| 序号 | 专利名 | 申请号 | 申请日 | 公开（公告）号 | 公开（公告）日 | 发明人 |
|---|---|---|---|---|---|---|
| 181 | PROCESS FOR THE PRODUCTION OF LOW SULFUR, LOW OLEFIN GASOLINE | PCT/US2005/029395 | 2005-08-18 | WO2006049673A2 | 2006-05-11 | ROCK, Kerry, L.; XOING, Yi-Gang; JUDZIS, Arvids, Jr. |
A process for the production of low sulfur, low olefin gasoline wherein a cracked naphtha, such as a full boiling range cracked naphtha, is first separated by fractional distillation into at least two fractions while simultaneously selectively hydrogenating the polyunsaturated compounds contained therein. The mono olefins in the light fraction are then subjected to etherification with alcohol to produce ethers or hydration with water to produce alcohols. The heavy fraction is subjected to sulfur removal by hydrodesulfurization or chemisorption. The two fractions are then combined to produce a low sulfur, low olefin gasoline. |
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| 182 | PROCESS FOR SULFUR REDUCTION IN NAPHTHA STREAMS | PCT/US0235294 | 2002-11-04 | WO03050207A8 | 2004-10-21 | GROTEN WILLIBRORD A |
| A process for fractionating and treating of a full range naphtha stream. The full boiling range naphtha stream is first split into a light boiling range naphta, an intermediate boiling range naphtha and a heavy boiling range naphtha. The bottoms are subjected to hydrodesulfurization and the effluent combined with the intermediate boiling range naphtha containing thiophene and thiophene and thiophene mercaptans and subjected to a second hydrodesulfurization. The effluent from the polishing reactor may be combined with the light boiling range naphtha to produce a new full boiling range naphtha containing substantially less total sulfur than the original feed. The mercaptans in the light naphtha may be removed by thioetherification prior to splitting or by wet caustic wash afterwards. The object being to meet higher standards for sulfur removal, by treating the components of the naphta feed with the process that preserves the olefinic while most expediently removing the sulfur compounds. | ||||||
| 183 | THE USE OF HYDROGEN TO REGENERATE METAL OXIDE HYDROGEN SULFIDE SORBENTS | PCT/US2001/022734 | 2001-07-19 | WO02008361A1 | 2002-01-31 | |
| A process to regenerate metal oxide desulfurization sorbents using hydrogen gas. The sorbents may be mono- or multi-metallic in nature, and preferably comprise Ni and/or Co. If desired, secondary metals may be incorporated to increase regeneration efficiency and/or capacity. Other additives suppress hydrocarbon craking. | ||||||
| 184 | PROCESS FOR THE SIMULTANEOUS TREATMENT AND FRACTIONATION OF LIGHT NAPHTHA HYDROCARBON STREAMS | PCT/US1999/018148 | 1999-08-10 | WO00015319A1 | 2000-03-23 | |
| A flow diagram of one embodiment of the invention having one catalyst bed (14A) in a distillation column/naphtha splitter (14). | ||||||
| 185 | Systems and processes for processing pyrolysis oil | US18464570 | 2023-09-11 | US11939542B1 | 2024-03-26 | Bruce D. Murray; Scott G. Morrison; Kenneth Fountain; Steven R. Horlacher; Vincent D. Mcgahee; Reza Khankal; David Dockter |
| A system for processing plastic waste may include a feed line, a feed fractionator, a hydrotreater, a catalytic reforming unit, a heavy oil cracker, and a steam cracker. A pyrolyzed plastics feed is separated into light, medium, and heavy hydrocarbon streams. The hydrotreater removes sulfur, and the catalytic reforming unit produces a circular aromatic-rich stream. The heavy oil cracker generates cracked streams. The steam cracker produces a circular olefin stream from a cracked stream. A system for processing plastic waste may include the feed line, the feed fractionator, the hydrotreater, a medium hydrocarbon fractionator, the catalytic reforming unit, a full-range reforming unit, the heavy oil cracker, and the steam cracker. The medium hydrocarbon fractionator produces two hydrocarbon streams. The full-range naphtha reforming unit produces a second circular aromatic-rich stream. | ||||||
| 186 | PROCESS FOR THE PREPARATION OF OLEFINS, INVOLVING DE-ASPHALTING, HYDROCONVERSION, HYDROCRACKING AND STEAM CRACKING | US17766794 | 2020-10-02 | US20240067891A1 | 2024-02-29 | Wilfried WEISS; Isabelle MERDRIGNAC |
| The present invention relates to a process for producing olefins from a hydrocarbon feedstock 11 having a sulfur content of at least 0.1 weight %, an initial boiling point of at least 180° C. and a final boiling point of at least 600° C. | ||||||
| 187 | PENTANE-ENRICHED HYDROCARBONS TO TRANSPORTATION FUEL | US18314613 | 2023-05-09 | US20230365878A1 | 2023-11-16 | Chengtian Wu; Jonathan Marda; Karthikeyan Marimuthu; Dhananjay Ghonasgi; Jianhua Yao |
