A gas flow measuring method is provided. A first pressure of a gas in a first and a second flow path is measured. A gas is supplied to the first and the second flow paths by repeating gas supply and stop of the gas supply, and a gas supply time is measured. A second pressure and a temperature of the gas in the first and the second flow path is measured, a third pressure of the gas in the second flow path is measured after the gas is exhausted from the second flow path, and a fourth pressure of the gas in the first and the second flow path is measured. The gas flow supplied to the first and the second flow path is calculated based on the first to fourth pressures and the temperature, and corrected based on a theoretical gas supply time and a calculated average time.

A flowmeter includes a fluid collection chamber for receiving a fluid flow, an adjustable collection tube configured to receive a portion of the fluid flow to generate one or more first measured parameters of multiple measured parameters of the fluid flow, a sampling chamber configured to measure samples of the fluid flow to generate one or more second measured parameters of the multiple measured parameters of the fluid flow, and a control module in signal communication with the adjustable collection tube and the sampling chamber and including one or more processors by which the control module automatically performs certain operations. Such operations include determining multiple output parameters of the fluid flow based on the multiple measured parameters and multiple input parameters. Such operations further include controlling a size of the adjustable collection tube based on a property of the fluid flow.

A flowmeter (5) is provided having a sensor assembly (10) connected to meter electronics (20), wherein the sensor assembly (10) comprises at least one driver (104) and at least one pickoff (105) and a variably modulated conduit (300) configured to change a flow area (304) therein.

A method and device for determining the flow rate of the wet gas using real-time THz imaging and for determining the flow rate of solid contaminants in oil and gas pipelines using real-time Tera Hertz (THz) imaging is disclosed. A THz imaging device for real-time multiphase flow measurement comprises a THz imaging subsystem having a THz source and an imaging capturing a captured image. Wherein the imaging having at least a two dimensional array of pixels, wherein the multiphase flow may comprise at least one of oil, water, gas and solid contaminants. Further, a method for real-time measurement of a wet gas flow of a gas is disclosed. The flow of gas comprising at least one of a fluid phase or solid contaminants in the gas flow. The method comprises at least the steps of using a THz subsystem on the gas flow to acquire a captured image and further processing the captured image to determine the flow rate of the flow of gas.

A non-destructive monitoring method for internal pressure intensity of a pipeline. The method establishes an equation relationship by the fact that the variation of the internal diameter of the pipeline is the same as that measured by FBG sensors, and can effectively obtain the value of the internal pressure intensity of the pipeline by measuring the strain values of the FBG sensors installed on the pipeline so as to monitor the internal pressure intensity of the pipeline. The present invention has the advantages of simple principle, convenient installation, no damage to pipeline structure, long-distance real-time on-line monitoring and the like, and can measure the pressure intensity of various pipelines with different diameters by changing the calibration distance of sensors and the dimension of sensor clamps. This can complete non-destructive, real-time and accurate monitoring on the internal pressure intensity of the pipeline.

The invention relates to a compound water meter, consisting of a main meter, connectable to a main line, for detecting larger flow rates, and an auxiliary meter, arranged in an annular channel, for detecting smaller flow rates, wherein the measuring insert of the main meter is assigned a switching valve connected with it and opening the passage through the main line upon achieving a certain differential pressure against the action of a spring element. In order to create an improved compound water meter, it is suggested within the scope of the invention that the spring element is arranged in the interior of the switching valve and a single seal of the switching valve is axially arranged on the non-moveable part. Through the arrangement of the spring element in the interior of the switching valve, the switching valve is only sealed via a seal. Through the axial arrangement of the seal, in contrast to the prior art, in which the one radial seal is provided, it is achieved that the sealing point is particularly low-wear. In contrast to the prior art, only one seal is provided in the compound water meter according to the invention, which entails a simplification of the manufacturing process, as well as also an increase of the operational safety.

A non-destructive monitoring method for internal pressure intensity of a pipeline. The method establishes an equation relationship by the fact that the variation of the internal diameter of the pipeline is the same as that measured by FBG sensors, and can effectively obtain the value of the internal pressure intensity of the pipeline by measuring the strain values of the FBG sensors installed on the pipeline so as to monitor the internal pressure intensity of the pipeline. The present invention has the advantages of simple principle, convenient installation, no damage to pipeline structure, long-distance real-time on-line monitoring and the like, and can measure the pressure intensity of various pipelines with different diameters by changing the calibration distance of sensors and the dimension of sensor clamps. This can complete non-destructive, real-time and accurate monitoring on the internal pressure intensity of the pipeline.

The present invention intends to more accurately diagnose a function of a flow rate sensor regardless of a variation in measurement ambient condition. The present invention includes: a flow rate sensor for measuring the flow rate of fluid; a correction part adapted to measure an output value of the flow rate sensor or a value related to the output value (hereinafter collectively referred to as an output-related value), relates the measured output-related value and a corresponding measurement ambient condition to each other, and in accordance with the measurement ambient condition in measurement data, correct the output-related value or a reference value that is predetermined in order to determine whether the output-related value is normal; and a diagnostic part adapted to compare the output-related value and the reference value on the basis of a correction result by the correction part and correct the function of the flow rate sensor.

A differential monitoring system of carbon dioxide levels within an associated building with a monitoring zone including a quantity of captured carbon dioxide and a reference zone that is spaced away from the monitoring zone. The differential monitoring system includes a first carbon dioxide monitoring inlet disposed within the monitoring zone. A second carbon dioxide monitoring inlet is disposed within the monitoring zone in spaced relation to the first carbon dioxide monitoring inlet and/or is disposed within the reference zone in spaced relation to the first carbon dioxide monitoring zone. A controller is operable to determine when a carbon dioxide level at the second carbon dioxide monitoring inlet exceeds a carbon dioxide level at the first carbon dioxide monitoring inlet by a predetermined differential threshold. The inlets can be part of an aspirated sampling system and/or part of a distributed sensor system. Methods of monitoring carbon dioxide levels are also included.

A polymer is flowed through a slim tube including porous media until steady state is achieved. A temperature of the porous media with the polymer is adjusted to emulate a reservoir temperature. A slug of a gel solution is flowed through the porous media in the slim tube. The gel solution includes the polymer and a crosslinker. The gel solution is configured to at least partially solidify at the temperature. Multiple pressure drops across the porous media in the slim tube are measured at corresponding locations along a length of the slim tube while the slug flows through the porous media in the slim tube. The slug at least partially solidifies within the slim tube, causing an increase in pressure. A location of gelation of the slug of gel solution within the slim tube is determined based on the increase in pressure.