| 序号 | 专利名 | 申请号 | 申请日 | 公开（公告）号 | 公开（公告）日 | 发明人 |
|---|---|---|---|---|---|---|
| 61 | Air conditioner for preventing corrosion of evaporator | US09030586 | 1998-02-25 | US06182741B2 | 2001-02-06 | Keiichi Yoshii; Sadayuki Kamiya |
| An air conditioner includes a case accommodating an evaporator having a core portion and a lower tan disposed at a bottom of the core portion. The case has a recess portion disposed at an upstream air side of the evaporator, and a covering wall is formed to extend upwardly from the bottom of the recess portion to cover only the lower tank at an immediately upstream air side. When air passes through the evaporator, alien substances contained in air collide with the evaporator and fall to be deposited in the recess portion. Therefore, the deposition of the alien substances do not directly adhere to the lower tank of the evaporator to prevent the evaporator from being corroded. | ||||||
| 62 | Corrosion inhibitor for aqueous ammonia absorption system | US696789 | 1996-08-14 | US5811026A | 1998-09-22 | Benjamin A. Phillips; Eugene P. Whitlow |
| A method of inhibiting corrosion and the formation of hydrogen and thus improving absorption in an ammonia/water absorption refrigeration, air conditioning or heat pump system by maintaining the hydroxyl ion concentration of the aqueous ammonia working fluid within a selected range under anaerobic conditions at temperatures up to 425.degree. F. This hydroxyl ion concentration is maintained by introducing to the aqueous ammonia working fluid an inhibitor in an amount effective to produce a hydroxyl ion concentration corresponding to a normality of the inhibitor relative to the water content ranging from about 0.015 N to about 0.2 N at 25.degree. C. Also, working fluids for inhibiting the corrosion of carbon steel and resulting hydrogen formation and improving absorption in an ammonia/water absorption system under anaerobic conditions at up to 425.degree. F. The working fluids may be aqueous solutions of ammonia and a strong base or aqueous solutions of ammonia, a strong base, and a specified buffer. | ||||||
| 63 | Method for removal of acid from compressor oil | US519095 | 1995-08-24 | US5770048A | 1998-06-23 | Robert Peter Scaringe; Nidal Abdul Samad; Lawrence Robert Grzyll |
| An alcohol, specifically ethanol, methanol and isopropanol, is used to remove acid from a refrigeration system, a heat pump or an air conditioner. The alcohol vaporizes acid, primarily inorganic acid, in the system and, in the filter/dryer, reacts with surfaces or is adsorbed. The alcohol, the quantity of which is determined from the capacity of the filter/dryer, is introduced into the compressor oil sump for thorough mixing with the oil during compressor lubrication. | ||||||
| 64 | Heat exchanging apparatus and a method of preventing corrosion | US903268 | 1992-06-24 | US5377494A | 1995-01-03 | Shinya Takagi; Kazuaki Minato; Masafumi Satomura |
| A heat exchanging apparatus includes a composite structure of a ferrosoferric oxide and a molybdenum oxide at the internal surface of a heat exchange cycle tube located in a generator. A process of suppressing corrosion of this heat exchanging apparatus includes the step of preparing an ammonia solution including dissolved oxygen of a concentration of approximately 3-8 ppm. Approximately 1 wt %-5 wt % molybdate is added into the ammonia solution. This ammonia solution is sealed within the heat exchange cycle tube to be heated to at least a predetermined temperature in the generator of the heat exchanging apparatus. Thus, a composite structure of a ferrosoferric oxide and molybdenum oxide is formed on the internal surface of the generator. This composite structure allows the suppression of corrosion in the internal surface of the generator. | ||||||
| 65 | Absorption refrigeration and heat pump system | US945090 | 1986-12-22 | US4742693A | 1988-05-10 | Edward A. Reid, Jr.; F. Bert Cook; Stephen P. Cremean; Richard H. Merrick; Edgar M. Purvis |
| This invention relates to a cooling and heating system which operates on the absorption and phase change heat exchange principle. More particularly it relates to a continuous heat actuated, air cooled, double effect generator cycle, absorption system. In further aspects, this invention relates to a system constructed for use with an absorption refrigeration solution pair consisting of a nonvolatile absorbent and a highly volatile refrigerant which is highly soluble in the absorbent. A disclosed refrigerant pair are ammonia as the refrigerant and sodium thiocyanate as the absorbent. An absorption cycle is disclosed using the thermo physical properties of sodium thiocyanate/ammonia, absorption/refrigerant pair. Also disclosed is the construction and configuration of a reverse cycle air cooled double effect generator absorption refrigeration system for use with the sodium thiocyanate/ammonia refrigeration pair, as well as subcompositions, subsystems and components that improve the system efficiency and reduce cost. | ||||||
| 66 | Absorption refrigeration and heat pump system | US945087 | 1986-12-22 | US4722193A | 1988-02-02 | Edgar M. Purvis; Edward A. Reid, Jr.; F. Bert Cook; Stephen P. Cremean |
