Patent application number | Description | Published |
20130017982 | LUBRICATING OIL COMPOSITION - The present invention provides a lubricating oil composition comprising at least one type of base oil selected from mineral oils and synthetic oils, and a succinate ester and a sarcosinic acid as rust prevention agents. The succinate ester content is preferably set at 0.01 to 0.1 wt. %, and the sarcosinic acid content is preferably set at 0.001 to 0.01 wt. %. Further, they are preferably set such that the resulting weight ratio of the succinate ester content and sarcosinic acid content is 1:0.01 to 0.7. The lubricating oil composition according to the present invention shows excellent rust prevention properties and a satisfactorily long oxidation lifetime. Further it allows to attain a high level of anti-sludge performance and extreme pressure performance and lubrication performance, even when it is used for example in turbine bearings in combined cycle generators having multiplier gears operated under severe high temperature and high pressure conditions. | 01-17-2013 |
20130032401 | METHODS AND SYSTEMS FOR DRILLING - A method of steering a drill bit to form an opening in a subsurface formation, comprises a) determining a distance from design of a well, and b) determining an angle offset from design of the well wherein angle offset from design is the difference between the inclination and azimuth of the hole and the inclination and azimuth of plan, c) wherein at least one distance from design and at least one angle offset from design are determined in real time based, at least in part, on a position of the hole at the last survey, a position at a projected current location of the bit, and a projected position of the bit. | 02-07-2013 |
20130032407 | METHODS AND SYSTEMS FOR DRILLING - A method of controlling a direction of a toolface of a bottom hole assembly for slide drilling, comprises a) synchronizing the toolface wherein synchronizing the toolface comprises determining a relationship between the rotational position of the down hole toolface with a rotational position at the surface of the formation for at least one point in time, b) stopping rotation of the drill string coupled to the bottom hole assembly, c) controlling torque at the surface of the drill string to control a rotational position of the toolface, and d) commencing a slide of the drill string. | 02-07-2013 |
20130043117 | APPARATUS FOR GASIFYING A FUEL WITH A DRIPPER EDGE AND HEAT SHIELD - The invention provides an apparatus for gasifying a fuel to form synthesis gas wherein also a slag is formed. The apparatus comprises: a pressure shell; a slag bath; a gasifier wall; a free-fall trajectory for slag; and a heat shield. The gasifier wall is arranged inside the pressure shell defining a gasification chamber. It comprises a converging wall part that is provided with a slag discharge opening, located above the quench fluid in the slag bath. The heat shield is arranged above the slag bath between the free-fall trajectory and the pressure shell. The heat shield has a wall structure for allowing passage of a cooling fluid, the wall structure comprising an upper wall part and a lower wall part. The lower wall part of the heat shield is essentially refractory free. | 02-21-2013 |
20130060055 | ORGANIC MOLYBDENUM COMPOUNDS AND LUBRICATING COMPOSITIONS WHICH CONTAIN SAID COMPOUNDS - Dicyclopentadienyl molybdenum crosslinked complexes which can be represented by general formula ( | 03-07-2013 |
20130071900 | PROCESS FOR PROCESSING A LIGNOCELLULOSIC MATERIAL - Calcium-containing lignocellulosic material is converted at a temperature in the range from equal to or more than 120° C. to equal to or less than 210° C. with an aqueous acid solution containing one or more inorganic acids and having a pH in the range from equal to or more than 1.8 to equal to or less than 4.0 to produce a mixture, containing pretreated lignocellulosic material and aqueous acid solution, having an overall pH in the range from equal to or more than 3.0 to equal to or less than 4.5. The process allows reduction in the formation of insoluble salts. | 03-21-2013 |
20130071901 | PROCESS FOR THE CONVERSION OF A XYLAN-CONTAINING FEED - A xylan-containing feed is contacted, in the first reactor essentially operated at plug flow, with an aqueous solution of an acid at a temperature in the range from equal to or more than 140° C. to equal to or less than 210° C. to produce an intermediate product. Then, the intermediate product is contacted, in the second reactor which comprises a continuously stirred tank reactor, with an aqueous solution of an acid at a temperature in the range from more than 130° C. to equal to or less than 200° C. to produce a final product. | 03-21-2013 |
