Provided are a method for supplying water of specified concentration, including: a step of adding at least two liquids, a conductive first liquid and a non-conductive second liquid, to ultrapure water to produce water of specified concentration containing a first liquid-component and a second liquid-component at specified concentrations, in which a mixed solution in which the first liquid and the second liquid are mixed at a specified mixing ratio in advance is prepared; and the mixed solution is added to the ultrapure water so that a conductivity or specific resistance of the ultrapure water after the addition satisfies a specified value, and an apparatus therefor.

A bioprocess fluid mixing system (3; 3′; 3″; 103; 103′), said fluid mixing system (3; 3′; 3″; 103; 103′) comprising: —at least two fluid inlets (5a, 5b, 5c, 5d, 5e), configured for providing a first fluid into the fluid mixing system through a first fluid inlet (5a) and for providing a second fluid into the fluid mixing system through a second fluid inlet (5b); —at least one valve arrangement (13a, 13b, 13c, 13a′), where a first valve arrangement (13a; 13a′) is in fluid communication with at least both the first fluid inlet (5a) and the second fluid inlet (5b); —at least two pumps (11a, 11b, 11c, 11d, 11e), where a first pump (11a) is in selective fluid communication with at least both the first and the second fluid inlets (5a, 5b) via the first valve arrangement (13a; 13a′) and a second pump (11b) is in fluid communication with at least one of the first and second fluid inlet (5b); and —a common fluid outlet (14) which is in fluid communication with both an outlet (15a) of the first pump (11a) and an outlet (15b) of the second pump (11b), wherein pump rates of the at least two pumps (11a, 11b) and valve positions in the at least one valve arrangement (13a; 13a′; 13b, 13c) are configured to be controllable by a control system (21) such that mixing of at least a first fluid from the first fluid inlet (5a) and a second fluid from the second fluid inlet (5b) can be performed to a requested mixing of the at least two fluids and to a requested combined fluid flow rate at the common fluid outlet (14).

In a method for evaporating a non-gaseous starting material, the starting material is introduced into an evaporation chamber; an evaporation element heats the starting material to create a vapor; a conveying gas flow transports the vapor through a conveying channel and past a sensor, which measures the concentration or partial pressure of the vapor in the gas flow flowing through the conveying channel; and the mass flow of the vapor through the conveying channel is controlled by varying the conveying gas flow with respect to a setpoint value. To keep the vapor flow largely constant over time, a compensating gas flow is fed into the conveying channel at a mixing point disposed between the evaporator and the sensor. A second mass flow controller controls the mass flow of the compensating gas flow such that, when the conveying gas flow varies, the gas flow flowing past the sensor remains constant.

A system and method provides a more precise mole delivery amount of a process gas, for each pulse of a pulse gas delivery, by measuring a concentration of the process gas and controlling the amount of gas mixture delivered in a pulse of gas flow based on the received concentration of the process gas. The control of mole delivery amount for each pulse can be achieved by adjusting flow setpoint, pulse duration, or both.

A system and method provides a more precise mole delivery amount of a process gas, for each pulse of a pulse gas delivery, by measuring a concentration of the process gas and controlling the amount of gas mixture delivered in a pulse of gas flow based on the received concentration of the process gas. The control of mole delivery amount for each pulse can be achieved by adjusting flow setpoint, pulse duration, or both.

In order to provide a concentration control apparatus that, without adding any new sensors or the like, makes it possible to accurately estimate a quantity of source consumed inside a vaporization tank, and to perform highly accurate concentration control in accordance with the remaining quantity of source, there is provided a concentration control apparatus that, in a vaporizer that is equipped with at least a vaporization tank containing a liquid or solid source, a carrier gas supply path that supplies a carrier gas to the vaporization tank, and a source gas extraction path along which flows a source gas which is created by vaporizing the source and is then extracted from the vaporization tank, controls a concentration of the source gas and includes a concentration monitor that is provided on the source gas extraction path, and outputs output signals in accordance with a concentration of the source gas.

An air cart for use in an agricultural air seeding system includes a first storage compartment for holding a first granular product type. The air cart also includes a second storage compartment for holding a second granular product type different from the first granular product type. The air cart further includes a common conduit configured to receive the first granular product type from the first storage compartment and the second granular product type from the second storage compartment to enable simultaneous flow of the first granular product type and the second granular product type. The air cart even further includes a multi-product particle flow rate sensing system configured to monitor respective flow rates for both the first granular product type and the second granular product type during simultaneous flow of the first granular product type and the second granular product type through the common conduit.

A fuel-gas blending system receives low-pressure tank vapors and high-pressure flash gases from an oil production facility, boosts the pressure of the tank vapors, and blends the tank vapors and high-pressure gases together to supply fuel gas at a pressure and quality required by an onsite fuel-gas-powered generator. The quality of the supplied fuel gas is maintained by controlling the proportion of a high-pressure gas, such as separator gas, in the blend while the volumetric flow rates of the various gases vary in response to the real-time demands of the generator. The system operates in one of multiple modes in order to maximize the use of tank vapors. In one mode, all the gases pass through a low-pressure blower. In another mode, only the tank vapors pass through the blower, and the high-pressure gases are blended with tank vapors downstream of the blower.

This invention relates generally to injection remediation systems and methods. In one embodiment, an injection remediation system includes, but is not limited to, at least one reservoir configured to contain material; at least one load sensor supporting the at least one reservoir; at least one dosing pump operably coupled to the at least one reservoir and configured to controllably source the material; and at least one processor configured to determine an amount of the material sourced from the at least one reservoir based at least partly on weight information obtained from the at least one load sensor.

This invention relates generally to injection remediation systems and methods. In one embodiment, an injection remediation system includes, but is not limited to, at least one reservoir configured to contain material; at least one load sensor supporting the at least one reservoir; at least one dosing pump operably coupled to the at least one reservoir and configured to controllably source the material; and at least one processor configured to determine an amount of the material sourced from the at least one reservoir based at least partly on weight information obtained from the at least one load sensor.