| 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 | Device for controlling flow rate of fluid | JP13334781 | 1981-08-27 | JPS5835419A | 1983-03-02 | SANO SHIGERU; SAKURAI KATSUMI; ONO TATSUO; ATAGO KAZUO; NOGUCHI HARUHIRO |
| PURPOSE:To make it possible to control the flow rate over the broad range, by providing a orifice for measuring a large flow rate and an orifice for measuring a small flow rate, measuring the flow rate by changing the orifice in response to the flow rate, thereby controlling flow rate. CONSTITUTION:The flow rate of gas is measured by the orifice 3g for measuring the large from rate and the orifice 4g for measuring the small flow rate. The measured result is outputted from a flow rate oscillator 13g and inputted to an operating device 9. The operating device outputs the operated result, and a regulating valve 8g is controlled. When the amount of the gas is reduced owing to an accident and the like, a first cut off valve 7g is closed by the output of the operating device, and flow rate is measured by only the orifice 4g for measuring the small flow rate. The flow rate is controlled by regulating the regulating valve 8g. In this way, the flow rate is controlled from the large flow rate to the small flow rate. | ||||||
| 82 | Flow rate measuring method | JP10151881 | 1981-06-30 | JPS582706A | 1983-01-08 | HATSUTORI TAKAAKI |
| PURPOSE:To make a high-precision measurement possible with a single measurer independently of the magnitude of flow rate, by installing plural pressure taking- out points in a flow passage and switching them to connect them to a differential pressure measurer in accordance with the flow rate. CONSTITUTION:Plural pressure taking-out points are installed in a flow passage, and a set of pressure taking-out points to be selected is determined in accordance with the flow rate of a fluid, and pressure values of the selected set of pressure taking-out points are measured to calculate the flow rate of the fluid. For example, by the switching of a three-way cock 8, a differential pressure P1- P2 between pressures at pressure taking-out points A and D is applied to a differential pressure measurer 7 for a low flow rate, and a differential pressure P1-P3 between pressures at pressure taking-out points A and G is applied to the measurer 7 for a high flow rate. The flow rate is measured by the permanent pressure loss method for a high flow rate, and the method is switched to the vena tap method to measure the flow rate for a low flow rate. | ||||||
| 83 | Measuring device for refrigerating performance | JP15765380 | 1980-11-11 | JPS5782715A | 1982-05-24 | HATORI MITSUO; NAGATOMO SHIGEMI |
| PURPOSE:To measure wide-range refrigerating performance precisely and easily by providing valves before or after orifices arranged in parallel to a flow passage, and providing by-pass pipes, which have valves, before and after the orifices. CONSTITUTION:At a low pressure side between a compressor 1 and a heat exchanger 6, orifices 9 and 10 differing in diameter are provided in parallel. First, valves 11 and 12 provided before the orifices 9 and 10 are closed, and the valve 14 of a by-pass pipe 13 is opened, constituting a cycle. Then, the valve 12 before the orifice 10 for the large quantity of flow is opened, and the valve 14 of the by-pass pipe 13 is closed gradually, constituting a cycle. When the quantity of flow has a margin, the valve 14 of the by-pass pipe 13 is opened, and the valve 12 is closed; and the valve 11 of the orifice 9 for the small quantity of flow is opened, and the valve 14 is closed gradually, constituting a cycle. Thus, wide- range refrigerating performance is measured precisely and easily. | ||||||
| 84 | Measuring device for refrigerating performance | JP15765280 | 1980-11-11 | JPS5782714A | 1982-05-24 | HATORI MITSUO; NAGATOMO SHIGEMI |
