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 |
|---|---|---|---|---|---|---|
| 101 | ストリームプローブ閉塞による歯科衛生検出装置における歯肉検出 | JP2015548867 | 2013-12-20 | JP2016507264A | 2016-03-10 | ゴール エドガー マルティヌス バン; マーク トーマス ジョンソン; ヨハネス ヘンドリクス マリア スプルイト |
| 検出装置400、1100は、第1のストリームプローブを介する第2の流体30の通過の妨害に関する信号の測定、及び、少なくとも部分的な妨害に関する信号を、第2のストリームプローブ402を介する流体30の通過を妨害しない物体と相関する信号と比較することによる、物質が検出装置の対象又はユーザーの歯肉ではなく、物質が検出装置の対象又はユーザーの歯肉である偽のアラーム信号の生成ではないことの確認に基づき、表面31、33上の物質116の存在を検出する。信号は圧力、フローレート、及び歪みを含み得る。 | ||||||
| 102 | ミスト含有ガス分析装置 | JP2011284659 | 2011-12-27 | JP5762273B2 | 2015-08-12 | 岡本 真一; 長安 弘貢; 平田 琢也; 千代丸 勝; 田中 裕士 |
| 103 | 溶接プロセス中に不活性ガスをモニタリングする方法及び装置 | JP2015511860 | 2013-11-11 | JP2015516304A | 2015-06-11 | ヨハネス・ツィマー; ダビド・シャリンガー; マヌエル・グラーダウアー; ヘルムート・プフリュゲルマイアー |
| 本発明は、溶接トーチ(7)を用いて行われる溶接プロセス中に不活性ガス(5)をモニタリングする方法及び装置(30)に関する。不活性ガス(5)のタイプに依存する少なくとも1つの測定変数(Pi)が少なくとも1つのセンサ(Si)によって測定される。本発明によれば、上記不活性ガス(5)の少なくとも2つの測定変数(Pi)を測定し、上記不活性ガス(5)の上記少なくとも2つの測定変数(Pi)の測定された値(Mi)を、上記少なくとも2つの測定変数(Pi)の複数の格納された値(Mi’)であって、複数の不活性ガスタイプ(Gi)に関連付けられた値と比較し、上記不活性ガス(5)の上記少なくとも2つの測定変数(Pi)の測定された値(Mi)に最も近接する、上記少なくとも2つの測定変数(Pi)の割り当てられた値(Mi’)に係る不活性ガスタイプ(Gi)を表示する。 | ||||||
| 104 | 吸入器の抵抗を測定するための装置、システムおよび方法 | JP2011554210 | 2010-03-11 | JP5667095B2 | 2015-02-12 | アダモ，ブノワ; マクリーン，スコット; スムトニー，チャド・シー; ポリドロ，ジョン・エム; サヒ，カール・アール |
| 105 | Method and apparatus for identifying the chemical composition of the gas | JP2010520234 | 2008-08-01 | JP2010539443A | 2010-12-16 | ジョゼフ アール． モンコウスキー; バートン レーン |
| 本発明の態様は、1つまたは複数のガス、たとえば、プラズマエッチングまたはプラズマ強化化学蒸着（PECVD）などの半導体製造プロセスから採取されたガス混合物の成分分析に関する。 特定の態様は、多数の分子および分子断片を個々の原子に解離させるために、試料のプラズマに十分な電力を提供する。 十分な電力（典型的には3〜40 W/cm
3の出力密度）がプラズマに送出されると、発光ピークのほとんどが個々の原子の発光により生じ、それによって、試験されているガスの化学組成の同定を単純化するのに役立つスペクトルを作製することができる。 このようにガスの成分を正確に同定することによって、行われているプロセスの段階を正確に決定すること、特に、プロセスのエンドポイントを検出することができる。
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| 106 | Fuel property measuring device and the internal combustion engine of the internal combustion engine | JP2004230997 | 2004-08-06 | JP4260079B2 | 2009-04-30 | 典保 天野; 信彦 小山; 隆修 河野 |
| 107 | Fuel characteristics measuring device for internal combustion engine, and internal combustion engine | JP2004230997 | 2004-08-06 | JP2006046261A | 2006-02-16 | AMANO NORIYASU; KONO TAKANAGA; KOYAMA NOBUHIKO |
| <P>PROBLEM TO BE SOLVED: To detect volatility of fuel to set a correct air-fuel ratio. <P>SOLUTION: To a measuring passage 21 having a restrictor 22 in the middle, a gas current is generated by a pump 41, and a differential pressure sensor 55 is provided to detect differential pressure between both ends of the restrictor 22. Change-over valves 31 and 32 are provided on the measuring passage 21 to realize a first concentration measuring state in which the measuring passage 21 is opened at both ends to set atmospheric air for the gas current to the measuring passage 21, and a second concentration measuring state in which the measuring passage 21 is connected to a fuel tank 11 to set gas from the fuel tank 11 for the gas current to the measuring passage21. Concentration of vaporized fuel is detected based on detected differential pressure in the first concentration measuring state and detected differential pressure in the second concentration measuring state by an ECU 51. Volatility is determined based on concentration of the vaporized fuel, and temperature detected by a temperature sensor 56 provided on the fuel tank 11. <P>COPYRIGHT: (C)2006,JPO&NCIPI | ||||||
| 108 | Self-indicating method and apparatus for constant stimulation representation creation at the time of organizational change of the sensing state | JP2002531359 | 2001-09-25 | JP2004534287A | 2004-11-11 | デビッド エヌ レヴィン |
