Patent application number | Description | Published |
20140027811 | SEMICONDUCTOR DEVICE - A semiconductor device includes a metal-oxide-semiconductor field effect transistor (MOSFET), in which parasitic silicon controlled rectifier (SCR) equivalent circuits are formed in the MOSFET, and the MOSFET further includes a drain region. The drain region includes P-type heavily doped regions which are different from each other, in which the P-type heavily doped regions are respectively operated as anodes of the SCR equivalent circuits. | 01-30-2014 |
20140061788 | SEMICONDUCTOR DEVICE AND METHOD OF FABRICATING THE SAME - A semiconductor device is provided. The semiconductor device includes a drain region, a source region, a channel region and a hybrid doped region. The drain region of a first conductivity type is located in a substrate. The source region of the first conductivity type is located in the substrate and surrounding the drain region. The channel region is located in the substrate between the source region and the drain region. The hybrid doped region includes a top doped region and a compensation doped region. The top doped region is of a second conductivity type, having a doping concentration decreased from a region near the channel region to a region near the drain region, and located in the substrate between the channel region and the drain region. The compensation doped region of the first conductivity type is located in the top doped region to compensate the top doped region. | 03-06-2014 |
20150340432 | SEMICONDUCTOR DEVICE - A semiconductor device is disclosed. A substrate of a first conductivity type is provided. The substrate has a first area and a second area. An epitaxial layer of a second conductivity type is disposed on the front side of the substrate. A first doped region of the first conductivity type is disposed in the epitaxial layer in the first area, wherein a doping depth of the first doped region is gradually decreased away from the second area. At least one second doped region of the second conductivity type is disposed in the first doped region, wherein a doping depth of the at least one second doped region is gradually increased away from the second area. A dielectric layer is disposed on the epitaxial layer. A first conductive layer is disposed on the dielectric layer. | 11-26-2015 |
Patent application number | Description | Published |
20100115829 | HYDROCARBON FUEL COMPOSITIONS - The present invention relates to a hydrocarbon fuel composition comprising (i) at least 99% by weight of a base gas; and (ii) additives comprising (a) 2 to 50 ppm organometallic compound; and (b) 100 to 5000 ppm aniline or substituted aniline and 100 to 5000 ppm toluidine. The present invention discloses addition of an additive or additive mixture to base fuel preferably, liquefied petroleum gas. The addition of additive mixture not only improves the properties of the base fuel for use as torch gas for cutting and welding application, but also reduces the consumption of both fuel and oxygen for cutting applications. | 05-13-2010 |
20120071572 | COUNTER-CURRENT MULTISTAGE FISCHER TROPSCH REACTOR SYSTEMS - The invention discloses an improved multistage fischer tropsch process scheme for the production of hydrocarbon fuels comprising feeding gaseous phase syngas and liquid stream hydrocarbons in a counter current manner such as herein described into the reaction vessel at a number of stages containing reaction catalysts; wherein fresh syngas enters into the stage where the product liquid stream leaves and the fresh liquid stream enters into the stage where the unreacted syngas leaves; wherein further the temperature of each stage can be controlled independently. More particularly the invention relates to improving the heat release in different reactors, product selectivity and reactor productivity of FT reactors. | 03-22-2012 |
20120311923 | GASOHOL FUEL COMPOSITION FOR INTERNAL COMBUSTION ENGINES - The present invention relates to a gasohol fuel composition that prevents corrosion of the metallurgies involved in fuel storage tanks, vehicle fuel tanks, fuel distribution systems, and transportation systems. The novel gasohol fuel composition comprises of a major portion of an alcohol blended gasoline fuel and a minor portion of a corrosion inhibitor formulation, wherein the corrosion inhibitor formulation comprises of (i) a reaction product of (a) a monosaturated fatty acid; and (b) an azomethine compound derived from a condensation reaction between a carbonyl compound and an amine compound; (ii) a fatty acid oil or ester selected from a group comprising of castor oil, palm oil, soyabean oil, and methyl soya ester; (iii) a dispersing agent, the dispersing agent being a sulfonate compound; and (iv) a viscosity reducing agent selected from a group comprising of ethanol, isopropanol, and propargyl alcohol. | 12-13-2012 |