| PURPOSE:To realize a small-sized, inexpensive device and to eliminate the need for correction, by measuring differential pressure by only one differential pressure gauge even when orifices are changed over during cycle operation. CONSTITUTION:Between a heat exchanger 6 and a compressor 1, two orifices 9 and 10 and a differential pressure gauge 15 are provided. First, valves 11 and 12 provided in front of the orifices 9 and 10 are closed and the valve 14 of a by- pass pipe 13 is opened, constituting a cycle. In this case, differential pressure gate valves 19-22 are closed. Then, the differential gate valves 21 and 22 of the orifice 10 for the large quantity of flow are opened, the valve 12 is opened, and the valve 14 of the by-pass pipe 13 is closed gradually, constituting a cycle. When the quantity of flow has a margin, the valve 14 is opened, and the valves 12, 21 and 22 are closed; and the valve 11 of the orifice 9 for the small quantity of flow and the differential pressure gate valves 19 and 20 are opened, and the valve 14 is closed gradually, constituting a cycle. Consequently, a small-sized, inexpensive device is realized and correction is unnecessary. | ||||||
| 85 | 測定範囲が拡張された統合型の流量測定プローブ | JP2017517109 | 2015-09-10 | JP6351839B2 | 2018-07-04 | メスナード,デイヴィッド,ラッセル; ストローム,グレゴリー,ロバート; ケニヨン,ナサニエル,カーク |
| 86 | 測定範囲が拡張された統合型の流量測定プローブ | JP2017517109 | 2015-09-10 | JP2017530364A | 2017-10-12 | メスナード，デイヴィッド，ラッセル; ストローム，グレゴリー，ロバート; ケニヨン，ナサニエル，カーク |
| 流量測定プローブ(300)は、その長さ方向に沿って配置された複数の上流側および下流側の開口部(303)を有する平均ピトー管(302)を有する細長いプローブと、前記細長いプローブに結合された熱流測定センサ(304)とを含む。プロセスにおいて流体流量を測定する方法は、差圧が少なくとも規定された測定閾値であるときに細長いプローブ内の平均ピトー管(302)の上流側および下流側の開口部(303)の差圧を使用して流体流量を計算することと、差圧が規定された測定閾値未満であるときに、流量測定プローブ(300)に結合された熱式質量流量センサ(304)を用いて流体流量を計算するステップとを含む。 | ||||||
| 87 | Flow rate measuring device | JP2008058789 | 2008-03-07 | JP5294388B2 | 2013-09-18 | 健一 賀門; 肇 宮田; 陽一 伊藤; 龍志 岩本; 大介 別荘 |
| Detecting a leak, or the like, with high accuracy on the basis of pressure and a flow volume acquired during use of fluid is made possible. A volume of gas flowing through a flow path 102 is measured by a flow volume measurement unit 106, and pressure is measured by a pressure measurement unit 108. Measured flow data and measured pressure data are input to an analysis unit 112, to thus analyze following of a pressure change by a flow volume change. An amount of flow volume change responsive to an amount of pressure change of a predetermined level or more is classified into a plurality of ranges by means of a predetermined threshold value, and a following flow value change is determined on the basis of determination conditions of the respective ranges of amounts of flow volume changes. | ||||||
| 88 | Calibration method of flow rate controller for gas supply device and flow rate measuring method | JP2010171626 | 2010-07-30 | JP2012032983A | 2012-02-16 | NAGASE MASAAKI; IKEDA SHINICHI; SAWADA YOHEI; HIRAI NOBORU; MORISAKI KAZUYUKI; NISHINO KOJI; DOI RYOSUKE |
| PROBLEM TO BE SOLVED: To provide a flow rate calibration method of flow rate controller by a build-up (or ROR) method which can be more rapidly performed with high precision by a downsized calibration unit.SOLUTION: A calibration unit 5, which comprises a build-up tank BT, on-off valves V, V, a temperature detector Td, and a pressure detector Pd, is branchedly connected to a gas supply passage L, and the on-off valve Vis connected to a vacuum evacuation device. At first, respective on-off valves Voto Voof flow rate controllers and an on-off valve Vo at a gas usage part are closed and the on-off valves Vo, Voare opened. Then, only an on-off valve of a flow rate controller to be calibrated is opened to allow a set flow rate of gas to flow into the calibration unit 5, and at a time tgas temperature and gas pressure in the tank are measured. Thereafter, the on-off valve V, is closed and build-up of the gas in the tank BT is carried out. At a time tthe on-off valve Vis closed, and at a time tgas temperature and gas pressure are measured. Then, a flow rate of gas Q is calculated from measured values and flow rate calibration is performed by comparing the set flow rate of gas with the calculated flow rate of gas Q. | ||||||
