| Class / Patent application number | Description | Number of patent applications / Date published |
|---|
| 585007000 | Component of indefinite molecular weight greater than 150 | 29 |
| 20130123553 | LUBRICATING OIL COMPOSITION AND LUBRICATING OIL COMPOSITION FOR CONTINUOUSLY VARIABLE TRANSMISSION - A lubricating oil composition of the invention contains longifolene represented by the following formula (1), that is, (1S,3aR,4S,8aS)-4,8,8-trimethyl-9-methylene-decahydro-1,4-methanoazulene. | 05-16-2013 |
| 585009000 | Wax | 2 |
| 20100125157 | HIGH SHEAR PROCESS FOR PRODUCING MICRONIZED WAXES - A method and system for producing dispersed waxes, including a high shear mechanical device. In one embodiment, the method comprises forming a dispersion of wax globules in a carrier liquid in a high shear device prior to implementation in a waxy product. In another instance the system for producing waxy products comprises a high shear device for dispersing wax in a carrier liquid. | 05-20-2010 |
| 20110087057 | Lubricating base oil - The present invention is directed to a heavy hydrocarbon composition useful as a heavy lubricant oil base stock and to a heavy lubricant composition derived from the heavy lubricant oil base stock that remains clear and bright even after being cooled to room temperature and stored for an extended period of time. | 04-14-2011 |
| 585010000 | Polymer | 8 |
| 20100286457 | Gear Oil Compositions, Methods of Making and Using Thereof - A gear oil composition is provided. The composition comprises a synergistic blend of mineral oil base stock and polyalphaolefin (PAO) base stock for the oil composition to have a traction coefficient at a slide to roll ratio of 40 percent at 15 mm | 11-11-2010 |
| 20110137091 | Manufacture of Oligomers from Nonene - In oligomerizing alpha-olefins to produce poly alpha-olefins, the feedstock consists of nonene, or a blend of alpha-olefins comprising nonene. The nonene comprising alpha-olefin feedstock and at least one catalyst are subjected to oligomerization or polymerization conditions in a reactor. Following reaction, the mixture may be subjected to distillations to removed unreacted alpha-olefins and dimers of the alpha-olefins. The resulting product may also be hydrogenated. The final product may also be fractioned to recover at least two fractions of poly alpha-olefins of differing nominal viscosities. | 06-09-2011 |
| 20120165580 | Process For Production of Polyolefins - A method for preparing a liquid polyolefin which includes contacting a feedstock comprising at least one olefin monomer with a catalyst system to produce a reactor effluent stream, filtering the reactor effluent stream, washing a created filter cake with a warm wash fluid comprising at least one hydrocarbon liquid, separating at least a portion of the wash fluid during the washing, sending said portion of the wash fluid through a distillation process, and recovering at least a portion of the liquid polyolefin that was in the filter cake. The catalyst system may be any conventional polyolefin catalyst system and, in any preferred embodiment of the invention, the catalyst system contains at least one activated metallocene catalyst. The reactor effluent stream comprises at least one liquid polyolefin, residual catalyst, and unreacted olefin monomer. | 06-28-2012 |
| 20150011807 | METHODS FOR THE PRODUCTION OF RENEWABLE DIMETHYL JP10 - A highly efficient method for the conversion of a natural product into the high density fuel RJ-4 with concomitant evolution of isobutylene for conversion to fuels and polymers, more specifically, embodiments of the invention relate to efficient methods for the conversion of the renewable, linear terpene alcohol, linalool into a drop-in, high density fuel suitable for ramjet or missile propulsion. | 01-08-2015 |
| 585011000 | Containing aromatic ring | 1 |
| 20160137925 | Process for Recycling Oil-Sorbing Polymeric Media - Recycling spent hydrophobic polymeric media can beneficially utilize waste oil to dissolve the media. The method employs simple equipment and materials, many or all of which are already on location in various industrial operations such as fracking operations or food production factories. The method does not call for landfilling spent media, thus reducing the environmental impact and reducing expense. Transport costs for spent media and disposal fees can likely decrease. The resulting product can be sold to refineries for further processing and repurposing, thus generating additional revenue. | 05-19-2016 |
