Abstract: In some implementations, a flow measuring device may include a piping network having a region of interest, an inlet region, and outlet region, where the region of interest is configured to provide fluid communication between the inlet region and the outlet region. In addition, the flow measuring device may include a first sensor positioned within the inlet region and a second sensor positioned within the outlet region. The flow measuring device may include a processing unit that determines a speed of sound of a process fluid within the region of interest using the first sensor and the second sensor.

Abstract: A method may include disposing an array of at least two sensors responsive to pressure perturbations within the process fluid along at least a portion of the length of a conduit and determining a first speed of sound of the process fluid associated with a first frequency range utilizing an output of the array of sensors. The method may include determining a second speed of sound of the process fluid associated with a second frequency range, where the second frequency range is at or above of a first acoustic cross mode frequency where the second frequency range is higher than the first frequency range and is lower than a bubble resonant frequency. Also, the method may include determining the parameter of the process fluid utilizing the first speed of sound of the process fluid and the second speed of sound of the process fluid in an optimization model.

Abstract: A method is disclosed that may include measuring a measured fluid density of a process fluid using a vibrational frequency of a fluid-conveying flow tube of the Coriolis meter where a density of a liquid phase of the process fluid is unknown. In addition, the method may include measuring at least one of an excitation energy metric of the Coriolis meter and a vibrational amplitude metric of the Coriolis meter. The method may include determining a Coriolis Mass Flowmeter Damping (CMFD) parameter using at least one of the excitation energy metric and the vibrational amplitude metric. Moreover, the method may include determining the density of the liquid phase of the process fluid using the measured fluid density and the CMFD parameter. Systems employing such methods are further disclosed.

Abstract: A method is disclosed including providing a process fluid that can be described as having a plurality of components where each of the plurality of components has a respective mass fraction. In addition, the method includes providing an initial estimate of a compositional description for the plurality of components of the process fluid, measuring an ultrasonic sound speed of the process fluid, predicting a predicted sound speed of a liquid phase of the process fluid using an equation of state model, generating an error function using the ultrasonic sound speed of the process fluid and the predicted sound speed of a liquid phase of the process fluid, minimizing the error function and updating the respective mass fractions of the plurality of components and determining an optimized compositional description of the process fluid. Also disclosed are corresponding computer systems, apparatus, and computer programs configured to perform the actions of the methods.

Abstract: A flow measuring device capable of measuring at least parameters of a multiphase flow and to quantify an effect of decoupling on an interpretation of the parameters based on at least one characteristic of the multiphase fluid is disclosed. The flow measuring system includes various augmentations and enhancements to a Coriolis meter. The flow measuring system is capable of determining decoupling parameters that can be used to improve the output of a Coriolis meter. A method of retrofitting a Coriolis meter is also disclosed.

Abstract: A method is disclosed that may include measuring a measured fluid density of a process fluid using a vibrational frequency of a fluid-conveying flow tube of the Coriolis meter where a density of a liquid phase of the process fluid is unknown. In addition, the method may include measuring at least one of an excitation energy metric of the Coriolis meter and a vibrational amplitude metric of the Coriolis meter. The method may include determining a Coriolis Mass Flowmeter Damping (CMFD) parameter using at least one of the excitation energy metric and the vibrational amplitude metric. Moreover, the method may include determining the density of the liquid phase of the process fluid using the measured fluid density and the CMFD parameter. Systems employing such methods are further disclosed.

Abstract: A method is disclosed including providing a process fluid that can be described as having a plurality of components where each of the plurality of components has a respective mass fraction. In addition, the method includes providing an initial estimate of a compositional description for the plurality of components of the process fluid, measuring an ultrasonic sound speed of the process fluid, predicting a predicted sound speed of a liquid phase of the process fluid using an equation of state model, generating an error function using the ultrasonic sound speed of the process fluid and the predicted sound speed of a liquid phase of the process fluid, minimizing the error function and updating the respective mass fractions of the plurality of components and determining an optimized compositional description of the process fluid. Also disclosed are corresponding computer systems, apparatus, and computer programs configured to perform the actions of the methods.

Abstract: A method is disclosed that may include measuring a measured fluid density of a process fluid using a vibrational frequency of a fluid-conveying flow tube of the Coriolis meter where a density of a liquid phase of the process fluid is unknown. In addition, the method may include measuring at least one of an excitation energy metric of the Coriolis meter and a vibrational amplitude metric of the Coriolis meter. The method may include determining a Coriolis Mass Flowmeter Damping (CMFD) parameter using at least one of the excitation energy metric and the vibrational amplitude metric. Moreover, the method may include determining the density of the liquid phase of the process fluid using the measured fluid density and the CMFD parameter. Systems employing such methods are further disclosed.

Abstract: In some implementations, a flow measuring device may include a piping network having a region of interest, an inlet region, and outlet region, where the region of interest is configured to provide fluid communication between the inlet region and the outlet region. In addition, the flow measuring device may include a first sensor positioned within the inlet region and a second sensor positioned within the outlet region. The flow measuring device may include a processing unit that determines a speed of sound of a process fluid within the region of interest using the first sensor and the second sensor.