20130072700 | PROCESS AND APPARATUS FOR THE PRODUCTION OF ETHYLENE OXIDE - The invention provides a process and an apparatus for the production of ethylene oxide from ethylene. Ethylene and oxygen are supplied to reactor tubes, wherein the reactor tubes are held by upper and lower tube sheets in a reactor vessel. The reactor vessel has a separation grid, dividing the reactor vessel into an upstream zone and a downstream zone. Coolant is supplied to the upstream zone from an upper coolant circuit and is removed from the upstream zone to the upper coolant circuit. A portion of coolant is removed as vapour from the upper coolant circuit. Coolant is supplied to the downstream zone from a lower coolant circuit and is removed from the downstream zone to the lower coolant circuit. Additional coolant is added to the lower coolant circuit. There is net flow of coolant through the separation grid from the downstream zone to the upstream zone. | 03-21-2013 |
20130086800 | FORMING INSULATED CONDUCTORS USING A FINAL REDUCTION STEP AFTER HEAT TREATING - A method for forming an insulated conductor heater includes placing an insulation layer over at least part of an elongated, cylindrical inner electrical conductor. An elongated, cylindrical outer electrical conductor is placed over at least part of the insulation layer to form the insulated conductor heater. One or more cold working/heat treating steps are performed on the insulated conductor heater. The cold working/heat treating steps include: cold working the insulated conductor heater to reduce a cross-sectional area of the insulated conductor heater by at least about 30% and heat treating the insulated conductor heater at a temperature of at least about 870° C. The cross-sectional area of the insulated conductor heater is then reduced by an amount ranging between about 5% and about 20% to a final cross-sectional area. | 04-11-2013 |
20130086803 | FORMING A TUBULAR AROUND INSULATED CONDUCTORS AND/OR TUBULARS - A method of forming a tubular around one or more insulated conductors includes providing one or more insulated conductors and a strip of carbon steel to a tubular assembly location. The strip of carbon steel is formed into a tubular shape in the tubular assembly location. At least a portion of the insulated conductors are provided lengthwise inside the tubular shape as the strip of carbon steel is being formed into the tubular shape such that the tubular shape at least partially surrounds the one or more insulated conductors. The longitudinal edges of the strip of carbon steel together are welded to form a carbon steel tubular around the insulated conductors. | 04-11-2013 |
20130087327 | USING DIELECTRIC PROPERTIES OF AN INSULATED CONDUCTOR IN A SUBSURFACE FORMATION TO ASSESS PROPERTIES OF THE INSULATED CONDUCTOR - A system for assessing one or more temperatures along an insulated conductor in an opening in a subsurface formation includes an insulated conductor with a length comprising at least two sections of insulation with different capacitances. The sections with the different capacitances include different takeoff temperatures for at least one dielectric property of the insulation. | 04-11-2013 |
20130087337 | THERMAL EXPANSION ACCOMMODATION FOR CIRCULATED FLUID SYSTEMS USED TO HEAT SUBSURFACE FORMATIONS - A method for accommodating thermal expansion of a heater in a formation includes flowing a heat transfer fluid through a conduit to provide heat to the formation and providing substantially constant tension to an end portion of the conduit that extends outside the formation. At least a portion of the end portion of the conduit is wound around a movable wheel used to apply tension to the conduit. | 04-11-2013 |
20130087383 | INTEGRAL SPLICE FOR INSULATED CONDUCTORS - A method includes coupling a core of a heating section to a core of an overburden section of an insulated conductor. A diameter of the core of the heating section is less than a diameter of the core of the overburden section. A first insulation layer is placed over the core of the heating section such that at least part of an end portion of the core of the heating section is exposed. A second insulation layer is placed over the core of the overburden section such that the second insulation layer extends over the exposed portion of the core of the heating section. A thickness of the second insulation layer is less than a thickness of the first insulation layer and an outer diameter of the overburden section is substantially the same as an outer diameter of the heating section. | 04-11-2013 |
20130087551 | INSULATED CONDUCTORS WITH DIELECTRIC SCREENS - An insulated conductor heater includes an electrical conductor that produce heats when an electrical current is provided to the electrical conductor. An inner electrical insulator at least partially surrounds the electrical conductor. The inner electrical insulator includes a first insulation material and a second insulation material. The second insulation material has a higher dielectric constant than the first insulation material. An outer electrical insulator at least partially surrounds the inner electrical insulator. The outer electrical insulator includes the first insulation material. An outer electrical conductor at least partially surrounds the electrical insulator | 04-11-2013 |
