Abstract: A method and system for a mobile power generation system is disclosed. The mobile power generation system may comprise one or more shipping containers, which may be pre-wired and pre-configured so that configuration and deployment at the deployment site is simplified. The one or more shipping containers may include a PV subsystem, a battery subsystem, PCS, control electronics, and the like. The one or more shipping containers may be pre-configured for power transfer and for communication between the various devices so that less configuration is necessary at the deployment site.

Abstract: The present invention relates to methods for regenerating nervous system tissue or treating a neurological disorder by administration of a therapeutically effective amount of synthetic tissue containing a cell population of one or more nervous system cell types (e.g., neurons) or multipotent cells (e.g., mesenchymal stem cells), where the cell population is embedded within a modular synthetic hydrogel that is biocompatible. In some preferred embodiments the modular synthetic hydrogel includes a PEG hydrogel crosslinked with a glycosaminoglycan such as hyaluronan.

Abstract: A composition comprising a fuel and at least one compound characterized by Formula I: wherein X is carbon, oxygen, or sulfur; R1 and R2 each independently are hydrogen, a C1 to C20 alkyl, or a C6 to C10 aryl; R3 and R3? each independently are hydrogen or a C1 to C4 alkyl; R4 and R4? each independently are hydrogen, a C1 to C4 alkyl, a C4 to C10 cycloalkyl, or a C6 to C10 aryl; R5 and R5? each independently are a C4 to C10 alkyl; R6 and R6? each independently are hydrogen or a C1 to C6 alkyl; and R7 and R7? each independently are hydrogen or a C1 to C4 alkyl; and wherein the compound of Formula I when subjected to GC-MS using electron ionization at greater than about 70 eV produces at least one ion having a mass-to-charge ratio of from 300 to 600.

Abstract: A composition comprising a fuel and at least one compound characterized by Formula I: wherein X is carbon, oxygen, or sulfur; R1 and R2 each independently are hydrogen, a C1 to C20 alkyl, or a C6 to C10 aryl; R3 and R3? each independently are hydrogen or a C1 to C4 alkyl; R4 and R4? each independently are hydrogen, a C1 to C4 alkyl, a C4 to C10 cycloalkyl, or a C6 to C10 aryl; R5 and R5? each independently are a C4 to C10 alkyl; R6 and R6? each independently are hydrogen or a C1 to C6 alkyl; and R7 and R7? each independently are hydrogen or a C1 to C4 alkyl; and wherein the compound of Formula I when subjected to GC-MS using electron ionization at greater than about 70 eV produces at least one ion having a mass-to-charge ratio of from 300 to 600.

Abstract: A method of forming a composition comprising contacting a fuel and at least one compound of Formula I: wherein X is carbon, oxygen, or sulfur; R1 and R2 each independently are hydrogen, a C1 to C20 alkyl, or a C6 to C10 aryl; R3 and R3? each independently are hydrogen or a C1 to C4 alkyl; R4 and R4? each independently are hydrogen, a C1 to C4 alkyl, a C4 to C10 cycloalkyl, or a C6 to C10 aryl; R5 and R5? each independently are a C4 to C10 alkyl; R6 and R6? each independently are hydrogen or a C1 to C6 alkyl; and R7 and R7? each independently are hydrogen or C1 to C4 alkyl; and wherein the compound of Formula I when subjected to GC-MS using electron ionization at greater than 70 eV produces at least one ion having a mass-to-charge ratio of 300 to 600.

Abstract: A method of forming a composition comprising contacting a fuel and at least one compound of Formula I: wherein X is carbon, oxygen, or sulfur; R1 and R2 each independently are hydrogen, a C1 to C20 alkyl, or a C6 to C10 aryl; R3 and R3? each independently are hydrogen or a C1 to C4 alkyl; R4 and R4? each independently are hydrogen, a C1 to C4 alkyl, a C4 to C10 cycloalkyl, or a C6 to C10 aryl; R5 and R5? each independently are a C4 to C10 alkyl; R6 and R6? each independently are hydrogen or a C1 to C6 alkyl; and R7 and R7? each independently are hydrogen or C1 to C4 alkyl; and wherein the compound of Formula I when subjected to GC-MS using electron ionization at greater than 70 eV produces at least one ion having a mass-to-charge ratio of 300 to 600.