Patent application number | Description | Published |
20150148581 | METHODS FOR PREPARING COMPOSITES OF ACTIVATED CARBON/ZINC OXIDE AND ACTIVATED CARBON/ZINC OXIDE/NICKEL OXIDE FOR DESULFURIZATION OF FUELS - Activated carbon\nickel oxide\zinc oxide (AC\NiO\ZnO) and activated carbon\zinc oxide (AC\ZnO) were prepared and used as adsorbents for removal of thiophene, benzothiophene (BT) and dibenzothiophene (DBT) as sulfur compounds from hydrocarbon materials such as diesel fuel. The materials exhibited an efficient and economical way for removing sulfur compounds due to its low-energy consumption, ambient operation temperature and atmospheric pressure. A simple regeneration method of the spent adsorbents. | 05-28-2015 |
20150182946 | NOVEL METHOD FOR PREPARING ALUMINA-ZINC OXIDE-NICKEL OXIDE COMPOSITE FOR DESULFURIZATION - Alumina/NiO/ZnO and Alumina/ZnO are synthesized via a novel modified hydrothermal method and investigated for the desulfurization activities. Sulfur compounds such as thiophene, benzothiophene (BT) and dibenzothiophene (DBT) are tested for their removal from model diesel fuel. The prepared composite materials were examined by the means of N | 07-02-2015 |
20150191582 | WEATHERABILITY AND DURABILITY OF LOW-DENSITY POLYETHYLENE NANOCOMPOSITES WITH CLAY, SILICA AND ZINC OXIDE - A low-density polyethylene nanocomposite comprising 5 weight percent or more of at least one nanoscale filler selected from the group consisting of montmorillonite clay, silica and zinc oxide. Changes in weatherability of the three low-density polyethylene nanocomposites based on the nanoscale fillers are determined. A surface area of the nanoscale filler in the nanocomposites is from 10 m | 07-09-2015 |
20150197636 | FREE RADICAL INITIATED METHYL METHACRYLATE-ARABIAN ASPHALTENE POLYMER COMPOSITES - A polymer-asphaltene composite matrix containing an Arabian heavy asphaltene which is a filler obtained from Arabian heavy residue. A method of synthesizing composites based on polymer-asphaltenes matrix with different amounts of Arabian heavy asphaltenes. The method includes mixing methyl methacrylate monomer with asphaltene and performing in-situ polymerization with dispersion of the asphaltene molecules into the styrene monomer mixture. | 07-16-2015 |
20150376352 | WEATHERABILITY AND DURABILITY OF LOW-DENSITY POLYETHYLENE NANOCOMPOSITES WITH CLAY, SILICA AND ZINC OXIDE - A low-density polyethylene nanocomposite comprising 5 weight percent or more of at least one nanoscale filler selected from the group consisting of montmorillonite clay, silica and zinc oxide. Changes in weatherability of the three low-density polyethylene nanocomposites based on the nanoscale fillers are determined. A surface area of the nanoscale filler in the nanocomposites is from 10 m | 12-31-2015 |
20150376370 | WEATHERABILITY AND DURABILITY OF LOW-DENSITY POLYETHYLENE NANOCOMPOSITES WITH CLAY, SILICA AND ZINC OXIDE - A low-density polyethylene nanocomposite comprising 5 weight percent or more of at least one nanoscale filler selected from the group consisting of montmorillonite clay, silica and zinc oxide. Changes in weatherability of the three low-density polyethylene nanocomposites based on the nanoscale fillers are determined. A surface area of the nanoscale filler in the nanocomposites is from 10 m | 12-31-2015 |
Patent application number | Description | Published |
20140163168 | POLYMER-CLAY NANOCOMPOSITE MATERIAL - The polymer-clay nanocomposite material is a nanocompo site formed from poly(styrene-co-butyl methacrylate) copolymer and organo-modified clay by in situ polymerization. Nanoparticles of a montmorillonite clay that has been modified with a quaternary ammonium salt is dispersed into a mixture of polystyrene and butyl methacrylate monomers to form a mixture, which then undergoes bulk radical polymerization. The poly(styrene-co-butyl methacrylate) copolymer may have a styrene to butyl methacrylate ratio of about 60 to 40 or about 20:80. Preferably, the organically modified montmorillonite clay forms between 1.0 wt % and 5.0 wt % of the mixture. A free radical initiator, such as benzoyl peroxide, is used to initiate polymerization. The clay nano-filler provides the nanocomposite with improved thermal stability. | 06-12-2014 |
20140305844 | IONIC LIQUID FOR DESULFURIZATION OF LIGHT FUELS - The ionic liquid for desulfurization of light fuels is 1-methyl-3-pentyl 1H-imidazolium periodate, having the structural formula: | 10-16-2014 |
