (see, for example, US patent 2009 / 0.278.075). However, it is observed that certain embodiments of the present invention through the recitation of HFO-1234ze as a component separate include HFO-1234ze whether or not its presence materially affects the innovative and basic characteristics of the refrigerant mixture (alone or in conjunction with other impurities and / or by-products which by itself would not substantially affect the innovative and basic characteristics of the mixture of soft drink).
[035] If the Depositor has defined a present invention or a part of it with an open term, such as "understands", it should be easily understood that (unless otherwise stated) the description should be interpreted as also describing that invention using the terms “Which essentially consists of” or “which consists of".
[036] In addition, the use of "one" or "one" is employed to describe the elements and components described herein. This is done for convenience only and to provide a general sense of the scope of the present invention. The present specification should be read including one or at least one and the singular also includes the plural, unless it is obvious that it is understood otherwise.
[037] Unless otherwise indicated, all technical and scientific terms used in the present have the same meaning as those generally understood by a regular technician in the subject to which the present invention belongs. Although methods and materials similar or equivalent to those described in this specification can be used in the practice or testing of the embodiments of the present invention, suitable methods and materials are described below. All publications, patent applications, patents and other references mentioned herein are incorporated by reference in their entirety, unless a specific passage is cited. In case of conflict, this specification, including definitions, will control it. In addition, the materials, methods and examples are illustrative only and are not intended to be a limitation.
[038] 2,3,3,3-tetrafluoropropene can also be referred to as HFO-1234yf, HFC-1234yf or R1234yf. HFO-1234yf can be produced using methods known in the art, such as by dehydrofluorination of 1,1,1,2,3-pentafluoropropane (HFC-245eb) or 1,1,1,2,2-pentafluoropropane (HFC-245cb).
[039] Difluoromethane (HFC-32 or R32) is commercially available or can be produced using methods known in the art, such as by dehydrofluorination of methylene chloride.
[040] Pentafluoroethane (HFC-125 or R125) is commercially available or can be produced using methods known in the art, such as by dehydrofluorination of 2,2-dichloro-1,1,1-trifluoroethane, as described in US patent 5,399,549, incorporated herein by reference.
[041] 1,1,1,2-tetrafluoroethane (HFC-134a or R134a) is commercially available or can be produced using methods known in the art, such as by hydrogenating 1,1-dichloro-1, 2,2,2-tetrafluoroethane (i.e., CCl2FCF3 or CFC-114a) for 1,1,1,2-tetrafluoroethane.
[042] 1,3,3,3-tetrafluoropropene (HFO-1234ze) can be prepared by dehydrofluorination of 1,1,1,2,3-pentafluoropropane (HFC-245eb, CF3CHFCH2F) or 1,1,1, 3,3-pentafluoropropane (HFC-245fa, CF3CH2CHF2). The dehydrofluorination reaction can occur in the vapor phase in the presence or absence of a catalyst, and also in the liquid phase, through the reaction with caustic soda, such as NaOH or KOH. These reactions are described in more detail in US patent publication 2006 / 0.106.263, incorporated herein by reference. HFO-1234ze can exist as one of two isomers of cis- or trans- configuration (also referred to as the E- and Z- isomers, respectively). Trans-HFO-1234ze is commercially available from certain fluorocarbon manufacturers (for example, Honeywell International Inc., Morristown, NJ). COMPOSITIONS
[043] Non-flammable refrigerant mixtures are described which essentially consist of (a) from 20% by weight to 25.5% by weight of HFO-1234yf, (b) from 20% by weight to 24.5% by weight of HFC-32, (c) from 24.5% by weight to 30 by weight of HFC-125 (d) from 25.5% by weight to 30% by weight of HFC-134a, and optionally (e) from about 0.0001% by weight to 10% by weight of HFO-1234ze.
[044] Also described are mixtures of non-flammable refrigerants that essentially consist of (a) from 20% by weight to 25.5% by weight of HFO-1234yf, (b) from 20% by weight to 24.5% in weight of HFC-32, (c) from 24.5% by weight to 30% by weight of HFC-125 (d) from 25.5% by weight to 30% by weight of HFC-134a, and (e) about 0.0001% by weight to 10% by weight of trans-HFO-1234ze.
[045] In another embodiment, mixtures of non-flammable refrigerants contain from about 0.0001% by weight to 5% by weight of HFO-1234ze. In another embodiment, non-flammable refrigerant mixtures contain from about 1% by weight to 10% by weight of HFO-1234ze. In yet another embodiment, non-flammable refrigerant mixtures contain from about 1% by weight to 5% by weight of trans-HFO-1234ze.
[046] In another embodiment, non-flammable refrigerant mixtures comprise (a) from 23% by weight to 25.5% by weight of HFO-1234yf, (b) from 22% by weight to 24.5% by weight HFC-32, (c) from 24.5% by weight to 27% by weight of HFC-125; (d) from 25.5% by weight to 28% by weight of HFC-134a; and (e) from about 0.0001% by weight to 5% by weight of trans-HFO-1234ze.
[047] In another embodiment, the non-flammable refrigerant mixtures are of the azeotrope type. In particular, the range of azeotrope-type soft drink mixes has been found to be those with from 20% by weight to 25.5% by weight of HFO-1234yf, from 20% by weight to 24.5% by weight of HFC-32, from 24.5% by weight to 30% by weight of HFC-125, and from 25.5% by weight to 30% by weight of HFC-134a. In addition, it was found that the soft drink mixes that also contain trans-HFO-1234ze are of the azeotrope type with from 20% by weight to 25.5% by weight of HFO-1234yf, from 20% in 24.5% by weight of HFC-32, from 24.5% by weight to 30% by weight of HFC-125, from 25.5% by weight to 30% by weight of HFC-134a and from about 0.0001% by weight to about 1% by weight of HFO-1234ze.
[048] In another embodiment, non-flammable refrigerant mixtures contain trans-HFO-1234ze from about 0.0001 to about 0.1% by weight.
[049] In another embodiment, the non-flammable refrigerant mixtures are of the azeotrope type and the trans-HFO-1234ze when present, is about 0.0001 to about 0.1% by weight.
[050] HFO-1234yf and mixtures containing HFO-1234yf are considered to be low GWP replacements for certain refrigerants and refrigerant mixtures that have relatively high GWP. In particular, R-404A (ASHRAE designation for a mixture containing 44% by weight of HFC-125, 52% by weight of HFC-143a (1,1,1-trifluoroethane), and 4% by weight of HFC- 134a) has a GWP of 3,922 and will need replacement. In addition, R-507 (ASHRAE designation for a mixture containing 50% by weight of HFC-125 and 50% by weight of HFC-143a), which has properties almost identical to R404A and can therefore be used in many R404A systems have a global warming potential of 3,985 and therefore do not provide a lower GWP replacement for the R404A, but will also need replacement.
[051] In some embodiments, in addition to tetrafluoropropene, difluoromethane, pentafluoroethane, tetrafluoroethane, the compositions described may comprise the optional non-refrigerant components.
[052] In one embodiment, a composition is provided that consists of (i) a non-flammable refrigerant component; and optionally (ii) a non-refrigerant component; wherein the refrigerant component is a non-flammable refrigerant mixture consisting essentially of (a) from 20% by weight to 25.5% by weight of HFO-1234yf, (b) from 20% by weight to 24.5% in weight of HFC-32, (c) from 24.5 weight% to 30% by weight of HFC-125 (d) from 25.5% by weight to 30% by weight of HFC-134a, and optionally (and ) of about 0.0001% by weight to 10% by weight of trans-HFO-1234z (e) of interest are compositions in which, when HFO-1234ze is present, it is at least about 90% of trans-HFO-1234ze, or 95% trans-HFO-1234ze. Also of interest are compositions in which the weight ratio of HFC-134a to HFO-1234yf is greater than 1: 1. Of particular interest are compositions in which HFO-1234yf is about 25% by weight of the composition and where HFC-134a is about 26% by weight of the composition.
[053] In some embodiments, the optional non-refrigerant components (also referred to herein as additives) in the compositions described herein may comprise one or more components selected from the group consisting of lubricants, dyes including dyes (UV), agents solubilization agents, compatibilizers, stabilizers, markers, perfluoropolyethers, anti-wear agents, extreme pressure agents, corrosion and oxidation inhibitors, metal surface energy reducers, metal surface deactivators, free radical scavengers, foam control agents, beneficiaries viscosity index, pour point depressants, detergents, viscosity regulators, and mixtures thereof. In fact, many of these optional non-refrigerant components fall into one or more of these categories and may have qualities that make it possible to achieve one or more performance characteristics.
[054] In some embodiments, one or more non-refrigerant components are present in small quantities in relation to the total composition. In some embodiments, the amount of the concentration of additive (s) in the described compositions is less than about 0.1% by weight to about 5% by weight of the total additive. In some embodiments of the present invention, additives are present in the described compositions in an amount from about 0.1% by weight to about 5% by weight of the total composition, or in an amount from about 0, 1% by weight to about 3.5% by weight. The component (s) of the selected additive (s) for the described composition is / are selected based on the utility and / or components of individual equipment or system requirements.