20130096328 | PROCESS FOR PREPARING AN EPOXIDE FROM AN OXYGENATE - The invention relates to an integrated process for preparing an epoxide from an oxygenate, wherein the production of a lower olefin from the oxygenate and the subsequent epoxidation of the lower olefin is combined and wherein isobutene, a by-product of the lower olefin production, is converted into a hydroperoxide that is used for the conversion of the lower olefin into the corresponding epoxide. | 04-18-2013 |
20130096329 | PROCESS FOR PREPARING AN EPOXIDE FROM AN OXYGENATE - The invention relates to an integrated process for preparing an epoxide from an oxygenate, wherein the oxygenate is converted into a lower olefin and the lower olefin is subsequently epoxidised, and wherein isobutane obtained after hydrogenation and subsequent normal/iso separation of C4 hydrocarbons obtained as by-product of the oxygenate conversion, is converted into a hydroperoxide that is used for the conversion of the lower olefin into the corresponding epoxide. | 04-18-2013 |
20130096352 | PROCESS FOR CONVERTING AN ALKYL TERT-ALKYL ETHER INTO AN ALKANOL AND AN ISO-ALKANE - The invention relates to a process for converting an alkyl tert-alkyl ether into an alkanol and an iso-alkane wherein the alkyl tert-alkyl ether is contacted with a hydrocracking catalyst in the presence of hydrogen under hydrocracking process conditions. | 04-18-2013 |
20130098806 | BITUMEN FROTH TREATMENT SETTLER FEED DISTRIBUTOR - A feed distributor for a settler is provided, the settler effective for separating a solvent-diluted bitumen froth into a water/solids stream and a hydrocarbon stream, the feed distributor comprising: an inlet conduit effective to route bitumen froth into the settler; and an essentially horizontal plate attached to a lower extremity of the inlet conduit and wherein the inlet conduit defines openings through which the solvent-diluted bitumen froth can pass from inside the inlet conduit to a volume above the essentially horizontal plate. | 04-25-2013 |
20130099167 | METHOD FOR PROCESSING FISCHER-TROPSCH OFF-GAS - A method for producing a gas comprising at least 80 vol % carbon monoxide from a Fischer-Tropsch off-gas comprising: (1) feeding Fischer-Tropsch off-gas through a column comprising an adsorbent bed at high pressure and discharging effluent; (2) reducing the pressure in the column and the bed slightly; (3) rinsing the column and the adsorbent bed with methane or carbon dioxide; (4) rinsing the column and the adsorbent bed with carbon dioxide; (5) reducing the pressure of the column and adsorbent bed to a low pressure; (6) rinsing the column and adsorbent bed with a mixture of hydrogen and nitrogen; (7) pressurizing the column and adsorbent bed to a high pressure using a mixture of hydrogen and nitrogen. The carbon monoxide rich product stream obtained in step (3) can be sent as feed to a Fischer-Tropsch reaction. In an embodiment, a gas comprising at least 80 vol % hydrogen is also produced. | 04-25-2013 |
20130102817 | PROCESS TO PREPARE JET FUELS AND ITS PRODUCTS - A jet fuel containing a major amount of a synthetic paraffinic kerosene fuel component is provided by:
| 04-25-2013 |
20130118059 | PROCESS FOR CONVERSION OF A CELLULOSIC MATERIAL - A process for conversion of a cellulosic material comprising
| 05-16-2013 |
20130118169 | SYSTEM AND PROCESS FOR GENERATION OF ELECTRICAL POWER - A system and process for generation of electrical power is provided. Electrical power is generated by a system including two integrated power cycles, a first power cycle utilizing water/steam as a working fluid and the second power cycle utilizing a fluid selected from the group consisting of molecular nitrogen, argon, a chemical compound having a boiling point of at most 65° C. at 0.101 MPa and a latent heat of vaporization of at least 350 kJ/kg, and a chemical compound having a boiling point of at most 65° C. at 0.101 MPa and a specific heat capacity as a liquid of at least 1.9 kJ/kg-° K as a working fluid. The working fluid of the second power cycle is expanded through a two-phase expander to produce power in the second power cycle, where the expanded working fluid of the second cycle has a vapor quality of at most 0.5. | 05-16-2013 |
20130118171 | SYSTEM AND PROCESS FOR GENERATION OF ELECTRICAL POWER - A system and process for generation of electrical power is provided. Electrical power is generated by a system including two integrated power cycles, a first power cycle utilizing water/steam as a working fluid and the second power cycle utilizing a fluid selected from the group consisting of molecular nitrogen, argon, a chemical compound having a boiling point of at most 65° C. at 0.101 MPa and a latent heat of vaporization of at least 350 kJ/kg, and a chemical compound having a boiling point of at most 65° C. at 0.101 MPa and a specific heat capacity as a liquid of at least 1.9 kJ/kg-° K as a working fluid. The working fluid of the second power cycle is expanded through a two-phase expander to produce power in the second power cycle, where the expanded working fluid of the second cycle has a vapor quality of at most 0.5. | 05-16-2013 |
