This disclosure relates generally to selective flocculation, and more particularly to portable test-device for performing selective flocculation experiments in continuous mode. The test-device includes a slurry inflow system, a flocculant tank, a static mixer, a control pumping system, and a thickener system. The static mixer is connected to the slurry inflow system and the flocculant tank, to receive and mix flocculant solution and slurry and cause formation of floc. The control pumping system connects the flocculant tank and the slurry inflow system to the static mixer to control the control parameters responsible for pumping the slurry and flocculant solution in the continuous mode in the static mixer. The thickener system comprises a thickener tank to receive treated slurry and the floc from the static mixer, separately collect tailings and the floc from the thickening tank. The components of the portable test-device are removably connected to each other.

A system (10) for treating produce includes an application system (12) for applying a treatment liquid to the produce. A piston pump (20) is connected in liquid flow receiving communication with a source of treatment liquid (16), and also is connected in liquid flow expelling communication with an application line (18) leading to the application system. A control system (22) controls the operation of the piston pump to pump a selected dosage of the treatment liquid from the source of treatment liquid (16) to the application system (12).

An apparatus for generating a powerful oxidative hydrogen peroxide foam and chemically stable application process comprises separate supply lines for respectively conveying liquid hydrogen peroxide and liquid foaming agent from separate storage receptacles, a mixer for mixing the liquid hydrogen peroxide and foaming agent once combined together, an air supply line for aerating the foamable liquid hydrogen peroxide mixture, and a foam generating device for mechanically agitating the aerated foamable liquid hydrogen peroxide mixture to form the hydrogen peroxide foam for subsequent discharge to a substrate. There is also disclosed a related method for generating the hydrogen peroxide foam.

A mixer apparatus for an exhaust gas aftertreatment system of a motor vehicle. The apparatus includes a housing having enveloping, first end, and second end walls. An injection opening for an exhaust gas aftertreatment agent is in the enveloping wall. An inlet opening is in the first end wall. The injection opening is configured for mounting a metering module. A rectilinear metering axis, which extends through the metering module and corresponds to an injection direction of exhaust gas aftertreatment agent injected into the housing, tangentially contacts, at a contact point, a theoretical cylinder, disposed in the housing, having a variable radius and a cylinder axis that is congruent with a central axis of the housing. A region of the metering axis extending from the injection opening to the contact point is located, with respect to inflowing exhaust gas, in the shelter of an opening-free region of the first end wall.

A device (1) for producing a solution of at least one liquid first medium and at least one second medium has a first container (2) for the first medium and a second container (3) for the second medium. Each container (2, 3) is connected to a supply line of a static mixer (9) via a pump (4, 5) that can be regulated by a controller (6). A sensor (10) is connected to the controller (6) downstream of the static mixer (9) in the flow direction. A branching valve (17) is downstream of the static mixer (9) in the flow direction and is controlled by the controller (6). A sterile filter (11) is downstream of the static mixer (9) and has an RFID tag (15) that stores process-relevant data to at least be read by the controller (6). A method also is provided for producing a solution using the device.

A device (1) for producing a solution of at least one liquid first medium and at least one second medium has a first container (2) for the first medium and a second container (3) for the second medium. Each container (2, 3) is connected to a supply line of a static mixer (9) via a pump (4, 5) that can be regulated by a controller (6). A sensor (10) is connected to the controller (6) downstream of the static mixer (9) in the flow direction. A branching valve (17) is downstream of the static mixer (9) in the flow direction and is controlled by the controller (6). A sterile filter (11) is downstream of the static mixer (9) and has an RFID tag (15) that stores process-relevant data to at least be read by the controller (6). A method also is provided for producing a solution using the device.

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.

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.

A fluid distributor comprises a first conduit extending along a first elongated axis and a second conduit circumscribing the first conduit. A first area comprises a cross-sectional flow area of the first conduit taken perpendicular to the first elongated axis. The first conduit comprises a first plurality of orifices comprising a first combined cross-sectional area. The second conduit comprises a second plurality of orifices comprising a second combined cross-sectional area. A first ratio of the first area to the first combined cross-sectional area can be about 2 or more. A second ratio of the first combined cross-sectional area to the second combined cross-sectional area can be about 2 or more. An angle between a direction of an orifice axis of a first orifice of the first plurality of orifices and a direction of an orifice axis of a first orifice of the second plurality of orifices can be from about 45° to 180°.

An engine exhaust aftertreatment system having an organization and arrangement of certain selected components which achieve significant catalytic reduction of the known NOx pollutants (NO and NO.sub.2) in tailpipe-out exhaust, while also achieving significant catalytic reduction of sulfate pollutants in tailpipe-out exhaust.