| Methods that increase production of a liquid transportation fuel blend component by utilizing C5 hydrocarbon streams taken from both a refinery naphtha stream and an NGL fractionator pentanes plus stream. A high vapor pressure pentane fraction from the NGL fractionator is separated to remove isopentane and produce lower vapor pressure commodity natural gasoline. A refinery naphtha stream (that is optionally an FCC naphtha stream) is separated to produce a C5 olefins stream that is then oligomerized to produce an upgraded stream having lower vapor pressure and higher octane rating, then combined with the remainder of the naphtha stream as well as the isopentane stream to produce a gasoline blend component that meets specifications for vapor pressure and octane rating. | ||||||
| 188 | Process for production of needle coke | US17478692 | 2021-09-17 | US11788013B2 | 2023-10-17 | Ponoly Ramachandran Pradeep; Shivam Ashok Dixit; Prantik Mondal; Jitumoni Brahma; Rajesh; Terapalli Hari Venkata Devi Prasad; Satyen Kumar Das; Madhusudan Sau; Gurpreet Singh Kapur; Sankara Sri Venkata Ramakumar |
| High-quality graphite/needle grade coke is produced with reduced impurity levels and improved coefficient of thermal expansion using an integrated hydrotreatment, catalytic cracking and coking reaction sections, employing a combination of highly paraffinic hydrotreated VGO stream and aromatic CLO stream, which is thereafter processed in a delayed coking section. | ||||||
| 189 | Process for upgrading ultralight crude oil and condensates | US16552123 | 2019-08-27 | US11180705B2 | 2021-11-23 | Michael F. Milam; Gerry Obluda |
| A method comprising the steps of feeding condensate to a splitter unit; directing the resulting naphtha product to a naphtha hydrotreater and the resulting diesel product to a diesel hydrotreater; directing ULSD product from the diesel hydrotreater to ULSD storage and naphtha product from the diesel hydrotreater to the naphtha hydrotreater; directing treated naphtha product from the naphtha hydrotreater to a naphtha splitter; isomerizing the light naphtha product and reforming the heavy naphtha product; sending the isomerate and the reformate to a gasoline separator; directing the products to storage. | ||||||
| 190 | Methods and systems of steam stripping a hydrocracking feedstock | US16701983 | 2019-12-03 | US11142704B2 | 2021-10-12 | Omer Refa Koseoglu |
| A process for producing cracked hydrocarbons from a feedstock, which includes a top portion that boils below 375° C. and a bottom portion that boils above 375° C., may include stripping the feedstock in a stripper to isolate the top portion from the bottom portion, hydrocracking the bottom portion in one or more hydrocracking reactors to produce a hydrocracked effluent, separating the hydrocracked effluent in a separating unit to produce a light product stream, a distillate stream, and a heavy unconverted stream; and recycling the heavy unconverted stream to an earlier stage of the process. | ||||||
| 191 | Polished turbine fuel | US16780517 | 2020-02-03 | US11104856B2 | 2021-08-31 | Mohammed Wohaibi; Tom F. Pruitt |
| Turbine fuel provided for large-scale land based turbines used by utilities for producing electricity and desalinated water, and for large mobile engines and turbines in marine and remote applications where only liquid fuels are available. Use results in less corrosion, ash formation and emissions (NOx, SOx, CO2 and noxious metals) than firing contaminated heavy crude, refinery residual oils or high sulfur fuel oils. Manufacture is by decontaminating crude oils, non-conventional crudes, and other highly contaminated feeds. Each fuel is produced as a single product of unit operations, not ex-plant blend of various refinery products, yet using an apparatus configuration less complex than conventional crude oil refining. These fuels can be fired by advanced high efficiency turbines of combined cycle power plants having hot flow paths and heat recovery steam generation systems susceptible to corrosion, which systems cannot otherwise risk contaminated heavy crudes or refinery residual oils feeds. | ||||||
| 192 | Polished turbine fuel | US16780405 | 2020-02-03 | US11015133B2 | 2021-05-25 | Mohammed Wohaibi; Tom F. Pruitt |
