序号 专利名 申请号 申请日 公开(公告)号 公开(公告)日 发明人
201 Volumetric flow corrector having a densitometer EP94100557.1 1994-01-15 EP0608736A2 1994-08-03 Vander Heyden, William H.

A method an apparatus for measuring a base condition volumetric flowrate of a pipeline gas flowing through a pipeline in which a pipeline gas flowrate is measured by a pipeline gas flowmeter; a volumetric correction ratio is derived by: measuring a sample gas flowrate of sample gas (12) tapped from the pipeline, measuring an energy flowrate of the sample gas (12), measuring a heating value of the sample gas (12), and measuring a base condition density of the sample gas (12); and the base condition volumetric flowrate of the pipeline gas flowing through the pipeline is determined by adjusting the pipeline gas flowrate as measured by the pipeline gas flowmeter by the volumetric correction ratio. The temperature of the sample gas (12) should be substantially the same as the pipeline gas in the pipeline when the sample gas flowrate is measured.

202 Flowmeter EP90312339.6 1990-11-13 EP0428364A1 1991-05-22 Drexel, Charles F.; Mudd, Daniel T.

A flowmeter has an elongated housing with a fluid inlet, a fluid outlet and an axial passage therebetween. The fluid passage contains a flow splitter section and is connected to a flow sensor assembly. The flow splitter section is formed by a surface defining a longitudinal fluid path and a flow splitter secured in the fluid path, so as to form an annular gap between the surface of the fluid path and the flow splitter.

The surface of the fluid path defines a tapered calibration bore. The flow splitter has a tapered calibration section comprising the upstream portion of the flow splitter and at least one tapered expansion section comprising the downstream portion of the flow splitter. The taper of the calibration section being substantially parallel to the taper of the calibration bore, and the taper of the expansion section diverges away from the taper of the calibration score.

In some embodiments, the surface of the fluid path defines a cylindrical bore located upstream of the calibration bore and the flow splitter has a cylindrical section located upstream of calibration section. In these embodiments, the flow splitter is adjustably secured in the fluid path between the cylindrical section and cylindrical bore. The flow splitter section provides fluid flows possessing excellent linearity over a wide range of flow rates, while minimizing the danger of contamination.

203 Flow sensor EP85111943.8 1985-09-20 EP0176051B1 1989-05-24 Kompelien, Arlon D.
204 Condition responsive sensing apparatus EP85103045.2 1985-03-16 EP0156271A1 1985-10-02 Bohrer, Philip J.; Johnson, Timothy L.; Higashi, Robert E.; Satren, Ernest A.

A condition responsive apparatus is provided with a sensor channel (20) that is interconnected to a capillary tube restriction (41) which can be readily interchanged on the device to change the response of a condition responsive sensor (30). A very small sensor (30) is placed in the sensor channel (20). The sensor channel (20) and the capillary tube (41) can be placed generally parallel to one another to reduce the overall length of the apparatus.

205 MULTIPHASE FLOW METERS AND RELATED METHODS PCT/US2016030165 2016-04-29 WO2016176596A9 2017-02-23 XIE CHENG-GANG; GERMOND BAPTISTE; JOLIVET GUILLAUME
Multiphase flow meters and related methods are disclosed herein. An example apparatus includes an inlet manifold; an outlet manifold, first and second flow paths coupled between the inlet and outlet manifolds; and an analyzer to determine a flow rate of fluid flowing through the first and second flow paths based on a parameter of the fluid flowing through the first flow path.
206 MEASUREMENT APPARATUS FOR MEASURING THE THROUGHFLOW OF A FLUID PCT/EP2012002220 2012-05-24 WO2012163500A2 2012-12-06 SCHAEFER BURGHARDT; CHU ANH TUAN
The present invention relates to a measurement apparatus, comprising a measurement tube (12; 112, 122) and a thermal sensor (20; 120) for measuring the throughflow of a fluid flowing through the measurement tube (12; 112), wherein the measurement tube (12; 112, 122) has an inlet (14; 114, 124) and an outlet (16; 116; 126), and also a measurement section (18; 118, 128), in which the sensor (20; 120) is arranged, wherein the inlet (14; 114, 124) has an inlet internal diameter and the measurement section (18; 118, 128) has a measurement section internal diameter and wherein the measurement section internal diameter is greater than the inlet internal diameter.
207 流量传感器组件 CN201620740341.7 2016-07-14 CN206488824U 2017-09-12 J.斯佩尔德里奇; R.C.索伦森
本实用新型涉及流量传感器组件,公开了一种流量传感器组件,包括限定入口端口、出口端口、主要通道和旁路通道的外壳。入流通道将所述流量传感器组件的所述入口端口流体连接到所述主要通道,并且出流通道将所述主要通道流体连接到所述出口端口。旁路馈流输入通道将所述主要通道流体连接到所述旁路通道,并且旁路馈流输出通道将所述旁路通道流体连接到所述主要通道。在一些情形中,穿过所述入流通道和所述出流通道总共下降施加在所述流量传感器组件的所述入口端口和所述出口端口之间的输入压差的至少百分之四十。传感器暴露于所述旁路通道中的流体并且感测与流动通过所述旁路通道的流体的流动速率有关的测量。
208 DURCHFLUSSMENGENMESSEINHEIT UND DURCHFLUSSMENGENSTEUEREINHEIT EP16195306.2 2016-10-24 EP3190391B1 2018-06-13 Bürgi, Stefan; Dänzer, Adrian; Bächler, Christoph
209 APPARATUS AND METHOD FOR DETECTING HEALTH DETERIORATION EP14780528.7 2014-10-03 EP3062682B1 2018-01-03 PEREZ DE ALEJO FORTUN, Rigoberto; FRANCO GAY, Mercedes
There is provided an apparatus for detecting the deteriorating health of a patient receiving gas from a respiratory device. The apparatus comprises a sensor unit configured to monitor a flow rate or pressure of a gas that is flowing in a pipe that connects the respiratory device to a gas delivery device worn by the patient, and a processor configured to measure a respiratory rate of the patient based on variations in the flow rate or pressure of gas in the pipe and to implement a trend analysis of the measured respiratory rate. The processor is configured to generate a warning when it determines that there is an upward trend in the measured respiratory rate and that a magnitude of the trend exceeds a threshold.
210 FLOW SENSOR ASSEMBLY WITH BYPASS CHANNEL EP16178737.9 2016-07-08 EP3118589A3 2017-01-25 SPELDRICH, Jamie; SORENSON, Richard C.