[055] In some embodiments, the lubricant is a mineral oil lubricant. In some embodiments, the mineral oil lubricant is selected from the group consisting of paraffins (including saturated linear carbon chain hydrocarbons, saturated branched carbon chain hydrocarbons, and mixtures thereof), naphthenes (including ring structures) and aromatic saturated cyclics) (those with unsaturated hydrocarbons containing one or more rings, where one or more ring is characterized by alternating carbon-carbon double bonds) and non-hydrocarbons (these molecules containing sulfur atoms, such as, nitrogen, oxygen and their mixtures), and their mixtures and combinations.
[056] Some designs may contain one or more synthetic lubricants. In some embodiments, the synthetic lubricant is selected from the group consisting of aromatics substituted by alkyl (such as benzene or naphthalene substituted by linear, branched or linear and branched mixtures, often generically referred to as alkylbenzenes), synthetic paraffins and naphthenes, poly (alpha-olefins), polyglycols (including polyalkylene glycols), dibasic acid esters, polyesters, polyol esters, neopentyl esters, polyvinyl ethers (PVEs), perfluoropolyether silicones (PFPEs), silic esters, esters fluorinated compounds, phosphate esters, polycarbonates and mixtures thereof, that is, mixtures of any of the lubricants described in this paragraph.
[057] Lubricants, as described herein, may be commercially available lubricants. For example, the lubricant may be a paraffinic mineral oil, marketed by BVA Oils as BVM 100 N, naphthenic mineral oils marketed by Crompton Co. under the trademarks Suniso® 1GS, Suniso® 3GS and Suniso® 5GS; naphthenic mineral oil marketed by Pennzoil under the trademark Sontex® 372LT; naphthenic mineral oil marketed by Calumet Lubricants under the trademark Calumet® RO-30; linear alkylbenzenes marketed by Shrieve Chemicals under the trademarks Zerol® 75, Zerol® 150 and Zerol® 500; and branched alkylbenzene marketed by Nippon Oil such as HAB 22; polyol esters (POEs) marketed under the trademark Castrol® 100 by Castrol; polyalkylene glycols (PAGs), such as Dow Chmical's RL-488A; perfluoropolyethers (PFPEs) marketed under the trademark Krytox® by E.I. du Pont de Nemours; marketed under the trademark Fomblin® by Ausimont; or marketed under the trademark Demnum by Daikin Industries; and their mixtures, that is, mixtures of any of the lubricants described in this paragraph.
[058] The lubricants used in the present invention can be designed to be used with hydrofluorocarbon refrigerants and can be miscible with the compositions as described in the present and, under operating conditions of the compression refrigeration and air conditioning equipment. In some embodiments, lubricants are selected, considering the requirements of a particular compressor and the environment in which the lubricant will be exposed.
[059] In the compositions of the present invention including a lubricant, the lubricant is present in an amount of less than 5.0% by weight of the total composition. In other embodiments, the amount of lubricant is between about 0.1 and 3.5% by weight of the total composition.
[060] Notwithstanding the weight ratios mentioned above for the compositions described in the present, it is understood that in some heat transfer systems, while the composition is being used, it can acquire an additional lubricant from one or more components of the equipment of such a heat transfer system. For example, in some refrigeration, air conditioning and heat pump systems, lubricants can be loaded in the compressor and / or in the compressor's lubricant reservoir. This lubricant would be in addition to any lubricant additives present in the refrigerant in such a system. In use, the refrigerant composition when in the compressor can select a quantity of lubricant from the equipment to change the refrigerant-lubricant composition from the starting ratio.
[061] In such heat transfer systems, even when most of the lubricant is found inside the compressor portion of the system, the entire system can contain a total composition, with as much as about 75% by weight at as little as about 1.0% by weight of the composition being lubricant. In some systems, for example, refrigerated supermarket displays, the system can contain about 3% by weight of the lubricant (above any lubricant present in the refrigerant composition before loading the system) and 97% by weight of refrigerant.
[062] The non-refrigerant component used with the compositions of the present invention can include at least one dye. The dye can be at least an ultraviolet (UV) dye. The UV dye can be a fluorescent dye. The fluorescent dye can be selected from the group consisting of naphthalimides, perylenes, coumarins, anthracenes, phenanthracenes, xanthines, thioxanthenes, naphthoxanthenes, fluoresceins and derivatives of such dyes and their combinations, that is, mixtures of any of the above or its derivatives described in this paragraph.
[063] In some embodiments, the described compositions contain from about 0.001% by weight to about 1.0% by weight of UV dye. In other embodiments, the UV dye is present in an amount of about 0.005% by weight to about 0.5% by weight; and in other embodiments, the UV dye is present in an amount of 0.01% by weight to about 0.25% by weight of the total composition.
[064] The UV dye is a useful component for detecting leaks in the composition, allowing to observe the fluorescence of the dye, or in the vicinity of a leak point in an apparatus (for example, the refrigeration unit, air conditioning or heat pump) heating). You can observe the emission of UV, for example, the fluorescence of the dye under an ultraviolet light. Therefore, if a composition containing a UV dye is leaking from a certain point in an apparatus, fluorescence can be detected at or near the leak point.
[065] Another non-refrigerant component, which can be used with the compositions of the present invention can include at least one solubilizing agent selected to enhance the solubility of one or more of the dye in the described compositions. In some embodiments, the weight ratio of the dye to the solubilizing agent ranges from about 99: 1 to about 1: 1. Solubilizing agents include at least one compound selected from the group consisting of hydrocarbons, hydrocarbon ethers, polyoxyalkylene glycol ethers (such as dipropylene glycol dimethyl ether), amides, nitriles, ketones, chlorocarbons (such as chloride methylene, trichlorethylene, chloroform or mixtures thereof), esters, lactones, aromatic ethers, fluoroethers and 1,1,1-trifluoroalkanes and mixtures thereof, that is, mixtures of any of the solubilizing agents described in this paragraph.
[066] In some embodiments, the non-refrigerant component comprises at least one compatibilizer to improve the compatibility of one or more lubricants, with the described compositions. The compatibilizer can be selected from the group consisting of hydrocarbons, hydrocarbon ethers, polyoxyalkylene glycol ethers (such as dipropylene glycol dimethyl ether), amides, nitriles, ketones, chlorocarbons (such as methylene chloride, trichlorethylene, chloroform or mixtures thereof), esters, lactones, aromatic ethers, fluoroethers, 1,1,1-trifluoroalkanes, and mixtures thereof, that is, mixtures of any of the compatibilizers described in this paragraph.
[067] The solubilizing and / or compatibilizing agent can be selected from the group consisting of hydrocarbon ethers consisting of ethers that only contain carbon, hydrogen and oxygen, such as dimethyl ether (DME) and mixtures thereof, that is, mixtures of any of the hydrocarbon ethers described in this paragraph.
[068] The compatibilizer can be a linear or cyclic, aliphatic or aromatic hydrocarbon compatibilizer, containing from 6 to 15 carbon atoms. The compatibilizer can be at least one hydrocarbon, which can be selected from the group consisting of at least hexanes, octanes, nonanes, and deans, among others. Commercially available hydrocarbon compatibilizers include, but are not limited to, Exxon Chemical (USA) under the trademark Isopar®, a mixture of -undecanoic (C11) and dodecane (C12), (a high purity isoparaffin C11 to C12), Aromatic 150 (a C9 to C11 aromatic), Aromatic 200 (a C9 to C15 aromatic) and Naphta 140 (a mixture of C5 to C11 paraffins, naphthenes and aromatic hydrocarbons) and their mixtures, that is, mixtures of any of the hydrocarbons described in this paragraph.
[069] The compatibilizer may alternatively be at least a polymeric compatibilizer. The polymeric compatibilizer can be a random copolymer of fluorinated and non-fluorinated acrylates, in which the polymer comprises the units of at least one monomer represented by the Formula CH2 = C (R1) CO2R2, CH2 = C (R3) C6H4R4, and CH2 = C (R5) C6H4XR6, where X is oxygen or sulfur; R1, R3, and R5 are independently selected from the group consisting of H and C1-C4 alkyl radicals; and R2, R4 and R6 are independently selected from the group consisting of carbon-based radicals containing C and F, and may also contain an H, Cl, oxygen ether, or sulfur, in the form of groups of thioether, sulfoxide or sulfone and mixtures thereof. Examples of such polymeric compatibilizers include those commercially available from E.I. du Pont de Nemours and Company, under the trademark Zonyl® PHS. Zonyl® PHS is a random copolymer produced using 40% by weight CH2 = C (CH3) CO2CH2CH2 (CF2CF2) mF (also referred to as Zonyl® fluoromethacrylate or ZML) where m is 1 to 12, preferably 2 to 8, and 60% by weight of lauryl methacrylate (CH2 = C (CH3) CO2 (CH2) 11CH3, also referred to as LMA).