20130119676 | METHOD OF PROCESSING FEED STREAMS CONTAINING HYDROGEN SULFIDE - A method of processing feed streams containing significant quantities of hydrogen sulfide is provided. The method includes providing a feed gas stream that includes hydrogen sulfide and hydrocarbons. The feed gas stream has at least 1% by volume hydrogen sulfide. At least a portion of the feed gas stream is separated into a hydrogen sulfide stream and a hydrocarbon stream. The hydrogen sulfide stream includes more hydrogen sulfide, by volume percent, than the feed stream; and the hydrocarbon stream contains less hydrogen sulfide, by volume percent, than the feed gas stream. The hydrocarbon gas stream is processed to produce a natural gas product selected from pipeline natural gas, compressed natural gas, and liquefied natural gas. Greater than one-third of the hydrogen sulfide stream, on a volume basis, is combusted to generate thermal power. | 05-16-2013 |
20130119677 | METHOD OF PRODUCING POWER - A process for producing power from a fuel stream containing at least 30 mol % hydrogen sulfide is provided. The fuel stream is combusted with an oxidant stream containing molecular oxygen to generate a combusted gas stream containing thermal power, where the molar ratio of molecular oxygen to hydrogen sulfide is at least 1:1. Electrical power is generated from the thermal power of the combusted gas stream. | 05-16-2013 |
20130122187 | METHOD OF PREPARING OR RECONDITIONING A LEAK STABLE GAS SEPARATION MEMBRANE SYSTEM - A method of making a gas separation membrane by providing a plating vessel with a volume of plating solution of gas-selective metal ions into which is placed a porous support. The plating solution is circulated over a surface of the porous support while maintaining conditions within the plating vessel so as to promote the electroless deposition. The circulation rate of the plating solution is such as to enhance the metal deposition onto the surface of the porous support in the formation of the gas separation membrane. | 05-16-2013 |
20130123551 | OLEFIN OLIGOMER COMPOSITION - Processes for the production of an alcohol, esters and aliphatic hydrocarbons are provided. In one embodiment, a process for the production of an alcohol comprises: oligomerizing an olefin or a mixture of olefins having the structural formula C | 05-16-2013 |
20130123556 | METHOD OF PRODUCING SULFUR DIOXIDE - A method of producing sulfur dioxide is provided. A feed gas stream comprising at least 5% by volume hydrogen sulfide is provided. The feed gas stream is separated into a hydrogen sulfide stream and a hydrocarbon gas stream. An oxidant stream is provided and is combusted with the hydrogen sulfide stream to produce thermal power and a combustion stream containing sulfur dioxide and steam. Sulfur dioxide is separated from the combustion stream. | 05-16-2013 |
20130123559 | METHOD OF PROCESSING FEED STREAMS CONTAINING HYDROGEN SULFIDE - A method of processing feed streams high in hydrogen sulfide is provided. The method includes providing a feed gas stream that includes hydrocarbons and at least 5 vol % hydrogen sulfide. At least a portion of the feed gas stream is separated into a hydrogen sulfide stream and a hydrocarbon stream. The hydrocarbon gas stream is processed to produce natural gas. At least 34 mol. % of the hydrogen sulfide in the hydrogen sulfide stream is combusted with an oxidant to generate thermal power. Thermal power generated by the combustion is utilized in one or more of the steps of separating the feed gas stream into the hydrogen sulfide stream and the hydrocarbon gas stream, and processing the hydrocarbon gas stream to produce natural gas, compressed natural gas, or liquefied natural gas. | 05-16-2013 |
20130126393 | HIGH SURFACE AREA COMPOSITION FOR USE IN THE CATALYTIC HYDROCONVERSION OF A HEAVY HYDROCARBON FEEDSTOCK, A METHOD MAKING SUCH COMPOSITION AND ITS USE - A catalyst composition that is especially useful in the hydroconversion of pitch, micro carbon residue and sulfur contents of a heavy hydrocarbon feedstock without the excessive formation of sediment. The catalyst composition is a reasonably high surface area composition containing alumina and a low molybdenum content with a high ratio of nickel-to-molybdenum. The catalyst composition further has a unique pore distribution that in combination with the special metals loading provide for good conversion of pitch and micro carbon residue without an excessive yield of sediment. | 05-23-2013 |
20130130958 | HIGH MOLECULAR WEIGHT POLYMERS AS VISCOSITY MODIFIERS - A lubricating composition comprises a base oil and between | 05-23-2013 |
20130133327 | SYSTEM AND PROCESS FOR GENERATION OF ELECTRICAL POWER - A system and process for generation of electrical power is provided. Electrical power is generated by a system including two integrated power cycles, a first power cycle utilizing water/steam as a working fluid and the second power cycle utilizing a fluid selected from the group consisting of molecular nitrogen, argon, a chemical compound having a boiling point of at most 65° C. at 0.101 MPa and a latent heat of vaporization of at least 350 kJ/kg, and a chemical compound having a boiling point of at most 65° C. at 0.101 MPa and a specific heat capacity as a liquid of at least 1.9 kJ/kg-° K as a working fluid. The working fluid of the second power cycle is expanded through a two-phase expander to produce power in the second power cycle, where the expanded working fluid of the second cycle has a temperature of at most 10° C. | 05-30-2013 |