| Turbine fuel provided for large-scale land based turbines used by utilities for producing electricity and desalinated water, and for large mobile engines and turbines in marine and remote applications where only liquid fuels are available. Use results in less corrosion, ash formation and emissions (NOx, SOx, CO2 and noxious metals) than firing contaminated heavy crude, refinery residual oils or high sulfur fuel oils. Manufacture is by decontaminating crude oils, non-conventional crudes, and other highly contaminated feeds. Each fuel is produced as a single product of unit operations, not ex-plant blend of various refinery products, yet using an apparatus configuration less complex than conventional crude oil refining. These fuels can be fired by advanced high efficiency turbines of combined cycle power plants having hot flow paths and heat recovery steam generation systems susceptible to corrosion, which systems cannot otherwise risk contaminated heavy crudes or refinery residual oils feeds. | ||||||
| 193 | System for conversion of crude oil to petrochemicals and fuel products integrating vacuum residue hydroprocessing | US16555799 | 2019-08-29 | US10808187B2 | 2020-10-20 | Mohammed Saeed Al-Ghamdi; Bader BaHammam; Naif Al Osaimi; Sami Barnawi |
| Process scheme configurations are disclosed that enable conversion of crude oil feeds with several processing units in an integrated manner into petrochemicals. The designs utilize minimum capital expenditures to prepare suitable feedstocks for the steam cracker complex. The integrated process for converting crude oil to petrochemical products including olefins and aromatics, and fuel products, includes mixed feed steam cracking and gas oil steam cracking. Feeds to the mixed feed steam cracker include one or more naphtha fractions from hydroprocessing zones within the battery limits, including vacuum residue hydrocracking, within the battery limits, recycle streams from the C3 and C4 olefins recovery steps, and raffinate from a pyrolysis gasoline aromatics extraction zone within the battery limits. Feeds to the gas oil steam cracker include gas oil range intermediates from the vacuum gas oil hydroprocessing zone and the vacuum residue hydrocracking zone. | ||||||
| 194 | POLISHED TURBINE FUEL | US16780517 | 2020-02-03 | US20200216766A1 | 2020-07-09 | Mohammed Wohaibi; Tom F. Pruitt |
| Turbine fuel provided for large-scale land based turbines used by utilities for producing electricity and desalinated water, and for large mobile engines and turbines in marine and remote applications where only liquid fuels are available. Use results in less corrosion, ash formation and emissions (NOx, SOx, CO2 and noxious metals) than firing contaminated heavy crude, refinery residual oils or high sulfur fuel oils. Manufacture is by decontaminating crude oils, non-conventional crudes, and other highly contaminated feeds. Each fuel is produced as a single product of unit operations, not ex-plant blend of various refinery products, yet using an apparatus configuration less complex than conventional crude oil refining. These fuels can be fired by advanced high efficiency turbines of combined cycle power plants having hot flow paths and heat recovery steam generation systems susceptible to corrosion, which systems cannot otherwise risk contaminated heavy crudes or refinery residual oils feeds. | ||||||
| 195 | POLISHED TURBINE FUEL | US16780405 | 2020-02-03 | US20200172819A1 | 2020-06-04 | Mohammed Wohaibi; Tom F. Pruitt |
| Turbine fuel provided for large-scale land based turbines used by utilities for producing electricity and desalinated water, and for large mobile engines and turbines in marine and remote applications where only liquid fuels are available. Use results in less corrosion, ash formation and emissions (NOx, SOx, CO2 and noxious metals) than firing contaminated heavy crude, refinery residual oils or high sulfur fuel oils. Manufacture is by decontaminating crude oils, non-conventional crudes, and other highly contaminated feeds. Each fuel is produced as a single product of unit operations, not ex-plant blend of various refinery products, yet using an apparatus configuration less complex than conventional crude oil refining. These fuels can be fired by advanced high efficiency turbines of combined cycle power plants having hot flow paths and heat recovery steam generation systems susceptible to corrosion, which systems cannot otherwise risk contaminated heavy crudes or refinery residual oils feeds. | ||||||
| 196 | Integrated process for in-situ organic peroxide production and oxidative heteroatom conversion | US15886200 | 2018-02-01 | US10508246B2 | 2019-12-17 | Omer Refa Koseoglu; Abdennour Bourane |
| An oxidative treatment process, e.g., oxidative desulfurization or denitrification, is provided in which the oxidant is produced in-situ using an aromatic-rich portion of the original liquid hydrocarbon feedstock. The process reduces or replaces the need for the separate introduction of liquid oxidants such as hydrogen peroxide, organic peroxide and organic hydroperoxide in an oxidative treatment process. | ||||||
