| 序号 | 专利名 | 申请号 | 申请日 | 公开（公告）号 | 公开（公告）日 | 发明人 |
|---|---|---|---|---|---|---|
| 81 | Compact, high-efficiency thermoelectric system | JP2004530980 | 2003-08-07 | JP4340902B2 | 2009-10-07 | ロン イー． ベル |
| 82 | Absorption chiller | JP2002178206 | 2002-06-19 | JP3966770B2 | 2007-08-29 | エス．グプテ ニールカンス |
| An absorption cooling machine of the type which uses a refrigerant and an absorbent and which includes a high stage generator (G1), absorber (A), condenser (C), heat exchangers (H), and an evaporator (E) and means for connecting the components to one another to form a closed absorption cooling system. The solution side of the high stage generator (G1) is fluidically divided into two sections (12,14) with a partition plate (16) whereby gas exiting one section (12) at relatively high temperature is further cooled in a second section (14) called a flue gas recuperator (FGR) to improve overall burner efficiency. |
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| 83 | High-temperature regenerator | JP295497 | 1997-01-10 | JP3837196B2 | 2006-10-25 | 伯一 久保田 |
| 84 | Compact, high-efficiency thermoelectric system | JP2004530980 | 2003-08-07 | JP2005536976A | 2005-12-02 | ロン イー． ベル |
| 製造可能なシステムにおいて作動媒体の流れまたは動きの方向に熱絶縁するという利点を用いた、コンパクトで、高効率のいくつかの熱電システムを説明する。 そのような構成は、高いシステム効率および出力密度を示す。 熱交換器同士の間にはさまれた複数の熱電モジュールまたは熱電素子を用いたいくつかの異なる実施形態および応用を開示する。 | ||||||
| 85 | High-temperature regenerator | JP4469896 | 1996-03-01 | JP3702026B2 | 2005-10-05 | 伯一 久保田 |
| 86 | Thermoelectric cooling transient and transient heating system | JP2003573366 | 2002-03-04 | JP2005519256A | 2005-06-30 | ロン イー． ベル |
| 非定常状態で熱電素子２０８を動作させることにより、効率の改善を図った熱電システムを提供する。 熱電素子２０８には、効率の向上を得るために、所定の時間電力が供給される。 電力供給期間の間に、抵抗加熱が最低になるように熱電素子２０８の抵抗を変化させることによって、上記の改善効果を得ることができる。 | ||||||
| 87 | High-temperature regenerator of the absorption chiller | JP12093696 | 1996-04-17 | JP3600367B2 | 2004-12-15 | 修行 井上; 貞一 望月; 素直 計良 |
| A generator which can prevent deterioration of the chilling performance and corrosion, and can provide a high degree of reliability and long service life is disclosed. The high-temperature generator comprises a combustion chamber for flowing a combustion gas therein, a first tube assembly and a second tube assembly provided in the combustion chamber each of which has a plurality of heat transfer tubes for containing liquid therein. The first tube assembly comprises a plurality of bare tubes and is arranged at an upstream of the second tube assembly. The second tube assembly comprises a plurality of finned tubes provided with fins on the outer surface thereof. The heat transfer tubes are arranged in a staggered manner in a direction of the combustion gas flow within each of the first tube assembly and the second tube assembly. The bare tubes and the finned tubes are arranged aligned to each other in a direction of the combustion gas flow at a boundary area between the first tube assembly and the second tube assembly. | ||||||
| 88 | Improved thermoelectric devices of the efficiency of using the convection type heat flow | JP2002564307 | 2002-02-07 | JP2004524498A | 2004-08-12 | ロン イー． ベル |
| 対流が熱電素子アレイ（８２１）を通るように活動的に促進され、効率の改善された熱電システム（８２０）を開示する。 一般に熱電装置は、冷却及び加熱に応用される。 熱出力が熱電素子アレイ（８２１）中を、その少なくとも一方の側に向かって対流され、これにより効率が高まる。 対流媒体を用いて対流式熱出力輸送を起こす幾つかの異なる構成を開示する。 さらに、熱電システム（８２０）を調節するために、１つ又は複数の入力に応答する制御システム（１９００）を開示する。 | ||||||
| 89 | Absorption refrigeration machine | JP2000569168 | 1999-09-03 | JP2002524716A | 2002-08-06 | クンツェ、ゲルハルト |
| (57)【要約】 本発明は、Ｐｌａｔｅｎ−Ｍｕｎｔｅｒｓシステムを使用した吸収冷凍機であって、溶媒中の冷媒を蒸発させるための発生器（７）と、冷媒から溶媒が分離される溶媒分離器（２）と、冷媒を液化するための凝縮器（３）と、冷媒が冷却中に乾性ガスを使用して蒸発させられる蒸発器（４）と、場合によっては第１のガス熱交換器（６）と、蒸発させられた冷媒が冷媒と溶媒との減損混合物に供給され、次いでその混合物が発生器（７）中で再び蒸発させられる吸収器（５）とを含んでいる吸収冷凍機に関する。 蒸発器（４）の出力または場合によっては蒸発器（４）の下流に配置された第１のガス熱交換器（６）の出力および発生器（７）の出力が、吸収器（５）に接続されたバイパス（８）中に排出する。 第１のガス熱交換器（６）を介して蒸発器（４）から到着する蒸発させられた冷媒と乾性ガスとからなる混合物が、発生器の出力に転送され、そこからバイパス（８）中に入り、そこでガス混合物が、発生器（７）からきた高温の部分的にガス抜きされた溶液に接触させられ、発生器（７）からさらなる冷媒を引き出す。 | ||||||
| 90 | Regenerator | JP11785091 | 1991-04-23 | JP2810558B2 | 1998-10-15 | 言彦 世古口; 雅裕 古川 |
