A method, for controlling a mixer that mixes materials through rotation of an impeller while a solvent contained in the materials is evaporated under negative pressure, performs a process in which the mixer is operated while the pressure inside the mixer is increased or decreased according to a predetermined profile. When a power value of the impeller exceeds a predetermined upper limit during the operation of the mixer, the pressure inside the mixer is increased. When the power value falls below a predetermined lower limit during the operation of the mixer, the pressure inside the mixer is decreased.

In one embodiment, the present system describes a system wherein a first fluid is within a tank. An intermittent mixer is used for agitating the first fluid within the tank. At least one data acquisition device within the tank is capable of measuring at least one characteristic within the first fluid. In the embodiment, at least one data analyzer is capable of receiving the characteristics within the first fluid, comparing the characteristics within the first fluid to the characteristics of a second fluid, generating a data packet which contains a calculated operational speed and an operational time needed for the intermittent mixer to agitate the first fluid to obtain the characteristics of the second fluid and transmitting the data packet to the intermittent mixer. In this system the intermittent mixer is capable of altering the first fluid within the tank into the second fluid.

In one embodiment, the present system describes a system wherein a first fluid is within a tank. An intermittent mixer is used for agitating the first fluid within the tank. At least one data acquisition device within the tank is capable of measuring at least one characteristic within the first fluid. In the embodiment, at least one data analyzer is capable of receiving the characteristics within the first fluid, comparing the characteristics within the first fluid to the characteristics of a second fluid, generating a data packet which contains a calculated operational speed and an operational time needed for the intermittent mixer to agitate the first fluid to obtain the characteristics of the second fluid and transmitting the data packet to the intermittent mixer. In this system the intermittent mixer is capable of altering the first fluid within the tank into the second fluid.

Viscosity and other properties are determined at desired temperatures in drilling mud and other fluids by using a versatile cavitation device which, operating in the cavitation mode, mixes and heats the fluid to a specified temperature, and, operating in the shear mode, acts as a spindle for application of Couette principles to determine viscosity as a function of shear stress and shear rate. The invention obviates the practice of adjusting rheology of a drilling fluid by passing it through the drill bit. Drilling fluid may be managed by a “straight-through” method to the well, or by placing the cavitation device in a loop which isolates an aliquot of known volume and circulating the fluid through the loop including the cavitation device. A controller may be programmed to manage the viscosity and other properties at various temperatures by controlling the power input and angular rotation of the “spindle” (which has cavities on its cylindrical surface), and feeding viscosity-adjusting agents and other additives to the fluid. Data may be collected from the loop and used in the “straight-through” mode until it is determined that conditions require a new set of data, or the loop may be used continuously. The system may be used with a supplemental viscometer, density meter, and other instruments.

Viscosity and other properties are determined at desired temperatures in drilling mud and other fluids by using a versatile cavitation device which, operating in the cavitation mode, mixes and heats the fluid to a specified temperature, and, operating in the shear mode, acts as a spindle for application of Couette principles to determine viscosity as a function of shear stress and shear rate. The invention obviates the practice of adjusting rheology of a drilling fluid by passing it through the drill bit. Drilling fluid may be managed by a “straight-through” method to the well, or by placing the cavitation device in a loop which isolates an aliquot of known volume and circulating the fluid through the loop including the cavitation device. A controller may be programmed to manage the viscosity and other properties at various temperatures by controlling the power input and angular rotation of the “spindle” (which has cavities on its cylindrical surface), and feeding viscosity-adjusting agents and other additives to the fluid. Data may be collected from the loop and used in the “straight-through” mode until it is determined that conditions require a new set of data, or the loop may be used continuously. The system may be used with a supplemental viscometer, density meter, and other instruments.