20150031811 | POLYMER-CLAY NANOCOMPOSITE MATERIAL - The polymer-clay nano composite material is a nanocomposite formed from poly(styrene-co-ethyl methacrylate) copolymer and organo-modified clay by in situ polymerization. Nanoparticles of a montmorillonite clay that has been modified with a quaternary ammonium salt are dispersed into a mixture of styrene and ethyl methacrylate monomers to form a mixture, which then undergoes bulk radical polymerization. The poly(styrene-co-ethyl methacrylate) copolymer preferably has a styrene to ethyl methacrylate ratio of about 1:1. Preferably, the organically modified montmorillonite clay forms between 1.0 wt % and 5.0 wt % of the mixture. A free radical initiator, such as benzoyl peroxide, is used to initiate polymerization. The clay nano-filler provides the nanocomposite with improved thermal stability. The poly(styrene-co-ethyl methacrylate) copolymer has the structural form: | 01-29-2015 |
20150073090 | ARABIAN ASPHALTENE REINFORCED POLYSTYRENE COMPOSITES - The Arabian asphaltene reinforced polystyrene composites include a matrix of polystyrene and an asphaltene filler isolated from Arab heavy crude oil residue that is distributed within the polystyrene matrix to form the Arabian asphaltene reinforced polystyrene composite. Asphaltenes are obtained from the Arab crude oil by precipitation in n-heptane. Styrene monomer and the asphaltenes filler are polymerized by using heat to initiate in situ polymerization. Testing shows that the asphaltene reinforced polystyrene composites have improved viscoelastic properties (e.g., flexural strength) and thermal stability. | 03-12-2015 |
Patent application number | Description | Published |
20100032343 | Metallic clay based FCC gasoline sulfur reduction additive compositions - Compositions and processed for their use as additives for reducing the sulfur content of FCC gasoline employ a support material having deposited on its surface (a) a first metal component from Group IIB of the Periodic Table and (b) a second metal component from Group III or Group IV of the Periodic Table. The additive composition is preferably made of a montmorillonite clay support containing zinc and gallium, zinc and zirconium. Alternatively, the additive composition includes support material having deposited on its surface a metal component from Group III of the Periodic Table, preferably a montmorillonite clay support containing gallium. The clay is impregnated with the metal(s) using the known incipient wetness method and the dried powdered additive composition is preferably formed into shapes suitable for use in the FCC unit. | 02-11-2010 |
20100216633 | Oil- based thermo-neutral reforming with a multi-component catalyst - A method is provided for the thermo-neutral reforming of liquid hydrocarbon fuels which employs a Ni,Ce | 08-26-2010 |
20110120912 | METALLIC CLAY BASED FCC GASOLINE SULFUR REDUCTION ADDITIVE COMPOSITIONS - Compositions and processed for their use as additives for reducing the sulfur content of FCC gasoline employ a support material having deposited on its surface (a) a first metal component from Group IIB of the Periodic Table and (b) a second metal component from Group III or Group IV of the Periodic Table. The additive composition is preferably made of a montmorillonite clay support containing zinc and gallium, zinc and zirconium. Alternatively, the additive composition includes support material having deposited on its surface a metal component from Group III of the Periodic Table, preferably a montmorillonite clay support containing gallium. The clay is impregnated with the metal(s) using the known incipient wetness method and the dried powdered additive composition is preferably formed into shapes suitable for use in the FCC unit. | 05-26-2011 |
20130165315 | METHOD OF FORMING A HYDROCARBON CRACKING CATALYST - The method of forming a hydrocarbon cracking catalyst provides a method of varying or tuning the mesophase MCM-41 or microporous ZSM-5 properties in biporous ZSM-5/MCM-41 composites, depending on the requirements of the intended application. The method includes the steps of performing a surfactant-mediated hydrolysis of ZSM-5 to form a solution, and then adjusting the pH of the solution to selectively tune the microporous and mesoporous properties of the final ZSM-5/MCM-41 catalyst product. Following tuning, soluble aluminosilicates are hydrothermically condensed to form a mesoporous material over the remaining ZSM-5 particles to form the ZSM-5/MCM-41 composite. The ZSM-5/MCM-41 composite may be used as a hydrocarbon cracking catalyst for cracking gas, oil or the like. | 06-27-2013 |
