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51results about How to "Large flow range" patented technology

Electromagnetic flow sensor

The flow sensor serves to measure an electrically conductive fluid flowing in a pipe. It comprises a flow tube designed to be inserted into the pipe for conducting the fluid, the flow tube being electrically nonconductive at least on a fluid-contacting inner side, an electrode arrangement consisting of at least two measuring electrodes disposed on the flow tube for picking up a voltage induced in the fluid, and a magnetic field system likewise disposed on the flow tube. The magnetic field system comprises at least two saddle-shaped field coils for producing a magnetic field cutting the fluid during operation of the flow sensor, a respective ferromagnetic pole piece for each of the two field coils, as well as at least one ferromagnetic return path extending around the flow tube upstream of the two field coils and at least one ferromagnetic return path extending around the flow tube downstream of the two field coils for directing the magnetic field around the flow tube. The pole pieces are magnetically coupled to the return paths by means of ferromagnetic coupling elements. Each of the, preferably identically shaped, coupling elements has at least one essentially trough-shaped cover segment which receives a first winding section of the respective associated field coil, lying essentially on a first periphery of the flow tube, or a second winding section of the associated field coil, lying essentially on a second periphery of the flow tube.
Owner:ENDRESS HAUSER FLOWTEC AG

Electromagnetic flow sensor

The flow sensor serves to measure an electrically conductive fluid flowing in a pipe. It comprises a flow tube designed to be inserted into the pipe for conducting the fluid, the flow tube being electrically nonconductive at least on a fluid-contacting inner side, an electrode arrangement consisting of at least two measuring electrodes disposed on the flow tube for picking up a voltage induced in the fluid, and a magnetic field system likewise disposed on the flow tube. The magnetic field system comprises at least two saddle-shaped field coils for producing a magnetic field cutting the fluid during operation of the flow sensor, a respective ferromagnetic pole piece for each of the two field coils, as well as at least one ferromagnetic return path extending around the flow tube upstream of the two field coils and at least one ferromagnetic return path extending around the flow tube downstream of the two field coils for directing the magnetic field around the flow tube. The pole pieces are magnetically coupled to the return paths by means of ferromagnetic coupling elements. Each of the, preferably identically shaped, coupling elements has at least one essentially trough-shaped cover segment which receives a first winding section of the respective associated field coil, lying essentially on a first periphery of the flow tube, or a second winding section of the associated field coil, lying essentially on a second periphery of the flow tube.
Owner:ENDRESS HAUSER FLOWTEC AG

Maximum extended load line limit analysis for a boiling water nuclear reactor

A method for expanding the operating domain of a boiling water nuclear reactor that permits safe operation of the reactor at low core flows is described. The operating domain is characterized by a map of the reactor thermal power and core flow. In an exemplary embodiment, the method for expanding the operating domain of a boiling water nuclear reactor permits operation of the reactor between about 120 percent of rated thermal power and about 85 percent of rated core flow to about 100 percent of rated thermal power and about 55 percent of rated core flow. The method includes determining an elevated load line characteristic that improves reactor performance, performing safety evaluations at the elevated load line to determine compliance with safety design parameters, and performing operational evaluations at the elevated load line. The method also includes defining a set of operating conditions for the reactor in an upper operating domain characterized by the elevated load line. Additionally, the method includes performing a detailed analysis of the performance of the core recirculation system and the system control components. further, the method provides for modifying the reactor process controls and computers to permit the reactor to operate in the expanded operating domain within predetermined safety parameters. Also, safety mitigation action setpoints are adjusted to permit reactor operation in the expanded operating domain.
Owner:GENERAL ELECTRIC CO

Maximum extended load line limit analysis for a boiling water nuclear reactor

A method for expanding the operating domain of a boiling water nuclear reactor that permits safe operation of the reactor at low core flows is described. The operating domain is characterized by a map of the reactor thermal power and core flow. In an exemplary embodiment, the method for expanding the operating domain of a boiling water nuclear reactor permits operation of the reactor between about 120 percent of rated thermal power and about 85 percent of rated core flow to about 100 percent of rated thermal power and about 55 percent of rated core flow. The method includes determining an elevated load line characteristic that improves reactor performance, performing safety evaluations at the elevated load line to determine compliance with safety design parameters, and performing operational evaluations at the elevated load line. The method also includes defining a set of operating conditions for the reactor in an upper operating domain characterized by the elevated load line. Additionally, the method includes performing a detailed analysis of the performance of the core recirculation system and the system control components. further, the method provides for modifying the reactor process controls and computers to permit the reactor to operate in the expanded operating domain within predetermined safety parameters. Also, safety mitigation action setpoints are adjusted to permit reactor operation in the expanded operating domain.
Owner:GENERAL ELECTRIC CO

Gas-liquid-sand mixed fluid automatic desanding system for natural gas extraction