| 91 | Drive unit with a gas blow pump | JP50386690 | 1990-03-14 | JP2732945B2 | 1998-03-30 | SHUTEIIRURIN HANSU |
| PCT No. PCT/CH90/00066 Sec. 371 Date Jan. 29, 1992 Sec. 102(e) Date Jan. 29, 1992 PCT Filed Mar. 14, 1990 PCT Pub. No. WO90/10834 PCT Pub. Date Sep. 20, 1990.The abstract concerns an expeller with six pump tubes positioned round the circumference of a circle. A weak refrigerant solution is conveyed through the tube by rising vapor bubbles. Heating is by means of sich flame tubes. To improve heat transfer, the pump tubes are welded to the flame tube. The pump tubes lead into an exhaust-gas flue and are located inside this flue. The hot exhaust gases can therefore transfer heat to the weak refrigerant solution. | ||||||
| 92 | High temperature reproducer for absorption water cooling and heating machine | JP12093696 | 1996-04-17 | JPH09280691A | 1997-10-31 | INOUE OSAYUKI; MOCHIZUKI SADAICHI; KERA SUNAO |
| PROBLEM TO BE SOLVED: To solve problems of lowering of refrigerating capacity and the trouble of corrosion due to the increase of generating amount of non-condensed gas based on local heating and improve reliability as well as durability. SOLUTION: In a high temperature reproducer for a liquid tube and absorption water cooling and heating machine, in which solution is received in tubes and combustion gas is conducted to flow the outside of the tubes, the tubes include at least a bear tube group 3, arrayed in zigzag, and a finned tube group 4, arrayed in zigzag, while the bear tube group 3 is arranged at the upstream of the flow of combustion gas and the finned tube group 4 is arranged in the downstream of the flow of combustion gas. In this case, respective foremost row finned tubes 41 of the finned tube group 4 are arranged so as to be hidden by the rearmost row bear tubes 31 of the bear tube group 3, in a connecting part between the bear tube group 3 and the finned tube group 4. COPYRIGHT: (C)1997,JPO | ||||||
| 93 | Regenerator | JP31140395 | 1995-11-29 | JPH09152228A | 1997-06-10 | SAWAKURA KAZUYA; DAINO MASAYUKI; IKEDA SUMIO |
| PROBLEM TO BE SOLVED: To make it possible to rapidly make solution concentration uniform while maintaining the convection force of the solution by installing spreaders having different solution scattering amounts between at one and the other sidewall sides of one box at the starting end side of a flue in the regenerator for an absorption type chilled and warm water generator in which refrigerant is evaporated and separated from the solution. SOLUTION: A flue 2 and exhaust gas passage 3 are contained in a case 1, and a heating convection area 4 and an evaporating separate area 5 are formed inside the case 1. The solution poured from a spreader 9 is heated by the heat generated from the flame of a gas burner and excess heat of waste gas, refrigerant is evaporated separately from the solution, discharged from a refrigerant discharge port 7, and the solution that the refrigerant concentration is reduced is discharged from a solution discharge port 8 provided at the sidewall 1a of a front plate 1c side. The spreaders 9 are arranged so that openings 9a of the same diameter are formed at a flat bottom plate in such a manner that the ones are rough and the others are gradually dense and that the side of the rough openings 9a is directed toward the sidewall 1a and the side of the dense openings 9a is directed toward the sidewall 1b. COPYRIGHT: (C)1997,JPO | ||||||
| 94 | High temperature regenerator absorption type cold/hot water apparatus and the apparatus | JP1046993 | 1993-01-26 | JPH06221718A | 1994-08-12 | NISHIGUCHI AKIRA; OUCHI TOMIHISA; SUGIMOTO SHIGEO; AIZAWA MICHIHIKO; NARUSE TAKAO; URAKI YASUO |
