| 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 | Centrifugal compressor | JP2012557354 | 2011-03-17 | JP2013522521A | 2013-06-13 | デイヴィー ガース |
| 入力駆動装置を有するインペラを備える遠心圧縮機であって、インペラは、インペラの周辺に位置決めされインペラを出るガスにより駆動される衝動タービンを有し、タービンの出力は、インペラの駆動装置に結合される遠心圧縮機。
【選択図】図１ |
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| 82 | Co2 separation/recovery apparatus and coal gasification-combined power generation plant equipped with co2 separation/recovery apparatus | JP2010225474 | 2010-10-05 | JP2012076970A | 2012-04-19 | TAKEUCHI HIROTO |
| PROBLEM TO BE SOLVED: To provide a CO2 separation/recovery apparatus from which a higher CO2 recovery rate is obtained, and a coal gasification-combined power generation plant equipped with a CO2 separation/recovery apparatus of high plant efficiency.SOLUTION: The CO2 separation/recovery apparatus includes a CO shift reactor which introduces a gas containing CO2 and H2 as principal components and produces CO and H2O, an inlet valve arranged at the entrance side of the CO shift reactor, an outlet valve arranged at the outlet side of the CO shift reactor, a steamy control valve for giving high temperature steam to the prestage of the inlet valve, and a gas composition analyzer which detects gas composition of a fluid which flows into the CO shift reactor, where the steamy control valve is controlled by the molar quantity difference of CO and H2O obtained from the result of analysis of the gas composition analyzer, and the inlet valve and the outlet valve of the CO shift reactor are controlled by the catalyst tank temperature of the CO shift reactor. | ||||||
| 83 | Electric power-generating and desalination combined plant and operation method of the same | JP2011133048 | 2011-06-15 | JP2011226489A | 2011-11-10 | GOTO KOICHI; SUGIMORI YOICHI |
| PROBLEM TO BE SOLVED: To improve the power generation efficiency of a combined cycle and reduce the annual total fuel consumption when an electric power-generating and desalination combined plant performs partial load operation according to electricity demand or freshwater demand.SOLUTION: In the method of operating an electric power-generating and desalination combined plant, which includes a combined-cycle electric power-generating facility including a gas turbine 1, an exhaust gas boiler 9 having a duct combustor 31 and heating supply water by heat of an exhaust gas introduced from the gas turbine to generate steam, and a steam turbine 11 operated by use of the steam generated by the exhaust gas boiler as an operating fluid; and a desalination facility 14 connected thereto, the desalination facility 14 producing freshwater by use of exhaust steam of the steam turbine 11 as a heat source, the operation is performed so that the power generation amount and the freshwater amount are predetermined values respectively by adjusting an operation load ratio of the gas turbine 1 and combustion of the duct combustor 31. The gas turbine 1 is operated at an operation load ratio at which the flow rate of surplus steam 15 that is not used in the desalination facility 14 of the exhaust steam of the steam turbine 11 is in a range of zero to a predetermined allowable value. | ||||||
| 84 | Volatile organic compound processing method and the volatile organic compound processing system using a gas turbine | JP2006531847 | 2005-08-18 | JP4677989B2 | 2011-04-27 | 茂一 宇治 |
| 85 | Oil removal from the organic Rankine cycle (orc) system of the turbine | JP2010518153 | 2007-07-27 | JP2010534785A | 2010-11-11 | ディー． アーナー，マイケル; エス． マットソン，ピーター |
| 有機ランキンサイクル（ＯＲＣ）システム（１０）において、特に起動時における故障を回避するために、該ＯＲＣシステム内のオイルを除去する方法およびシステムが使用される。 ＯＲＣシステム（１０）は、蒸発器、タービン、凝縮器およびポンプを備え、該ＯＲＣシステム内に冷媒を循環させるように構成されている。 オイル除去システムは、タービン（１８）の特定の領域からオイルを除去するように使用され、エダクタライン（３２）およびエダクタシステム（２０）を備える。 エダクタライン（３２）は、タービン（１８）の上流に配置され、蒸発器から流出する冷媒（２２ｂ）の一部を受けるように構成されている。 エダクタライン（３２）は、この冷媒（２２ｂ）を、エダクタシステム（２０）に送り、このエダクタシステム（２０）は、タービン（１８）内からオイルを除去し、このオイルを油溜め（５８）に送る。 | ||||||