A gas-liquid-sand mixed fluid automatic desanding system for natural gas extraction comprises a shell and a desanding feeding port in the shell, a main separation cavity communicating with the desanding feeding port is formed in the shell, a first liquid discharging port and a sand discharging port are formed below the desanding feeding port, and the sand discharge port is connected with an automatic sand discharge branch; and a sand discharging system further comprises an automatic control system, the automatic control system comprises a controller, a sand level detector and a liquid level detector, the sand level detector and the liquid level detector are connected with the controller, the sand level detector is installed below the main separation cavity, the liquid level detector is installed between the installation height of the sand level detector and the installation height of the sand discharging opening, and the automatic sand discharging branch is controlled by the controller. By arranging a sensor and the control system, sand can be automatically discharged according to the stacking height in a sand remover, the whole sand discharging process is fully automatically completed, and manual operation is greatly reduced; and liquid is discharged through the liquid outlet, so that the desilting operation frequency and the subsequent sand-liquid separation work are reduced. By arranging a cyclone sand discharger, the equipment adaptability is improved, the advantages of gravity settling and cyclone separation are integrated, and the flow adaptation range is large.
Owner:成都汇川新能科技有限公司 +1

Marine steam flow measuring device and method

The invention provides a marine steam flow measuring device and method. The device comprises a flow measuring assembly and a flow converter, the flow measuring assembly is composed of a throttle pipesection, a pressure guide pipe, a valve set and a sensor assembly, connecting flanges are arranged at the two ends of the throttle pipe section, two ends of the throttle pipe section are connected with a steam pipeline, and the sensor assembly is provided with a pressure sensor and three differential pressure sensors with different measuring ranges and is connected to the throttle pipe section through the valve set and the pressure guide pipe; and the flow converter comprises a shell, a signal acquisition module, a signal processing module and a power module are arranged in the shell, a display screen is arranged on the front face of the shell, and a plurality of electric connectors are arranged on the two side faces of the shell and are connected with an external power source, the sensorassembly and an upper computer respectively. The straight pipe section of the flow measuring assembly is short, other special requirements of the straight pipe sections on the upstream and the downstream are avoided, and saturated steam measurement can be conducted in a narrow space of a ship.
Owner:CHINA SHIP DEV & DESIGN CENT

Parallel structure and detection method of dual-gas flow standard device

The invention provides a parallel structure and detection method of dual-gas flow standard device, and relates to the technical field of measurement. The gas source is connected with a tested flow meter, and the tested flow meter is respectively connected with a bell jar and a standard gas flowmeter through a tee joint; the gas accumulation amount of the bell jar, the standard gas flow meter and the tested flow meter is calculated through the pulse calculation, the gas accumulation amount of the bell jar and the standard gas flow meter is converted into the gas accumulation amount under the pressure and temperature state of the tested flow meter and is added to obtain a standard gas magnitude, and the measured flow meter value error is calculated according to the gas accumulation amount ofthe tested flow meter. The parallel structure and detection method of dual-gas flow standard device solves the technical problems that in the prior art, only the 'single type' standard device value is adopted, the flow range cannot be expanded, and the pressure loss is large. The parallel structure and detection method of dual-gas flow standard device has the advantages that different detection methods are achieved on the same set of devices, and meanwhile, the method is applied to the operation process; compared with a single or serial standard device, the flow range is larger; the test is richer than that of the method; the pressure loss is smaller.
Owner:GUANGZHOU INST OF ENERGY TESTING

Urea condensate pump

The invention discloses a urea condensate pump. The pump comprises a first shaft and a second shaft which are arranged coaxially, wherein the right end of the first shaft is detachably connected with the left end of the second shaft; a bearing sleeve, a third shaft sleeve and a couplingsleevesthe second shaft in sequence from the left end of the second shaft; a bearing seat and a bearing seat end cover connected with the bearing seat sleeve the bearing sleeve and the third shaft sleeve separately; a bearing sleeves the third bearing sleeve, and the axial movement of the bearing along the third shaft sleeve is limited by a round nut; the bearing seat end covercommunicateswith a bend pipe; the second shaft is sleeved by a stopper ring, a second shaft sleeve and a fixed sleeve from the left end to the right end; the second shaft sleeve is sleeved by a first shaft sleeve, a spring, a movable ring, a static ring and a cooling sleeve from the left end to the right end; a first pipe joint communicatingwith the side wall of the cooling sleeve is a coolant inlet, a second pipe joint communicatingwith the side wall of the first shaft sleeve is an outlet; a pump port, an impeller sleeve, an impeller and a medium shell sleeve the first shaft in sequence from the left end; a diversion disk communicating with the pump outlet sleeves the impeller sleeve by the bearing; and the axial movement of the impeller along the first shaft is limited by a fourth screw.
Owner:陕西奥维乾元化工有限公司

