Abstract: A method and system are provided for an integrated fluid and vapor delivery system design that optimizes vapor delivery. The method and system utilize a purgeable valve assembly which is closely coupled to a vaporizer. The purgeable valve assembly includes a liquid control valve and a purge gas valve which are connected by an outlet to the vaporizer in a manner minimizing the dead volume of the liquid supplied to the vaporizer. The system does not require the liquid precursor to be subjected to vacuum prior to entry into the vaporizer.

Abstract: A mercury ionic gas standard generator for use in the continuous emissions monitoring of exhaust flue gas streams is disclosed. More specifically, the mercury ionic gas standard generator uses a reservoir being coated with an inert silicon-based coating for transporting a volume of an aqueous ionic mercury solution to a liquid mass flow controller and vaporizer.

Abstract: In one aspect, the inventive process comprises a process for pyrolyzing a hydrocarbon feedstock containing nonvolatiles in a regenerative pyrolysis reactor system. The inventive process comprises: (a) heating the nonvolatile-containing hydrocarbon feedstock upstream of a regenerative pyrolysis reactor system to a temperature sufficient to form a vapor phase that is essentially free of nonvolatiles and a liquid phase containing the nonvolatiles; (b) separating said vapor phase from said liquid phase; (c) feeding the separated vapor phase to the pyrolysis reactor system; and (d) converting the separated vapor phase in said pyrolysis reactor system to form a pyrolysis product.

Abstract: A method for quantifying the permanganate-reducing compounds (PRCs) in an acetic acid sample is disclosed. The method comprises establishing a correlation between permanganate absorbances of standard samples and their PRC contents and determining the PRC content of the acetic acid sample by measuring its permanganate absorbance of a reaction mixture containing a standard permanganate solution and the acetic acid sample. The permanganate absorbance is obtained by subtracting the manganese dioxide absorbance from the absorbance of the mixture.

Abstract: A gas separation vessel has a vessel shell and a partition therein. A first bed support is mounted between the partition and the shell, and a second bed support is mounted within the partition to define a second bed space. First and second ports on the vessel shell beneath the bed supports permit gas flow between the bed spaces and the exterior of the vessel shell. A separation medium is placed in the bed spaces. A feed gas is introduced into the vessel to flow through the first bed and then through the second bed to separate at least one component of the feed gas from the other intermixed gases. Output gas is then collected from the vessel. The vessel may have a L:D ratio of not more than 4:1.

Abstract: According to one embodiment, there is provided a method of analyzing antimony contained in glass according to its valency. This method includes milling glass containing antimony into a glass powder, weighing the glass powder and dissolving the glass powder by using hydrofluoric acid and hydrochloric acid to obtain a glass solution, masking hydrofluoric acid by adding aluminum ions to the glass solution, adding sodium borohydride and hydrochloric acid to the glass solution in which hydrofluoric acid is masked to generate a hydride of antimony (III), determining a concentration of antimony (III) contained in the glass solution based on the hydride, determining a total concentration of antimony contained in the glass solution and calculating a difference between the concentration of antimony (III) and the total concentration of antimony to obtain a concentration of antimony (V) from the difference.

Abstract: A system for evaporating excess water from a source includes a housing having: an air inlet, the air inlet directing air in a first direction; an air outlet; a plurality of channels arranged generally perpendicular to the first direction, the channels having undulations; and a water reservoir that feeds water into the channels. In some embodiments, baffles are created with walls that depend from the ceiling of the housing and that are interdigitated with dividers that separate the channels. This configuration can remove water generated by the source (such as an external compressor unit) in a quick and efficient manner.

Abstract: Compositions comprising a tripeptide having the sequence XC1C2; wherein X is any amino acid such that XC1C2 is capable of binding a metal in a square planar orientation or square pyramidal orientation or both; and wherein C1 and C2 are the same or different; and wherein C1 and C2 individually are chosen from a cysteine and a cysteine-like nonnatural amino acid, as well as metal-XC1C2 complexes and methods for forming such complexes.

Abstract: A constructed permeability control infrastructure can include a permeability control impoundment defining a substantially encapsulated volume. A comminuted water-containing hydrocarbonaceous material can form a permeable body within the encapsulated volume. The impoundment includes a water vapor outlet for removing water vapor from the encapsulated volume. A heating device is also embedded within the permeable body to provide convective heating thereof. The permeable body can be heated sufficient to initially remove water therefrom as a water vapor. The water vapor can be removed from the infrastructure via the outlet which can be controlled or shut off when the permeable body is sufficiently dewatered. The dewatered permeable body can then be heated sufficient to remove hydrocarbons therefrom. During heating the hydrocarbonaceous material is substantially stationary as the constructed infrastructure is a fixed structure.

Abstract: Disclosed is a process for recovery power from an FCC product. Gaseous hydrocarbon product from an FCC reactor is heat exchanged with a heat exchange media which is delivered to an expander to generate power. Cycle oil from product fractionation may be added to the gaseous FCC product to wash away coke precursors.

