子分类：
| 序号 | 专利名 | 申请号 | 申请日 | 公开（公告）号 | 公开（公告）日 | 发明人 |
|---|---|---|---|---|---|---|
| 21 | 廃熱回収システム | JP2014022158 | 2014-02-07 | JP6217426B2 | 2017-10-25 | 阿部 誠 |
| 22 | スプレーノズル | JP2017508031 | 2016-02-16 | JP2017527435A | 2017-09-21 | クリシュナン モーハンクマー ヴァリヤムバス; イェン レン パン; ジフェン シュウ |
| 本発明は、近位端7と遠位端8とを含むエラストマー管1を含むスプレーノズルに関する。流体が、近位端7を通り、エラストマー管1に入る。スプレーノズルは更に、近位端7と遠位端8との間でエラストマー管1に形成され、エラストマー管1から流体を噴き出させるスリット9を含む。エラストマー管1は、エラストマー管1の変形を制限する補強要素10、11を含む。エラストマー管の近位端と遠位端との間で、エラストマー管にスリットを設けることによって、スリットは、広い噴霧パターンを噴霧するようなサイズにされる。補強要素は、エラストマー管の過度の膨張又は過度の変形を阻止する。 | ||||||
| 23 | 酸素燃焼ボイラの排ガスクーラ蒸気発生防止装置 | JP2013192549 | 2013-09-18 | JP6163994B2 | 2017-07-19 | 内田 輝俊 |
| 24 | 液−蒸気エジェクタと作動部ポンプを適用した高効率海洋温度差発電システム{High−efficiency ocean thermal energy conversion(OTEC) applying a liquid−vapor ejector and a motive pump} | JP2016564936 | 2015-03-05 | JP6103418B2 | 2017-03-29 | キム,ヒョン−ジュ; リ,ホ−セン; チャ,サン−ウォン; ジョン,ヨン−クォン; ユン,ジョン−イン; ソン,チャン−ヒョ; ソル,ソン−フン; イェ,ビョン−ヒョ |
| 25 | 液−蒸気エジェクタと作動部ポンプを適用した高効率海洋温度差発電システム｛Ｈｉｇｈ−ｅｆｆｉｃｉｅｎｃｙ ｏｃｅａｎ ｔｈｅｒｍａｌ ｅｎｅｒｇｙ ｃｏｎｖｅｒｓｉｏｎ（ＯＴＥＣ） ａｐｐｌｙｉｎｇ ａ ｌｉｑｕｉｄ−ｖａｐｏｒ ｅｊｅｃｔｏｒ ａｎｄ ａ ｍｏｔｉｖｅ ｐｕｍｐ｝ | JP2016564936 | 2015-03-05 | JP2017505407A | 2017-02-16 | キム，ヒョン−ジュ; リ，ホ−セン; チャ，サン−ウォン; ジョン，ヨン−クォン; ユン，ジョン−イン; ソン，チャン−ヒョ; ソル，ソン−フン; イェ，ビョン−ヒョ |
| 本発明は、移送された冷媒液を表層水と熱交換させて高温高圧の冷媒蒸気に変換させる蒸発器と、前記蒸発器出口に設置されて液体と気体状態の冷媒にそれぞれ分離させる気液分離器と、前記蒸発器入口に設置されて蒸発器に流入する配管を多方面に分離させる分配器と、前記気液分離器または前記蒸発器から移送された高圧の気体状態の冷媒を利用して電力を生産するタービンと、前記分配器において分枝され、または気液分離器から分離した液状態の冷媒を昇圧させる作動部ポンプと、前記タービンを通過した低圧の気体状態の冷媒と前記作動部ポンプを通過した高圧の液状態冷媒とを混合させ、膨脹と圧縮過程を有する液−蒸気エジェクタと、前記液−蒸気エジェクタにおいて混合した冷媒と深層水とを熱交換させて冷媒を凝縮させる凝縮器と、前記凝縮器において凝縮された冷媒を蒸発圧力まで昇圧及び循環せしめる冷媒循環ポンプと、を含んで構成されることを特徴とする分配器、液−蒸気エジェクタ及び作動部ポンプを利用した高効率海洋温度差発電システムに関するものである。【選択図】図1 | ||||||
| 26 | サーモスタット流れ制御装置および使用の方法 | JP2016033228 | 2016-02-24 | JP2016156503A | 2016-09-01 | ジェフリー エフ. マギー |
| 【課題】流体が所定の温度を超えて上昇したときに流体の流れを増大させる比較的少数の構成部品を備える信頼できる温度作動式弁アセンブリを提供する。 【解決手段】流れ制御装置12の少なくとも幾つかの部分は、その特定のサーモスタット特性に基づいて選択された1つまたは複数のサーモスタット材料から製造されている。流れ制御装置の基本的配列は、互いに反対側に位置する開放端部を備える中空の内部領域を形成するように、少なくとも1つのサーモスタットビーム24と、サーモスタットビームに固定された少なくとも1つの壁部26とを備える少なくとも1つのハウジング22と、中央プラグ部材であって、中央プラグ部材20の少なくとも1つの壁部48に少なくとも1つの開口50を備え、内部領域に配置され、温度に依存して流体の流れが開口を通過する、中央プラグ部材とを有する。 【選択図】図5 |
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| 27 | 復水器及びタービン設備 | JP2014057167 | 2014-03-19 | JP2015178937A | 2015-10-08 | 笠原 二郎; 西田 圭吾; 中村 太一; 堀田 克広 |
| 【課題】抽気管による空気等の不凝縮性ガスの抽気性能を維持することができる復水器等を提供する。 【解決手段】本発明の復水器は、蒸気が内部に流入する容器と、容器の内部に設けられ、蒸気を冷却して復水とする冷却管25と、容器の内部に含まれる空気を抽気するための抽気管13と、抽気管13に形成され、抽気管13の内部と容器の内部とを連通する抽気孔31と、抽気管13と所定の隙間Cを空けて設けられ、復水の抽気孔31への流入を規制するように、抽気孔31を覆う円筒カバー14と、を備える。 【選択図】図4 |
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| 28 | 乾き度測定装置 | JP2013272668 | 2013-12-27 | JP2015127647A | 2015-07-09 | 五所尾 康博; 西野 義一; 田邉 志功 |