A flow sensor assembly includes a housing (12) that defines an inlet port (16), an outlet port (18), a main channel (22) and a bypass channel (28). An inlet flow channel (34) fluidly connects the inlet port (16) of the flow sensor assembly to the main channel (22) and an outlet flow channel (40) fluidly connects the main channel (22) to the outlet port (18). A bypass feeder input channel (46) fluidly connects the main channel (22) to the bypass channel (28) and a bypass feeder output channel (52) fluidly connects the bypass channel (28) to the main channel (22). In some instances, at least 40 percent of an input pressure differential applied between the inlet port and the outlet port of the flow sensor assembly drops across the inlet flow channel and the outlet flow channel collectively. A sensor (10) is exposed to a fluid in the bypass channel (28) and senses a measure related to a flow rate of the fluid flowing through the bypass channel. The housing (12) may be configured to accommodate a relatively high pressure drop between the inlet port (16) and the outlet port (18), while still providing a good flow measurement with relatively low noise, having laminar flow in the bypass channel, and a relatively small mounting footprint.

211 FLOW SENSOR ASSEMBLY WITH BYPASS CHANNEL EP16178737.9 2016-07-08 EP3118589A2 2017-01-18 SPELDRICH, Jamie; SORENSON, Richard C.

A flow sensor assembly includes a housing (12) that defines an inlet port (16), an outlet port (18), a main channel (22) and a bypass channel (28). An inlet flow channel (34) fluidly connects the inlet port (16) of the flow sensor assembly to the main channel (22) and an outlet flow channel (40) fluidly connects the main channel (22) to the outlet port (18). A bypass feeder input channel (46) fluidly connects the main channel (22) to the bypass channel (28) and a bypass feeder output channel (52) fluidly connects the bypass channel (28) to the main channel (22). In some instances, at least 40 percent of an input pressure differential applied between the inlet port and the outlet port of the flow sensor assembly drops across the inlet flow channel and the outlet flow channel collectively. A sensor (10) is exposed to a fluid in the bypass channel (28) and senses a measure related to a flow rate of the fluid flowing through the bypass channel. The housing (12) may be configured to accommodate a relatively high pressure drop between the inlet port (16) and the outlet port (18), while still providing a good flow measurement with relatively low noise, having laminar flow in the bypass channel, and a relatively small mounting footprint.

212 Flow measuring device EP10153809.8 2010-02-17 EP2270441B1 2014-10-15 Ueda, Naotsugu; Yamamoto, Katsuyuki; Maeda, Shuji; Tsuji, Yuji
213 Messvorrichtung mit einem Drucksensor EP13154409.0 2013-02-07 EP2626681A1 2013-08-14 Lück, Rudolf; Hackenberg, Peter

Die Erfindung betrifft eine Messvorrichtung mit einem Drucksensor, wobei der Drucksensor eine Messzelle (1) aufweist, die dazu ausgebildet ist, einen Druck zu erfassen. Es ist vorgesehen, dass die Messzelle (1) des Drucksensors in einer oder angrenzend an eine Schutzzelle (2, 2') angeordnet ist, die mit einem Messfluid (7) gefüllt ist, das über mindestens eine Trennmembran (3, 31, 32) mit einem zu messenden Fluid (8) koppelbar ist. Des Weiteren ist vorgesehen, dass in der Schutzzelle (2, 2') zwischen der Trennmembran (3, 31, 32) und der Messzelle (1) eine Dämpfungseinrichtung angeordnet ist, die eine Verengungsstruktur (4) und ein dahinter angeordnetes Volumenerweiterungsmittel (5) umfasst, das bei einer Druckerhöhung im Messfluid (7) ein vergrößertes Volumen zwischen der Verengungsstruktur (1) und der Messzelle (1) bereitstellt.