| 本発明の方法及び装置は、感知状態の組織的変化を引き起こす過程において刺激を不変的に表現する感知装置を含む。 このような過程は、１）本装置の検出器の変化、２）感知装置及び刺激の外部にある観察環境における変化、並びに、３）刺激そのものの表現におけるある種の変化を含む。 本発明の具体的一実施例は、このような表現「エンジン」から構成される「初期段階」を有する知的感知装置である。 上述した変化過程の存在を把握するために、再計測される必要がなく、そのパターン解析モジュールは再教育される必要がない。 本発明のその他の具体的実施例は、メッセージを信号の表現として復号する通信システムである。 送信装置、受信装置及び両者間の経路に影響を与えるさまざまな過程が原因で、メッセージが信号変化によって破損されることはない。 | ||||||
| 109 | Method and apparatus for measuring composition of multi-component mixed gas | JP2002369085 | 2002-12-20 | JP2004198328A | 2004-07-15 | KUROKAWA AKIRA; ICHIMURA SHINGO; NONAKA HIDEHIKO |
| PROBLEM TO BE SOLVED: To solve the problem that it has not been possible to measure an accurate mixture ratio (composition) when the pressure of multi-component mixed gases is not of the atmospheric pressure at measurement on the composition of the multi-component mixed gases and that it has not been possible to measure mixed gases which may pose explosion hazards by a measuring method by irradiating heat and light. SOLUTION: Constituent gases of the multi-component mixed gases are previously known such as the multi-component mixed gases of nitrogen, oxygen, and ozone, and their composition is univocally defined from the viscosity of the mixed gases. For simultaneous pressure measurement, an absolute pressure probe 1 such as a diaphragm gauge for measuring absolute pressure and a crystal friction vacuum gauge or a spinning rotor gauge sensitive to a material property value of gases such as viscosity or a pressure probe 2 sensitive to another material property value are connected to piping 4 of multi-component mixed gases in which the mixture ratio of ozone is not known. The true material property values of the multi-component mixed gases is determined from both pressure measurement values, their composition is determined from corresponding data of the material property values and composition. COPYRIGHT: (C)2004,JPO&NCIPI | ||||||
| 110 | Method and apparatus for measuring the para content of the hydrogen gas flow | JP3776995 | 1995-02-03 | JP3441547B2 | 2003-09-02 | マンフレード・ヴァナー |
| 111 | Monitor device | JP52472794 | 1994-05-06 | JPH08509815A | 1996-10-15 | ケネス ジヨン デイビー |
| (57)【要約】 構成要素又は構造体（１０）内の切迫した亀裂等を静的あるいは動的にモニターするためのモニター装置であり、一定真空源（１７）に接続された構成要素あるいは構造体上、又はその内部にシールされたキャビティ（１１）と、高インピーダンス流体装置（１５）を含んだキャビティ（１１）と真空源（１７）との間の接続部と、キャビティ（１１）と真空源（１７）との間の圧力変化をモニターするモニター手段（１８）とを含む。 | ||||||
| 112 | Method for measuring para-hydrogen content in hydrogen gas flow and its device | JP3776995 | 1995-02-03 | JPH07229887A | 1995-08-29 | MANFUREEDO BUANAA |
| PURPOSE: To determine a para-hydrogen content easily by measuring temperature and pressure of a gas flow before the hydrogen gas flow advances into a para- ortho converting catalyst, by having the gas flow pass through the catalyst till it reaches equilibrium, by measuring temperature and pressure of the gas flow discharged from the catalyst, and by calculating specific expressions. CONSTITUTION: A hydrogen gas flow supplied from a duct 1 is given heat- exchange to the temperature of a cooling medium in a heat exchanger 2 and made to pass through a connecting duct 3 to be supplied to a para-ortho catalyst 4. Temperature and pressure measuring devices T1 and T2 are provided each at an entrance and an exit of the catalyst 4. Suppose that the gas flow having advanced into the catalyst 4 with a temperature T1 and a pressure r1 passes through the catalyst 4 till equilibrium is achieved, and that a temperature T2 and a pressure r2 are gained at discharge. By using this and relational expressions in equilibrium state h1 (X1 , T1 , r1 )=h2 (X2 , T2 , r2 ) and X2 =Xg T2 (h1 , h2 ; enthalpies of the gas flow at the entrance and the exit of the catalyst 4), a para-hydrogen content X1 of the gas flow before advancing into the catalyst 4 is determined. | ||||||