Abstract: A composition comprising a fuel and at least one compound characterized by Formula I: wherein X is carbon, oxygen, or sulfur; R1 and R2 each independently are hydrogen, a C1 to C20 alkyl, or a C6 to C10 aryl; R3 and R3? each independently are hydrogen or a C1 to C4 alkyl; R4 and R4? each independently are hydrogen, a C1 to C4 alkyl, a C4 to C10 cycloalkyl, or a C6 to C10 aryl; R5 and R5? each independently are a C4 to C10 alkyl; R6 and R6? each independently are hydrogen or a C1 to C6 alkyl; and R7 and R7? each independently are hydrogen or a C1 to C4 alkyl; and wherein the compound of Formula I when subjected to GC-MS using electron ionization at greater than about 70 eV produces at least one ion having a mass-to-charge ratio of from 300 to 600.

Abstract: A compound characterized by Formula I: wherein X can be carbon (C), oxygen (O), or sulfur (S); R1 and R2 can each independently be hydrogen, a C1 to C20 alkyl group, or a C6 to C10 aryl group; R3 and R3? can each independently be hydrogen or a C1 to C4 alkyl group; R4 and R4? can each independently be hydrogen, a C1 to C4 alkyl group, a C4 to C10 cycloalkyl group, or a C6 to C10 aryl group; R5 and R5? can each independently be a C4 to C10 alkyl group; R6 and R6? can each independently be hydrogen or a C1 to C6 alkyl group; and R7 and R7? can each independently be hydrogen or a C1 to C4 alkyl group; and wherein the compound characterized by Formula I when subjected to gas chromatography-mass spectrometry (GC-MS) using electron ionization produces at least one ion having a mass-to-charge ratio of greater than about 300 at an ionization energy of equal to or greater than about 70 eV.

Abstract: A method of determining adulteration of a fuel including subjecting to an analytical technique a marked fuel mixture comprising (a) a fuel; (b) a compound characterized by Formula I: wherein X is carbon, oxygen, or sulfur; when X is O or S, R1 and R2 are lone non-bonding electron pairs; when X is C, R1 and R2 each independently are hydrogen, C1 to C20 alkyl, or C6 to C10 aryl; R3 and R3? each independently are hydrogen or C1 to C4 alkyl; R4 and R4? each independently are hydrogen, C1 to C4 alkyl, C4 to C10 cycloalkyl, or C6 to C10 aryl; R5 and R5? each independently are C4 to C10 alkyl; R6 and R6? each independently are hydrogen or C1 to C6 alkyl; and R7 and R7? each independently are hydrogen or C1 to C4 alkyl; and (c) a heavy compound, wherein the heavy compound comprises a compound of Formula I having at least one atom replaced with an isotope tag.

Abstract: The present invention relates to a method of preparing lanthanide-doped NaYF4 nanocrystals, the method comprising: (A) providing a first solution comprising a non-coordinating solvent, a fatty acid coordinating ligand, sodium trifluoroacetate, yttrium trifluoroacetate, a first doping lanthanide trifluoroacetate and a second doping lanthanide trifluoroacetate, and a second solution comprising the non-coordinating solvent and the fatty acid coordinating ligand, the first and second solutions being substantially free of water and oxygen; (B) in an inert atmosphere, slowly adding the first solution heated at a temperature between about 100° C. and about 150° C. to the second solution heated at temperature between about 290° C. and about 330° C., thereby producing a reaction mixture containing the nanocrystals; and (C) recovering the nanocrystals from the reaction mixture.

Abstract: The present invention relates to a method of preparing lanthanide-doped NaYF4 nanocrystals, the method comprising: (A) providing a first solution comprising a non-coordinating solvent, a fatty acid coordinating ligand, sodium trifluoroacetate, yttrium trifluoroacetate, a first doping lanthanide trifluoroacetate and a second doping lanthanide trifluoroacetate, and a second solution comprising the non-coordinating solvent and the fatty acid coordinating ligand, the first and second solutions being substantially free of water and oxygen; (B) in an inert atmosphere, slowly adding the first solution heated at a temperature between about 100° C. and about 150° C. to the second solution heated at temperature between about 290° C. and about 330° C., thereby producing a reaction mixture containing the nanocrystals; and (C) recovering the nanocrystals from the reaction mixture.