| This invention relates to a cooling and heating system which operates on the absorption and phase change heat exchange principle. More particularly it relates to a continuous heat actuated, air cooled, double effect generator cycle, absorption system. In further aspects, this invention relates to a system constructed for use with an absorption refrigeration solution pair consisting of a nonvolatile absorbent and a highly volatile refrigerant which is highly soluble in the absorbent. A disclosed refrigerant pair are ammonia as the refrigerant and sodium thiocyanate as the absorbent. An absorption cycle is disclosed using the thermo physical properties of sodium thiocyanate/ammonia, absorption/refrigerant pair. Also disclosed is the construction and configuration of a reverse cycle air cooled double effect generator absorption refrigeration system for use with the sodium thiocyanate/ammonia refrigeration pair, as well as subcompositions, subsystems and components that improve the system efficiency and reduce cost. | ||||||
| 67 | Absorption refrigeration and heat pump system | US683187 | 1984-11-13 | US4646541A | 1987-03-03 | Edward A. Reid, Jr.; F. Bert Cook; Edward M. Winter; Edgar M. Purvis, Jr.; Horatio H. Krause, Jr. |
| This invention relates to a cooling and heating system which operates on the absorption and phase change heat exchange principle. More particularly it relates to a continuous heat actuated, air cooled, double effect generator cycle, absorption system. In further aspects, this invention relates to a system constructed for use with an absorption refrigeration solution pair consisting of a nonvolatile absorbent and a highly volatile refrigerant which is highly soluble in the absorbent. A disclosed refrigerant pair are ammonia as the refrigerant and sodium thiocyanate as the absorbent. An absorption cycle is disclosed using the thermo physical properties of sodium thiocyanate/ammonia, absorption/refrigerant pair. Also disclosed is the construction and configuration of a reverse cycle air cooled double effect generator absorption refrigeration system for use with the sodium thiocyanate/ammonia refrigeration pair, as well as subcompositions, subsystems and components that improve the system efficiency and reduce cost. | ||||||
| 68 | Method and apparatus for increasing air conditioner efficiency | US913528 | 1978-06-07 | US4213306A | 1980-07-22 | William A. Peabody; Ernest M. Schaaf |
| A method and apparatus for increasing air conditioner efficiency comprising means and method to cool the high temperature high pressure gas output of the air conditioning unit compressor pump at or before the unit condenser utilizing water which has been pre-treated to retain particulate matter dissolved and suspended therein in order that scale not be formed upon the high pressure tubing and fins of the condenser. As a result of the cooling, the air conditioning unit operates with increased efficiency and reduced compressor head pressures for longer life. Additionally, means and method are provided for controllably regulating the flow of the cooling water and spray to protect the compressor from damage as a result of the increased efficiency. | ||||||
| 69 | Corrosion inhibitor in absorption refrigeration system | US22593451 | 1951-05-12 | US2580984A | 1952-01-01 | ERIK WIDELL NILS |
| 70 | Method and means for stabilizing the atmosphere of refrigerating systems | US17816927 | 1927-03-25 | US1809834A | 1931-06-16 | DAVENPORT RANSOM W |
| 71 | Kühleinrichtung und Kühlverfahren | EP11188061.3 | 2011-11-07 | EP2532993A3 | 2018-03-21 | Strässer, Peter; Seufferheld, Daniel |
Die Erfindung betrifft eine Kühleinrichtung |
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| 72 | DESICATING SYNTHETIC REFRIGERATION LUBRICANT COMPOSITION | EP15737397.8 | 2015-01-15 | EP3094700A1 | 2016-11-23 | DIXON, Elizabeth |
| The disclosure relates to a working fluid for use in a compression refrigeration, air conditioning or heat pump system, comprising a refrigerant comprising a fluoro-olefin, and a lubricant which comprises a mixture of a polyol ester and a polyoxyalkylene glycol, said polyol ester being present in an amount of at least 50% by weight based on the total weight of the polyol ester and the polyoxyalkylene glycol. Novel lubricants are also described and claimed. | ||||||
| 73 | CORROSION RESISTANCE LIFE DIAGNOSIS COMPONENT, HEAT EXCHANGER, AND REFRIGERATION AND AIR CONDITIONING DEVICE | EP13896643.7 | 2013-10-31 | EP3023728A1 | 2016-05-25 | KIMATA, Akinori; OKAJIMA, Rumi; HIRAI, Yasunobu; MIYA, Kazuhiro; KURIKI, Hironori |
A lifetime diagnosis component for anticorrosive coating includes a plate-shaped base member having an aluminum layer on a surface thereof; and a sacrificial anode layer portion formed of zinc on the base member. The surface of the base member has a base-member exposing portion where the aluminum layer is exposed. |
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| 74 | MICROCHANNEL HEAT EXCHANGER MODULE DESIGN TO REDUCE WATER ENTRAPMENT | EP09811874 | 2009-04-24 | EP2321608A4 | 2013-03-06 | TARAS MICHAEL F; ESFORMES JACK LEON |
| 75 | Kühleinrichtung und Kühlverfahren | EP11188061.3 | 2011-11-07 | EP2532993A2 | 2012-12-12 | Strässer, Peter; Seufferheid, Daniel |