[070] In some embodiments, the compatibilizing component contains from about 0.01 to 30% by weight (based on the total amount of the compatibilizer) of an additive that reduces the surface energy of metallic copper, aluminum, steel or other metals and their metal alloys found in heat exchangers in a way that reduces the adhesion of lubricants to the metal. Examples of energy-reducing additives for metal surfaces include those commercially available from DuPont under the trademarks Zonyl® FSA Zonyl FSP®, and Zonil® FSJ.
[071] Another non-refrigerant component, which can be used with the compositions of the present invention can be a metal surface deactivator. The metal surface deactivator is selected from the group consisting of areoxalyl bis (benzylidene) hydrazide (CAS reg. No. 6629-10-3), N, N'-bis (3,5-di-tert-butyl-4 -hydroxyhydrocinamoyl hydrazine (CAS reg. No. 32687-78-8), 2,2'-oxamidobis-ethyl- (3,5-di-tert-butyl-4-hydroxyhydrocinamate (CAS reg. 70331-94-1) , N, N '- (disalicyclidene) -1,2-diaminopropane (CAS reg. No. 94-91-7) and ethylene diaminetetraacetic acid (CAS reg. 60-00-4) and their salts and mixtures, that is, mixtures of any of the metal surface deactivators described in this paragraph.
[072] The non-refrigerant component used with the compositions of the present invention may alternatively be a stabilizer selected from the group consisting of hindered phenols, thiophosphates, butylated triphenylphosphorothionates, organo phosphates, or phosphites, aryl alkyl ethers, terpenes , terpenoids, epoxides, fluorinated epoxides, oxetanes, ascorbic acid, thiols, lactones, thioethers, amines, nitromethane, alkylsilanes, benzophenone derivatives, aryl sulfides, divinyl terephthalic acid, diphenyl terephthalic acid, ionic liquids and mixtures thereof, that is, mixtures of any of the stabilizers described in this paragraph.
[073] The stabilizer can be selected from the group consisting of tocopherol; hydroquinone; t-butylhydroquinone; monothiophosphates; and dithiophosphates, commercially available from Ciba Specialty Chemicals, hereinafter “Ciba”, under the brand Irgalube® 63; dialkylthiophosphate esters, commercially available from Ciba under the brands Irgalube® 353 and Irgalube® 350, respectively; butylated triphenylphosphorothionates, commercially available from Ciba under the trade name Irgalube® 232; amine phosphates, commercially available from Ciba under the brand name Irgalube® 349 (Ciba); hindered phosphites, commercially available from Ciba Irgalube® 349 (Ciba); hindered phosphites, commercially available from Ciba as Irgafos® 168 and tris- (di-tert-butylphenyl) phosphite, commercially available from Ciba under the trademark Irgafos® OPH; (di-n-octyl phosphite); and diphenyl iso-decyl phosphite, commercially available from Ciba under the trademark Irgafos® DDPP; trialkyl phosphates, such as trimethyl phosphate, triethyl phosphate, tributyl phosphate, trioctyl phosphate, and tri (2-ethylhexyl) phosphate; triaryl phosphates including triphenyl phosphate, tricresyl phosphate and trixylenyl phosphate; and mixed alkyl-aryl phosphates including isopropylphenyl phosphate (IPPP) and bis (t-butylphenyl) phenia (TBPP) phosphate; butylated triphenyl phosphates, such as those commercially available under the brand name Syn-O-Ad®, including Syn-O-Ad® 8784; tert-butyl triphenyl phosphates, such as those commercially available under the trademark Durad® 620; isopropylated triphenyl phosphates, such as those commercially available under the brand name Durad 220® and Durad® 110; anisole; 1,4-dimethoxybenzene; 1,4-diethoxybenzene; 1,3,5-trimethoxybenzene; mircene, allocimene, limonene (in particular, d-limonene); retinal; pinene; menthol, geraniol, farnesol, phytol, vitamin A; terpinene; delta-3-carene, terpinolene; felandrene; fenchene; dipentene; carotenoids, such as lycopene, beta carotene, and xanthophylls, such as zeaxanthin; retinoids, such as hepaxanthin and isotretinoin; bornane; 1,2-propylene oxide; 1,2-butylene oxide, n-butyl glycidyl ether; trifluoromethyloxirane; 1,1-bis (trifluoromethyl) oxirane; 3-ethyl-3-hydroxymethyl-oxetane, such as OXT-101 (Toagosei Co., Ltd), 3-ethyl-3 - ((phenoxy) methyl) -oxetane, such as OXT-211 (Toagosei Co., Ltd), 3-ethyl-3 - ((2-ethylhexyloxy) methyl) -oxetane, such as OXT-212 (Toagosei Co., Ltd); Ascorbic acid; methanethiol (methylmercaptan); ethanethiol (ethyl mercaptan); Coenzyme A, dimercaptosuccinic acid (DMSA); grapefruit mercaptan ((R) -2- (4-methyl-cyclohex-3-enyl) propane-2-thiol)); cysteine ((R) -2-amino-3-sulfanyl-propanoic acid); lipoamide (1,2-dithiolane-3-pentanamide); 5,7-bis (1,1-dimethylethyl) -3- [2,3 (or 3,4) -dimethylphenyl] -2 (3H) - benzofuranone, commercially available from Ciba under the brand name Irganox® HP-136; benzyl sulfyl phenyl; diphenyl sulfide; diisopropylamine; 3,3'-thiodipropionate dioctadecyl, commercially available from Ciba under the trademark Irganox® PS 802 (Ciba); didodecyl 3,3'-thiopropionate, commercially available from Ciba under the trademark Irganox® PS 800; di- (2,2,6,6-tetramethyl-4-piperidyl), commercially available from Ciba under the trademark Tinuvin® 770; poly- (N-hydroxyethyl-2,2,6,6-tetramethyl-4-hydroxy-piperidyl succinate, commercially available from under the trade name Tinuvin 622LD® (Ciba); methyl tallow bis amine; bis tallow amine; phenol-alpha -naftilamine; bis (dimethylamino) methylsilane (DMAMS); tris (trimethylsilyl) silane (TTMSS); vinyltriethoxysilane; vinyltrimethoxysilane; 2,5-difluorobenzophenone; 2 ', 5'-dihydroxyacetophenone; 2-aminobenzophenone; 2-aminobenzophenone; 2-aminobenzophenone; 2-aminobenzophenone; benzyl; diphenyl sulfide; dibenzyl sulfide; ionic liquids, and their mixtures and combinations.
[074] The additive used with the compositions of the present invention may, alternatively, be an ionic liquid stabilizer. The ionic liquid stabilizer can be selected from the group consisting of organic salts that are liquid at room temperature (about 25 ° C), the salts that contain the cations selected from the group consisting of pyridinium, pyridazinium, pyrimidinium , pyrazinium, imidazolium, pyrazolium, thiazolium, oxazolium and triazolium and their mixtures; and the anions selected from the group consisting of [BF4] -, [PF6] -, [SbF6] -, [CF3SO3] -, [HCF2CF2SO3] -, [CF3HFCCF2SO3] -, [HCClFCF2SO3] -, [(CF3SO2) 2N] -, [(CF3CF2SO2) 2N] -, [(CF3SO2) 3C] -, [CF3CO2] -, and F- and mixtures thereof. In some embodiments, liquid ionic stabilizers are selected from the group consisting of emim BF4 (1-ethyl-3-methylimidazolium tetrafluoroborate); bmim BF4 (1-butyl-3-methylimidazolium tetraborate); emim PF6 (1-ethyl-3-methylimidazolium hexafluorophosphate); and bmim PF6 (1-butyl-3-methylimidazolium hexafluorophosphate), all are available from Fluka (Sigma-Aldrich).
[075] In some embodiments, the stabilizer may be a hindered phenol, which is a substituted phenol compound, including phenols comprising one or more substituted or cyclic, straight-chain or branched aliphatic substituent groups, such as alkylated monophenols including 2,6-di-tert-butyl-4-methylphenol; 2,6-di-tert-butyl-4-ethylphenols; 2,4-dimethyl-6-tert-butylphenol; tocopherol; and the like, hydroquinone and alkylated hydroquinones including t-butylhydroquinone, other hydroquinone derivatives; and the like, hydroxylated thiodiphenyl ethers, including 4,4'-thio-bis (2-methyl-6-tert-butylphenol); 4,4'-thiobis (3-methyl-6-tert-butylphenol); 2,2'-thiobis (4-methyl-6-tert-butylphenol), and the like, alkylidene-bisphenols including: 4,4'-methylenebis (2,6-di-tert-butylphenol), 4,4'-bis (2,6-di-tert-butylphenol), 2,2'- or 4,4-biphenoldiole derivatives; 2,2'-methylenebis (4-ethyl-6-tert-butylphenol), 2,2'-methylenobis (4-methyl-tert-butylphenol-6); 4,4-butylidenobis (3-methyl-6-tert-butylphenol); 4,4-isopropylidenobis (2,6-di-tert-butylphenol), 2,2'-methylenebis (4-methyl-6-nonylphenol); 2,2'-isobutylidenobis (4,6-dimethylphenol; 2,2'-methylenebis (4-methyl-6-cyclohexylphenol, 2,2- or 4,4-biphenyldiols including 2,2'-methylenebis (4 -ethyl-6-tert-butylphenol), butylated hydroxytoluene (BHT, or 2,6-di-tert-butyl-4-methylphenol), bisphenols comprising heteroatoms, including 2,6-di-tert-alpha-dimethylamino- p-cresol, 4,4-thiobis (6-tert-butyl-m-cresol); and the like; acylaminophenols; 2,6-di-tert-butyl-4 (N, N'-dimethylaminomethylphenol), including sulfides; bis (3-methyl-4-hydroxy-5-tert-butyl) sulfide, bis (3,5-di-tert-butyl-4-hydroxybenzyl) sulfide and mixtures thereof, that is, mixtures of any of the phenols described in this paragraph.
[076] The non-refrigerant component, which is used with the compositions of the present invention can alternatively be a marker. The marker can be two or more marker compounds from the same class of compounds or from different classes of compounds. In some embodiments, the marker is present in the compositions at a total concentration of about 50 parts per million by weight (ppm) to about 1,000 ppm, based on the weight of the total composition. In other embodiments, the marker is present in a total concentration of about 50 ppm to about 500 ppm. Alternatively, the marker is present in a total concentration of about 100 ppm to about 300 ppm.