| PURPOSE: To provide an absorption type cold/hot water apparatus and a high temperature regenerator of the same in which a heat transfer surface of the high temperature regenerator is prevented from being locally overheated and hereby corrosion is produced, and in which miniaturization is ensured. CONSTITUTION: A high temperature regenerator 1 comprises an outer cylinder 101, an inner cylinder 102, a plurality of solution pipes 103, a burner 104, a solution inflow pipe 105, and a gas/liquid isolation plate 106. The inner cylinder 102 is located in the outer cylinder 101, between which a solution is retained in which solution the inner cylinder 102 is dipped. The burner 104 penetrates the inner cylinder 102 and is mounted on the side of the outer cylinder 101. The inside of the inner cylinder 102 forms a combustion chamber. A plurality of solution pipes 103 communicating the upper and lower portions of the inner cylinder 102 are disposed on the downstream side of the combustion chamber. The inreriors of the pipes are filled with a solution. The solution pipe 13 has a horizontal cross section of an elliptical shape. A plurality of the solution pipes are arranged such that stright portions of the elliptical shapes are disposed parallely. A combustion gas passage is formed between the solution pipes 103. COPYRIGHT: (C)1994,JPO&Japio | ||||||
| 95 | JPH04506860A - | JP50508091 | 1991-02-08 | JPH04506860A | 1992-11-26 | |
| A refrigeration and heating system in which an absorber (97), condenser (100) and recuperator are placed (107) in a single module (270) and are provided with tube-in-tube or tube-in-cylinder construction with fluted inner tubes. A general purpose, divided-flow, tube-in-cylinder, heat transfer device (400) is used to reduce the pressure drop in the circulating fluid. | ||||||
| 96 | JPH01502844A - | JP50282588 | 1988-03-17 | JPH01502844A | 1989-09-28 | |
| 97 | JPS6342291Y2 - | JP1098183 | 1983-01-28 | JPS6342291Y2 | 1988-11-07 | |
| A spray generator for an absorption refrigeration system that includes a heat exchanger comprised of a multiplicity of variably spaced heat exchange tubes. The tubes are spaced close together near the top of the heat exchanger and spaced more widely apart near the bottom of the heat exchanger. Dilute absorbent solution is sprayed down through the heat exchanger. The close nesting of the tubes in the top portion of the heat exchanger retards liquid flow and aids heating of the solution. The wide spacing of the tubes in the lower section of the heat exchanger facilitate vapor flow out of the heat exchanger and eliminates liquid "blow-off". The top tubes are covered by a baffle to prevent the liquid solution from splashing out of the heat exchanger off of these top tubes. | ||||||
| 98 | Recuperative device for absorption refrigeration system | JP15392585 | 1985-07-12 | JPS61119956A | 1986-06-07 | ROBAATO SHII REIMAN; RICHIYAADO EI RUUTO |
| 99 | Heat exchanger with pipe with fin | JP24174385 | 1985-10-30 | JPS61107098A | 1986-05-24 | UIREMU RUDOBUIKUSU NIKORAASU B; YAKOBUSU PASUTOORU; YOHANESU KURISUCHIANUSU MARUTE |
| A heat exchanger comprises a vertically arranged circular-cylindrical holder closed at its upper end and at its lower end, and a pipe coaxially arranged within the holder. A fin is secured to the inner pipe and consists of a plurality of interconnected lamellae extending radially from the pipe, the fin being helically wound around the pipe so that the adjacent lamellae of successive turns of the resulting helix overlap each other in part, viewed in the circumferential direction of the pipe. A capillary passage is located in each lamella above the surface of an underlying lamella in a position shifted with respect to the capillary passage of the underlying lamella. | ||||||
| 100 | Absorption heat pump | JP24174485 | 1985-10-30 | JPS61107061A | 1986-05-24 | UIREMU RUDOBUIKUSU NIKORAASU B; YAKOBUSU PASUTOORU; YOHANESU KURISUCHIANUSU MARUTE |
| An absorption heat pump comprising a heat-mass-exchanger (57) which is arranged in an absorber (3) and has a metal pipe (77) to which a metal fin is secured. The metal fin consists of a number of interconnected lamellae (81) which are helically wound around the pipe (77), while adjacent lamellae (81) of successive turns overlap each other in part, viewed in the circumferential direction of the pipe (77). The finned pipe (77) yields a comparatively strong heat-mass transfer in the absorber (3). | ||||||
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