214 FLUID FLOW METER AND MIXER HAVING REMOVABLE AND REPLACABLE DISPLACEMENT MEMBER EP04780693 2004-08-10 EP1800090A4 2008-02-27 MCCALL FLOYD; PETERS ROBERT J W
A fluid flow meter (10), including a displacement member (40) removably mounted in a conduit (20) and a pipe extending through the wall of the conduit and having a portion extending through the displacement member to its downstream face for sensing flow conditions at the axis of the conduit downstream of the displacement member. The displacement member is removable and replacebly mounted so that one member can be replaced by another and thereby accommodate a very broad range of flows.
215 FLUID FLOW METER AND MIXER HAVING REMOVABLE AND REPLACABLE DISPLACEMENT MEMBER EP04780693.0 2004-08-10 EP1800090A1 2007-06-27 MCCALL, Floyd; PETERS, Robert, J., W.
A fluid flow meter (10), including a displacement member (40) removably mounted in a conduit (20) and a pipe extending through the wall of the conduit and having a portion extending through the displacement member to its downstream face for sensing flow conditions at the axis of the conduit downstream of the displacement member. The displacement member is removable and replacebly mounted so that one member can be replaced by another and thereby accommodate a very broad range of flows.
216 FLOWMETER EP97943458.6 1997-09-23 EP0876588B1 2007-05-02 SHAMBAYATI, Ali
A fluid flowmeter (10) comprises a frame (14) having a cavity that is open to one side thereof for the acceptance of a laminar flow module (16) and open to the other side for the acceptance of sensing electronics that measure pressure drop across the module. The module comprises a plurality of plates that are spaced apart by wires and bound to one another to form a unitary assembly that facilitates exchange and replacement.
217 FLOW AND PRESSURE SENSOR FOR HARSH FLUIDS EP02776275.6 2002-10-24 EP1440294A1 2004-07-28 BONNE, Ulrich; SPELDRICH, Jamie, W.
Methods and systems for preventing degradation of a sensor exposed to a harsh fluid, such as one that might corrode or be exposed to radioactive contaminants, live pathogens, freezing temperatures, overheating, particle deposition or condensable vapors is disclosed. An auxiliary purge stream of comparatively clean fluid or purge fluid is utilized, which flows past the sensor in opposition to the harsh fluid, thereby preventing the harsh fluid from contacting and degrading the sensor. The clean fluid itself may comprise a purge gas, such as clean, dry air, or a liquid that is compatible with the composition of the harsh fluid. The flow and pressure of the clean fluid can be adjusted utilizing one or more supply regulator valves.
218 Armatur zur hydraulischen Durchflussmessung EP99104569.1 1999-03-08 EP0943901B1 2002-12-18 Spiess, Fritz
219 Volumetric flow corrector having a densitometer EP94100557.1 1994-01-15 EP0608736A3 1995-06-14 Vander Heyden, William H.

A method an apparatus for measuring a base condition volumetric flowrate of a pipeline gas flowing through a pipeline in which a pipeline gas flowrate is measured by a pipeline gas flowmeter; a volumetric correction ratio is derived by: measuring a sample gas flowrate of sample gas (12) tapped from the pipeline, measuring an energy flowrate of the sample gas (12), measuring a heating value of the sample gas (12), and measuring a base condition density of the sample gas (12); and the base condition volumetric flowrate of the pipeline gas flowing through the pipeline is determined by adjusting the pipeline gas flowrate as measured by the pipeline gas flowmeter by the volumetric correction ratio. The temperature of the sample gas (12) should be substantially the same as the pipeline gas in the pipeline when the sample gas flowrate is measured.

220 Volumetric flow corrector and method EP93119396.5 1993-12-02 EP0608514A3 1995-06-14 Vander Heyden, William H.

A method and apparatus for measuring a base condition volumetric flowrate of a pipeline gas (14) flowing through a pipeline (16) in which a pipeline gas flowrate is measured by a pipeline gas flowmeter (22) that responds to density in a characteristic manner, a sample gas flowrate is measured by a sample gas flowmeter (10) that responds to density in the same manner as a pipeline gas flowmeter (22), and a base condition sample gas volumetric flowrate is measured by measuring the base condition energy flowrate of the sample gas (12), measuring the base condition heating value of the sample gas and dividing the base condition energy flowrate by the base condition heating value. The measured pipeline gas flowrate through the pipeline (16) is then adjusted by the ratio of the base condition sample gas flowrate divided by the measured flowrate of the sample gas (12). The temperature of the sample gas (12) should be substantially the same as the pipeline gas (14) in the pipeline when the sample gas flowrate is measured.

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