A device and a method for mixing a fluid in a specimen bag is provided herein. In one embodiment, the device includes a mechanism for creating a first vortex and a second vortex. The first vortex is on a first side of a bag containing the fluid, and the second vortex is on a second side of the bag. The mechanism includes a first inflatable airbag and a second inflatable airbag. The first inflatable airbag is configured to create the first vortex when inflated and the second inflatable airbag is deflated. The second inflatable airbag is configured to create the second vortex when inflated and the first inflatable airbag is deflated.

A method for preparing an aqueous solution of a defined pH comprising an acid, a base and optionally one or more additives is provided. The method comprises the steps of: a) calculating the theoretical concentrations of acid and base for the solution to have the defined pH using the Henderson-Hasselbach equation in combination with the Debye Huckel theory for a range of different additive concentrations; b) preparing a sample of the buffer for the range of additive concentrations and measuring the actual pH for each additive concentration; c) calculating a value for delta pH, pH, being the difference between the theoretical pH and the actual pH, for each additive concentration; d) generating a mathematical model describing the relationship of pH with additive concentration; e) selecting the defined pH and additive concentrations; f) using the mathematical model generated in step d) to calculate pH for the defined pH and additive concentration; g) calculating a pH-corrected pH by summing the defined pH and delta pH; h) using the pH-corrected pH to calculate the concentrations of acid and base using the Henderson-Hasselbach equation in combination with the Debye Huckel theory; i) preparing the solution using the concentrations calculated in step h).

A method for preparing an aqueous solution of a defined pH comprising an acid, a base and optionally one or more additives is provided. The method comprises the steps of: a) calculating the theoretical concentrations of acid and base for the solution to have the defined pH using the Henderson-Hasselbach equation in combination with the Debye Huckel theory for a range of different additive concentrations; b) preparing a sample of the buffer for the range of additive concentrations and measuring the actual pH for each additive concentration; c) calculating a value for delta pH, pH, being the difference between the theoretical pH and the actual pH, for each additive concentration; d) generating a mathematical model describing the relationship of pH with additive concentration; e) selecting the defined pH and additive concentrations; f) using the mathematical model generated in step d) to calculate pH for the defined pH and additive concentration; g) calculating a pH-corrected pH by summing the defined pH and delta pH; h) using the pH-corrected pH to calculate the concentrations of acid and base using the Henderson-Hasselbach equation in combination with the Debye Huckel theory; i) preparing the solution using the concentrations calculated in step h).

Systems and methods for processing one or more waste fluids by measuring one or more properties of a waste fluid and adjusting the flow and/or flowability of the waste fluid based on the measurement are disclosed. The one or more properties of the waste fluid can include a viscosity of the waste fluid, a pressure of the waste fluid, and/or or a difference in pressure of the waste fluid. Adjusting the flow and/or flowability of the waste fluid can include adjusting the one or more properties of the waste fluid and/or affecting the direction of flow of the waste fluid in a manner which changes the destination of the waste fluid.

Systems and methods for processing one or more waste fluids by measuring one or more properties of a waste fluid and adjusting the flow and/or flowability of the waste fluid based on the measurement are disclosed. The one or more properties of the waste fluid can include a viscosity of the waste fluid, a pressure of the waste fluid, and/or or a difference in pressure of the waste fluid. Adjusting the flow and/or flowability of the waste fluid can include adjusting the one or more properties of the waste fluid and/or affecting the direction of flow of the waste fluid in a manner which changes the destination of the waste fluid.

System and method for dispensing a flowable product are provided. The system includes a mixing chamber having a first inlet, a second inlet and an outlet. The mixing chamber of the system contains a mixing element capable of motion. The system also includes a paste located in an enclosure configured to flow into the mixing chamber via a first channel connected to the first inlet, and a flowable medium configured to flow into the mixing chamber via a second channel connected to the second inlet. The mixing chamber is configured to mix the paste and the flowable medium using the mixing element, thus, producing the flowable product that may be output via the outlet.

An exhaust line includes a housing having a wall with an opening and a baffle disposed within the opening. In certain embodiments, the exhaust line includes a divider between the wall and baffle that partially defines a mixing chamber for receiving an exhaust and a reducing agent, and partially defines a bypass chamber for receiving another portion of the exhaust. The divider defines an inlet and outlet facing respective upstream and downstream ends. The divider transfers heat from exhaust passing through the bypass chamber to the reducing agent inside the mixing chamber. In other embodiments, the baffle partially defines a first passageway substantially parallel to and offset from a center axis for delivering a portion of the exhaust to the mixing chamber, and a ramped surface partially defining a second passageway transverse to the first passageway for delivering another portion of the exhaust to the mixing chamber.

A system for continuously treating recycled polymeric material includes a hopper configured to feed the recycled polymeric material into the system. An extruder can turn the recycled polymeric material in a molten material. In some embodiments, the extruder uses thermal fluids, electric heaters, and/or a separate heater. The molten material is depolymerized in a reactor. In some embodiments, a catalyst is used to aid in depolymerizing the material. In certain embodiments, the catalyst is contained in a permeable container. The depolymerized molten material can then be cooled via a heat exchanger. In some embodiments, multiple reactors are used. In certain embodiments, these reactors are connected in series. In some embodiments, the reactor(s) contain removable static mixer(s) and/or removable annular inserts.

There are provided a method for producing a hydrogen gas-containing material in which higher safety than in a production method of the related art is secured and which is simple and has high production efficiency, and a method for producing a hydrogen gas-containing material and a device for producing a hydrogen gas-containing material in which it is possible to prevent nitrogen gas from being mixed into the hydrogen gas-containing material produced by the production method and it is easy to control an amount of hydrogen contained in the hydrogen gas-containing material. As one aspect, there is provided a method for producing a hydrogen gas-containing material including mixing a liquid composition containing a gelling agent or a thickener and a liquid medium with hydrogen gas in a line mixer (20) and cooling the liquid composition containing hydrogen gas in a liquid-transfer pipe (22) connected to the line mixer (20) and causing the liquid composition containing hydrogen gas to gel or thicken.

An apparatus for creating an emulsion, including: an inlet chamber; a channel comprising a length L, height H, an inlet and an outlet, and walls having surface energies, the channel inlet adjacent to the inlet chamber. The channel inlet walls have a first surface energy and the outlet walls have a second surface energy substantially different from the first surface energy. An outlet chamber is disposed adjacent to the channel outlet, the outlet chamber height H2 being greater than the channel height H.