Abstract:
A method for producing acetic anhydride that includes operating a high shear device at a shear rate of greater than about 20,000 s−1, wherein the high shear device is configured with a rotor and a stator; forming in the high shear device an emulsion having a liquid catalyst dispersed in an acetic acid solution; introducing the emulsion into a reactor at conditions suitable for the production of ketene; and reacting at least some ketene with acetic acid to produce acetic anhydride.
Abstract:
Herein disclosed is a method of hydrating an alkylene oxide that includes introducing an alkylene oxide into water to form a first stream; flowing the first stream through a high shear device to produce a second stream; and contacting the second stream with a catalyst in a reactor to hydrate the alkylene oxide and form an alkylene glycol.
Abstract:
Herein disclosed is a method of generating products from microorganisms, comprising super-saturating a liquid medium with a gas consumable by the microorganisms in a high shear device operating at a shear rate of greater than 1,000,000 s−1 to produce a gas-super-saturated (GSS) medium, wherein the GSS medium maintains a GSS level for at least 10 minutes; feeding the GSS medium to microorganisms; allowing the microorganisms to grow by consuming the gas and generate products via photosynthesis or chemosynthesis; and recovering the products. In an embodiment, the microorganisms are genetically modified. In an embodiment, the microorganisms include bacteria, protozoa, algae, or fungi, or a combination thereof. In an embodiment, the gas consumable by the microorganisms is selected from the group consisting of carbon dioxide, nitrogen, air, oxygen, methane, and combinations thereof. A suitable system is also discussed in this disclosure.
Abstract:
Herein disclosed is a method of generating products from microorganisms, comprising super-saturating a liquid medium with a gas consumable by the microorganisms in a high shear device operating at a shear rate of greater than 1,000,000 s−1 to produce a gas-super-saturated (GSS) medium, wherein the GSS medium maintains a GSS level for at least 10 minutes; feeding the GSS medium to microorganisms; allowing the microorganisms to grow by consuming the gas and generate products via photosynthesis or chemosynthesis; and recovering the products. In an embodiment, the microorganisms are genetically modified. In an embodiment, the microorganisms include bacteria, protozoa, algae, or fungi, or a combination thereof. In an embodiment, the gas consumable by the microorganisms is selected from the group consisting of carbon dioxide, nitrogen, air, oxygen, methane, and combinations thereof. A suitable system is also discussed in this disclosure.
Abstract:
Herein disclosed is a method of generating products from microorganisms, comprising super-saturating a liquid medium with a gas consumable by the microorganisms in a high shear device operating at a shear rate of greater than 1,000,000 s−1 to produce a gas-super-saturated (GSS) medium, wherein the GSS medium maintains a GSS level for at least 10 minutes; feeding the GSS medium to microorganisms; allowing the microorganisms to grow by consuming the gas and generate products via photosynthesis or chemosynthesis; and recovering the products. In an embodiment, the microorganisms are genetically modified. In an embodiment, the microorganisms include bacteria, protozoa, algae, or fungi, or a combination thereof. In an embodiment, the gas consumable by the microorganisms is selected from the group consisting of carbon dioxide, nitrogen, air, oxygen, methane, and combinations thereof. A suitable system is also discussed in this disclosure.
Abstract:
A reactor comprising at least one contact surface made from, coated with, or impregnated by a catalyst, wherein the contact surface comprises a sintered metal or a ceramic, and wherein the reactor is configured to subject a reactant stream to shear. A system for carrying out a heterogeneously catalyzed reaction, the system comprising a reactor as described above and a pump configured for delivering reactants to the at least one reactor. A method for carrying out a heterogeneously-catalyzed reaction by introducing reactants into a reactor comprising at least one contact surface made from, coated with, or impregnated by a catalyst under conditions which promote production of a desired product, wherein the contact surface comprises a sintered metal or a ceramic, and forming a dispersion of reactants within the reactor, wherein the dispersion comprises droplets or gas bubbles of reactant with an average diameter of less than about 5 μm.
Abstract:
Herein disclosed is a method of producing value-added product from light gases, the method comprising: (a) providing light gases comprising at least one compound selected from the group consisting of C1-C6 compounds and combinations thereof; (b) intimately mixing the light gases with a liquid carrier in a high shear device to form a dispersion of gas in the liquid carrier, wherein the dispersion is supersaturated with the light gases and comprises gas bubbles at least some of which have a mean diameter of less than or equal to about 5 micron(s); (c) allowing the value-added product to form and utilizing vacuum to extract unreacted light gases from the liquid carrier; (d) extracting the value-added product; wherein the value-added product comprises at least one component selected from the group consisting of higher hydrocarbons, hydrogen, olefins, alcohols, aldehydes, and ketones. A system for producing value-added product from light gases is also disclosed.
Abstract:
Herein disclosed is a method for producing a predispersed wax product comprising: operating a high shear device having at least one rotor/stator, configurable for a shear rate of at least 20,000 s−1; introducing wax and a carrier liquid into said high shear device; and forming a dispersion of wax in a carrier liquid, wherein the wax comprises globules with an average diameter less than 5 mm.
Abstract:
Herein disclosed is a method for coal liquefaction comprising: supersaturating a hydrocarbonaceous liquid stream in a high shear device with a gas stream comprising hydrogen and optionally one or more C1-C6 hydrocarbons to form a supersaturated dispersion; and contacting the supersaturated dispersion with coal in the high shear device or in a coal liquefaction reactor to generate a product stream. In some embodiments, the method further comprises utilizing a conversion catalyst, wherein the catalyst is provided as a slurry, a fluidized bed, or a fixed bed. In some embodiments, the method further comprises feeding a conversion catalyst into the high shear device. In some embodiments, the method further comprises recycling at least a portion of an off gas from the reactor, recycling at least a portion of the product stream from the reactor, or both. Herein also disclosed is a system for coal liquefaction.
Abstract:
Herein disclosed is a catalyst composition for producing organic compounds comprising (a) a catalyst that promotes the oxidative coupling of methane (OCM) and a methane steam reforming (MSR) catalyst, wherein the catalyst composition causes oxidative dehydrogenation to form reactive species and oligomerization of the reactive species to produce the organic compounds; or (b) a catalyst that promotes syngas generation (SG) and a Fischer-Tropsch (FT) catalyst wherein the catalyst composition causes non-oxidative dehydrogenation to form reactive species and oligomerization of the reactive species to produce the organic compounds; or (c) a SG catalyst, a MSR catalyst, and a FT catalyst wherein the catalyst composition causes non-oxidative dehydrogenation to form reactive species and oligomerization of the reactive species to produce the organic compounds; or (d) a FT catalyst and a MSR catalyst wherein the catalyst composition causes reforming reactions and chain growing reactions to produce the organic compounds.