Double standard gas flow device parallel structure and detection method

ActiveCN110160609AEliminate the influence of installation factorsLarge flow rangeTesting/calibration apparatusSingle typeEngineering
The invention provides a double standard gas flow device parallel structure and a detection method, and relates to the technical field of measurement. A gas source is connected to a to-be-detected flowmeter. The to-be-detected flowmeter is connected to a bell jar and a standard gas flowmeter through a tee joint. Gas accumulation amount of the bell jar, the standard gas flowmeter and the to-be-detected flowmeter through pulse. The gas accumulation amount of the bell jar and the standard gas flowmeter is converted into gas accumulation amount of the to-be-detected flowmeter under pressure and temperature, and the gas accumulation amount of the bell jar and the standard gas flowmeter and the gas accumulation amount of the to-be-detected flowmeter under pressure and temperature are added together to obtain a standard gas volume value. A to-be-detected flowmeter value error is obtained by calculation of the gas accumulation amount of the to-be-detected flowmeter. The double standard gas flow device parallel structure and the detection method solve the technical problems in the prior art that a standard device only uses a ''single type'' standard device value, a flow range cannot be expanded and the pressure loss is large. The double standard gas flow device parallel structure and the detection method have the beneficial effects that different detection methods are implemented on thesame set of device and applied in calculation processes, the flow range is large, the pressure loss is small, and the device calibrates single points of the standard gas flowmeter on line, which eliminates mounting errors.
Owner:GUANGZHOU INST OF ENERGY TESTING

A urea condensate pump

The invention discloses a urea condensate pump. The pump comprises a first shaft and a second shaft which are arranged coaxially, wherein the right end of the first shaft is detachably connected with the left end of the second shaft; a bearing sleeve, a third shaft sleeve and a couplingsleevesthe second shaft in sequence from the left end of the second shaft; a bearing seat and a bearing seat end cover connected with the bearing seat sleeve the bearing sleeve and the third shaft sleeve separately; a bearing sleeves the third bearing sleeve, and the axial movement of the bearing along the third shaft sleeve is limited by a round nut; the bearing seat end covercommunicateswith a bend pipe; the second shaft is sleeved by a stopper ring, a second shaft sleeve and a fixed sleeve from the left end to the right end; the second shaft sleeve is sleeved by a first shaft sleeve, a spring, a movable ring, a static ring and a cooling sleeve from the left end to the right end; a first pipe joint communicatingwith the side wall of the cooling sleeve is a coolant inlet, a second pipe joint communicatingwith the side wall of the first shaft sleeve is an outlet; a pump port, an impeller sleeve, an impeller and a medium shell sleeve the first shaft in sequence from the left end; a diversion disk communicating with the pump outlet sleeves the impeller sleeve by the bearing; and the axial movement of the impeller along the first shaft is limited by a fourth screw.
Owner:陕西奥维乾元化工有限公司

Sand supply instrument for slope-variable water flume

The invention relates to a sand supply instrument for a slope-variable water flume. The sand supply instrument comprises lifting platforms, a first water supply tank, a sand supply groove, a sand supply device and a second water supply tank, wherein the lifting platforms comprise a first lifting platform and a second lifting platform; the first lifting platform is higher than the second lifting platform; the height difference between the first lifting platform and the second lifting platform is the vertical height of the sand supply groove; the first water supply tank is horizontally placed on the first lifting platform, and the second water supply tank is horizontally placed on the second lifting platform; the upper end of the sand supply groove is hermetically connected with the water outlet side surface of the first water supply tank; the lower end of the sand supply groove is connected with the water inlet end of the second water supply tank; a cambered transitional belt is arranged at the other end of the second water supply tank; the transitional belt is joined with the slope-variable water flume; the sand supply device is arranged over the sand supply groove and provides test silt required by the sand supply groove for the sand supply groove. The sand supply instrument can be connected with the slope-variable water flume by adjusting the heights of the lifting platforms, sand is added to the sand supply groove through the sand supply device, water flow containing sand is generated in the sand supply groove, and the water flow falls on the slope-variable water flume through the water supply tank. Thus, the sand content of the water flow can be well controlled, and the purpose of controlling the sand content of the water flow is achieved.
Owner:BEIJING FORESTRY UNIVERSITY

A two-phase bubbly flow mixing device and method at the bottom inlet of a vertical rod bundle channel

A two-phase bubbly flow mixing device and method at the bottom inlet of a vertical rod bundle channel. The auxiliary water inlet area composed of the auxiliary water inlet chamber, the filter element structure composed of the filter element circular tube section, the filter element transition section and the filter element porous section, and the device consisting of the upper and lower pipe seats of the device, the filter element casing, the filter element fixing plate and the filter element casing fixing plate Support and fixed structure; after the gas enters from the round pipe section of the filter element, it flows out from the porous section of the filter element through the transition section of the filter element and mixes with the auxiliary water inlet to flow upward. The gas-liquid two-phase formed by mixing is then mixed with the main water inlet. Obtain bubbly two-phase flow with different gas content, and finally enter the rod bundle channel area; the present invention can obtain a larger range of bubbly two-phase flow, satisfying the two-phase bubbly flow for different vapor content in the rod bundle channel Experimental requirements; in addition, the present invention also has the advantages of simple operation, high stability, and easy processing and installation of the device.
Owner:XI AN JIAOTONG UNIV
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