| 197 | CATALYTIC GASOLINE DESULFURIZATION METHOD HAVING ALSO AN OLEFIN SELECTIVE REMOVAL FUNCTION | US16343679 | 2017-05-16 | US20190241821A1 | 2019-08-08 | Tianzhen HAO; Xuhui GAO |
| The present invention provides a catalytic gasoline desulfurization method having also an olefin selective removal function, which comprises: when a catalytic gasoline is pre-hydrotreated, cutting into a light fraction, a middle fraction and a heavy fraction; performing liquid-liquid extraction desulfurization treatment on the middle fraction to produce a sulfur-poor oil and a rich solvent containing sulfur-rich oil; the light fraction back-extracting the rich solvent, using C5 olefin therein to replace a macromolecular acyclic olefin in the sulfur-rich oil, so as to gather together C5 iso-olefins, cycloolefins, aromatic hydrocarbons and sulfides in the sulfur-rich oil; performing hydrogenation, olefin-reduction and desulfurization treatment on the heavy fraction together with the sulfur-rich oil removed from the back-extracted rich solvent to saturate the olefin therein; and finally, preparing together with the sulfur-poor oil to produce a full range gasoline. The sulfur-content of the catalytic gasoline produced by the method of the present invention can be reduced to 10 ppm or less, the olefin content of the catalytic gasoline can be reduced to 22%, the olefin is saturated by up to 8 percentage, and the RON loss of the full range gasoline is 1.5 or less, so that while reducing the olefin content of the catalytic gasoline, it ensures the less octane number loss, thereby satisfying the olefin-reduction requirements upgraded in the gasoline National VI Standard for ethanol-gasoline supply area enterprises. | ||||||
| 198 | METHOD FOR PROCESSING VISCOUS OIL OR OIL PRODUCTS AND A PLANT FOR THEIR REFINING. | US15616893 | 2017-06-07 | US20190177625A1 | 2019-06-13 | Alex Prutkovsky |
| The invention describes and claims a processing plant and a method for processing viscous oil and oil products. The processing is effectuated with a plant, which comprises a plurality of reaction modules, a plurality of rectifying chambers and pipelines. Each reaction module and each rectifying chamber comprises a tank, a pump, a hydrocavitation generator. Each reaction module comprises a plurality of intermediate reaction stages. Each rectifying chamber comprises a plurality of intermediate rectifying stages. The reaction module and the rectifying chamber are interconnected. Intermediate reaction stages are connected by pipelines, with the last one connected to a rectifying chamber. | ||||||
| 199 | Process for the refining of crude oil | US13881137 | 2011-10-27 | US10316258B2 | 2019-06-11 | Giacomo Rispoli; Giuseppe Bellussi |
| A process for the refining of crude oil, comprising a separation unit of the crude oil, consisting of at least one atmospheric distillation unit for separating the various fractions, a unit for the conversion of the heavy fractions obtained, a unit for improving the quality of some of the fractions obtained by actions on the chemical composition of their constituents, and units for the removal of undesired components, characterized in that the heaviest fraction, the atmospheric distillation residue, is sent to the conversion unit comprising a hydroconversion reactor in slurry phase or of the ebullated bed type, into which hydrogen or a mixture of hydrogen and ¾S is introduced in the presence of a suitable nanodispersed hydrogenation catalyst. | ||||||
| 200 | Integrated isomerization and hydrotreating process | US13559802 | 2012-07-27 | US10100261B2 | 2018-10-16 | Omer Refa Koseoglu |
| Deep desulfurization of hydrocarbon feeds containing undesired organosulfur compounds to produce a hydrocarbon product having low levels of sulfur, i.e., 15 ppmw or less of sulfur, is achieved by flashing the feed at a target cut point temperature to obtain two fractions. A low boiling temperature fraction contains refractory, sterically hindered sulfur-containing compounds, which have a boiling point at or above the target cut point temperature. A high boiling temperature fraction, having a boiling point below the target cut point temperature, is substantially free of refractory sulfur-containing compounds. The high boiling temperature fraction is contacted with isomerization catalyst, and the isomerized effluent and the low boiling temperature fraction are combined and contacted with a hydrotreating catalyst in a hydrodesulfurization reaction zone operating under mild conditions to reduce the quantity of organosulfur compounds to an ultra-low level. | ||||||
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