20130210613 | CATALYST ADDITIVE FOR REDUCTION OF SULFUR IN CATALYTICALLY CRACKED GASOLINE - The present invention concerns a novel additive composition for reducing sulfur content of a catalytically cracked gasoline fraction. This additive composition comprises a support consisting of porous clay into which a first metal from group IVB is incorporated and a second metal from group IIB is impregnated. Preferably, the first incorporated metal is zirconium and the second impregnated metal is zinc. The sulfur reduction additive is used in the form of a separate particle in combination with a conventional cracking catalyst in a fluidized catalytic cracking process to convert hydrocarbon feed stocks into gasoline having comparatively lower sulfur content and other liquid products. | 08-15-2013 |
20140106958 | CLAY ADDITIVE FOR REDUCTION OF SULFUR IN CATALYTICALLY CRACKED GASOLINE - Compositions and processes for their use as additives for reducing the sulfur content of FCC gasoline employ a support material montmorillonite clay material. A fluid catalytic cracking (FCC) mixture, therefore, is provided comprising an FCC catalyst and separate particles of sulfur reduction additive consisting of porous montmorillonite clay. | 04-17-2014 |
20160107153 | MODIFIED ZEOLITE CATALYST AND METHODS FOR PRODUCING AND USING SAME - The invention pertains to a zeolite catalyst, methods of making same, and its use in the catalytic cracking of naphtha for the production of lower molecular weight olefins and alkanes, while minimizing production less desirable products. A zeolite is modified by base leaching and by the addition of a metal cation, thereby lowering the Si/Al | 04-21-2016 |
Patent application number | Description | Published |
20140260413 | ABSORPTION COOLING SYSTEM - The absorption cooling system is capable of continuous operation both day and night while using only solar power for its basic operation. The system is an absorption type system using phase changes of aqua-ammonia and a storage system for storing chilled refrigerant for operations when solar power is not available. When solar power is available during the day, the system operates according to the principles of absorption cooling systems, and also stores a reserve of chilled refrigerant in the storage unit. The stored refrigerant then continues the absorption process during the night when solar energy is not available, thereby providing uninterrupted cooling during the day, and also at night when solar energy is not available. | 09-18-2014 |
20150052931 | HEAT EXCHANGER - The heat exchanger is adapted for cooling a coolant (e.g., water), used to cool a device or an area (e.g., building interior), such as during periods of peak energy cost and usage, to save energy and energy costs. The heat exchanger includes a coolant storage tank with one or more refrigerant circulators in contact with the floor of the tank. The circulators use a refrigerant having a freezing temperature colder than the coolant, with coolant on the floor of the tank forming a layer of ice thereon. A rotary scraper extends up through the tank floor from each circulator, with the scrapers operating to remove the thin layer of ice from the floor as the ice forms. The resulting ice chips are relatively small and thin, thus having a relatively large surface area for their volume in order to maximize melting and rapid cooling of the coolant. | 02-26-2015 |
20150053385 | HEAT EXCHANGER FLOW BALANCING SYSTEM - The heat exchanger flow balancing system serves to substantially equalize fluid flow through essentially identical diameter heat exchanger tubes in a heat exchanger having a single inlet plenum, a single outlet plenum, and a series of equal diameter heat exchanger tubes extending therebetween. In one embodiment, a series of different diameter orifices are provided at the inlet end of each of the tubes, with those tubes farther from the single larger diameter inlet pipe to the plenum generally having smaller orifices. In another embodiment, each of the tubes is provided with a conical nozzle at its inlet end, with those tubes farther from the single inlet pipe to the plenum generally having smaller diameter nozzles. The effect is to substantially equalize fluid flow through all of the heat exchanger tubes, thus increasing the efficiency of the heat exchanger. | 02-26-2015 |
20150143827 | ECONOMIZER FOR AN INTERMITTENT ABSORPTION REFRIGERATION SYSTEM - An economizer for a solar powered intermittent absorption refrigeration system improves the coefficient of performance of the refrigeration system. The economizer recovers waste energy rejected by an absorber during an absorption process, stores the waste energy, and supplies the waste energy to a generator during a generation process, thereby reducing the amount of energy input needed to operate the system. | 05-28-2015 |