| 585012000 | Plural polymers or copolymer of specified olefins | 3 |
| 20090281360 | POLYALPHAOLEFINS AND PROCESSES FOR FORMING POLYALPHAOLEFINS - The invention is directed to polyalphaolefins (PAOs) and processes for forming PAOs. In one embodiment, the invention is to a process for forming a PAO comprising polymerizing C | 11-12-2009 |
| 20140235909 | 1-DECENE/1-DODECENE COPOLYMER AND LUBRICATING-OIL COMPOSITION CONTAINING SAME - Provided are an α-olefin copolymer useful as a high-viscosity lubricant oil excellent in viscosity characteristics, low-temperature characteristics and oxidation stability, and a lubricant oil containing the copolymer. The α-olefin copolymer is a 1-decene/1-dodecene copolymer produced by the use of a doubly bridged metallocene catalyst. | 08-21-2014 |
| 20140256997 | 1-OCTENE, 1-DECENE, 1-DODECENE TERNARY COPOLYMER AND LUBRICANT COMPOSITION CONTAINING SAME - Provided are an α-olefin copolymer useful as a high-viscosity lubricant oil excellent in viscosity characteristics, low-temperature characteristics and oxidation stability, and a lubricant oil containing the copolymer. The α-olefin copolymer is a 1-octene/1-decene/1-dodecene ternary copolymer produced by the use of a doubly crosslinked metallocene catalyst. | 09-11-2014 |
| 585013000 | Mineral oil (petroleum) fraction | 18 |
| 20090093658 | Process to Blend a Mineral and a Fischer-Tropsch Derived Product Onboard a Marine Vessel - Process to blend a mineral derived hydrocarbon product and a Fischer-Tropsch derived hydrocarbon product by providing in a storage vessel of a marine vessel a quantity of mineral derived hydrocarbon product and Fischer-Tropsch derived hydrocarbon product such that initially the mineral derived hydrocarbon product is located substantially above the Fischer-Tropsch derived hydrocarbon product, transporting the combined products in the marine vessel from one location to another location, also referred to as the destination, and obtaining a blended product at arrival of the marine vessel at its destination. | 04-09-2009 |
| 20120149952 | PRODUCTION OF DIESEL FUEL FROM VEGETABLE AND ANIMAL OILS - A process for producing a fuel composition from vegetable and/or animal oil comprises hydrodeoxygenating and hydroisomerizing the oil in a single step. The fuel composition has acceptable lubricity and comprises a mixture of C | 06-14-2012 |
| 20130023705 | LUBRICANT COMPOSITION FOR AN INTERNAL COMBUSTION ENGINE - A lubricating oil composition for an internal combustion engine contains a component (A) of a polyalphaolefin having a kinematic viscosity at 100 degrees C. of 5.5 mm | 01-24-2013 |
| 20130030226 | LUBRICANT COMPOSITION FOR AN INTERNAL COMBUSTION ENGINE - A lubricating oil composition for an internal combustion engine contains: a base oil including a component (A) of a polyalphaolefin having a kinematic viscosity at 100 degrees C. of 5.5 mm | 01-31-2013 |
| 20130096354 | Process for Treating Heavy Oils - A process for treating a heavy oil which comprises subjecting a heavy oil to cavitation to reduce the viscosity of the heavy oil. The treated heavy oil, which has a reduced viscosity and specific gravity, thus is more pumpable and transportable, which facilitates further processing. The treated heavy oil also can be fractionated with less severity than untreated heavy oil. | 04-18-2013 |
| 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 |
| 20130131406 | PROCESS FOR RECOVERING PRODUCTS FROM TWO REACTORS - A process is disclosed for catalytically converting two feed streams. The feed to a first catalytic reactor may be contacted with product from a second catalytic reactor to effect heat exchange between the two streams and to transfer catalyst from the product stream to the feed stream. The feed to the second catalytic reactor may be a portion of the product from the first catalytic reactor. | 05-23-2013 |
| 20130303809 | METHODS FOR EXPANDING AND ENRICHING HYDROCARBON DILUENT POOLS - The invention provides a method for enriching diluents with butane so as not to violate pre-defined limits for liquid hydrocarbon fuels with respect to density, volatility and low density hydrocarbon content. | 11-14-2013 |