| 【課題】水平方向に敷設された配管で正確な乾き度を測定することができる、乾き度測定装置を提供する。 【解決手段】本発明に係る乾き度測定装置は、水平方向に設置された配管と、前記配管の最低部を通る鉛直面に沿って光を入射させる光入射部と、前記配管に流れる湿り蒸気を透過し又は反射した光を透過させる光透過部と、透過した前記光の強度を検出する検出部と、検出された前記光の強度に基づいて、前記湿り蒸気の乾き度を測定する乾き度測定部と、を備え、前記光透過部は、水平平面部を含む立体形状を有し、前記鉛直面が前記光透過部の前記水平平面部と交差する第1部分が、当該鉛直面が前記最低部と交差する第2部分と同じ高さとなるか、または、前記第1部分が前記第2部分よりも高くなるように、且つ、前記光が前記水平平面部に入射する点を含む前記配管の断面が前記配管の内面および前記光透過部と交差する交差線上において、前記水平平面部と交差する部分が最も低くなるように、前記配管の底部に配置されている。 【選択図】図1 |
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| 29 | クアトロ・ジェネレーションシステム | JP2013198636 | 2013-09-25 | JP2015063954A | 2015-04-09 | 八木田 寛之; 安部 浩史; 小出 敬雄; 野口 敏秀; 中井 智章; 石川 博章; 江刺 弘之; 兵頭 潤 |
| 【課題】従来のコ・ジェネレーションシステムよりもトータルの熱効率が高い新規なクアトロ・ジェネレーションシステムを提供すること。 【解決手段】本発明のクアトロ・ジェネレーションシステム(1)は、燃料ガスによって駆動する発電機関(2)と、発電機関から排出される排気ガスのエネルギーを利用して蒸気を生成する排熱ボイラ(4)と、排熱ボイラで生成された蒸気を蒸気エネルギー回収手段(6)に供給するとともに該蒸気の凝縮水を再び排熱ボイラに供給するボイラ水循環装置(8)と、排熱ボイラから排出される排気ガスの凝縮潜熱を利用して熱媒体を加熱する凝縮エコノマイザ(10)と、凝縮エコノマイザで加熱された熱媒体を熱エネルギー回収手段(12)に供給するとともに該熱媒体を再び凝縮エコノマイザに供給する熱媒体循環装置(14)と、を備える。 【選択図】図1 |
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| 30 | 酸素燃焼ボイラの排ガスクーラ蒸気発生防止装置 | JP2013192549 | 2013-09-18 | JP2015059679A | 2015-03-30 | UCHIDA TERUTOSHI |
| 【課題】高温の排ガスとの熱交換によって引き起こされる排ガスクーラにおける蒸気発生を未然に防止し得る酸素燃焼ボイラの排ガスクーラ蒸気発生防止装置を提供する。【解決手段】復水器12の給水出側と排ガスクーラ6の給水入側とをつなぐバイパスライン24を設け、バイパスライン24に蒸気発生防止用ポンプ25と入口遮断弁26とを設け、排ガスクーラ6の給水出側と復水器12の給水入側とをつなぐ蒸気発生防止用水循環ライン27を設け、蒸気発生防止用水循環ライン27に出口遮断弁28を設け、ボイラ燃料遮断時におけるボイラ給水ポンプ18停止時に、入口遮断弁26と出口遮断弁28を開き、蒸気発生防止用ポンプ25を起動することにより、水をバイパスライン24から排ガスクーラ6へ流通させ、蒸気発生防止用水循環ライン27を介し復水器12へ戻して循環させる。【選択図】図1 | ||||||
| 31 | Waste-heat recovering apparatus | JP18735682 | 1982-10-27 | JPS5977083A | 1984-05-02 | HARA HIROYUKI |
| PURPOSE:To take-out motive-power from gas energy by utilizing the gas occluding metal which occludes gas and discharges the gas having a pressure through heating and by the repetition of discharge and occlusion of gas by heating and cooling the metal. CONSTITUTION:A heat exchanger 2 is installed onto a discharge apparatus 1 for discharging hydrogen gas from the hydrogen occluding metal which occludes hydrogen gas. A power generator 4 generates electric power by ustilizing the motive power supplied from an expansion machine 3 for decompressing the hydrogen gas having a pressure which is discharged from the discharge apparatus 1. Said hydrogen gas having a pressure is sent into the gas expansion machine 3 and decompressed. The energy due to expansion of hydrogen gas is taken-out as the rotary power for a shaft by the expansion machine and used for driving the power generator 4 to generate electric power. Since the temperature of the hydrogen gas which is adiabatically expanded lowers below the temperature before decompression, the hydrogen occuluding metal can be used as the cooling heat-source for a refrigerator. | ||||||
| 32 | Method and apparatus for storing and deriving low temperature heat energy | JP15870477 | 1977-12-29 | JPS5389044A | 1978-08-05 | ERUNSUTO AKE BURUNBERUKU; REI ORUSON |