20150176869 | INTERMITTENT ABSORPTION REFRIGERATION SYSTEM EQUIPPED WITH A WASTE ENERGY STORAGE UNIT - A solar powered intermittent absorption refrigeration system utilizes helical coil heat exchangers for generation, absorption, dephlegmation, condensation and heat recovery. The thermo-siphon effect is used to supply and reject heat from the system, to recover and utilize heat from a waste energy unit, to reject heat of absorption, and to pressurize and depressurize the system. The system produces ice blocks during the nighttime without any requirement of electrical energy for the operation of the system. | 06-25-2015 |
20150285542 | INTERMITTENT ABSORPTION SYSTEM WITH A LIQUID-LIQUID HEAT EXCHANGER - The intermittent absorption system with a liquid-liquid heat exchanger includes two generator/absorber units that operate out-of-phase, a solar collector unit, a dephlegmator, a condenser unit, an evaporator, and valves to control the flow of aqua-ammonia coolant through the system. The system operates on a two-day cycle. On the first day, during the daytime, the first generator/absorber unit generates liquid ammonia, while on the second day of the cycle, the roles are reversed, the second generator/absorber unit generating liquid ammonia. At the start of each day, one generator/absorber unit is partially pressurized and the other partially depressurized by liquid-liquid heat exchange between their heat exchangers, followed by disconnecting the heat exchangers from each other and connecting the generator to the solar collector to complete pressurization. The liquid-liquid heat exchange between the generator/absorber units reduces the heat required from the solar collector to generate liquid ammonia refrigerant, improving the coefficient of performance. | 10-08-2015 |
20150285543 | SOLAR POWERED INTERMITTENT OPERATION BASED CONTINUOUS ABSORPTION SYSTEM - An intermittent operation based continuous absorption system (IOBCAS) which supports cooling effect during the daytime without the use of a solution pump is provided. The IOBCAS may utilize an isochoric process for pressurization of the system and the system may include a plurality of generator-absorber units that intermittently operate in succession to provide a continuous refrigeration cooling effect during the daytime. The system of the present disclosure enables the plurality of generator-absorber units to switch between a generation, absorption, and heat recovery mode of operation to provide cooling effect during the daytime which a higher coefficient of performance compared with conventional intermittent system. | 10-08-2015 |
20150300702 | INTERMITTENT ABSORPTION REFRIGERATION SYSTEM - The intermittent absorption refrigeration system includes a primary circuit having a generator/absorber, a dephlegmator, a condenser, an evaporator, and solar collectors to provide heat to the generator. The system also includes an ejector-based secondary circuit having a generator/absorber, an ejector, a condenser, a refrigerant storage unit, and solar collectors. Both circuits are aqua-ammonia systems, using ammonia as the refrigerant and water as the absorber liquid. The ejector permits evaporation during the daytime and storage of liquid ammonia refrigerant that is used for cooling in the heat exchanger of the primary circuit condenser and in the primary circuit absorber, thus permitting the primary circuit evaporator to operate at lower temperatures for low temperature freezing applications in the daytime, even at high ambient temperature. | 10-22-2015 |
20150300703 | INTERMITTENT ABSORPTION REFRIGERATION SYSTEM WITH AN EJECTOR - The intermittent absorption refrigeration system with an ejector includes a generator/absorber unit, a solar collector unit, a dephlegmator, a condenser unit, a first evaporator, and valves to control the flow of aqua-ammonia coolant through the system, as in a conventional intermittent absorption refrigeration system. However, the present system also includes an ejector disposed between the dephlegmator and the condenser, and also a second evaporator disposed in a feedback loop between the first evaporator and the ejector, together with appropriate valves to control coolant flow through the feedback loop. The utilization of the ejector and the feedback loop in the intermittent system allows the intermittent system to produce a cooling effect during the daytime, as well as during the nighttime, which increases the coefficient of performance of the intermittent system. | 10-22-2015 |