[077] The marker can be selected from the group consisting of hydrofluorocarbons (HFCs), deuterated hydrofluorocarbons, perfluorocarbons, fluoroethers, brominated compounds, iodinated compounds, alcohols, aldehydes and ketones, nitrous oxide and their combinations. Alternatively, the marker can be selected from the group consisting of fluoroethane, 1,1, -difluoroethane, 1,1,1-trifluoroethane, 1,1,1,3,3,3-hexafluoropropane, 1.1 , 1,2,3,3,3-heptafluoropropane, 1,1,1,3,3-pentafluoropropane, 1,1,1,3,3-pentafluorobutane, 1,1,1,2,3,4,4 , 5,5,5- decafluoropentane, 1,1,1,2,2,3,4,5,5,6,6,7,7,7-tridecafluoroeptane, iodotrifluoromethane, deuterated hydrocarbons, deuterated hydrofluorocarbons, perfluorocarbons, fluoroethers , brominated compounds, iodinated compounds, alcohols, aldehydes, ketones, nitrous oxide (N2O) and their mixtures. In some embodiments, the marker is a mixture that contains two or more hydrofluorocarbons, or a hydrofluorocarbon in combination with one or more perfluorocarbons.
[078] The marker can be added to the compositions of the present invention in pre-determined amounts to allow the detection of any dilution, contamination or other alteration of the composition.
[079] The additive, which can be used with the compositions of the present invention, may alternatively be a perfluoropolyether, as described in detail in US patent 2007/0284555, incorporated herein by reference.
[080] It will be recognized that some of the additives mentioned above as being suitable for the non-refrigerant component have been identified as potential refrigerants. However, according to the present invention, when these additives are used, they are not present in an amount that would affect the innovative and basic characteristics of the refrigerant mixtures of the present invention. Preferably, the mixtures of non-flammable refrigerants and the compositions of the present invention that contain them, do not contain an amount greater than about 0.5% by weight of refrigerants other than HFO-1234yf, HFC-32, HFC-125, HFC-134a,, and when HFO-1234ze is present.
[081] In one embodiment, the compositions described herein can be prepared by any convenient method for combining the desired amounts of the individual components. A preferred method is to weigh the desired amounts of components and then combine the components in a suitable container. Stirring can be used, if desired.
[082] The compositions of the present invention have zero ozone depletion potential and low global warming potential (GWP). In addition, the compositions of the present invention will have global warming potentials that are lower than many hydrofluorocarbon refrigerants currently in use. One aspect of the present invention is to provide a refrigerant with a global warming potential of less than 1,000, less than 700, less than 500, less than 400, less than 300, less than 150, less than 100, or less than 50. EQUIPMENT, METHODS AND PROCESSES OF USE
[083] The compositions described herein are useful as heat transfer or refrigerant compositions.
[084] Steam compression refrigeration systems include an evaporator, a compressor, a condenser, and an expansion device. A refrigeration cycle reuses the refrigerant in several stages, producing a cooling effect in one stage and a heating effect in a different stage. The cycle can be described simply as follows. The liquid refrigerant enters an evaporator through an expansion device, and the liquid refrigerant boils in the evaporator, removing heat from the environment, at a low temperature to form a gas and produce the cooling. Often, air or a heat transfer fluid flows over or around the evaporator to transfer the cooling effect caused by the evaporation of the refrigerant in the evaporator to a body to be cooled. Low pressure gas enters the compressor, where the gas is compressed to increase its pressure and temperature. The high-pressure gaseous refrigerant (compressed) then enters the condenser in which the refrigerant condenses and discharges its heat into the environment. The refrigerant returns to the expansion device through which the liquid expands from the high pressure level in the condenser to the low pressure level in the evaporator, therefore repeating the cycle.
[085] In one embodiment, there is described in the present a process for the production of refrigeration which comprises condensing a mixture of refrigerant, as described in the present, and then evaporating said composition in the vicinity of a body to be cooled.
[086] A body to be cooled can be defined as any space, place, object or body from which it is desired to be cooled. Examples include spaces (open or closed) that require refrigeration or cooling, such as a refrigerator or freezer in a supermarket.
[087] By proximity it is understood that the evaporator of the system containing the refrigerant mixture is located inside or adjacent to the body to be cooled, in such a way that the movement of air over the evaporator moves into or around the body to be cooled.
[088] Non-flammable refrigerant mixtures useful in the process for the production of cooling essentially consist of (a) 20 wt% to 25.5 wt% HFO-1234yf, (b) 20 wt% to 24 , 5 wt% HFC-32, (c) 24.5 wt% to 30 wt% HFC-125 (d) 25.5 wt% to 30 wt% HFC-134a, and optionally (e) from about 0.0001% by weight to 10% by weight of HFO-1234ze.
[089] In another embodiment, non-flammable refrigerant mixtures useful in the process for the production of cooling essentially consist of (a) 20% by weight to 25.5% by weight of HFO-1234yf, (b) 20 % by weight to 24.5% by weight of HFC-32, (c) 24.5% by weight to 30% by weight of HFC-125 (d) from 25.5% by weight to 30% by weight of HFC-134a, and (e) from about 0.0001% by weight to 10% by weight of trans-HFO-1234ze.
[090] In another embodiment, non-flammable refrigerant mixtures useful in the process for the production of refrigeration contain from about 0.0001% by weight to 5% by weight of HFO-1234ze. In another embodiment, non-flammable refrigerant mixtures contain from about 1% by weight to 10% by weight of HFO-1234ze. In yet another embodiment, non-flammable refrigerant mixtures contain from about 1% by weight to 5% by weight of trans-HFO-1234ze.
[091] In another embodiment, non-flammable refrigerant mixtures useful in the process for the production of refrigeration comprise (a) from 23% by weight to 25.5% by weight of HFO-1234yf, (b) from 22% in weight at 24.5% by weight of HFC-32, (c) from 24.5% by weight at 27% by weight of HFC-125; (d) from 25.5% by weight to 28% by weight of HFC-134a; and (e) from about 0.0001% by weight to 5% by weight of trans-HFO-1234ze.
[092] In another embodiment, the mixtures of non-flammable refrigerants useful in the process for the production of cooling are of the azeotrope type. In particular, the range of azeotrope-type soft drink mixes has been found to be from 20 wt% to 25.5 wt% HFO-1234yf, from 20 wt% to 24.5 wt% weight of HFC-32, from 24.5% by weight to 30% by weight of HFC-125, and from 25.5% by weight to 30% by weight of HFC-134a. In addition, it was found that the soft drink mixes that also contain trans-HFO-1234ze are of the azeotrope type with from 20% by weight to 25.5% by weight of HFO-1234yf, from 20% in 24.5% by weight of HFC-32, from 24.5% by weight to 30 by weight of HFC-125, from 25.5% by weight to 30% by weight of HFC-134a and from about 0.0001% by weight to about 1% by weight of HFO-1234ze.
[093] In another embodiment, non-flammable refrigerant mixtures useful in the process for the production of refrigeration contain trans-HFO-1234ze from about 0.0001 to about 0.1% by weight.
[094] In another embodiment, the mixtures of non-flammable refrigerants useful in the process for the production of cooling are of the azeotrope type and the trans-HFO-1234ze, when present, is from about 0.0001 to about 0.1 % by weight.
[095] In some embodiments, refrigerant mixtures, as described in the present, can be useful, especially in refrigeration applications including medium or low refrigeration temperature. Medium temperature refrigeration systems include refrigerated supermarket and convenience store spaces for drinks, dairy products, fresh food transport and other items that need refrigeration. Low temperature refrigeration systems include the refrigerated cabinet and shelf in supermarkets and convenience stores, ice machines and the transport of frozen foods. Other specific uses may be commercial, industrial or residential refrigerators and freezers, ice machines, independent refrigerators and freezers, supermarket distributed systems and shelves, commercial refrigerators and freezers and refrigerated cabinets, and combined systems. Of particular interest are the low temperature refrigeration systems that contain the compositions of the present invention.
[096] In addition, in some embodiments, the described compositions can function as primary refrigerants in secondary cycle systems responsible for cooling to remote locations through the use of a secondary heat transfer fluid, which can comprise water, a glycol, a carbon dioxide, or a fluorinated hydrocarbon fluid. In this case, the secondary heat transfer fluid is the body to be cooled as it is adjacent to the evaporator and is cooled before moving to a remote body to be cooled.
[097] The compositions described herein may be useful as substitutes for low GWP (global warming potential) for the currently used refrigerants, including R404A (ASHRAE designation for a mixture of 44% by weight of R125, 52% by weight of R143a (1,1,1-trifluoroethane), and 4.0% by weight of R134a) and R507 (ASHRAE designation for a mixture of 50% by weight of R125 and 50% by weight of R143a).
[098] Substitute refrigerants are often more useful if they are capable of being used in original refrigeration equipment designed for a different refrigerant. In addition, the compositions, as described in the present, may be useful as substitutes for the R404A or R507 in equipment designed for the R404A or R507, with some modifications to the system. In addition, the compositions, as described herein, comprising HFO-1234yf, HFC-32, HFC-125, HFC-134a, and, optionally, HFO-1234ze can be useful as replacements for R404a or R507 in equipment specifically modified or designed entirely by these new compositions comprising HFO-1234yf, HFC-32, HFC-125, HFC-134a, and, optionally, HFO-1234ze.