| Heat energy is stored chemically in and extracted from an energy accumulator containing a substance which contains less liquid in the charged, high-energy condition of the accumulator than it does in the discharged low-energy condition of the accumulator, which is associated with vapor condensing and generating means which is maintained at a low temperature as compared with the accumulator in which a liquid container is comprised. Vapor is driven off from the accumulator substance and transferred to the vapor condensing and generating means when energy is stored in the accumulator, and is returned to the accumulator when heat energy is extracted therefrom. The system comprising the accumulator and said vapor condensing and generating means is maintained substantially free from other gases than said vapor. | ||||||
| 33 | ENERGY CONVERSION SYSTEM AND METHOD | EP16762053.3 | 2016-03-02 | EP3265655A1 | 2018-01-10 | BROHALL, David; FORSLUND, Örjan |
| The present invention relates to an energy conversion system for converting thermal energy to mechanical energy, comprising an evaporator, an expander, a condenser, a first tank, and a second tank. The energy conversion system further comprises flow control devices for controlling flow or working fluid between the evaporator, the expander, the condenser and the tanks, and a control unit for controlling operation of the energy conversion system by controlling the flow control devices. Each of the tanks has an outlet connected to an inlet of the evaporator, and an inlet connected to the condenser as well as to an outlet of the evaporator. Hereby, some of the pressurized vapor state working fluid flowing from the outlet of the evaporator can be used for pressurizing liquid state working fluid supplied from one the tanks to the evaporator. This configuration of the energy conversion system provides for improved energy conversion efficiency. | ||||||
| 34 | SEALING UNIT AND FLUID ENGINE | EP16709484.6 | 2016-02-03 | EP3253950A1 | 2017-12-13 | LUCKING, Graham Stuart; HORDLEY, Timothy Stephen; BUFFERY, Harry Martin; PALMER, Don Charles |
| A valve stem sealing unit (65) for forming a seal round a valve stem (41, 43) of a poppet valve (19, 21) in an engine (1) having a body (5, 7, 13) and operated by a working fluid, the valve stem sealing unit (65) including: a housing (67) defining a through passage (79) running from a first end to a second end, the through passage (69) being arranged to receive a portion of the valve stem (41, 43); a first seal (85) arranged to form a seal between the valve stem (41, 43) and the housing (69) to prevent egress of the working fluid from the first end of the housing (69); and a second seal (89) arranged to form a seal between the housing (69) and a body (5, 7, 13) of the engine (1) to prevent egress of the working fluid from the second end of the housing (69). | ||||||
| 35 | WASTE HEAT RECOVERY AND CONVERSION | EP16744270.6 | 2016-02-01 | EP3250791A1 | 2017-12-06 | Filippone, Claudio |