20130137913 | PROCESS FOR THE REJUVENATION OF A SPENT MOLECULAR SIEVE CATALYST - The present invention relates to a process for the rejuvenation of a spent molecular sieve, comprising at least the steps of:
| 05-30-2013 |
20130139431 | BALANCED UNLEADED FUEL COMPOSITIONS - Balanced unleaded fuel compositions exhibiting: a pump octane rating of greater than 93; a T50 (maximum) of 104.4° C. (220° F.) and a T90 (maximum) of 165.6° C. (330° F.), as required under the CARB Phase 3 model; and, producing a higher average torque and/or higher average power output than commercially available fuels stated to meet the CARB Phase 3 model. | 06-06-2013 |
20130144078 | METHOD OF RECOVERING LIPIDS FROM MICROBIAL BIOMASS - A method of obtaining lipids from microbial biomass such as algae is provided by treating microbial biomass with a solution containing at least one α-hydroxysulfonic acid to extract and recover liposoluble components. The α-hydroxysulfonic acid can be easily removed from the product containing liposoluble compoenents and recycled. | 06-06-2013 |
20130145682 | METHOD FOR PROCESSING A LIGNOCELLULOSIC BIOMASS MATERIAL - Method for processing a lignocellulosic biomass material, comprising (a) a pretreatment process, in which the biomass is prepared for enzymatic hydrolysis, and (b) a subsequent hydrolysis process, in which the pretreated biomass is subjected to enzymatic hydrolysis of its cellulosic components to convert them into sugars, wherein the pretreatment process (a) is carried out in the presence of a tertiary polyamide additive. The additive may be used to improve the efficiency of the hydrolysis process (b). Also provided are processes for the production of a fermentation product from lignocellulosic biomass, and/or for the production of a biofuel or biofuel component. | 06-13-2013 |
20130150609 | PROCESS FOR PRODUCING AROMATIC CARBONATES - This invention provides a method for producing an alkylaryl carbonate comprising: a) contacting a stream comprising an aromatic hydroxy compound and a stream comprising a dialkylcarbonate in a reactive distillation column containing a bed of heterogeneous transesterification catalyst, the bed having a top and a bottom; and b) withdrawing a product stream comprising the alkylaryl carbonate from the reactive distillation column wherein the aromatic hydroxy compound is fed to the column at a first feed point located above the top of the catalyst bed. This invention further provides an apparatus suitable for carrying out this method. | 06-13-2013 |
20130152784 | METHOD OF MAKING A COMPOSITE GAS SEPARATION MODULE - A method of making a composite gas separation module by providing a porous support material having deposited thereon a metal membrane layer, by imposing upon the surface of the metal membrane layer certain surface characteristics including an abrasion pattern and a relatively high surface roughness that provides for surface activation that enhances the placement thereon of a subsequent metal membrane layer without the use of a chemical activating solution. The composite gas separation module is useful in the separation of hydrogen from hydrogen-containing gas streams. | 06-20-2013 |
20130152785 | METHOD OF PREPARING A PALLADIUM-SILVER ALLOY GAS SEPARATION MEMBRANE SYSTEM - A method of preparing a palladium-silver alloy gas separation membrane system, wherein the surface of the palladium layer or a silver layer is activated by a non-chemical activation method involving abrasion to a controlled surface roughness and abrasion pattern, thereby permitting the plating or deposition of an overlayer of silver on the palladium layer, silver on a silver layer, or palladium on a silver layer. The palladium and silver layers are preferably supported on a porous metal support to which an intermetallic diffusion barrier has been applied. | 06-20-2013 |
20130153228 | SYSTEM AND METHOD FOR PRODUCING OIL - The present invention provides a system and method for producing oil in which an ether-containing formulation is injected into a formation containing oil and an oil-immiscible formulation is injected into the formation, and oil is produced from the formation. The oil-immiscible formulation has a salt content of at most 5 wt. % and is comprised of water having a salt content of at most 5 wt. %. | 06-20-2013 |
20130153463 | TITANIA-BOUND ZSM-12 ZEOLITE COMPOSITION AND METHOD OF MAKING AND USING SUCH COMPOSITION - Presented is a composition useful in the catalytic dewaxing of a waxy hydrocarbon feedstock. The composition includes a mixture of ZSM-12 zeolite and titania and may further include a noble metal. The ZSM-12 zeolite preferably has a high silica-to-alumina ratio within its framework. The mixture may be dealuminated either by acid leaching using a fluorosilicate salt or by steam treating. | 06-20-2013 |