| 20140051897 | RENEWABLE JET FUEL BLENDSTOCK FROM ISOBUTANOL - The present invention in its various embodiments is directed to methods for preparing a renewable jet fuel blendstock, and blendstocks prepared by such methods, comprising fermenting a biomass-derived feedstock to form one or more C | 02-20-2014 |
| 20150065759 | EXTERNAL STEAM REDUCTION METHOD IN A FLUIDIZED CATALYTIC CRACKER - The present disclosure generally relates to methods to reduce the external steam supplied to a fluidized catalytic cracker by injecting a stream comprising a water-containing renewable fuel oil into a riser of a fluidized catalytic cracker. | 03-05-2015 |
| 20150065760 | FLUIDIZED CATALYTIC CRACKER RISER QUENCH SYSTEM - The present application generally relates to a riser quench system comprising a quench line and one or more quench injecting ports for injecting a renewable fuel oil into the riser of a fluidized catalytic cracker co-processing a renewable fuel oil and a petroleum fraction as reactants. | 03-05-2015 |
| 20150337225 | FUEL COMPOSITIONS - Low sulphur marine fuel compositions are provided. Embodiments comprise greater than 50 to 90 wt % of a residual hydrocarbon component, with the remaining 10 to 50 wt % selected from a non-hydroprocessed hydrocarbon component, a hydroprocessed hydrocarbon component, and a combination thereof. Embodiments of the marine fuel composition can have a sulphur content of about 0.1 wt % or less. | 11-26-2015 |
| 20150337226 | FUEL COMPOSITIONS - Low sulphur marine fuel compositions are provided. Embodiments comprise greater than 50 to 90 wt % of a residual hydrocarbon component, with the remaining 10 and up to 50 wt % selected from a non-hydroprocessed hydrocarbon component, a hydroprocessed hydrocarbon component, and a combination thereof. Embodiments of the marine fuel composition can have a sulphur content of about 0.1 wt % or less. | 11-26-2015 |
| 20150360185 | CRUDE OIL COMPOSITIONS AND METHODS OF PRODUCING HIGH FLASH POINT CRUDE OIL COMPOSITIONS - Transport compositions include a crude oil composition and a solvent formulation including at least one terpene component. In some embodiments, the terpene is a monoterpene. In some embodiments, the terpene is pure gum turpentine, oil of turpentine, a component of turpentine, or a combination of these. Addition of a minimal amount of solvent formulation to the crude oil composition raises the flash point of the mixture, preferably to a predetermined value, which may be in the range of 100 to 120° F., in the range of 120 to 140° F., above 140° F., or above 170° F., depending on the application. The amount of terpene is preferably in the range about 0.005 to about 5 percent by total weight of the transport composition. Methods of raising the flash point of a crude oil composition and methods of increasing the safety of handling a crude oil composition are also disclosed. | 12-17-2015 |
| 20160046872 | RENEWABLE HYDROCARBON COMPOSITION - The present invention provides a composition comprising 10-40 mass! of C | 02-18-2016 |
| 20160053192 | BRIGHT STOCK BASE OIL BLEND - A method is disclosed for making a bright stock base oil blend meeting API Group II specifications. The method comprises blending (a) a major amount of a petroleum-derived bright stock component having kinematic viscosity at 100° C. of from 20 to 50 mm | 02-25-2016 |
| 20160090539 | FCC UNITS, APPARATUSES AND METHODS FOR PROCESSING PYROLYSIS OIL AND HYDROCARBON STREAMS - Fluid catalytic cracking (FCC) units, apparatuses, and methods for catalytically cracking a mixture of a pyrolysis oil stream and a hydrocarbon stream are provided herein. In an embodiment, an FCC unit includes a reaction chamber suitable for contacting a pyrolysis oil, a hydrocarbon, and a catalyst. The FCC unit includes a coolant conduit having an coolant outlet in communication with the reaction chamber and suitable for introducing a coolant stream through the coolant outlet into the reaction chamber. The FCC unit further includes a pyrolysis oil conduit including a pyrolysis oil outlet positioned within the coolant conduit and suitable for injecting the pyrolysis oil through the pyrolysis oil outlet into the reaction chamber. | 03-31-2016 |
| 20160178132 | CONVERSION OF ORGANIC OXYGENATES TO HYDROCARBONS | 06-23-2016 |
