Viscometers and Viscometry methods are disclosed. In one general aspect a capillary bridge viscometer comprises an input port an output port a first capillary tubing arm in a first hydraulic path between the input port and a first differential detection point, a second capillary tubing arm in a second hydraulic path between the first differential detection point and the output port, a third capillary tubing arm in a third hydraulic path between the input port and a second differential detection point, a fourth capillary tubing arm in a fourth hydraulic path between the second differential detection point and the output port, an adjustable mechanical flow restrictor in one of the first, second, third, and fourth hydraulic paths, wherein the adjustable mechanical flow restrictor is operative to mechanically adjust a resistance to flow of a fluid while the fluid flows through the adjustable mechanical flow restrictor.

A viscometer includes a viscosity sensor with a liquid flow channel and at least two pressure sensors positioned along the liquid flow channel and configured to measure a pressure drop of a liquid flowing through the liquid flow channel, and a dispensing mechanism configured to cause dispensing of a liquid from the syringe to the viscosity sensor at a known flow rate. The dispensing mechanism and the viscosity sensor are configured to couple with a syringe configured to contain a liquid. The viscometer further includes an electronic controller configured to control operations of the dispensing mechanism and receive and process data from the viscosity sensor. The viscometer includes a sample loading interface, included in the syringe, through which the viscometer is configured to receive the liquid. The sample loading interface includes a selection valve coupled with, and located between, the viscosity sensor and the syringe.

A viscometer includes a viscosity sensor with a liquid flow channel and at least two pressure sensors positioned along the liquid flow channel and configured to measure a pressure drop of a liquid flowing through the liquid flow channel, and a dispensing mechanism configured to cause dispensing of a liquid from the syringe to the viscosity sensor at a known flow rate. The dispensing mechanism and the viscosity sensor are configured to couple with a syringe configured to contain a liquid. The viscometer further includes an electronic controller configured to control operations of the dispensing mechanism and receive and process data from the viscosity sensor. The viscometer includes a sample loading interface, included in the syringe, through which the viscometer is configured to receive the liquid. The sample loading interface includes a selection valve coupled with, and located between, the viscosity sensor and the syringe.

A flow rate detector of an exhalation measurement device includes: a pipe body having a flow inlet at a first end into which exhalation flows, and a flow outlet at a second end out of which exhalation flows; and a differential pressure sensor connected to the pipe body. The pipe body includes: a partition gasket which partitions the inside of the pipe body into a flow-in space of exhalation and a flow-out space of exhalation; a connection aperture being provided at the flow-in space and connecting the differential pressure sensor to the flow-in space; a connection aperture being provided at the flow-out space and connecting the differential pressure sensor to the flow-out space; and an air duct of an elongated shape, extending through the partition gasket and allowing the flow-in space and the flow-out space to communicate with each other.

A flow rate detector of an exhalation measurement device includes: a pipe body having a flow inlet at a first end into which exhalation flows, and a flow outlet at a second end out of which exhalation flows; and a differential pressure sensor connected to the pipe body. The pipe body includes: a partition gasket which partitions the inside of the pipe body into a flow-in space of exhalation and a flow-out space of exhalation; a connection aperture being provided at the flow-in space and connecting the differential pressure sensor to the flow-in space; a connection aperture being provided at the flow-out space and connecting the differential pressure sensor to the flow-out space; and an air duct of an elongated shape, extending through the partition gasket and allowing the flow-in space and the flow-out space to communicate with each other.

Disclosed herein is a method for viscosity measurement of non-Newtonian fluid for in-line measurement and process control. The process involves mixing additives to a base fluid to form the non-Newtonian fluid. The non-Newtonian fluid is fed to an in-line viscosity measurement device to obtain a rheological measurement. The addition of the additives to the base fluid is then adjusted based on the rheological measurement. A system for accomplishing the same is also disclosed.

In-line viscosity measurement systems and related methods may be useful in measuring the viscosity of a fluid in a flow path and, more specifically, in-line measuring the viscosity of a drilling fluid when integrated with drilling systems. For example, a method may include drilling a wellbore penetrating a subterranean formation while circulating a drilling fluid through the wellbore; measuring the viscosity of the drilling fluid with an in-line viscometer system after the drilling fluid has circulated through the wellbore, the in-line viscometer systems comprising either: (1) a two coaxial cylinder configuration, (2) a parallel plates configuration, or (3) a combination thereof positioned to allow for the drilling fluid to flow between the coaxial cylinders or parallel plates.

In-line viscosity measurement systems and related methods may be useful in measuring the viscosity of a fluid in a flow path and, more specifically, in-line measuring the viscosity of a drilling fluid when integrated with drilling systems. For example, a method may include drilling a wellbore penetrating a subterranean formation while circulating a drilling fluid through the wellbore; measuring the viscosity of the drilling fluid with an in-line viscometer system after the drilling fluid has circulated through the wellbore, the in-line viscometer systems comprising either: (1) a two coaxial cylinder configuration, (2) a parallel plates configuration, or (3) a combination thereof positioned to allow for the drilling fluid to flow between the coaxial cylinders or parallel plates.

The present invention relates to a method of continuously determining the shear viscosity () of a product paste to be delivered to a spray nozzle for spray-drying applications wherein the continuous determination of the shear viscosity () of the product paste is carried out in a bypass to the product paste stream to the spray nozzle.

The present invention relates to a method of continuously determining the shear viscosity () of a product paste to be delivered to a spray nozzle for spray-drying applications wherein the continuous determination of the shear viscosity () of the product paste is carried out in a bypass to the product paste stream to the spray nozzle.