[099] In many applications, some embodiments, the compositions described are useful as refrigerants and provide at least comparable cooling performance (meaning cooling capacity and energy efficiency), as the refrigerant for which a substitute is being wanted.
[0100] In another embodiment, a method is provided for replacing a refrigerant selected from the group consisting of R-404A and R-507. The method comprises charging a refrigeration apparatus with a refrigerant mixture comprising HFO-1234yf, HFC-32, HFC-125, HFC-134a, and, optionally, HFO-1234ze, as described herein. In one embodiment, the refrigeration apparatus is suitable for use with the R-404A and / or R-507. In another embodiment, the apparatus includes refrigeration systems with evaporation temperatures in the range from about 40 ° C to about 0 ° (c) of interest are the embodiments in which the apparatus includes refrigeration systems with temperatures evaporation in the range from about 40 ° C to about 20 ° C. Also of interest are the embodiments in which the appliance includes cooling systems with evaporation temperatures in the range from about 20 ° C to about 0 ° C
[0101] Non-flammable refrigerant mixtures, useful in the method of replacing a refrigerant essentially consist of (a) 20% by weight to 25.5% by weight of HFO-1234yf, (b) 20% by weight to 24.5% by weight of HFC-32, (c) 24.5% by weight to 30% by weight of HFC-125 (d) 25.5% by weight to 30% by weight of HFC-134a, and, optionally, (e) from about 0.0001% by weight to 10% by weight of HFO-1234ze.
[0102] In another embodiment, non-flammable refrigerant mixtures useful in the refrigerant replacement method essentially consist of (a) 20 wt% to 25.5 wt% HFO-1234yf, (b) 20 % by weight to 24.5% by weight of HFC-32, (c) 24.5% by weight to 30% by weight of HFC-125 (d) from 25.5% by weight to 30% by weight of HFC-134a, and (e) from about 0.0001% by weight to 10% by weight of trans-HFO-1234ze.
[0103] In another embodiment, mixtures of non-flammable refrigerants useful in the method of replacing a refrigerant contain from about 0.0001% by weight to 5% by weight of HFO-1234ze. In another embodiment, non-flammable refrigerant mixtures contain from about 1% by weight to 10% by weight of HFO-1234ze. In yet another embodiment, non-flammable refrigerant mixtures contain from about 1% by weight to 5% by weight of trans-HFO-1234ze.
[0104] In another embodiment, mixtures of non-flammable refrigerants useful in the method of replacing a refrigerant comprise (a) from 23% by weight to 25.5% by weight of HFO-1234yf, (b) from 22% in weight at 24.5% by weight of HFC-32, (c) from 24.5% by weight at 27% by weight of HFC-125; (D) from 25.5% by weight to 28% by weight of HFC-134a; and (e) from about 0.0001% by weight to 5% by weight of trans-HFO-1234ze.
[0105] In another embodiment, the mixtures of non-flammable refrigerants useful in the method of replacing a refrigerant are of the azeotrope type. In particular, the range of azeotrope-type soft drink mixes has been found to be those with from 20% by weight to 25.5% by weight of HFO-1234yf, from 20% by weight to 24.5% by weight of HFC-32, from 24.5% by weight to 30% by weight of HFC-125, and from 25.5% by weight to 30% by weight of HFC-134a. In addition, it was found that the soft drink mixes that also contain trans-HFO-1234ze are of the azeotrope type with from 20% by weight to 25.5% by weight of HFO-1234yf, from 20% in 24.5% by weight of HFC-32, from 24.5% by weight to 30 by weight of HFC-125, from 25.5% by weight to 30% by weight of HFC-134a and from about 0.0001% by weight to about 1% by weight of HFO-1234ze.
[0106] In another embodiment, non-flammable refrigerant mixtures useful in a refrigerant replacement method contain trans-HFO-1234ze from about 0.0001 to about 0.1% by weight.
[0107] In another embodiment, the mixtures of non-flammable refrigerants useful in the method of replacing a refrigerant are of the azeotrope type and the trans-HFO-1234ze, when present, is from about 0.0001 to about 0 , 1% by weight.
[0108] In another embodiment, a method is provided to recharge a heat transfer system that contains a refrigerant to be replaced and a lubricant, said method comprises removing the refrigerant to be replaced from the heat transfer system, maintaining a substantial portion of the lubricant in said system and introducing one of the compositions described herein into the heat transfer system.
[0109] In another embodiment, a heat exchange system is provided, comprising a composition described in the present, in which said system is selected from the group consisting of freezers, refrigerators, commercial refrigerators, freezer systems or freezers. supermarket refrigeration, mobile refrigerators, and systems that have their combinations.
[0110] In one embodiment, a heat transfer system is provided that contains a composition as described herein. In another embodiment, a refrigeration apparatus is described, which contains a composition as described herein. In another embodiment, a refrigeration apparatus is described, which contains a composition as described herein. In a particular embodiment, a medium temperature refrigeration apparatus, which contains the composition of the present invention, is described. In another particular embodiment, a low temperature refrigeration apparatus is described, which contains the composition of the present invention. The device typically includes an evaporator, a compressor, a condenser, and an expansion device.
[0111] In yet another embodiment, a mobile refrigeration apparatus is described which contains a composition as described herein.
[0112] Non-flammable refrigerant mixtures useful in heat exchange systems, heat transfer systems or refrigeration appliances essentially consist of (a) 20% by weight to 25.5% by weight of HFO-1234yf, ( b) from 20% by weight to 24.5% by weight of HFC-32, (c) from 24.5% by weight to 30% by weight of HFC-125 (d) from 25.5% by weight to 30 % by weight of HFC-134a, and optionally (e) from about 0.0001% by weight to 10% by weight of HFO-1234ze.
[0113] In another embodiment, mixtures of non-flammable refrigerants useful in heat exchange systems, heat transfer systems or refrigeration appliances essentially consist of (a) from 20% by weight to 25.5% by weight of HFO-1234yf, (b) 20 wt% to 24.5 wt HFC-32, (c) 24.5 wt% to 30 wt% HFC-125 (d) 25.5 wt% weight at 30% by weight of HFC-134a, and (e) from about 0.0001% by weight to 10% by weight of trans-HFO-1234ze.
[0114] In another embodiment, non-flammable refrigerant mixtures useful in heat exchange systems, heat transfer systems or refrigeration appliances contain from about 0.0001% by weight to 5% by weight of HFO -1234ze. In another embodiment, non-flammable refrigerant mixtures contain from about 1% by weight to 10% by weight of HFO-1234ze. In yet another embodiment, non-flammable refrigerant mixtures contain from about 1% by weight to 5% by weight of trans-HFO-1234ze.
[0115] In another embodiment, non-flammable refrigerant mixtures useful in heat exchange systems, heat transfer systems or refrigeration appliances comprise (a) from 23% by weight to 25.5% by weight of HFO- 1234yf, (b) from 22% by weight to 24.5% by weight of HFC-32, (c) from 24.5% by weight to 27% by weight of HFC-125; (D) from 25.5% by weight to 28% by weight of HFC-134a; and (e) from about 0.0001% by weight to 5% by weight of trans-HFO-1234ze.
[0116] In another embodiment, the mixtures of non-flammable refrigerants useful in heat exchange systems, heat transfer systems or refrigeration appliances are of the azeotrope type. In particular, the range of azeotrope-type soft drink mixes has been found to be those with from 20% by weight to 25.5% by weight of HFO-1234yf, from 20% by weight to 24.5% by weight of HFC-32, from 24.5% by weight to 30% by weight of HFC-125, and from 25.5% by weight to 30% by weight of HFC-134a. In addition, refrigerant mixtures that also contain trans-HFO-1234ze have been found to be of the azeotrope type with from 20% by weight to 25.5% by weight of HFO-1234yf, from 20% by weight. 24.5% by weight of HFC-32, from 24.5% by weight to 30 by weight of HFC-125, from 25.5% by weight to 30% by weight of HFC-134a and from about 0.0001% by weight to about 1% by weight of HFO-1234ze.
[0117] In another embodiment, non-flammable refrigerant mixtures useful in heat exchange systems, heat transfer systems or refrigeration appliances contain the trans-HFO-1234ze from about 0.0001 to about 0 , 1% by weight.
[0118] In another embodiment, the mixtures of non-flammable refrigerants useful in heat exchange systems, heat transfer systems or refrigeration appliances are of the azeotrope type and the trans-HFO-1234ze, when present, is about 0.0001 to about 0.1% by weight. EXAMPLES
[0119] The concepts described herein will be described in the following examples, which do not limit the scope of the present invention described in the claims. EXAMPLE 1 IMPACT OF STEAM LEAK
[0120] A container is loaded up to 90% with an initial composition at the indicated temperature, and the initial vapor pressure of the composition is measured. The composition can leak from the container, while the temperature is kept constant, until 50% by weight of the initial composition is removed, at the moment the vapor pressure of the composition that remains in the container is measured. The changes in vapor pressure are listed in Table 1. TABLE 1


