6629 results about "Propane" patented technology

The present disclosure relates to compositions comprising a copolymer that includes a first monomer and a second monomer that is different from the first monomer, wherein both the first and second monomer are selected from the group consisting of 3-sulfopropyl acrylate potassium salt, sodium acrylate, N-(tris(hydroxyl methyl)methyl)acrylamide, and 2-acrylamideo-2-methyl-1-propane sulfonic acid. The present disclosure further relates to methods for preparing the copolymer compositions and shaped articles comprising the copolymers.

Tobaccos are cured in a manner so as to provide tobaccos having extremely low tobacco specific nitrosamine (TSNA) contents. Harvested Virginia tobacco is subjected to flue-curing so as to provide flue-cured tobacco. During the curing processing steps, contact of the tobacco with nitric oxide gases, such as those produced as combustion products of propane burning heating units, is avoided. Tobacco in curing barns is not subjected to direct-fire curing techniques, but rather, heat for tobacco curing can be provided by heat exchange or electrical heating methods.

A process for the recovery of ethane, ethylene, propane, propylene and heavier hydrocarbon components from a hydrocarbon gas stream is disclosed. In recent years, the preferred method of separating a hydrocarbon gas stream generally includes supplying at least portions of the gas stream to a fractionation tower having at least one reboiler, and often one or more side reboilers, to supply heat to the column by withdrawing and heating some of the tower liquids to produce stripping vapors that separate the more volatile components from the desired components. The reboiler and side reboilers (if any) are typically integrated into the feed stream cooling scheme to provide at least a portion of the refrigeration needed to condense the desired components for subsequent fractionation in the distillation column. In the process disclosed, the tower reboiling scheme is modified to use one or more tower liquid distillation streams from a point higher in the column than is used in the conventional reboiling scheme, providing colder stream(s) for the reboiler(s) that allow more effective cooling of the feed streams and thereby improve the efficiency with which the desired components are recovered. In addition, the tower liquid streams withdrawn from a higher point in the column contain larger quantities of the more volatile components, which when vaporized provide better stripping of undesirable components like carbon dioxide without reducing the recovery of the desired components. The heated distillation stream is returned to a lower point on the fractionation tower that is separated from the withdrawal point by at least one theoretical stage.

Disclosed are processes for the production of fluorinated olefins, preferably adapted to commercialization of CF3CF═CH2 (1234yf). Three steps may be used in preferred embodiments in which a feedstock such as CCl2═CClCH2Cl (which may be purchased or synthesized from 1,2,3-trichloropropane) is fluorinated (preferably with HF in gas-phase in the presence of a catalyst) to synthesize a compound such as CF3CCl═CH2, preferably in a 80-96% selectivity. The CF3CCl═CH2 is preferably converted to CF3CFClCH3 (244-isomer) using a SbCl5 as the catalyst which is then transformed selectively to 1234yf, preferably in a gas-phase catalytic reaction using activated carbon as the catalyst. For the first step, a mixture of Cr2O3 and FeCl3 / C is preferably used as the catalyst to achieve high selectivity to CF3CCl═CH2 (96%). In the second step, SbCl5 / C is preferably used as the selective catalyst for transforming 1233xf to 244-isomer, CF3CFClCH3. The intermediates are preferably isolated and purified by distillation and used in the next step without further purification, preferably to a purity level of greater than about 95%.

Energy commodities in the form of electricity and combustible fuel (e.g. natural gas, propane) are used by appliances in a fashion which is monitored and controlled through a Premises Energy Management System (PEMS). The system facilitates direct monitoring and control of energy-consuming appliances, in real time, utilizing automated programmatic control and a plurality of human interfaces including local display and control, email, web browser, text messaging, and integrated voice response (IVR). A Monitoring and Control Coordinator (MCC) provides centralized coordination of functions and one or more Communicating Appliance Interfaces (CAI) interacting with energy consuming appliances are interconnected via wired and wireless communication networks and protocols. The system may retrieve information from third parties, such as weather services, for optimizing energy usage. An interface may be provided to the energy provider / purveyor to enhance the provision of energy by providing additional real-time services such as demand management and service outage management.

The invention provides a fracturing sand mixing device used for mixing fracturing fluid. The fracturing sand mixing device comprises a solid-liquid mixing device, and the solid-liquid mixing device is a pressure container. The solid-liquid mixing device comprises a solid lead-in port capable of leading in solid particles of the fracturing fluid, a base fluid lead-in port for leading in base fluid of the fracturing fluid, a mixing inner cavity for accommodating the solid particles and the base fluid and a solid-liquid lead-out port for leading out the fracturing fluid formed by mixing. Substances such as carbon dioxide or petroleum gas which are in a gas state under normal temperature can be kept in a liquid state by high pressure through the fracturing sand mixing device and are mixed with the solid particles to form the fracturing fluid, and the goal of preparing the fracturing fluid with liquid carbon dioxide or liquefied petroleum gas (propane) serving as the base fluid is achieved.

The invention provides a fracturing sand mixing device used for mixing fracturing fluid. The fracturing sand mixing device comprises a solid conveying device and a solid-liquid mixing device communicated with the solid conveying device, wherein the solid-liquid mixing device is a pressure container. The solid-liquid mixing device comprises a solid lead-in port capable of leading in solid particles of the fracturing fluid output by the solid conveying device, a base fluid lead-in port for leading in base fluid of the fracturing fluid, a mixing inner cavity for accommodating the solid particles and the base fluid and a solid-liquid lead-out port for leading out the fracturing fluid formed by mixing. Substances such as carbon dioxide or petroleum gas which are in a gas state under normal temperature can be kept in a liquid state by high pressure through the fracturing sand mixing device and are mixed with the solid particles to form the fracturing fluid, and the goal of preparing the fracturing fluid with liquid carbon dioxide or liquefied petroleum gas (propane) serving as the base fluid is achieved.