A specific resistance value adjustment apparatus includes: a hollow fiber membrane module; a module passing pipe which passes through the hollow fiber membrane module; a bypassing pipe which bypasses the hollow fiber membrane module; a liquid discharge pipe which communicates with the module passing pipe and the bypassing pipe through a joint portion; a first flow rate detection unit which detects a first flow rate of a liquid flowing to at least one of a liquid supply pipe and the liquid discharge pipe; a control valve which opens and closes the module passing pipe; and a control unit which sets an opening degree of the control valve in response to the first flow rate detected by the first flow rate detection unit.

A mixer for a vehicle exhaust gas system includes a mixer housing defining an internal cavity and having a mixer inlet configured to receive exhaust gas and a mixer outlet to direct exhaust gas to downstream exhaust components. A flow device is configured to receive the exhaust gas from the mixer inlet and to facilitate mixing of the exhaust gas and a reductant introduced into the first flow device. The flow device comprises a Venturi body centered on a body center axis, and the Venturi body comprises a body inlet configured to receive the exhaust gas from the mixer inlet and a body outlet configured to provide the exhaust gas to the mixer outlet. The Venturi body also includes a louver extending from an internal surface of the mixer housing to a distal edge that is downstream of the body outlet. An upstream vane is positioned within the Venturi body proximate the body inlet and is coupled to an upstream vane hub that is centered on an upstream vane hub axis. A downstream vane is positioned within the Venturi body proximate the body outlet and is coupled to a downstream vane hub that is centered on a downstream vane hub axis. The upstream vane hub axis is radially offset from the body center axis by an offset distance and/or the downstream vane hub axis is radially offset from the body center axis by an offset distance.

A process for producing a microemulsion or nanoemulsion comprising water and at least one hydrocarbon or oil, comprising the steps of: a) providing the hydrocarbon or oil, water, one or more additives, a solvent, and a hydrophilic surfactant formulation comprising an amine or amide derivative non-ionic surfactant which is a fatty acid alkanolamide, one or more ethoxylated alcohols and/or ethoxylated alkylphenols, and a non-ionic fatty acid ester; b) by a mixing or stirring device operating at a mixing or stirring speed in the range 100 rpm and 15000 rpm, mixing or stirring the hydrophilic surfactant formulation and additive into the solvent, to produce a hydrophilic self-emulsifying blend; c) adding water to the hydrophilic self-emulsifying blend and the hydrocarbon or oil to produce a water-in-hydrocarbon/oil microemulsion or nanoemulsion, wherein the microemulsion or nanoemulsion comprises: 46% or more by mass of the hydrocarbon or oil, 4% to 36% by mass of water, a mass ratio of hydrophilic surfactant formulation to water in the range 1:10 to 1:2, 0.1% to 5% by mass of additive, 1.2% or more by mass of the solvent, a dispersed particle size in the range 1 nm to 500 nm, and a polydispersity index of 35% PdI or less, wherein the percentages by mass of the hydrocarbon or oil, water, formulation, additive and solvent together add up to 100%.

A process for producing a microemulsion or nanoemulsion comprising water and at least one hydrocarbon or oil, comprising the steps of: a) providing the hydrocarbon or oil, water, one or more additives, a solvent, and a hydrophilic surfactant formulation comprising an amine or amide derivative non-ionic surfactant which is a fatty acid alkanolamide, one or more ethoxylated alcohols and/or ethoxylated alkylphenols, and a non-ionic fatty acid ester; b) by a mixing or stirring device operating at a mixing or stirring speed in the range 100 rpm and 15000 rpm, mixing or stirring the hydrophilic surfactant formulation and additive into the solvent, to produce a hydrophilic self-emulsifying blend; c) adding water to the hydrophilic self-emulsifying blend and the hydrocarbon or oil to produce a water-in-hydrocarbon/oil microemulsion or nanoemulsion, wherein the microemulsion or nanoemulsion comprises: 46% or more by mass of the hydrocarbon or oil, 4% to 36% by mass of water, a mass ratio of hydrophilic surfactant formulation to water in the range 1:10 to 1:2, 0.1% to 5% by mass of additive, 1.2% or more by mass of the solvent, a dispersed particle size in the range 1 nm to 500 nm, and a polydispersity index of 35% PdI or less, wherein the percentages by mass of the hydrocarbon or oil, water, formulation, additive and solvent together add up to 100%.