| 113 | Method and apparatus for analyzing amount of dispersed air in liquid | JP16653291 | 1991-04-11 | JPH04230830A | 1992-08-19 | PAORO ZANERA |
| PURPOSE: To analyze the amt. of dispersed air in a liquid in nucleus forming air especially within the polyurethane component housed in a pressure tank. CONSTITUTION: An apparatus for measuring the amt. of dispersed air in a pressurized liquid sample is connected to a test cylinder having a freely slidable piston element 11 and a tank 14 housing a liquid analyzed through a control valve 18 on one side of the cylinder 10 and a first control means 19 supplies the signal corresponding to the liquid pressure in the tank 14 and a second control means 28 supplies the vol. data of the liquid sample and is connected to a water pressure source 21 in an operable manner on the other side of the test cylinder 10 and connected to a control unit CU controlling and calculating the vol. of dispersed air in the liquid sample in an operable manner. COPYRIGHT: (C)1992,JPO | ||||||
| 114 | Method and device for measuring steam pressure of liquid component | JP3856590 | 1990-02-21 | JPH02272341A | 1990-11-07 | DONARUDO BII RIIDO |
| PURPOSE: To measure a true steam pressure of a multi-component liquid by, with the use of an eductor device, allowing a liquid flaw through the eductor to increase, in acceleration, while a pressure difference in the eductor and a pressure at the in-take opening of the eductor are measured. CONSTITUTION: With initiation under a flow condition of a pipe flaw area where intrinsically no pressure drop takes place in the neck part of an eductor, while the pressure at an eductor in-take opening for each pressure difference condition is recorded, the flow is acceleratingly increased for obtaining a pressure difference in the eductor which successively becomes larger, for measuring a pressure difference in the eductar. Thus, an initiation of evaporation of maximum steam pressure component of a multi-component liquid, which is a true steam pressure of the liquid, is obtained accurately and easily. This is simple in mechanics and reliable, in addition, relatively non-complex and effective. COPYRIGHT: (C)1990,JPO | ||||||
| 115 | Jokiatsusokuteihoho | JP17639384 | 1984-08-24 | JPH0248857B2 | 1990-10-26 | SAEKI TOSHIO; TOKAWA JUNJI; ISHITOBI TAKESHI |
| 116 | Method and device for determining vapor pressure of liquid composition of crude oil and natural gas liqued | JP26555187 | 1987-10-22 | JPS63111442A | 1988-05-16 | ROIDO EI BEIRII; JIEEMUZU ERU SUKINAA |
| 117 | Humidity sensor | JP23344483 | 1983-12-09 | JPS60125539A | 1985-07-04 | TAKEUCHI KENZOU; KINOSHITA AKIRA |
| PURPOSE:To make a device small-sized and simple by burying a Peltier element in a heat insulating layer on the lower face side of a gas storage vessel and freezing and evaporating water in a gas to be measured in the same vessel. CONSTITUTION:The first solenoid valve 5 is connected to a gas introducing path 4a of a branch pipe 4 piercing a heat insulating layer 2 provided in a gas storage vessel 1 of a humidity sensor, and the second solenoid valve 6 is connected to a gas discharge path 4b, and a pressure sensor 7 is connected to a connecting path 4c, and a Peltier element 8 is buried in the heat insulating layer 2 on the lower face side of the vessel 1. The gas to be measured is introduced from a drier 9 into the vessel 1, and thereafter, power is supplied to the Peltier element 8 to cool the inside of the vessel 1, and water in the gas to be measured is frozen and is stuck to the wall surface of the heat insulating layer 2. The gas to be measured is discharged, and the inside of the vessel 1 is heated to evaporate water stuck to the wall surface, and a partial pressure of steam at a prescribed humidity is detected to measure an absolute humidity. | ||||||
