Abstract: Disclosed herein are phase separator devices, and related methods of fabrication and use. The disclosure provides improved phase separator devices for phase separation of input feeds, and systems/methods for utilizing and fabricating the devices. The disclosure provides phase separator devices utilizing inertial separation and porous media extraction for the phase separation of two-phase input feeds (e.g., to separate an input feed of a two-phase mixture to a first phase output (e.g., to a liquid output flow) and to a second phase output (e.g., to a gas output flow)). The device can separate a mixed fluid flow of both liquid and gases. The liquid and gas can include liquid and vapor phases of the same chemical/constituent (e.g., ammonia), or may include liquid and gases of two different constituents (e.g., liquid water and air). The phase separator devices can be utilized at standard gravity to micro-gravity to zero gravity environments.

Abstract: The present disclosure relates to a pipeline for supplying a gas to an internal combustion engine, with a pipeline cross section forming a passage for the gas and a gas mass measuring device for measuring a gas mass flow. The pipeline is characterized in particular in that it comprises a mixing element made from a wire structure upstream from the gas mass measuring device and in that the mixing element serves for the thorough mixing of the gas in order to homogenize an inhomogeneous flow profile which is present upstream from the mixing element.

Abstract: A consistent water to chemical ratio in each of two described operating modes is achieved by implementing a closed loop insert comprising a single straw with a dual dilution rate. The closed loop insert is installed at the packaging level and is recessed into the neck of the container so that it does not interfere with the bottle cap or the dispensing unit to which it might be attached. The closed loop engages with a mating cap adapter or chemical dispenser that keys up to a closed insert to allow the dilution dispenser to draw chemical out of the container through the use of a vacuum pressure. The dual dilution rate closed loop insert of the invention has two different metering tip sizes that fit inside a single straw closed loop insert, selected based upon operating modes.

Abstract: A thermal management device for dissipating heat from one or more electrical components in an aircraft, the thermal management device including: a heat spreader with a plurality of layers of annealed pyrolytic graphite, the heat spreader having higher thermal conductivity in a plane defined by the layers than in a direction perpendicular to the layers; a flow path for a cooling fluid defined through the heat spreader, such that at least a portion of the flow path is surrounded by the heat spreader, wherein the flow path is helical, around a central axis extending through the plurality of layers; and a housing encasing the heat spreader, the housing arranged to have one or more electrical components mounted there-on and to form a thermal interface between the heat spreader and one or more electrical components.

Abstract: A food product sterilizer includes a food product source and a regenerative heat exchanger configured to receive a flow of food product from the food product source. The heat exchanger includes an input channel configured to receive a flow of food product to be sterilized. The heat exchanger also includes an output channel fluidly coupled to the input channel. The output channel is adjacent the input channel. The output channel and the input channel are configured to transfer heat between the two channels. The heat exchanger further includes an integrated heating section of at least a portion of the input channel or the output channel. The heating section is configured to heat the flow of food product.

Abstract: An object of the present invention is to provide a reforming apparatus and the like capable of uniformly mixing water (steam) and a raw material together, of preventing the precipitation of carbon without using a temperature controller, and of efficiently heating the water and the mixture by heating gas. Accordingly, the reforming apparatus has the following configuration. The reforming apparatus includes: a first vaporizer (05) that is cylindrically shaped and includes a first flow passage; a second vaporizer (06) that is cylindrically shaped and includes a second flow passage; a duct (027) that connects an outlet of the first flow passage to an inlet of the second flow passage; a raw-material mixing portion (028) formed at a certain point of the duct. The first vaporizer and the second vaporizer are concentrically disposed. An interstice between the first vaporizer and the second vaporizer serves as a heating-gas flow passage (024).

Abstract: The auger gasifier described includes, in its preferred embodiments, a vertically elongated (“oblong”) primary gasifier chamber with an auger that can move up and down, allowing for large amounts of fuel input when necessary. This improvement, in turn, requires and/or is facilitated by provision for simultaneous elevation adjustments of the auger and bed dam to assure that fuel material is processed in degrees from the top downward without sweeping massive amounts of the fluidized bed materials towards the output end of the chamber. Another improvement involves provision for pressurization of the primary gasifier chamber, allowing substantial improvements in the speed of processing materials through the gasifier. Due to issues arising from thermal expansion of the refractory material lining the chamber, provision is made for nozzle and refractory imbedded pipe hole thermal expansion capability.

Abstract: The invention relates to a reformer mixing chamber comprising a water vapour-air mixture feeding line and a binary nozzle for supplying a fuel-air mixture, wherein said mixing chamber is rotationally symmetrically shaped and the flow direction of the binary nozzle and the water vapour-air mixture feeding line are axially and oppositely oriented. The inventive mixing chamber is advantageous in that it makes it possible to carry out the fuel as complete as possible conversion. For this purpose, the fuel-air mixture is supplied to the mixing chamber by means of a second binary nozzle, thereby making it possible to supply the mixing chamber with the water vapour-air mixture by another feeding line, wherein the fuel-air mixture flows in the direction opposite to the water vapour-air mixture.

Abstract: A mixture formation means for the reformer of a fuel cell system or for a heater. The fuel feed includes a pressure impulse injection means and the mixture formation area is a swirl chamber having a discharge nozzle connected to the pressure impulse injection device. Also included is a fuel heater for preheating the fuel before injection in order to achieve complete vaporization of the fuel, such as diesel fuel.

Abstract: An evaporator device for generating a hydrocarbon-air mixture which can be decomposed in a reformer for producing hydrogen comprises a burner/evaporator area, which has a combustion/mixing chamber (14), into which air enters via an inlet opening device (16), a hydrocarbon evaporating means (24, 34), comprising a porous evaporator medium (24) and, associated with same, a first heating means (34) and a glow-type igniting member (28) for igniting the hydrocarbon-air mixture present in the combustion/mixing chamber (14).

Abstract: A reformer (5) which generates hydrogen-rich reformate gas by causing a catalytic reaction of fuel and air comprises a premixing chamber (12) for premixing the fuel with the air. High temperature air is supplied to the premixing chamber (12) from an air intake tube (13) via an orifice (14). A fuel injector (16) injects the fuel into the flow of the high temperature air in the premixing chamber (12) to generate fuel-air mixture. A homogenizing filter (17) homogenizes the composition of the fuel-air mixture in the premixing chamber (12) and supplies a uniform fuel-air mixture to a reforming catalyst (11).

Abstract: A chemical hydride hydrogen generation system and an energy system incorporating the same are provided. The hydrogen generation system comprises: a storage means for storing a chemical hydride solution; a reactor containing a catalyst; a first supplying means for supplying the chemical hydride solution from the said storage means to the said reactor so that the chemical hydride solution reacts to generate hydrogen in the presence of the catalyst; and a second supplying means for continuously supplying the solvent of the said solution to the chemical hydride solution during the reaction. The said energy system comprises the said hydrogen generation system, a fuel cell for generating electricity and water from hydrogen and an oxidant, and a means for recovering the water generated in the said fuel cell and supplying the said water to the chemical hydride solution during the reaction.