| Embodiments in accordance with the present disclosure provide systems and methods for a waste heat recovery and conversion. The waste heat recovery and conversion system includes a housing non-invasively mountable onto an engine. The waste heat recovery and conversion system also includes a power conversion unit (PCU) entirely within the housing. The PCU includes heat exchangers, an expander, an electrical power generator, and a fluid pump. The heat exchangers, the expander, the fluid pump, and the fluid reservoir form a thermodynamic loop that drives the electrical power generator using thermal energy from waste heat. Under various configurations the waste heat recovery and conversion system offer pollutant reduction features all together with fuel savings. | ||||||
| 36 | WASTE HEAT RECOVERY SYSTEM | EP15746099 | 2015-02-02 | EP3103975A4 | 2017-11-29 | ABE MAKOTO |
| Connected in parallel to an expander (3) and a condenser (4) of a Rankine cycle (6) are n sets (S) each of which comprises a different expander (E) and a different condenser (C). Moreover, operation stopping means (B 1 -B n ) are provided for stopping operations of the expanders (E 1 -E n ) in the sets (S 1 -S n ) connected in parallel, and a pressure sensor (10) and a temperature sensor (11) are installed respectively in an inlet and outlet of an evaporator (2). An ECU (12) sets or releases at least one of the operation stopping means (B 1 -B n ) such that a measured value (T) of the temperature sensor (11) reaches a prescribed temperature value (Ts) which is equal to or less than a thermal decomposition temperature of a refrigerant (5) and which is set in advance, and the ECU (12) controls a rotational speed of a refrigerant pump (1) such that a measured value (P) of the pressure sensor (10) reaches a prescribed pressure value (Ps) set in advance. | ||||||
| 37 | Exhaust gas treatment system and method, as well as ship comprising, and use of, such a system | EP14199534.0 | 2014-12-22 | EP3037635B1 | 2017-08-09 | Mølgaard, Søren; Christensen, Kenneth |
| A system and a method for treatment of engine exhaust gas (EEG) from an engine (3), which engine exhaust gas (EEG) has a temperature of between T 1 and T 2 , are provided. Provided are also a ship comprising such a system and a use of such a system. The system (1) comprises a SCR reactor (9) for converting NO x contained in a medium (M) containing the engine exhaust gas (EEG) into N 2 and H 2 O. The SCR reactor (9) has an inlet (33) for receiving the medium (M) and an outlet (35) for outputting the NO x reduced medium (M-NO x ). The system (1) is characterized in that it further comprises a mixing unit (7) and a first boiler unit (5). The first boiler unit (5) has a first outlet (19) for outputting boiler exhaust gas (BEG) from the first boiler unit (5), which boiler exhaust gas (BEG) has a temperature of more than T 3 , T3>T 1 . The