[0121] It was found that the compositions, as defined in the present invention, are of the azeotrope type, with modifications of less than 10% of the vapor pressure, after 50% of the composition has leaked. EXAMPLE 2 FLAMMABILITY
[0122] Flammable mixtures can be identified by testing under ASTM (American Society for Testing and Materials) E681-04, with an electronic ignition source. Such flammability tests were performed in refrigerant mixtures at 50% relative humidity.
[0123] To determine a flammability limit, the flammability of two refrigerant mixtures was determined in both liquid and gaseous phases at 36 ° C (10 degrees above the bubble point, as designated in ASHRAE Standard 34) for a container that it is 90% filled with liquid. The compositions contained HFO-1234yf / HFC-32 / HFC-125 / HFC-134a at the concentrations indicated in Table 2.

[0124] Clearly, compositions with an amount greater than about 24.5% by weight of HFC-32 and less than about 24.5% by weight of HFC-125 would be classified as flammable refrigerants. EXAMPLE 3 REFRIGERATION PERFORMANCE
[0125] Table 3 shows the performance of some exemplary compositions, compared to R-404A. In Table 3, Temp Evap is the evaporator temperature, Pres Evap is the evaporator pressure, Pres Cond is the condenser pressure, Temp Exit Compr is the compressor outlet temperature (sometimes also called the compressor discharge temperature), COP is the coefficient of performance (analogous to energy efficiency), and CAP is volumetric cooling capacity. The data is based on the following conditions. Condenser temperature40 ° C Amount of subcooling 10 K Compressor efficiency 75% TABLE 3


