Harandi
Ali Harandi, Molndal SE
Patent application number | Description | Published |
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20100330101 | BIFUNCTIONAL CpG OR OLIGO-/POLYNUCLEOTIDE AND TOXIN OR ENTEROTOXIN CONTAINING COMPOSITION - A bifunctional composition comprising an intracellularly effective immunomodulating nucleic acid component containing at least one immunostimulatory, immunoinhibitory or immunomodulating motif and selected from a mononucleotide, a dinucleotide, an oligonucleotide or a polynucleotide with either a natural phosphodiester backbone or a modified backbone, optionally in combination with a specific antigen, in association with a protein binding to specific receptors on mammalian cell surfaces selected from the group consisting of cholera toxin (CT), the subunit B of CT (CTB), | 12-30-2010 |
Mohsen N. Harandi, Calgary CA
Patent application number | Description | Published |
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20090071332 | Management of Hydrogen in Hydorgen-Containing Streams from Hydrogen Sources - The use of rapid cycle pressure swing adsorption having a cycle time of less than 30 s for increasing the hydrogen concentration in hydrogen-containing steams, from a hydrogen source, such as a stream reforming unit. | 03-19-2009 |
20110147267 | RAPID CYCLE REFORMING PROCESS - This invention relates to process for producing a reformate or gasoline product. The process involves a rapid cycle of reacting hydrocarbon feedstock to form the product and then regenerating the catalyst used in the reaction. The process can be carried out at relatively high liquid hourly space velocities and preferably at relatively low hydrogen to hydrocarbon ratios to produce a reformed product having relatively high liquid yield and hydrogen content. | 06-23-2011 |
Mohsen N. Harandi, The Woodlands, TX US
Patent application number | Description | Published |
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20150368572 | FLUIDIZED BED COKING WITH FUEL GAS PRODUCTION - A Flexicoking™ unit which retains the capability of converting heavy oil feeds to lower boiling liquid hydrocarbon products while making a fuel gas from rejected coke to provide only a minimal coke yield. The heater section of the conventional three section unit (reactor, heater, gasifier) is eliminated and the cold coke from the reactor is passed directly to the gasifier which is modified by the installation of separators to remove coke particles from the product gas which is taken out of the gasifier for ultization. Hot coke from the gasifier is passed directly to the coking zone of the reactor to supply heat to support the endothermic cracking reactions and supply seed nuclei for the formation of coke in the reactor. Coke is withdrawn from the gasifier to remove excess coke and to purge the system of metals and ash. | 12-24-2015 |