| 86 | Control system of heat transfer system which connect nuclear power installation and sea water desalting device | JP9997082 | 1982-06-12 | JPS58216774A | 1983-12-16 | KAWANA SEIZOU |
| PURPOSE: To prevent the leakage of harmful material components such as radioactivity in the stage of transferring heat from a heat generation system to a heat utilization system, by monitoring the pressure of an intermediate heat medium in the heat transfer part in the mid-way thereof in such a way that said pressure is kept always higher than the steam bleeding pressure of a turbine in the heat generation system. CONSTITUTION: If the standard value of the extraction steam S to be bled from a steam bleeding part 1a of a nuclear power installation is defined as 14kg/cm 2ab, prescribed horse power is beforehand given to a circulation pump 18 in order to assure 16kg/cm 2 ab which is higher than said value in the intermediate heat medium (k) to be circulated in a piping system 4 for the heat medium in an intermediate indirect heat exchanger 3. A differential pressure indicating controller 16 is beforehand so set that an output is produced therefrom when th differential pressure Δpc is at the value except the value in a 2kg/cm 2ab< ΔPC4kg/cm 2ab. The pressure of the extraction steam pressure and the pressure of the intermediate heat medium are inputted respectively through pressure detectors 14, 15 to the controller 16. A flow rate control valve 17 is throttled in accordance with the detected output thereof, whereby the pressure within the differential pressure range is maintained. COPYRIGHT: (C)1983,JPO&Japio | ||||||
| 87 | Power generation refrigerating system and operating method thereof | JP13129279 | 1979-10-11 | JPS5551905A | 1980-04-16 | RUISU EICHI REONAADO |
| 88 | JPS5472203U - | JP14533878 | 1978-10-24 | JPS5472203U | 1979-05-23 | |
| 89 | Desalting distillation apparatus with vapor power apparatus | JP8242976 | 1976-07-10 | JPS5211171A | 1977-01-27 | NAMAN ATSUARI |
| 1501068 Desalinization distillation/steam power plant N AZHARI 9 July 1976 [12 July 1975] 28729/76 Heading BIB A combined desalinization/steam power plant comprises a multistage flash evaporator 3, a steam turbine 27 and associated boiler 26 driving an electric-generator 28 and a compressor 16 and a falling-film evaporator 14. A mixture of seawater and concentrated brine which has previously passed through the plant is passed from the cooling coils 10 of the flash evaporator, if necessary via an auxiliary heater 12 heated by steam from the turbine, to the falling-film evaporator 14 wherein part is evaporated and the resulting vapour compressed in the compressor 16 and fed to the heating chamber 43 of 14, if necessary after mixing with cooling water at 18, to provide heat for the evaporation therein. Water condensing in the heating chamber is fed to the distillate trays 21 of the multistage flash evaporator 10 via line 19 and unevaporated brine from 43 is fed to the flash evaporator via line 20 and evaporated therein under reduced pressure produced by steam ejector 36. | ||||||
| 90 | 温度軌道を介して機械応力を制御するためのシステムおよび方法 | JP2018013297 | 2018-01-30 | JP2018150931A | 2018-09-27 | ベンジャミン・ディヴィッド・ラスコウスキー; ウィリアム・フォレスター・シーリー |
| 【課題】温度軌道を介して機械応力を制御するためのシステムおよび方法を提供する。 【解決手段】方法は、プロセッサを介して、蒸気タービンシステムの構成要素のための指令された温度速度を決定するステップを含む。この方法は、プロセッサを介して、蒸気タービンシステムの構成要素のための測定された温度速度を決定するステップをさらに含む。この方法はさらに、プロセッサを介して、指令された温度速度および測定された温度速度に少なくとも部分的に基づいて可変乗数を決定するステップを含む。この方法はまた、プロセッサを介して、可変乗数を指令された温度速度に適用することによって乗算された温度速度コマンドを導出するステップを含む。 【選択図】図1 |
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| 91 | 多機能糞便廃棄物・ごみ処理装置及び関連方法 | JP2017544836 | 2015-11-09 | JP2018502717A | 2018-02-01 | ジャニッキ ピーター |
