Rheological measurement systems for use with systems including pressurized polymer melts and/or other viscous materials are described. In one embodiment, a rheometer is connected to an associated system with a bent, curved, or bendable tube to permit the rheometer to measure rheological properties in locations where the rheometer could not otherwise be located due to the presence of obstructions. Embodiments including rigid straight tubes for connecting a rheometer to an associated system are also described. In another embodiment, a flow-through rheometer is connected to an industry standard ?-20 thermowell aperture that is typically used for attaching temperature and pressure probes to a vessel containing a viscous material such as an extruder or injection molding system.

A reagent pre-loading system for a measuring device includes: a reagent admission arrangement arranged for receiving a reagent into the reagent pre-loading system; a sample admission arrangement arranged for receiving a sample fluid to be measured into the reagent pre-loading system, wherein the reagent admission arrangement and the sample admission arrangement are each arranged in selective fluid communication with a sample and reagent combination conduit for combining the sample fluid and the reagent; wherein the sample admission arrangement and the reagent admission arrangement are arranged to selectively: whilst the sample and reagent combination conduit is closed to fluid communication with the sample fluid at the sample admission arrangement, receive the reagent into the sample and reagent combination conduit so as to expel air from the sample and reagent combination conduit as the reagent is received therein and prime the sample and reagent combination conduit with the reagent.

Systems and methods for determining the yield stress of a non-Newtonian fluid in real time are provided. A pressure loss and/or liquid rise technique, an ultrasonic technique, and/or a penetrometer technique can be used to determine the yield stress of a non-Newtonian fluid. The ultrasonic technique can include a longitudinal wave approach and/or a shear wave approach. The methods and systems are non-invasive and only require slight modifications to the piping containing the non-Newtonian fluid in order to measure the yield stress.

Systems and methods for determining the yield stress of a non-Newtonian fluid in real time are provided. A pressure loss and/or liquid rise technique, an ultrasonic technique, and/or a penetrometer technique can be used to determine the yield stress of a non-Newtonian fluid. The ultrasonic technique can include a longitudinal wave approach and/or a shear wave approach. The methods and systems are non-invasive and only require slight modifications to the piping containing the non-Newtonian fluid in order to measure the yield stress.

An oil quality sensor to determine the quality of deep-frying oil by measuring the capacitance of the deep-frying oil in a deep fryer includes a housing and a hollow space in the housing through which the deep-frying oil is guided. An inlet opening introduces deep-frying oil to the hollow space, and a drain opening guides the deep-frying oil out of the hollow space. A first bent electrode extends along the hollow space, and a second bent electrode extends along the hollow space and is arranged opposite the first electrode, in which case the two electrodes form a capacitor and deep-frying oil is guided through the space formed between these two electrodes to measure its capacitance. A first temperature sensor measures the temperature of the oil used for deep frying that needs to be measured. An evaluation unit records the measured capacitance of the capacitor and the measured temperature, digitalizes these measured values, and calculates the polar fractions in the deep-frying oil, in which case these polar fractions are a criterion for the quality of the deep-frying oil.

The invention relates to a device and a method for testing materials, and is characterized in that the device comprises application units (2) for interaction modules (1) and an exchange system for the interaction modules, and the device is designed such that the application units (2) automatically feed interaction modules (1) to the exchange system after a control signal and the exchange system is designed to feed the interaction modules to a test position.

The present invention provides a MEMS thermal flow sensor or meter for measuring the flow rate of a fluid without need for calibration of the flow sensor for that particular fluid. A response curve is determined by plotting the sensor output voltage against the volume flow rate divided by fluid thermal diffusivity for a calibration fluid of known thermal diffusivity, and storing response curve data in memory. A conversion factor is employed to provide a measure of correct flow rate of an unknown fluid. This conversion factor is derived from the ratio of the thermal time constant of the calibration fluid to the thermal time constant of the measured fluid, the time constants being measured at zero flow. These time constants are stored in memory. This conversion factor in conjunction with the response curve data is utilized by the processor to produce the correct flow rate. The invention also encompasses a method for measuring fluid flow rate of fluids of differing properties without necessity of a separate flow calibration for each fluid.

A viscometer includes a viscosity sensor with a liquid flow channel for measuring a viscosity of a liquid flowing through the liquid flow channel, a manifold with an inlet and an outlet for receiving a liquid sample through the inlet of the manifold and providing the received liquid sample through the outlet of the manifold to the viscosity sensor, and a pump coupled with the manifold for causing an in-flow of the liquid sample into the manifold through the inlet of the manifold and an out-flow of the received liquid sample from the manifold through the outlet of the manifold. Also disclosed is a viscosity sensor module with two or more viscosity sensors.

A viscometer includes a viscosity sensor with a liquid flow channel for measuring a viscosity of a liquid flowing through the liquid flow channel, a manifold with an inlet and an outlet for receiving a liquid sample through the inlet of the manifold and providing the received liquid sample through the outlet of the manifold to the viscosity sensor, and a pump coupled with the manifold for causing an in-flow of the liquid sample into the manifold through the inlet of the manifold and an out-flow of the received liquid sample from the manifold through the outlet of the manifold. Also disclosed is a viscosity sensor module with two or more viscosity sensors.

A rheology device comprises an elongated body having a flow path defined therein, first and second pressure lines in communication with the first and second ends of the flow path, respectively, and a differential pressure sensor for measuring a difference in pressure between the first and second pressure lines. In embodiments, the pressure lines are filled with a spacer fluid different from the fluid in the flow path. Based on at least three measurements of difference in pressure and corresponding flow rates, a yield point, a consistency factor, and a power factor can be calculated, and a rheology model of the fluid can be generated. Related methods are described which allow fluid rheology models to be determined and updated frequently. The device and methods herein may be useful in oil and gas operations, for example for rheology and hydraulic modeling in drilling operations.