Abstract: An energy efficient process scheme for a highly exothermic reaction-distillation system in which the reactor is external to the distillation column and the feed to the reactor is a mixture of at least one liquid product stream from the distillation column with or without other liquid/vapor reactants. The reactor is operated under adiabatic and boiling point conditions and at a pressure that results in vaporizing a portion of the liquid flow through the reactor due to the heat of reaction. Under these conditions, reaction temperature is controlled by reactor pressure. The pressure (and hence the temperature) is maintained at a sufficiently high level such that the reactor effluent can be efficiently used to provide reboil heat for the distillation column.

Abstract: A curable composition is provided comprising an oligomer having a plurality of pendent and/or terminal ethylenically unsaturated, free-radically polymerizable functional groups, a free-radically polymerizable crosslinking agent, and/or a diluent monomer, and a photoinitiator. The composition, when cured, is non-yellowing, exhibits low shrinkage and low birefringence making it suitable for many optical applications such as optical lenses, optical fibers, prisms, light guides, optical adhesives, and optical films.

Abstract: A process for the isomerization of normal heptane contained within a naphtha stream, such as a C6-C8 naphtha, in which the naphtha stream is fractionated into a fraction substantially free of normal heptane and a fraction containing normal heptane. The fraction containing normal heptane is contacted with an isomerization catalyst in an isomerization zone operated as a singe pass fixed bed reactor having a single effluent to isomerize a portion of said normal heptane to branched heptane. The effluent is recovered from said isomerization zone and the effluent is fractionated to recover said branched heptane. The unconverted normal heptane is recovered and returned to the isomerization since it can be separated from the branded heptanes by fractionation.

Abstract: This invention provides methods for selectively killing a hyperproliferative cell by contacting the cell with the compound BVdU, its derivatives and pharmaceutically acceptable salts. Further provided by this invention is a method for treating a pathology in a subject characterized by pathological, hyperproliferative cells by administering to the subject an effective amount of the compound BVdU, its derivatives and pharmaceutically acceptable salts. The invention also provides a method for screening for potential therapeutic agents by contacting a neoplastic cell with the agent and with BVdU and performing an assay to detect inhibition of proliferation and cell killing. The invention also provides methods for selecting from among a patient population, patients that are likely to benefit from treatment with BVdU, by determining the level of endogenous, intracellular TK and TS.

Abstract: A process for the removal of oxygenated sulfur compounds from a hydrocarbon stream, especially the effluent from a sulfuric acid alkylation reactor, in which the hydrocarbon stream is first subjected to deentrainment of any carryover liquid sulfuric acid and then passed over a sorbent which removes the oxygenated sulfur compounds.

Abstract: A process for the isomerization of heptane preferably contained within a naphtha stream is disclosed wherein the naphtha is stripped of the butanes and the pentanes and hexanes are removed for isomerization. The heptanes and heavier are fed to a distillation column reactor containing an isomerization catalyst where the normal heptane is isomerized to mono and di branched heptane and removed as overheads. The cyclic heptanes and heavier are removed as bottoms and for feed to a catalytic reforming process.

Abstract: Cumene and secondary butyl benzene are produced simultaneously in a distillation column reactor by feeding propylene, butylene and benzene to the reactor. Unreacted benzene is removed as overheads and cumene and secondary butyl benzene are removed as products. The catalysts used are acid cation exchange resins, zeolites, particularly beta zeolite.

Abstract: A selected boiling range fluid catalytically cracked naphtha stream is subjected to simultaneous splitting, thioetherification of a light boiling range naphtha and selective hydrogenation of the dienes in a medium boiling range naphtha.

Abstract: An energy efficient process scheme for a highly exothermic reaction-distillation system in which the reactor is external to the distillation column and the feed to the reactor comprises a mixture of at least one liquid product stream from the distillation column with or without other liquid/vapor reactants. The reactor is operated under adiabatic and boiling point conditions and at a pressure that results in vaporizing a portion of the liquid flow through the reactor due to the heat of reaction. Under these conditions, reaction temperature is controlled by reactor pressure. The pressure (and hence the temperature) is maintained at a sufficiently high level such that the reactor effluent can be efficiently used to provide reboil heat for the distillation column.