| 89 | Flow rate range variable type flow control device | JP2005185845 | 2005-06-27 | JP4856905B2 | 2012-01-18 | 和幸 三浦; 智一 今井; 俊英 吉田; 亮介 土肥; 忠弘 大見; 強 嶋津; 薫 平田; 隆 広瀬; 雅仁 斎藤; 昭一 日野; 勝幸 杉田; 正明 永瀬; 信一 池田; 久士 田中; 努 篠原; 功二 西野 |
| 90 | System and method for measuring a flow rate | JP2007546711 | 2005-11-29 | JP2008524585A | 2008-07-10 | タイソン，スチュアート・エイ; リュー，シリアン |
| この発明の一実施例は、一次流量測定システムと、当該一次流量測定システムと流体連通している二次流量測定システムと、一次流量測定システムおよび二次流量測定システムに結合されたコントローラとを含み得る。 当該コントローラは、プロセッサと、当該プロセッサがアクセス可能なメモリとを含み得る。 当該プロセッサは、第１の動作モードでは、一次流量測定システムを用いて流量を算出し、第２の動作モードでは、二次流量測定システムを用いて流量を算出するよう、当該メモリに記憶されたコンピュータ命令を実行し得る。 当該コンピュータ命令はさらに、予め規定されたパラメータに基づいて第１の動作モードと第２の動作モードとを切替えるよう実行可能であり得る。 | ||||||
| 91 | Flow rate range variable flow control device | JP2005185845 | 2005-06-27 | JP2007004644A | 2007-01-11 | OMI TADAHIRO; SAITO MASAHITO; HINO SHOICHI; SHIMAZU TSUTOMU; MIURA KAZUYUKI; NISHINO KOJI; NAGASE MASAAKI; SUGITA KATSUYUKI; HIRATA KAORU; DOI RYOSUKE; HIROSE TAKASHI; SHINOHARA TSUTOMU; IKEDA SHINICHI; IMAI TOMOKAZU; YOSHIDA SHUNEI; TANAKA HISASHI |
| <P>PROBLEM TO BE SOLVED: To miniaturize a flow control device and to reduce the facility cost by enabling accurate flow control of a fluid in a further wide flow area by use of one flow control device. <P>SOLUTION: The pressure type flow control device is adapted to calculate the flow rate of a fluid passing through an orifice 8 using an orifice upstream pressure P<SB>1</SB>and/or an orifice downstream pressure P<SB>2</SB>as Qc=KP<SB>1</SB>(K is a proportionality factor) or Qc=KP<SB>2</SB><SP>m</SP>(P<SB>1</SB>-P<SB>2</SB>)<SP>n</SP>(K is a proportionality factor, and m and n are constant numbers). In this pressure type flow control device, a fluid passage between the downstream side of a control valve and a fluid supplying conduit is formed of at least two or more parallel fluid passages, and orifices differed in fluid flow characteristic are interposed in the parallel fluid passages, respectively. The fluid in a small flow area is distributed to one orifice in flow control of the fluid in the small flow area, and the fluid in a large flow area is switchingly distributed to the other orifice in flow control of the fluid in the large flow area. <P>COPYRIGHT: (C)2007,JPO&INPIT | ||||||
| 92 | Flowmeter and measurement method of the high void fraction of multiphase fluid flow | JP26082595 | 1995-09-13 | JP3453228B2 | 2003-10-06 | ジョラム・アガール; デビット・ファーチ |
| 93 | Aerosol distributor | JP20505896 | 1996-08-02 | JPH09164205A | 1997-06-24 | LLOYD PETER M; RITSON CARL; JOHANSSON ERIC T; RUBSAMEN REID M |
| PROBLEM TO BE SOLVED: To supply medicines conforming to the scale of respiratory pattern of patient by actuating the discharge of aerosol medicines into a tube based on a signal to be transmitted after the decision of respiratory flow corresponding to the distribution value of medicines based on information from a flow transducer. SOLUTION: This device is provided with a canister 3200 for selected medicines having a specified code, nozzle 3160 for deciding the medicines of canister 3200 based on the specified code, discharging the medicines from there to a sucked air duct 3140 of tube 3141 and making the medicines into aerosol, and flow sensor 3300 for measuring the respiratory flow of patient through the tube 3141. Based on the information from the flow sensor 3300, a microprocessor calculates the distribution value of medicines and decides the respiratory flow of patient corresponding to that distribution value and based on the reception of signal transmitted later, an aerosol supply system 3130 starts discharging the medicines through the nozzle 3160 into the tube 3141 while using a solenoid valve 3150. | ||||||