Die Erfindung betrifft eine Kühleinrichtung |
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| 76 | Corrosion inhibitor for ammonia/water absorption systems | EP02022025.7 | 2002-10-01 | EP1304398A2 | 2003-04-23 | Guerra, Marco |
A corrosion inhibitor for ammonia/water absorption circuits for heat pumps and refrigerators in which the operating fluid is an ammonia/water solution, the inhibitor being added to said solution and comprising zinc borate in mixture with a buffer formed from potassium hydroxides and nitrates. |
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| 77 | HEAT EXCHANGER | EP01901438.0 | 2001-01-19 | EP1273858A1 | 2003-01-08 | FUKUSHIMA, M. ZEXEL VALEO CLIMATE CONTROLCORP.; KATO, S. ZEXEL VALEO CLIMATE CONTROL CORP.; SAKURADA, M. ZEXEL VALEO CLIMATE CONTROL CORP. |
The upstream side ends of fins (16) along the ventilating direction project out relative to the upstream side ends along the ventilating direction of tubes (14) without being allowed to project out beyond the end faces of tanks (2) and (3) along the ventilating direction so as to set the tubes (14) at positions recessed toward the downstream side along the ventilating direction relative to the fins (16), and the downstream side ends of the fins (16) along the ventilating direction are recessed further toward the upstream side along the ventilating direction relative to the downstream side ends of tubes (15) along the ventilating direction. As a result, the evaporator achieves a lower profile along the ventilating direction and, at the same time, condensed water manifesting at the surfaces of the tubes and fins is drained downward with a high degree of efficiency, thereby minimizing occurrence of spattering of the condensed water onto the downstream side and also, it becomes possible to prevent corrosion from advancing at the tubes due to dirt adhering onto the upstream side of the tubes along the ventilating direction. |
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| 78 | PIPE CONNECTING METHOD AND PIPE STRUCTURE | EP95932219.9 | 1995-09-21 | EP0730125B1 | 2001-08-29 | NAKAO, Noriaki, Kanaoka Factory; NISHINO, Haruhiko, O.K. Kizai Co., Ltd. |
| Pipes (40) of a predetermined length are filled with a nitrogen gas (4a). Cross-sectionally hat-shaped plugs (50) comprising a brazing filler metal are press fitted in open ends of joint portions (42, 42) at both ends of the pipes (40) so as to seal the pipes (40), whereby the plugs (50) are fixed to the joint portions (42, 42). One side portion of a connecting piece (60) is then inserted into the joint portion (42) of one pipe (40) by breaking the relative plug (50) thereby, while the other side portion of the connecting piece (60) is inserted into the joint portion (42) of the other pipe (40) by breaking the relative plug (50) thereby. The plugs (50) are then melted to braze the joint portions (42) of the pipes (40) and the connecting piece (60) to each other. | ||||||
| 79 | Process of suppressing corrosion of a heat exchanging apparatus | EP92110584.7 | 1992-06-23 | EP0520384A3 | 1993-03-17 | Takagi, Shinya; Minato, Kazuaki; Satomura, Masafumi |
A heat exchanging apparatus includes a composite structure of a ferrosoferric (40) oxide and a molybdenum oxide (41) at the internal surface of a heat exchange cycle tube located in a generator (21, 51). A process of suppressing corrosion of this heat exchanging apparatus includes the step of preparing ammonia solution including dissolved oxygen of a concentration of approximately 3 -8ppm. Approximately 1wt% - 5wt% molybdate is added into the ammonia solution. This ammonia solution is sealed within the heat exchange cycle tube to be heated to at least a predetermined temperature in the generator (21, 51) of the heat exchanging apparatus. Thus, a composite structure of a ferrosoferric oxide (40) and molybdenum oxide (41) is formed on the internal surface of the generator (21, 51). This composite structure allows the suppression of corrosion in the internal surface of the generator (21, 51). |
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| 80 | Process of suppressing corrosion of a heat exchanging apparatus | EP92110584.7 | 1992-06-23 | EP0520384A2 | 1992-12-30 | Takagi, Shinya; Minato, Kazuaki; Satomura, Masafumi |
A heat exchanging apparatus includes a composite structure of a ferrosoferric (40) oxide and a molybdenum oxide (41) at the internal surface of a heat exchange cycle tube located in a generator (21, 51). A process of suppressing corrosion of this heat exchanging apparatus includes the step of preparing ammonia solution including dissolved oxygen of a concentration of approximately 3 -8ppm. Approximately 1wt% - 5wt% molybdate is added into the ammonia solution. This ammonia solution is sealed within the heat exchange cycle tube to be heated to at least a predetermined temperature in the generator (21, 51) of the heat exchanging apparatus. Thus, a composite structure of a ferrosoferric oxide (40) and molybdenum oxide (41) is formed on the internal surface of the generator (21, 51). This composite structure allows the suppression of corrosion in the internal surface of the generator (21, 51). |
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