Abstract: A humidifier including a housing which is used to receive a humidifier module. The housing can be connected by the housing cover and is provided with at least one first sealing element, which seals the humidifier module in relation to the housing. The humidifier module is arranged in an axially displaceable manner on the first sealing element.

Abstract: A filter assembly includes a laterally extending filter element having an element plate extending laterally outwardly therefrom and mounted between axially spaced first and second housing shells. First and second sets of one or more windows are formed axially through the element plate and define a flow path through the assembly.

Abstract: A system for curing tires that does not require a traditional bladder is described. The system disclosed has top and bottom assembly rings that are coupled to modified mold rings. The bottom assembly ring has a curing medium delivery system, which has ports and a diverter that disperses the curing medium thereby reducing the momentum of the curing medium striking a liner of the tire being cured. The system is adapted for easy installation to existing center post presses.

Abstract: A process comprises constructing a sub-assembly including a rigid layer and a poly (vinyl acetal) interlayer in a vacuum bag or vacuum press; applying vacuum to the vacuum bag or vacuum press for a maximum of 30 to 60 minutes while maintaining the sub-assembly at a temperature between 10° C. and 22° C. to produce a cooled sub-assembly; increasing the temperature of the cooled sub-assembly to at least 100° C. or 125° C. over a minimum of 10 minutes or 20 minutes to produce a heated sub-assembly; maintaining the heated sub-assembly at minimum of 100° C. or 125° C. for a minimum of 10 minutes or 20 minutes to form a laminate; cooling the laminate at a rate of at least 0.5° C./minute until the laminate reaches a temperature below 40° C.; contemporaneously with the cooling, removing the vacuum from the vacuum bag, containing the laminate, and allowing the laminate to reach atmospheric pressure.

Abstract: Oil soluble catalysts are used in a process to hydrodesulfurize petroleum feedstock having a high concentration of sulfur-containing compounds and convert the feedstock to a higher value product. The catalyst complex includes at least one attractor species and at least one catalytic metal that are bonded to a plurality of organic ligands that make the catalyst complex oil-soluble. The attractor species selectively attracts the catalyst to sulfur sites in sulfur-containing compounds in the feedstock where the catalytic metal can catalyze the removal of sulfur. Because the attractor species selectively attracts the catalysts to sulfur sites, non-productive, hydrogen consuming side reactions are reduced and greater rates of hydrodesulfurization are achieved while consuming less hydrogen per unit sulfur removed.

Abstract: A non-autoclave process for producing a glass laminate comprises applying a sub-assembly including a rigid layer and an ionomer interlayer in a vacuum bag or vacuum press under vacuum followed by heating, cooling, and releasing vacuum.

Abstract: A membrane humidifier for a fuel cell system is disclosed wherein the membrane humidifier includes a plurality of membrane layers, a first pair of spaced apart sealing bars disposed between a first membrane layer and a second membrane layer adjacent to perimeter edges thereof to form a first flow channel, a second pair of spaced apart sealing bars disposed between the second membrane layer and a third membrane layer adjacent to perimeter edges thereof to form a second flow channel, and a plurality of supports, wherein a first support is disposed adjacent the second planar layer and extending between the second pair of spaced apart sealing bars, and a second support is disposed adjacent the third planar layer and extending between the second pair of spaced apart sealing bars.

Abstract: Provided is a method for simply quantitatively determining hexavalent chromium, including: separately bringing a plurality of test solutions into contact with a sample, the plurality of test solutions each containing a color change agent which changes in color upon reaction with hexavalent chromium, and an acid which dissolves the sample, the plurality of test solutions having different contents of the acid from each other; detecting color change in each of the test solutions; and when the color change is detected, specifying a range of content of hexavalent chromium in the sample on the basis of the content of the acid in a test solution with the color changed among the plurality of test solutions.

Abstract: A process for removing organic sulfur from a fuel gas stream that further contains light olefins by catalytic hydrodesulfurization to yield a treated fuel gas having an very low concentration of organic sulfur. The effluent of the catalytic hydrodesulfurization reactor may be cooled with a portion thereof being recycled and introduced along with the fuel gas stream that is charged to the hydrodesulfurization reactor. The remaining, unrecycled portion of the effluent may further be treated to remove the hydrogen sulfide that is yielded from by the hydrodesulfurization of the fuel gas stream.

Abstract: A dispersion apparatus for dispersing a treating agent into a fluid treatment system that includes a flow duct in which a fluid stream flowing through the duct is mixed with the treating agent. The apparatus is based on a multi-pipe lance positioned in the stream flow, where each pipe supplies a minimum of feed discharge nozzles (typically one to four), and the individual pipes branch off from the same location. Use of the multi-pipe lance, in combination with a suitable baffle, results in better overall dispersion/distribution of the injected medium by surface area. By improving the surface area distribution, better utilization of the injected sorbent can be achieved. The baffle acts to generate a low pressure zone on its downstream side and creates a high-intensity turbulence plume in the fluid. The orifices of the pipe are located to inject the treating agent into the turbulence plume to better distribute and intermix the injected treating agent into the surrounding fluid.