| 94 | JPH05506598A - | JP50743992 | 1992-03-03 | JPH05506598A | 1993-09-30 | |
| Apparatus and methods for delivering an amount of aerosolized medicine for inspiration by a patient in response to the occurrence of appropriate delivery point or points in the patient's detected breath flow. The aerosol medication may be administered as one or more pulses having a pulse width, shape, and frequency that will maximize the respirable fraction of the aerosolized compound being administered. The delivery point or points may be predetermined or determined from a prior inspiratory flow for depositing the selected medication at one or more desired locations in the patient's airway. Determined delivery points are recursively lowered for each inspiratory flow that does not satisfy one of the predetermined and previously lowered threshold. Changes in the patient's breath flow patterns during the course of an aerosolized medication inspiration therapy program may be detected and used to adjust the controlled amount of medication to be delivered in a given administration and/or to inform the patient of the patient's condition or change in condition. The device also may contain a library of administration protocols or operating parameters for different medications and a means for identifying from the canister the medicinal contents of the canister for customizing operation of the apparatus. | ||||||
| 95 | Instrument for measuring and controlling flow rate and heating value | JP8150190 | 1990-03-30 | JPH03202743A | 1991-09-04 | PEETAA RIISU; PAURU NAUAA; BUORUFUGANKU FUUBAA |
| PURPOSE: To measure the flow rate or heating value of a fluid with sufficiently high accuracy by inputting a prescribed signal indicating the target value of a flow rate or heating value to be outputted and converting the signal into a signal indicating the presence/absence of a pulse, and then, driving a constricting device with the signal. CONSTITUTION: A prescribed signal which is proportional to the target value of a flow rate/heating value to be outputted is supplied to the input terminal E of a computer 14. The signal is converted into a signal indicting the presence/absence of a pulse by means of a converter 36. As the flow rate/heating value to be outputted becomes larger, individual pulses outputted from the converter 36 becomes longer and no-pulse periods become shorter. When, for example, a signal '0.8' is impressed upon the terminal E and a pulse signal is outputted from a clock generator 37, an H-level signal is generated at an output terminal 44. Consequently, the H-level pulse appears at an output terminal 19 and a motor 3 moves the constricting device 4 to an releasing (opening 5) position by controlling the device 4. When the input signal has a value between '0' and '1' in such a way, the device 4 is released for a different period in accordance with the length of the signal. COPYRIGHT: (C)1991,JPO | ||||||
| 96 | Flow-rate sensor, low flow-rate range thereof is extended | JP21346182 | 1982-12-07 | JPS58144713A | 1983-08-29 | RONARUDO BAANAADO WARUTAASU |
| 97 | Flow Rate Measurement System | US15891635 | 2018-02-08 | US20180224311A1 | 2018-08-09 | Toshihito Ueda; Jun Tanaka; Shinsuke Kawamura |
| A flow rate measurement system measures, by using a flow rate measurement device, a flow rate of cleaning gas in a container storage facility including a storage rack including supporting portions; a transport device that transports a container to the supporting portions; and a gas supply device that supplies the cleaning gas to the container supported by the supporting portions. The transport device and the flow rate measurement device are connected via a power line communicatively by wire or wireless. The flow rate measurement device measures the flow rate of the cleaning gas in a state in which the transport device has transported the flow rate measurement device and the flow rate measurement device is placed on a target supporting portion. | ||||||