20130153511 | PROCESS FOR DEWATERING OF OIL SAND TAILING MUDS - The present invention relates to a process for dewatering oil sand tailing muds, comprising: (a) adding a flocculant into oil sand tailing muds and mixing the flocculant and the tailing muds; (b) filtering the flocculated tailing muds using a dynamic filtration system, wherein in step (b) a pressure difference is applied over the filter and wherein the dynamic filtration system comprises a means for producing a dynamic action by which the filter cake is continuously or intermittently moved, deformed and/or broken, the filter cake being the solidified material that sets on the filter during filtration. The process is useful for dewatering oil sand tailing muds from tailing ponds, such as those produced in the Athabasca Oil Fields in Canada. | 06-20-2013 |
20130156945 | METHOD OF MAKING A GAS SEPARATION SYSTEM - A method of making a gas separation system is described. The method comprises the steps of (1) providing a porous support having an initial mean pore size and initial surface roughness and (2) applying a particulate material to a surface of the porous support to (a) functionally reduce the mean pore size of the support and (b) functionally reduce the measurable surface roughness of the support. Additional layers of particulate material of decreasing size are applied to further reduce the mean pore size and reduce the roughness of the support. When the support reaches the desired level of smoothness a thin membrane of gas selective material is deposited thereon. The membrane and support are then annealed under conditions that prevent or substantially reduce cracking of the membrane during commercial use. | 06-20-2013 |
20130157333 | METHOD OF TREATING ETHANOL PRODUCTION BYPRODUCTS - A method of treating ethanol production byproduct is provided by treating wet distillers grain or stillage with a solution containing at least one α-hydroxysulfonic acid to produce at least one fermentable sugar containing product. Fermentable sugar useful for the production of biofuels or ethanol can be produced from such methods. The α-hydroxysulfonic acid can be easily removed from the product and recycled. | 06-20-2013 |
20130157334 | PROCESS FOR CONVERTING A LIGNOCELLULOSIC BIOMASS - A process for converting a lignocellulosic biomass comprising
| 06-20-2013 |
20130160354 | ORGANIC NITRATES AS IGNITION ENHANCERS - A diesel fuel composition comprising an organic nitrate is described. The organic nitrate may be a terpene nitrate. Methods of using an organic nitrate for achieving a desired cetane number, and uses of organic nitrates for the purpose of reducing the ignition delay of the fuel and/or for increasing its cetane number to a defined level are also described, as are methods of operating a compression ignition engine. | 06-27-2013 |
20130161010 | OIL RECOVERY PROCESS - The present invention provides a method for enhancing the recovery of oil from a formation. A hydrocarbon-containing gas and an ether are injected into an oil-bearing formation to mobilize the oil. The mobilized oil is then produced from the formation. | 06-27-2013 |
20130161233 | BLENDING HYDROCARBON STREAMS TO PREVENT FOULING - A method of reducing the fouling propensity of a hydrocarbon feed stream having a Total Base Number based on ASTM method D2896-11 of less than 150 ppm and/or a P-value according to ASTM method D7060-09 of less than 1.15 which method comprises processing the feed stream such that the product obtained has a calculated Total Base Number of at least 150 ppm, a calculated P-value of at least 1.15 and a calculated Po-value higher than the FRmax of the feed stream, more specifically blending at least two hydrocarbon feed streams to prepare a blend having these properties. | 06-27-2013 |
20130165712 | INTEGRATED PROCESS FOR THE PREPARATION OF A LOWER OLEFIN PRODUCT - A process for the preparation of an olefin product comprising ethylene, comprising a) cracking a cracker feedstock to obtain a cracker effluent comprising olefins; b) converting an oxygenate feedstock in an oxygenate-to-olefins conversion system, comprising a reaction zone in which an oxygenate feedstock is contacted a catalyst to obtain a conversion effluent comprising ethylene and/or propylene; c) combining at least part of the cracker effluent and at least part of the conversion effluent to obtain a combined effluent wherein the combined effluent comprises a C | 06-27-2013 |
20130165716 | INTEGRATED PROCESS FOR THE PREPARATION OF AN AROMATIC PRODUCT - A process preparing an aromatic product comprising xylene, the process comprising: a) cracking a feedstock to obtain a cracker effluent comprising olefins and aromatics; b) converting an oxygenate feedstock in an oxygenate-to-olefins conversion system, comprising a reaction zone in which an oxygenate feedstock is contacted with a catalyst to obtain a conversion effluent comprising benzene, toluene, xylene and olefins; c) combining at least part of the cracker effluent and at least part of the conversion effluent to obtain a combined effluent, the combined effluent comprising aromatics; d) separating at least a portion of the benzene and/or toluene from the combined effluent to form a benzene and/or toluene stream; e) separating the olefins from the combined effluent; f) separating xylene from the combined effluent to form a xylene stream; and g) recycling at least a part of the benzene and/or toluene streams as recycled aromatics to step b). | 06-27-2013 |