[0126] The results show the compositions of the present invention that exhibit the cooling capacity that is comparable with R-404a, which also demonstrates that these compositions may be suitable to adapt an existing R-404A system or be useful in new systems of cooling. The compositions also have a higher energy efficiency than R-404A. EXAMPLE 4 REFRIGERATION PERFORMANCE
[0127] Table 4 shows the performance of some exemplary compositions, compared to R404A and Comparative Examples (A) and (B). In Table 4, Pres Evap is evaporator pressure, Pres Cond is the condenser pressure, Temp Exit Compr is the compressor outlet temperature (sometimes also called the compressor discharge temperature), COP is the performance coefficient (analogous energy efficiency), and CAP is volumetric cooling capacity. The data is based on the following conditions. Evaporator temperature -10 ° C Return gas temperature 10 ° C Condenser temperature40 ° C Subcooling quantity 10 K Compressor efficiency75% TABLE 4


[0128] The results show that the compositions of the present invention provide an improved energy efficiency over R-404A. In addition, the compositions of the present invention provide the cooling capacity in only a small percentage than that for R-404A. It can be seen that Comparative Example (B) falls far short of the cooling capacity of the other compositions. Also note that Comparative Example (A), providing similar cooling performance, shows a higher compressor outlet temperature. Higher compressor temperatures are expected to shorten the life of the compressor, thereby increasing the cost of operating a system. SELECTED ACHIEVEMENTS
[0129] Realization A1. The non-flammable refrigerant mixture consisting essentially of: (a) from 20% by weight to 25.5% by weight of HFO-1234yf; (b) from 20% by weight to 24.5% by weight of HFC-32; (c) from 24.5% by weight to 30% by weight of HFC-125; (d) from 25.5% by weight to 30% by weight of HFC-134a; and optionally (e) from about 0.0001% by weight to about 10% by weight of trans-HFO-1234ze.
[130] Output A1a. The A1 non-flammable refrigerant mixture consisting essentially of: (a) from 20% by weight to 25.5% by weight of HFO-1234yf; (b) from 20% by weight to 24.5% by weight of HFC-32; (c) from 24.5% by weight to 30% by weight of HFC-125; (d) from 25.5% by weight to 30% by weight of HFC-134a; and (e) from about 0.0001% by weight to about 10% by weight of trans-HFO-1234ze.
[131] Output A2. The realization A1 non-flammable refrigerant mixture comprising: (a) 23% by weight, 25.5% by weight HFO-1234yf; (b) from 22% by weight to 24.5% by weight of HFC-32; (c) from 24.5% by weight to 27% by weight of HFC-125; and (d) from 25.5% by weight to 28% by weight of HFC-134a.
[0132] Realization A3. The non-flammable refrigerant mixture of any of the A1 or A2 Embodiments in which trans-HFO-1234ze is present.
[0133] Achievement A4. The non-flammable refrigerant mixture of any of the A1 or A2 designs where trans-HFO-1234ze is not present.
[0134] Accomplishment A5. The mixture of non-flammable refrigerant from any of A1 to A4, which is of the azeotrope type.
[0135] Achievement A6. The non-flammable refrigerant mixture of any of Embodiments A1 through A5, wherein trans-HFO-1234ze when present, is from about 0.0001 to about 5.0% by weight.
[0136] Accomplishment A7. The realization A6 non-flammable refrigerant mixture, which when used as a refrigerant in a refrigeration system with an evaporator temperature of -40 to about 0 ° C, has a capacity of approximately 10% of the capacity of R-404A, at the same temperature as the evaporator.
[0137] Accomplishment A8. The non-flammable refrigerant mix from Realization A7 which, when used as a refrigerant in a refrigeration system with an evaporator temperature of about -40 to -20 °, has a capacity of approximately 10% of the capacity of R-404A, at the same temperature as the evaporator C.
[0138] Accomplishment A9. The non-flammable refrigerant mixture of any of Embodiments A1 through A8 in which trans-HFO-1234ze when present, is from about 0.0001 to about 1.0% by weight.
[0139] Accomplishment A10. The non-flammable refrigerant mixture of any of embodiments A1 to A9 in which trans-HFO-1234ze when present, is from about 0.0001 to about 0.1% by weight.
[0140] Accomplishment A11. The non-flammable refrigerant mix from any of Embodiments A1 through A10, where HFO-1234ze when present, is from at least about 80% trans-HFO-1234ze.
[0141] Accomplishment A11a. The non-flammable refrigerant mixture from any of A1 to A10, where HFO-1234ze when present, is at least about 90% trans-HFO-1234ze.
[0142] Accomplishment A12. The non-flammable refrigerant mix from any of A1 to A11, where the weight ratio of HFC-134a to HFO-1234yf is greater than 1: 1.
[0143] Accomplishment A13. The non-flammable refrigerant mixture of any of A1 to A12, where HFO-1234yf is about 25% by weight of the refrigerant mixture, and where HFC-134a is about 26% by weight of the mixture of soda.
[0144] Accomplishment A14. The non-flammable refrigerant mix from any of A1 to A13, which contains an amount greater than about 0.5% by weight of refrigerants other than HFO-1234yf, HFC-32, HFC-125, HFC-134a and, when trans-HFO-1234ze is present.
[0145] Realization B1. A composition consisting of: (i) a non-flammable refrigerant component; and optionally (ii) a non-refrigerant component; wherein the refrigerant component is a mixture of non-flammable refrigerant of any of the embodiments A1 through A14.
[0146] Accomplishment B2. The composition of Realization B1, in which the non-refrigerant component is not present.
[0147] Realization B3. The composition of Realization B1, in which the non-refrigerant component is present.
[0148] Realization B4. The composition of any of the embodiments from B1 to B3, in which the non-refrigerant component, if present, is selected from the group consisting of lubricants, dyes including dyes (UV), solubilizing agents, compatibilizers, stabilizers, markers , perfluoropolyethers, anti-wear agents, extreme pressure agents, corrosion and oxidation inhibitors, metal surface energy reducers, metal surface deactivators, free radical scavengers, foam control agents, viscosity index improvers, spot depressants drains, detergents, viscosity regulators, and their mixtures.
[0149] Realization B4a. The composition of any of Achievements B1 to B4, in which the non-refrigerant component is a lubricant selected from the group consisting of mineral oil, aromatics substituted by alkyl, alkylbenzenes, synthetic paraffins and naphthenes, poly (alpha-olefins), polyglycols, polyalkylene glycols, dibasic acid esters, polyesters, polyol esters, neopentyl esters, polyvinyl ethers, perfluoropolyethers, silicones, silicate esters, fluorinated compounds, phosphate esters, polycarbonates and mixtures thereof.
[0150] Realization B5. The composition of any of Embodiments B1 to B4, which contains an amount greater than about 0.5% by weight of refrigerants other than HFO-1234yf, HFC-32, HFC-125, HFC-134a and, when present, the trans -HFO-1234ze
[0151] Realization C1. A process for the production of refrigeration which comprises the condensation of a refrigerant mixture from any of the A1 to A14 Embodiments and subsequently evaporating said refrigerant mixture in the vicinity of a body to be cooled.
[0152] Realization D1. A method for replacing a refrigerant selected from the group consisting of R-404A and R-507 which comprises charging a refrigeration appliance with a refrigerant mixture from any of Embodiments A1 through A14 or charging a composition of any of the Achievements from B1 to B4.
[0153] Accomplishment D2. A method of Embodiment D1, in which R-404A is replaced.
[0154] Accomplishment D3. A method of Realization D1, in which the R-507 is replaced.
[0155] Accomplishment E1. A refrigeration appliance that contains a mixture of refrigerant from any of Embodiments A1 through A14 or a composition from any Embodiment B1 through B4.