Viscosity and other properties are determined at desired temperatures in drilling mud and other fluids by using a versatile cavitation device which, operating in the cavitation mode, mixes and heats the fluid to a specified temperature, and, operating in the shear mode, acts as a spindle for application of Couette principles to determine viscosity as a function of shear stress and shear rate. The invention obviates the practice of adjusting rheology of a drilling fluid by passing it through the drill bit. Drilling fluid may be managed by a “straight-through” method to the well, or by placing the cavitation device in a loop which isolates an aliquot of known volume and circulating the fluid through the loop including the cavitation device. A controller may be programmed to manage the viscosity and other properties at various temperatures by controlling the power input and angular rotation of the “spindle” (which has cavities on its cylindrical surface), and feeding viscosity-adjusting agents and other additives to the fluid. Data may be collected from the loop and used in the “straight-through” mode until it is determined that conditions require a new set of data, or the loop may be used continuously. The system may be used with a supplemental viscometer, density meter, and other instruments.

A dynamic magnetic coupling method employs running drive magnet(s) on a plane at in general a 90-degree angle to and below a magnetic stirring element's laying plane, and a kinetic energy transfer from the drive magnet(s) to the magnetic stirring element through a joint effect of its space velocity and the magnetic attraction force between the two, so that axle(s) to rotate the drive magnet(s) can be placed sideways in a horizontal direction. With horizontally placed axle or axles and the dynamic magnetic coupling mechanism, multiple coupling and stirring positions can be placed in parallel on a single flattened drive train and fit in hard-to-reach places. Magnetic coupling assembly of this dynamic nature allows virtual running coupling dipoles of drive magnets to be configured and reconfigured for different stir motions on the same drive train.

A dynamic magnetic coupling method employs running drive magnet(s) on a plane at in general a 90-degree angle to and below a magnetic stirring element's laying plane, and a kinetic energy transfer from the drive magnet(s) to the magnetic stirring element through a joint effect of its space velocity and the magnetic attraction force between the two, so that axle(s) to rotate the drive magnet(s) can be placed sideways in a horizontal direction. With horizontally placed axle or axles and the dynamic magnetic coupling mechanism, multiple coupling and stirring positions can be placed in parallel on a single flattened drive train and fit in hard-to-reach places. Magnetic coupling assembly of this dynamic nature allows virtual running coupling dipoles of drive magnets to be configured and reconfigured for different stir motions on the same drive train.

Viscosity and other properties are determined at desired temperatures in drilling mud and other fluids by using a versatile cavitation device which, operating in the cavitation mode, mixes and heats the fluid to a specified temperature, and, operating in the shear mode, acts as a spindle for application of Couette principles to determine viscosity as a function of shear stress and shear rate. The invention obviates the practice of adjusting rheology of a drilling fluid by passing it through the drill bit. Drilling fluid may be managed by a “straight-through” method to the well, or by placing the cavitation device in a loop which isolates an aliquot of known volume and circulating the fluid through the loop including the cavitation device. A controller may be programmed to manage the viscosity and other properties at various temperatures by controlling the power input and angular rotation of the “spindle” (which has cavities on its cylindrical surface), and feeding viscosity-adjusting agents and other additives to the fluid. Data may be collected from the loop and used in the “straight-through” mode until it is determined that conditions require a new set of data, or the loop may be used continuously. The system may be used with a supplemental viscometer, density meter, and other instruments.

Viscosity and other properties are determined at desired temperatures in drilling mud and other fluids by using a versatile cavitation device which, operating in the cavitation mode, mixes and heats the fluid to a specified temperature, and, operating in the shear mode, acts as a spindle for application of Couette principles to determine viscosity as a function of shear stress and shear rate. The invention obviates the practice of adjusting rheology of a drilling fluid by passing it through the drill bit. Drilling fluid may be managed by a “straight-through” method to the well, or by placing the cavitation device in a loop which isolates an aliquot of known volume and circulating the fluid through the loop including the cavitation device. A controller may be programmed to manage the viscosity and other properties at various temperatures by controlling the power input and angular rotation of the “spindle” (which has cavities on its cylindrical surface), and feeding viscosity-adjusting agents and other additives to the fluid. Data may be collected from the loop and used in the “straight-through” mode until it is determined that conditions require a new set of data, or the loop may be used continuously. The system may be used with a supplemental viscometer, density meter, and other instruments.