A mixer for a vehicle exhaust gas system includes a mixer housing defining an internal cavity and having a mixer inlet configured to receive exhaust gas and a mixer outlet to direct exhaust gas to downstream exhaust components. A flow device is configured to receive the exhaust gas from the mixer inlet and to facilitate mixing of the exhaust gas and a reductant introduced into the first flow device. The flow device comprises a Venturi body centered on a body center axis, and the Venturi body comprises a body inlet configured to receive the exhaust gas from the mixer inlet and a body outlet configured to provide the exhaust gas to the mixer outlet. The Venturi body also includes a louver extending from an internal surface of the mixer housing to a distal edge that is downstream of the body outlet. An upstream vane is positioned within the Venturi body proximate the body inlet and is coupled to an upstream vane hub that is centered on an upstream vane hub axis. A downstream vane is positioned within the Venturi body proximate the body outlet and is coupled to a downstream vane hub that is centered on a downstream vane hub axis. The upstream vane hub axis is radially offset from the body center axis by an offset distance and/or the downstream vane hub axis is radially offset from the body center axis by an offset distance.

An after treatment system (ATS) for a vehicle includes, fluidly connected in series, an inlet, a urea mixer and an outlet. The inlet is fluidly connected to an output of an engine of the vehicle and the outlet is fluidly connected to an outlet tube of the vehicle. The urea mixer is provided with a dosing module, an inner element and an outer element. The inner element is configured such that a first flow of exhaust gas flow flowing from the inlet into the urea mixer flows into an first volume defined by the inner element. The outer element is configured such that a second flow flows in a volume defined between inner element and outer element, wherein the first and second flows rejoin together in a mixing chamber fluidly connected to the volume and to the first volume downstream with respect inner and outer elements.

The present disclosure relates to an apparatus for adding a liquid reducing agent, preferably an aqueous urea solution, to the exhaust gas from an internal combustion engine. The apparatus according to the present disclosure comprises a dosing device arranged in an exhaust line of the internal combustion engine, which device is designed to generate a reducing agent spray by means of an injector. The apparatus furthermore comprises a swirl generator device, designed as a hollow body, preferably a hollow cylinder, about a longitudinal axis, which has a first end facing the injector and a second end facing away from the injector. The shell surface L of the swirl generator device, designed as a hollow body, furthermore comprises at least one exhaust inlet opening extending substantially in the longitudinal direction and a guide element, attached adjacent to the exhaust inlet opening and covering the exhaust inlet opening in the interior of the swirl generator device, at least in part at a distance, for deflecting an exhaust gas flow. According to the present disclosure, the guide element is closed in the direction of the first end of the swirl generator device, by means of a wall or connection to the shell surface, for example, and open in the direction of the second end of the swirl generator device. The present disclosure furthermore relates to a motor vehicle, preferably a utility vehicle, having a corresponding apparatus.

A pressure washer includes a pump for pressurizing a primary fluid flow, the pump including a pump inlet for receiving fluid from a common fluid source and a pump outlet for supplying a pressurized primary fluid and a jet pump including a primary fluid inlet fluidly coupled to the pump outlet, a secondary fluid inlet configured to receive fluid from the common fluid source, and a fluid outlet. In a high pressure operating mode, all of the pressurized primary fluid flows through the jet pump and exits through the fluid outlet of the jet pump. In a high flow operating mode, all the pressurized primary fluid flows through the jet pump and entrains a secondary fluid supplied through the secondary fluid inlet from the common fluid source so that the secondary fluid also flows through the jet pump, resulting in a combined fluid flow of the primary fluid and the secondary fluid that exits through the fluid outlet of the jet pump.

A chemical injection unit consisting of one or more injection loops that uses a Venturi injector and motorized valve with a control system to isolate chemicals from water until operating conditions are suitable to carry the chemical and water mixture down the main flow pipe. The invention adjusts chemical injection rate to maintain desirable operational properties, including chemical injection rate, chemical concentration, or fluid viscosity. Accurate and real-time injection of chemicals is beneficial for safety as well as economics of the drilling operation in terms of reduced drilling time, efficient use of chemicals, and minimal variation in processing conditions.

A system for introducing gas from an unconventional source into a gas grid pipeline includes a passive blender (10) that introduces gas from an unconventional source (1) into a gas grid (2), the passive blender (10) having gas inputs (3, 11) from the unconventional source (1) and the gas grid (2) and a blended gas output (12), and wherein an internal flow path within the passive blender (10) is shaped and sized to provide entraining and mixing of the gases. The passive blender (10) acts to entrain gas from a gas grid (2) through input (11) by utilising the flow of gas from an unconventional source (1) through input 3, proportionally blending inputs 3 and 11 before outputting the blended gas back to the main gas grid (2). The system comprises the passive blender (10) of the present invention, a first gas input pipe (11) from a grid gas pipeline (2) into the passive blender (10) a second gas input pipe (3) from the unconventional source (1) into the passive blender (1), and an output pipe (12) from the passive blender (10) into the grid gas pipeline (2). The blender (10) and system of the present invention are advantageous in that they can greatly reduce the necessary conditioning of unconventional gas before it is introduced into a gas grid supply (2) without additional means of flow motivation or controls.