Abstract: Provided are forward osmosis processes to increase the concentration of a dilute metal salt solution, e.g., a vanadium electrolyte solution. In embodiments, such a process comprises: (a) delivering a draw solution to a draw chamber of a forward osmosis module, the draw solution comprising water and sulfuric acid at a draw acid concentration, wherein the draw solution is free of vanadium cations; and (b) delivering a feed solution to a feed chamber of the forward osmosis module, the draw and feed chambers separated by a membrane, the feed solution comprising water, vanadium cations, and sulfuric acid at a feed acid concentration that is lower than the draw acid concentration, wherein water passes across the membrane from the feed solution to the draw solution, thereby providing a concentrated vanadium electrolyte solution as a feed chamber output and a diluted acid solution as a draw chamber output.

Abstract: Flow battery systems are provided, including flowing a liquid electrolyte from a storage tank of a flow battery system to an electrode chamber of the flow battery system, the liquid electrolyte comprising a solvent and a first active ion dissolved in the solvent, wherein the storage tank comprises the liquid electrolyte and a first solid composed of the active ion and an ion of the solvent; inducing an electrochemical reaction in the electrode chamber to convert the first active ion dissolved in the solvent to a second active ion dissolved in the solvent, wherein the first solid dissolves to provide more of the first active ion dissolved in the solvent; flowing the liquid electrolyte comprising the solvent and the second active ion dissolved in the solvent from the electrode chamber back to the storage tank; and precipitating a second solid composed of the second active ion and the ion of the solvent in the storage tank.

Abstract: In embodiments, a method of forming a membrane electrode assembly comprises pressing a stack comprising a cathode, an anode, a proton exchange membrane between the cathode and the anode, and a porous catalyst layer in contact with the proton exchange membrane, the porous catalyst layer comprising an ionomer, the ionomer coating internal surfaces of pores of the porous catalyst layer, thereby providing internal ionomer-gas interfaces within the porous catalyst layer; for a time, a pressure, and a temperature to bind the ionomer to the proton exchange membrane, whereby steam is generated within the porous catalyst layer. The steam is removed via pores of the porous catalyst layer to increase the hydrophobicity of the internal ionomer-gas interfaces within the porous catalyst layer.

Abstract: A gas diffusion layer having a first major surface and a second major surface which is positioned opposite to said first major surface and an interior between said first and second major surfaces is formed. The gas diffusion layer comprises a porous carbon substrate which is directly fluorinated in the interior and is substantially free of fluorination on at least one of the first major surfaces or the second major surfaces, and preferably both surfaces. The gas diffusion layer may be formed using protective sandwich process during direct fluorination or by physically or chemically removing the C—F atomic layer at the major surfaces, for example by physical plasma etching or chemical reactive ion etching.

Abstract: In embodiments, a method of forming a membrane electrode assembly comprises pressing a stack comprising a cathode, an anode, a proton exchange membrane between the cathode and the anode, and a porous catalyst layer in contact with the proton exchange membrane, the porous catalyst layer comprising an ionomer, the ionomer coating internal surfaces of pores of the porous catalyst layer, thereby providing internal ionomer-gas interfaces within the porous catalyst layer; for a time, a pressure, and a temperature to bind the ionomer to the proton exchange membrane, whereby steam is generated within the porous catalyst layer. The steam is removed via pores of the porous catalyst layer to increase the hydrophobicity of the internal ionomer-gas interfaces within the porous catalyst layer.

Abstract: A gas diffusion layer having a first major surface and a second major surface which is positioned opposite to said first major surface and an interior between said first and second major surfaces is formed. The gas diffusion layer comprises a porous carbon substrate which is directly fluorinated in the interior and is substantially free of fluorination on at least one of the first major surfaces or the second major surfaces, and preferably both surfaces. The gas diffusion layer may be formed using protective sandwich process during direct fluorination or by physically or chemically removing the C—F atomic layer at the major surfaces, for example by physical plasma etching or chemical reactive ion etching.

Abstract: A gas diffusion layer having a first major surface and a second major surface which is positioned opposite to said first major surface and an interior between said first and second major surfaces is formed. The gas diffusion layer comprises a porous carbon substrate which is directly fluorinated in the interior and is substantially free of fluorination on at least one of the first major surfaces or the second major surfaces, and preferably both surfaces. The gas diffusion layer may be formed using protective sandwich process during direct fluorination or by physically or chemically removing the C—F atomic layer at the major surfaces, for example by physical plasma etching or chemical reactive ion etching.

Abstract: A gas diffusion layer having a first major surface and a second major surface which is positioned opposite to said first major surface and an interior between said first and second major surfaces is formed. The gas diffusion layer comprises a porous carbon substrate which is directly fluorinated in the interior and is substantially free of fluorination on at least one of the first major surfaces or the second major surfaces, and preferably both surfaces. The gas diffusion layer may be formed using protective sandwich process during direct fluorination or by physically or chemically removing the C—F atomic layer at the major surfaces, for example by physical plasma etching or chemical reactive ion etching.

Abstract: A proton exchange membrane fuel cell comprises a membrane formed from a fluorocarbon ionic polymer material capable of being bonded to an acrylic, preferably a polymethylmethacrylate polymer, and at least one desirably electrically conductive plate bonded to an area of a face of the membrane via an acrylic plastic material. The bond may be accomplished by positioning a layer of the acrylic plastic material between a surface of the plate and an area of a face of the membrane. Alternatively, the plate may be constructed of the acrylic plastic material and a surface thereof may be bonded directly to an area of a face of the membrane.