权利要求:
Claims (7)
[0001]
1. NON-FLAMMABLE REFRIGERANT MIXTURE, characterized by essentially consisting of: (a) from 23% by weight to 25.5% by weight of HFO-1234yf; (b) from 22% by weight to 24.5% by weight of HFC-32; (c) from 24.5% by weight to 27% by weight of HFC-125; (d) from 25.5% by weight to 28% by weight of HFC-134a; and (e) from 0.0001% by weight to 5% by weight of trans-HFO-1234ze.
[0002]
2. COMPOSITION, characterized by consisting of: (i) a non-flammable refrigerant component; and optionally (ii) a non-refrigerant component; wherein the refrigerant component is a mixture of non-flammable refrigerant as defined in claim 1.
[0003]
3. COMPOSITION, according to claim 2, characterized by the non-refrigerant component being present and selected from the group consisting of lubricants, dyes (including UV dyes), solubilizing agents, compatibilizers, stabilizers, markers, perfluoropolyethers, anti-wear agents, extreme pressure agents, corrosion and oxidation inhibitors, metal surface energy reducers, metal surface deactivators, free radical scavengers, foam control agents, viscosity index improvers, flow point depressants, detergents, viscosity regulators, and mixtures thereof.
[0004]
4. COMPOSITION according to claim 3, characterized in that the non-refrigerant component is a lubricant selected from the group consisting of mineral oil, aromatics substituted by alkyl, alkylbenzenes, synthetic paraffins and naphthenes, poly (alpha-olefins), polyglycols , polyalkylene glycols, dibasic acid esters, polyesters, polyol esters, neopentyl esters, polyvinyl ethers, perfluoropolyethers, silicones, silicate esters, fluorinated compounds, phosphate esters, polycarbonates and mixtures thereof.
[0005]
5. PROCESS TO PRODUCE REFRIGERATION, characterized by comprising the condensation of a refrigerant mixture, as defined in claim 1, and then evaporating said composition in the vicinity of a body to be cooled.
[0006]
6. METHOD FOR REPLACING A REFRIGERANT selected from the group consisting of R-404A and R-507, characterized by comprising charging a refrigeration appliance with a mixture of refrigerant, as defined in claim 1 or a composition, as defined in claim two.
[0007]
7. REFRIGERATION APPLIANCE, characterized in that it contains a mixture of refrigerant, as defined in claim 1, or a composition, as defined in claim 2.

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法律状态:
2018-03-27| B06F| Objections, documents and/or translations needed after an examination request according [chapter 6.6 patent gazette]|

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2019-08-27| B06U| Preliminary requirement: requests with searches performed by other patent offices: procedure suspended [chapter 6.21 patent gazette]|

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2021-01-12| B09A| Decision: intention to grant [chapter 9.1 patent gazette]|

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2021-02-09| B16A| Patent or certificate of addition of invention granted [chapter 16.1 patent gazette]|Free format text: PRAZO DE VALIDADE: 20 (VINTE) ANOS CONTADOS A PARTIR DE 12/02/2013, OBSERVADAS AS CONDICOES LEGAIS. |

优先权:

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申请号 | 申请日 | 专利标题

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US201261598120P| true| 2012-02-13|2012-02-13|

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US61/598,120|2012-02-13|

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PCT/US2013/025656|WO2013122892A1|2012-02-13|2013-02-12|Refrigerant mixtures comprising tetrafluoropropene, difluoromethane, pentafluoroethane, and tetrafluoroethane and uses thereof|

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