| 118 | JPS5849818B2 - | JP4174375 | 1975-04-05 | JPS5849818B2 | 1983-11-07 | OORE GARUNE KURENERU; ERITSUKU NIIRUSEN |
| 119 | Measuring method of vapor density | JP4926682 | 1982-03-26 | JPS58166242A | 1983-10-01 | MIKI MASATOSHI |
| PURPOSE:To measure accurately the vapor density from a constant specified by a temperature and a pressure, by memorizing the most suitable constant at each temperature as a function of the temperature from a vapor density list in a domain being capable of approximating the vapor density to a prescribed expression using the pressure for a subordinate variable. CONSTITUTION:A vapor piping 1, a vapor temperature detector 2 and a pressure detector 3 are provided and temperature indicators 4, 5 indicating the temperature by receiving an output of the detector 2 and a pressure indicator 6 indicating the pressure by receiving the pressure of the detector 3 are provided. Arithmetic units 7, 8 storing constants (a) and (b) as a function of the temperature and outputting each value in accordance with each output of the indicators 4, 5, are provided and indicators 9, 10 are those for indicating the constants (a) and (b). The value of y=ax+b is operated by an arithmetic unit 11 by receiving the outputs (a) and (b) of the units 7, 8 and an output (x) of the indicator 6 and a vapor density (y) in a domain of superheated steam is computed. Further, the saturated vapor density corresponding to the output of the indicator 6 is computed. | ||||||
| 120 | Measuring device of boiler water concentrated state in boiler system | JP21505581 | 1981-12-28 | JPS58115342A | 1983-07-09 | FUJITA TADAO; TANIGUCHI SHIN; HIRAIWA ICHIROU |
| PURPOSE:To continuously measure the concentrated degree of boiler water without complicating the constitution of titled device by operating and determing an evaluation value having high correlation to the concentrated degree of the boiler water on the basis of the reference voltage falling period and reference voltage rising period of a boiler which are found by measurement and operation. CONSTITUTION:When an output from a pressure sensor 1a in a vapor pressure detecting part 1 is processed by comparators 1b, 1c and the vapor pressures of the boiler A reaches the lower limit or upper limit, the outputs of the comparators 1b, 1c are inverted and the inverted outputs are applied to a heating control part 2 which is an essential constituting element for boiler heating and adiabatic control. When outputs C1-C3 which are in the high level during the reference pressure falling period, the whole pressure falling period and the whole pressure rising period are generated from the control part 2 to measure the reference pressure falling period t2, the whole pressure falling period t2, the whole pressure rising period t1, etc. and calculate the reference pressure rising period t1 on the basis of the formulaI. The evaluation value K having high correlation to the concentrated degree of the boiler water is determined by operating the formula II, measuring the concentrated degree of the boiler water accurately and continuously without complicating the constitution of the device. | ||||||
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