Abstract: An apparatus for interfacing a test head to a peripheral system is provided. The apparatus includes a first unit having a first connection member for providing electrical communication with the peripheral system, a second unit having a second connection member for providing electrical communication with the test system, and pivot members coupling the first unit and the second unit. The pivot members enable motion in the following sequence as one of the first and second unit moves towards the other: a) pivotal motion between the first connection member and the second connection member; and b) linear motion which decreases linear distance between the first connection member and the second connection member while maintaining respective contact surfaces of the first and second connection members in parallel.

Abstract: An apparatus for interfacing a test head to a peripheral system is provided. The apparatus includes a first unit having a first connection member for providing electrical communication with the peripheral system, a second unit having a second connection member for providing electrical communication with the test system, and pivot members coupling the first unit and the second unit. The pivot members enable motion in the following sequence as one of the first and second unit moves towards the other: a) pivotal motion between the first connection member and the second connection member; and b) linear motion which decreases linear distance between the first connection member and the second connection member while maintaining respective contact surfaces of the first and second connection members in parallel.

Abstract: An apparatus for interfacing a test head to a peripheral system is provided. The apparatus includes a first unit having a first connection member for providing electrical communication with the peripheral system, a second unit having a second connection member for providing electrical communication with the test system, and pivot members coupling the first unit and the second unit. The pivot members enable motion in the following sequence as one of the first and second unit moves towards the other: a) pivotal motion between the first connection member and the second connection member; and b) linear motion which decreases linear distance between the first connection member and the second connection member while maintaining respective contact surfaces of the first and second connection members in parallel.

Abstract: An apparatus for interfacing a test head to a peripheral system is provided. The apparatus includes a first unit having a first connection member for providing electrical communication with the peripheral system, a second unit having a second connection member for providing electrical communication with the test system, and pivot members coupling the first unit and the second unit. The pivot members enable motion in the following sequence as one of the first and second unit moves towards the other: a) pivotal motion between the first connection member and the second connection member; and b) linear motion which decreases linear distance between the first connection member and the second connection member while maintaining respective contact surfaces of the first and second connection members in parallel.

Abstract: A proton exchange membrane fuel cell comprises a membrane formed from a fluorocarbon ionic polymer material capable of being bonded to an acrylic, preferably a polymethylmethacrylate polymer, and at least one desirably electrically conductive plate bonded to an area of a face of the membrane via an acrylic plastic material. The bond may be accomplished by positioning a layer of the acrylic plastic material between a surface of the plate and an area of a face of the membrane. Alternatively, the plate may be constructed of the acrylic plastic material and a surface thereof may be bonded directly to an area of a face of the membrane.

Abstract: An apparatus for interfacing a test head to a peripheral system is provided. The apparatus includes a first unit having a first connection member for providing electrical communication with the peripheral system, a second unit having a second connection member for providing electrical communication with the test system, and pivot members coupling the first unit and the second unit. The pivot members enable motion in the following sequence as one of the first and second unit moves towards the other: a) pivotal motion between the first connection member and the second connection member; and b) linear motion which decreases linear distance between the first connection member and the second connection member while maintaining respective contact surfaces of the first and second connection members in parallel.

Abstract: A fuel cell system made up of a plurality of fuel cells. Each cell includes a fuel inlet, an oxidant inlet, a fuel side product outlet and an oxidant side product outlet. A common fuel supply line is provided for the fuel inlets. A common oxidant supply line is provided for the oxidant inlets. A common product purging mechanism is coupled to the outlets for purging the same of unused fuel, unused oxidant, fuel side product and oxidant side product. The product purging mechanism includes valving structure operable to selectively and independently open the outlets of a given cell. A method for operating such a fuel cell system includes supplying fuel to the fuel inlets from a common source of fuel and supplying an oxidant to the oxidant inlets from a common source of oxidant. The outlets of a given cell are selectively opened to purge fuel product and oxidant product from the given cell while the outlets of other cells are kept closed.

Abstract: A fuel cell system made up of a plurality of fuel cells. Each cell includes a fuel inlet, an oxidant inlet, a fuel side product outlet and an oxidant side product outlet. A common fuel supply line is provided for the fuel inlets. A common oxidant supply line is provided for the oxidant inlets. A common product purging mechanism is coupled to the outlets for purging the same of unused fuel, unused oxidant, fuel side product and oxidant side product. The product purging mechanism includes valving structure operable to selectively and independently open the outlets of a given cell. A method for operating such a fuel cell system includes supplying fuel to the fuel inlets from a common source of fuel and supplying an oxidant to the oxidant inlets from a common source of oxidant. The outlets of a given cell are selectively opened to purge fuel product and oxidant product from the given cell while the outlets of other cells are kept closed.

Abstract: A fuel cell system made up of a plurality of fuel cells. Each cell includes a fuel inlet, an oxidant inlet, a fuel side product outlet and an oxidant side product outlet. A common fuel supply line is provided for the fuel inlets. A common oxidant supply line is provided for the oxidant inlets. A common product purging mechanism is coupled to the outlets for purging the same of unused fuel, unused oxidant, fuel side product and oxidant side product. The product purging mechanism includes valving structure operable to selectively and independently open the outlets of a given cell. A method for operating such a fuel cell system includes supplying fuel to the fuel inlets from a common source of fuel and supplying an oxidant to the oxidant inlets from a common source of oxidant. The outlets of a given cell are selectively opened to purge fuel product and oxidant product from the given cell while the outlets of other cells are kept closed.