Abstract: A method is disclosed including providing a process fluid that can be described as having a plurality of components where each of the plurality of components has a respective mass fraction. In addition, the method includes providing an initial estimate of a compositional description for the plurality of components of the process fluid, measuring an ultrasonic sound speed of the process fluid, predicting a predicted sound speed of a liquid phase of the process fluid using an equation of state model, generating an error function using the ultrasonic sound speed of the process fluid and the predicted sound speed of a liquid phase of the process fluid, minimizing the error function and updating the respective mass fractions of the plurality of components and determining an optimized compositional description of the process fluid. Also disclosed are corresponding computer systems, apparatus, and computer programs configured to perform the actions of the methods.

Abstract: In accordance with example embodiments of the present disclosure, a method for determining parameters for, and application of, models that correct for the effects of fluid inhomogeneity and compressibility on the ability of Coriolis meters to accurately measure the mass flow and/or density of a process fluid on a continuous basis is disclosed. Example embodiments mitigate the effect of multiphase fluid conditions on a Coriolis meter.

Abstract: Methods and apparatus are disclosed utilizing a low-order parametric model for decoupling in conjunction with an optimization procedure to improve the ability to determine the density of the liquid phase of a bubbly mixtures within Coriolis meters by characterizing the effect of decoupling in the presence of bubble coalescence.

Abstract: A vibrating plate densitometer system and methods are disclosed that can provide information related to the density of a fluid in a vessel. Also disclosed are apparatus and methods to determine the speed of sound of the fluid and methods for designing such apparatus. Embodiments of the present disclosure include systems and methods to measure such parameters including the density, or the density and the entrained air, of wet concrete within a vessel. The present disclosure also provides means for maintaining accurate measurement that exploits the rotating nature of many vessels that contain concrete.

Abstract: In accordance with example embodiments of the present disclosure, a method for determining parameters for, and application of, models that correct for the effects of fluid inhomogeneity and compressibility on the ability of Coriolis meters to accurately measure the mass flow and/or density of a process fluid on a continuous basis is disclosed. Example embodiments mitigate the effect of multiphase fluid conditions on a Coriolis meter.

Abstract: Methods and apparatus are disclosed utilizing a low-order parametric model for decoupling in conjunction with an optimization procedure to improve the ability to determine the density of the liquid phase of a bubbly mixtures within Coriolis meters by characterizing the effect of decoupling in the presence of bubble coalescence.

Abstract: In accordance with example embodiments of the present disclosure, a method for determining parameters for, and application of, models that correct for the effects of fluid inhomogeniety and compressibility on the ability of Coriolis meters to accurately measure the mass flow and/or density of a process fluid on a continuous basis is disclosed. Example embodiments mitigate the effect of multiphase fluid conditions on a Coriolis meter.

Abstract: A system is provided for testing a component. This system includes a support structure, an excitation system and a sensor system. The support structure is configured to support the component. The excitation system includes a plurality of permanent magnets and a plurality of electromagnets. The permanent magnets are arranged in an array and configured for rigid connection to the component. Each of the electromagnets is associated with a respective one of the permanent magnets. The excitation system is configured to respectively control interaction of the electromagnets with the permanent magnets to excite a vibratory response in the component. The sensor system is configured to output data indicative of the vibratory response.

Abstract: A system is provided for testing a component. This system includes a support structure, an excitation system and a sensor system. The support structure is configured to support the component. The excitation system includes a plurality of permanent magnets and a plurality of electromagnets. The permanent magnets are arranged in an array and configured for rigid connection to the component. Each of the electromagnets is associated with a respective one of the permanent magnets. The excitation system is configured to respectively control interaction of the electromagnets with the permanent magnets to excite a vibratory response in the component. The sensor system is configured to output data indicative of the vibratory response.

Abstract: Example embodiments are directed to fluid turbines that include a turbine shroud, a rotor and an ejector shroud. The turbine shroud includes an inlet, an outlet, a leading edge and a trialing edge. The leading edge of the turbine shroud can be round and the trialing edge of the turbine shroud can include linear faceted segments. The rotor can be disposed within the turbine shroud and can define a rotor plane. The turbine shroud can provide a first portion of a fluid stream to the rotor plane via the inlet of the turbine shroud. The ejector shroud can provide a second portion of the fluid stream to the outlet of the turbine shroud via an open area. An example method of operating a fluid turbine is also provided.

Abstract: A flow measurement apparatus is provided that combines the functionality of an apparatus that uses strain-based sensors and ultrasonic sensors to measure the speed of sound propagating through a fluid flowing within a pipe, and measure pressures disturbances (e.g. vortical disturbances or eddies) moving with a fluid to determine respective parameters of the flow propagating through a pipe. The apparatus includes a sensing device that includes an array of pressure sensors used to measure the acoustic and convective pressure variations in the flow to determine desired parameters and an ultrasonic meter portion to measure the velocity and volumetric flow of the fluid. In response to an input signal or internal logic, the processor can manually or dynamically switch between the pressure sensors and ultrasonic sensors to measure the parameters of the flow.