| 98 | Flow rate range variable type flow rate control apparatus | US15171333 | 2016-06-02 | US09921089B2 | 2018-03-20 | Tadahiro Ohmi; Masahito Saito; Shoichi Hino; Tsuyoshi Shimazu; Kazuyuki Miura; Kouji Nishino; Masaaki Nagase; Katsuyuki Sugita; Kaoru Hirata; Ryousuke Dohi; Takashi Hirose; Tsutomu Shinohara; Nobukazu Ikeda; Tomokazu Imai; Toshihide Yoshida; Hisashi Tanaka |
| A pressure type flow rate control apparatus is provided wherein flow rate of fluid passing through an orifice is computed as Qc=KP1 (where K is a proportionality constant) or as Qc=KP2m (P1-P2)n (where K is a proportionality constant, m and n constants) by using orifice upstream side pressure P1 and/or orifice downstream side pressure P2. A fluid passage between the downstream side of a control valve and a fluid supply pipe of the pressure type flow rate control apparatus comprises at least 2 fluid passages in parallel, and orifices having different flow rate characteristics are provided for each of these fluid passages, wherein fluid in a small flow quantity area flows to one orifice for flow control of fluid in the small flow quantity area, while fluid in a large flow quantity area flows to the other orifice for flow control of fluid in the large flow quantity area. | ||||||
| 99 | FLOW RATE RANGE VARIABLE TYPE FLOW RATE CONTROL APPARATUS | US15171333 | 2016-06-02 | US20160274595A1 | 2016-09-22 | Tadahiro Ohmi; Masahito Saito; Shoichi Hino; Tsuyoshi Shimazu; Kazuyuki Miura; Kouji Nishino; Masaaki Nagase; Katsuyuki Sugita; Kaoru Hirata; Ryousuke Dohi; Takashi Hirose; Tsutomu Shinohara; Nobukazu Ikeda; Tomokazu Imai; Toshihide Yoshida; Hisashi Tanaka |
| A pressure type flow rate control apparatus is provided wherein flow rate of fluid passing through an orifice is computed as Qc=KP1 (where K is a proportionality constant) or as Qc=KP2m(P1−P2)n (where K is a proportionality constant, m and n constants) by using orifice upstream side pressure P1 and/or orifice downstream side pressure P2. A fluid passage between the downstream side of a control valve and a fluid supply pipe of the pressure type flow rate control apparatus comprises at least 2 fluid passages in parallel, and orifices having different flow rate characteristics are provided for each of these fluid passages, wherein fluid in a small flow quantity area flows to one orifice for flow control of fluid in the small flow quantity area, while fluid in a large flow quantity area flows to the other orifice for flow control of fluid in the large flow quantity area. | ||||||
| 100 | Flow rate range variable type flow rate control apparatus | US14977162 | 2015-12-21 | US09383758B2 | 2016-07-05 | Tadahiro Ohmi; Masahito Saito; Shoichi Hino; Tsuyoshi Shimazu; Kazuyuki Miura; Kouji Nishino; Masaaki Nagase; Katsuyuki Sugita; Kaoru Hirata; Ryousuke Dohi; Takashi Hirose; Tsutomu Shinohara; Nobukazu Ikeda; Tomokazu Imai; Toshihide Yoshida; Hisashi Tanaka |
| A pressure type flow rate control apparatus is provided wherein flow rate of fluid passing through an orifice is computed as Qc=KP1 (where K is a proportionality constant) or as Qc=KP2m(P1−P2)n (where K is a proportionality constant, m and n constants) by using orifice upstream side pressure P1 and/or orifice downstream side pressure P2. A fluid passage between the downstream side of a control valve and a fluid supply pipe of the pressure type flow rate control apparatus comprises at least 2 fluid passages in parallel, and orifices having different flow rate characteristics are provided for each of these fluid passages, wherein fluid in a small flow quantity area flows to one orifice for flow control of fluid in the small flow quantity area, while fluid in a large flow quantity area flows to the other orifice for flow control of fluid in the large flow quantity area. | ||||||
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