20130165718 | PROCESS FOR THE PREPARATION OF OLEFINS - A process for the preparation of an olefin product, which process comprises the steps of: a) converting an oxygenate feedstock in an oxygenate-to-olefins conversion system, comprising a reaction zone in which an oxygenate feedstock is contacted with an oxygenate conversion catalyst under oxygenate conversion conditions, to obtain a conversion effluent comprising ethylene and/or propylene; b) separating at least a portion of the ethylene from the conversion effluent to form an ethylene stream; c) feeding the ethylene stream to an oligomerization step to produce higher molecular weight olefins; d) recycling at least a portion of the olefins as a recycle higher molecular weight olefins stream to step a). | 06-27-2013 |
20130165725 | PROCESS FOR THE PREPARATION OF AN AROMATIC PRODUCT - A process for the preparation of an aromatic product comprising xylene, which process comprises the steps of: a) converting an oxygenate feedstock in an oxygenate-to-olefins conversion system, comprising a reaction zone in which an oxygenate feedstock is contacted with an oxygenate conversion catalyst under oxygenate conversion conditions, to obtain a conversion effluent comprising benzene, toluene, xylene and olefins; b) separating at least a portion of the benzene and toluene from the conversion effluent to form an aromatics containing stream; c) separating the olefins from the conversion effluent; d) separating xylene from the conversion effluent to produce a xylene product stream; and e) recycling at least a portion of the aromatics containing stream to step a). | 06-27-2013 |
20130167430 | PROCESS FOR CONVERTING A SOLID BIOMASS MATERIAL - A process for converting a solid biomass material comprising (a) mixing the solid biomass material with a fluid to form a fluidized biomass stream; and (b) propagating the fluidized biomass stream into the riser reactor via one or more delivery aperture(s); wherein the solid biomass material has a particle size distribution with a mean particle size diameter, and wherein the delivery aperture has a diameter equal to or more than three times the mean particle size diameter of the particle size distribution of the solid biomass material. | 07-04-2013 |
20130168089 | METHOD FOR PRODUCING OIL - The present disclosure relates to enhanced oil recovery methods including the injection of solvent and polymer floods to increase hydrocarbon production from oil bearing underground rock formations. One method includes injecting a solvent slug into the underground formation for a first time period from a first well. The solvent slug solubilizes the oil and generates a mixture of mobilized oil and solvent. An aqueous polymer slug may then be injected into the underground formation for a second time from the first well. The polymer slug may have a viscosity greater than the solvent slug and thereby generates an interface between the solvent slug and the polymer slug. The solvent slug and the mobilized oil are then forced towards a second well using a buoyant hydrodynamic force generated by the aqueous polymer slug. Oil and/or gas may then be produced from the second well. | 07-04-2013 |
20130168097 | METHOD AND SYSTEM FOR ENHANCING OIL RECOVERY (EOR) BY INJECTING TREATED WATER INTO AN OIL BEARING FORMATION - A process and a system for enhancing recovery of oil from an oil-bearing formation are provided in which water having a total dissolved solids content is filtered to remove some solids in a filter assembly, the filtered water is treated to remove some ions in a capacitive deionization assembly, and the filtered deionized water is injected into the oil-bearing formation to mobilize crude oil and enhance oil recovery from the formation. | 07-04-2013 |
20130172432 | PROCESS FOR PREPARING A PARAFFIN PRODUCT - The invention is a process for preparing a paraffin product from a carbonaceous feedstock comprising (a) partial oxidation of the carbonaceous feedstock to obtain a mixture comprising hydrogen and carbon monoxide, (b) performing a Fischer-Tropsch reaction using the mixture as obtained in step (a) and recovering an off-gas from the Fischer-Tropsch reaction and a paraffin product, (c) hydrogenating at least a part of the off-gas from the Fischer-Tropsch reaction using a steam/off-gas mol ratio in the range of between 0.7 and 1.5 and a catalyst comprising copper and zinc and/or a catalyst comprising copper and manganese, and (d) preparing a hydrogen comprising gas from at least a part of the off-gas from the Fischer-Tropsch reaction. | 07-04-2013 |