mixing unit (7) is arranged to mix the engine exhaust gas (EEG) with the boiler exhaust gas (BEG) to produce said medium (M). The mixing unit (7) has a first inlet (27) communicating with the engine (3) for receiving the engine exhaust gas (EEG), a second inlet (29) communicating with the first outlet (19) of the first boiler unit (5) for receiving the boiler exhaust gas (BEG) and an outlet (31) for outputting said medium (M). The outlet (31) of the mixing unit (7) communicates with the inlet (33) of the SCR reactor (9). | ||||||
| 38 | THERMO-ACOUSTIC REACTOR WITH NON-THERMAL ENERGY ABSORPTION IN INERT MEDIUM | EP16154159.4 | 2016-02-04 | EP3115689A1 | 2017-01-11 | Tomoiu, Constantin |
An air, fuel, and inert fluid or liquid water mixture is injected into a resonance chamber forming micro-packets. The air and fuel mixture in the micro-packets form micro-explosions in a combustion chamber where acoustic and electromagnetic energy are absorbed by the inert fluid instead of thermal energy. A standing wave is created in the central resonance chamber by the micro-explosions. Interfering waves are in phase increasing energy in the air, fuel and water mixture. Acoustic energy is transferred from the hot combustion gases to the colder inert fluid or water. A thermal equilibrium is reached without substantial energy transfer from the hot body to the cold body. Efficient combustion is achieved with reduced carbon emissions. The heat generated from the combustion may be used to produce work by any conventional device, such as a steam engine or turbine or generate heat for a building.
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| 39 | DISPOSITIF DE RÉCUPÉRATION D'ÉNERGIE À BOUCLE DE RANKINE | EP15169813.1 | 2015-05-29 | EP2957741B1 | 2016-12-28 | DINY, Mouad; LEGROS, Arnaud |
| 40 | WASTE HEAT RECOVERY SYSTEM | EP15746099.9 | 2015-02-02 | EP3103975A1 | 2016-12-14 | ABE,Makoto |
Connected in parallel to an expander (3) and a condenser (4) of a Rankine cycle (6) are n sets (S) each of which comprises a different expander (E) and a different condenser (C). Moreover, operation stopping means (B1-Bn) are provided for stopping operations of the expanders (E1-En) in the sets (S1-Sn) connected in parallel, and a pressure sensor (10) and a temperature sensor (11) are installed respectively in an inlet and outlet of an evaporator (2). An ECU (12) sets or releases at least one of the operation stopping means (B1-Bn) such that a measured value (T) of the temperature sensor (11) reaches a prescribed temperature value (Ts) which is equal to or less than a thermal decomposition temperature of a refrigerant (5) and which is set in advance, and the ECU (12) controls a rotational speed of a refrigerant pump (1) such that a measured value (P) of the pressure sensor (10) reaches a prescribed pressure value (Ps) set in advance. |
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