| 本技術の少なくとも1つの観点は、高含水率有機廃棄物、例えば糞便スラッジや生ごみを電気に変換する一方で更に飲料水を生じさせて集めるよう構成された自蔵式処理施設を提供する。 | ||||||
| 92 | CO2捕獲/利用およびN2生産のための発電所による圧力スイング吸着の統合 | JP2015517418 | 2013-06-13 | JP6209212B2 | 2017-10-04 | ナラシムハン・サンダラム; ラメシュ・グプタ; ハンス・トーマン; ヒューゴ・エス・カラム; ローレン・ケイ・スターチャー; フランクリン・エフ・ミトリッカー; サイモン・クリストファー・ウエストン; スコット・ジェイ・ウェイゲル |
| 93 | 発電システム、発電方法 | JP2012288963 | 2012-12-28 | JP6086726B2 | 2017-03-01 | 久保田 裕孝; 桜井 貴夫; 平尾 豊隆; 小林 直樹 |
| 94 | 熱補償付きボイラーユニット抽出蒸気汚泥乾燥システム | JP2013558292 | 2011-12-19 | JP5881751B2 | 2016-03-09 | ▲銭▼学略 |
| 95 | 二酸化炭素の回収システム及び方法 | JP2011084929 | 2011-04-06 | JP5843464B2 | 2016-01-13 | 飯嶋 正樹 |
| 96 | 煙道ガス再循環を備えるコンバインドサイクル発電プラント | JP2011117927 | 2011-05-26 | JP5836645B2 | 2015-12-24 | マルタ デ ラ クルス ガルシア; ティエリ ラショ; アンドレ ブルデ; ヤーン ヘラート |
| 97 | 発電プラント | JP2011228776 | 2011-10-18 | JP5721605B2 | 2015-05-20 | エリベルト・ベンツ; ギャン−ルイジ・アゴスティネリ; アンドレーアス・ブラウチュ; ギスベルト・ヴォルフガング・ケーファー; フェーリクス・ギューテ |
| 98 | The systems and methods of the integrated gas adsorption separation of the combustion gas | JP2014517360 | 2012-06-29 | JP2014524829A | 2014-09-25 | ボウレット，アンドレ |
| ガス吸着分離を備える統合的燃料燃焼システムは、燃焼混合ガスから二酸化炭素の一部を分離し、分離した二酸化炭素を、燃焼用に燃料燃焼炉の吸入口に再循環する。 二酸化炭素の分離および再循環のプロセスは：吸着剤を備えるガス吸着分離システム接触器への燃焼ガスの流入；二酸化炭素の一部の吸着；二酸化炭素が減少した第１の生成ガスの、放出または使用目的での回収；吸着剤からの二酸化炭素の脱着、また、二酸化炭素が豊富な、脱着させた第２の生成ガスの、隔離または使用目的での回収；調節流体の接触器への流入、また、二酸化炭素が豊富な調節流を回収するための、二酸化炭素の第２の部分の脱着；燃焼用に燃料燃焼炉に通すための、二酸化炭素が豊富な調節流の一部の、燃料燃焼炉の流入口への再循環を含む。
【選択図】図１ |
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| 99 | Power generation system and power generation method | JP2012288963 | 2012-12-28 | JP2014129799A | 2014-07-10 | KUBOTA HIROTAKA; SAKURAI TAKAO; HIRAO TOYOTAKA; KOBAYASHI NAOKI |
| PROBLEM TO BE SOLVED: To reliably cool a generator while preventing degradation of power generation efficiency.SOLUTION: A power generation system 20A includes a medium circulation circuit 22 for circulating a medium, a circulation pump 23, an evaporator 25 for evaporating the medium by an external heat source of variable heat quantity, an expander 26 driven by the medium evaporated by the evaporator 25, a condenser 27 for condensing the medium discharged from the expander 26, a generator 28 driven by the expander 26 and generating electric power, a cooling system 30 for cooling the generator 28 by the medium taken out from a downstream side of the condenser 27, and a gas-liquid separator 31 for separating the heated medium into gas and liquid by cooling the generator 28 by circulating the same in the cooling system 30, allowing a gas phase of the medium to flow into the medium circulation circuit 22 at an upstream side of the condenser 27, and allowing a liquid phase of the medium to flow into the medium circulation circuit 22 at a downstream side of the condenser 27. | ||||||
| 100 | Thermal power system | JP2012286609 | 2012-12-28 | JP2014129731A | 2014-07-10 | SHIBATA TSUYOSHI; TSUDA SHINJI; KUSAKA HIROTO |
| PROBLEM TO BE SOLVED: To provide a thermal power system with high efficiency and economic performance even under a location condition where water cannot be obtained from the ocean or a large river around a power-generating plant and industrial water cannot be conveyed from outside the plant.SOLUTION: A thermal power system is provided with a water recovering facility for recovering moisture by condensing steam in exhaust gas of a boiler, a water purifying facility for removing particulate substances and harmful substances from the recovered water to adjust the pH, a reservoir for storing the purified water, and an air-cooling type cooling tower to which water of the reservoir is supplied. A water cooling system of a closed circulation type is constituted by the water recovering facility and the air-cooling type cooling tower. | ||||||
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