20130172627 | PROCESS FOR PREPARING LOWER OLEFINS - The invention is a process for preparing lower olefins comprising: a) steam cracking a paraffinic feedstock to obtain a cracker effluent comprising olefins and saturated and unsaturated C4 hydrocarbons; b) contacting an oxygenate feedstock with a molecular sieve-comprising catalyst, at a temperature in the range of from 350 to 1000° C. to obtain an oxygenate conversion effluent comprising olefins and saturated and unsaturated C4 hydrocarbons; c) subjecting the cracker effluent and the oxygenate conversion effluent to one or more separation steps such that an olefin product stream comprising ethylene and/or propylene, and a stream comprising saturated and unsaturated C4 hydrocarbons are obtained; and d) subjecting part of the stream comprising C4 hydrocarbons from both the cracker effluent and the oxygenate conversion effluent to extractive distillation to obtain a stream enriched in unsaturated C4 hydrocarbons and a stream enriched in saturated C4 hydrocarbons. | 07-04-2013 |
20130172644 | PROCESS FOR PREPARING LOWER OLEFINS FROM AN OXYGENATE - The invention relates to a process for preparing lower olefins from an oxygenate, the process comprising: subjecting C4 hydrocarbons obtained in an oxygenate-to-olefins conversion step to extractive distillation to an etherification step to convert isobutene into an alkyl tertiary butyl ether to obtain an isobutene-depleted C4 hydrocarbon stream and alkyl tertiary-butyl ether; | 07-04-2013 |
20130172645 | PROCESS FOR PREPARING LOWER OLEFINS FROM AN OXYGENATE - The invention relates to a process for preparing lower olefins from an oxygenate, the process comprising subjecting C4 hydrocarbons obtained in an oxygenate-to-olefins conversion step to extractive distillation to obtain a stream enriched in unsaturated C4 hydrocarbons comprising isobutene and n-butenes, and a stream enriched in saturated C4 hydrocarbons; converting the isobutene in the stream enriched in unsaturated C4 hydrocarbons into an alkyl tertiary butyl ether to obtain an isobutene-depleted unsaturated C4 hydrocarbon stream and alkyl tertiary-butyl ether; and recycling at least part of the isobutene-depleted unsaturated C4 hydrocarbon stream and/or at least part of the alkyl tertiary-butyl ether, optionally after conversion into tertiary butanol and/or isobutene, to the oxygenate-to-olefins conversion step. | 07-04-2013 |
20130172652 | PROCESS FOR THE PREPARATION OF A LOWER OLEFIN PRODUCT - A process for the preparation of an olefin product comprising ethylene, which process comprises the steps of: a) converting an oxygenate feedstock in an oxygenate-to-olefins conversion system, comprising a reaction zone in which an oxygenate feedstock is contacted with an oxygenate conversion catalyst under oxygenate conversion conditions, to obtain a conversion effluent comprising ethylene and/or propylene; b) separating at least a portion of the propylene from the conversion effluent to form a propylene stream; c) separating the remainder of the olefins from the conversion effluent; and d) recycling at least a portion of the propylene stream to step a). | 07-04-2013 |
20130177824 | SYSTEMS AND PROCESSES OF OPERATING FUEL CELL SYSTEMS - The present invention is directed to systems and processes for operating molten carbonate fuel cell systems. A process for operating the molten carbonate fuel cell includes providing a hydrogen-containing stream comprising molecular hydrogen to a molten carbonate fuel cell anode; heating a hydrocarbon stream, at least a majority of which is comprised of hydrocarbons that are liquid at 20° C. and atmospheric pressure, with a heat source comprising an anode exhaust from the molten carbonate fuel cell anode; contacting at least a portion of the heated hydrocarbon stream with a catalyst to produce a steam reforming feed comprising gaseous hydrocarbons, hydrogen, and at least one carbon oxide; separating at least a portion of the molecular hydrogen from the steam reforming feed; and providing at least a portion of the separated molecular hydrogen to the molten carbonate fuel cell anode as at least a portion of the stream comprising molecular hydrogen. | 07-11-2013 |
20130178672 | PROCESS FOR MAKING A DISTILLATE PRODUCT AND/OR C2-C4 OLEFINS - A process for making a distillate product and one or more C2-C4 olefins from a FCC feedstock containing a cellulosic material and a hydrocarbon co-feed is provided. | 07-11-2013 |
20130196400 | TREATING BIOMASS TO PRODUCE MATERIALS USEFUL FOR BIOFUELS - Fermentable sugar useful for the production of biofuels can be produced from biomass by contacting the biomass with a solution containing at least one α-hydroxysulfonic acid. The α-hydroxysulfonic acid can be easily removed from the product and recycled. | 08-01-2013 |
20130199085 | DIRECT AQUEOUS PHASE REFORMING OF BIO-BASED FEEDSTOCKS - A method comprises providing a bio-based feedstock; contacting the bio-based feedstock with a solvent in a hydrolysis reaction to form an intermediate stream comprising carbohydrates; contacting the intermediate stream with an apr catalyst to form a plurality of oxygenated intermediates, wherein a first portion of the oxygenated intermediates are recycled to form the solvent; and processing at least a second portion of the oxygenated intermediates to form a fuel blend. | 08-08-2013 |