Pillow with retractable umbrella
A pillow assembly having a supporting assembly and a retractable umbrella assembly that is easily transportable and allows a user to support his/her head while covering their face from sunlight.
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| Number | Title | Issue Date |
| 7683228 | Production of high purity cumene from non-extracted feed and hydrocarbon composition useful therein A process for producing an cumene product having a purity of at least 99.50 percent based on the weight of cumene present in the product by the propylation of the benzene present in non-extracted hydrocarbon composition feed, e.g., non-extracted reformate. The non-e... | 03/23/2010 |
| 7393988 | Process for production of ethylbenzene from dilute ethylene streams An improvement in a process for the production of ethylbenzene from a dilute ethylene stream wherein an ethylene-containing stream derived from a cracking process is directed to an ethylene fractionator for separation of ethylene and ethane. The improvement includes... | 07/01/2008 |
| 7282616 | Process for conversion of olefins A process for converting an olefin feed to hydrocarbons suitable for fuel components or their feedstock. According to the process, an olefin feed, possibly together with another hydrocarbon feed, is contacted in a reactor with a catalyst in order to produce a hydroc... | 10/16/2007 |
| 7259282 | Process for production of ethylbenzene from dilute ethylene streams An improvement in a process for the production of ethylbenzene from a dilute ethylene stream wherein an ethylene-containing stream derived from a cracking process is directed to an ethylene fractionator for separation of ethylene and ethane. The improvement includes... | 08/21/2007 |
| 7223714 | Method of transferring catalyst in a reaction system The invention is directed to methods of transfering catalyst particles into and within reaction systems. The reaction systems are those that use catalysts that comprise molecular sieves, particularly metalloaluminophosphate molecular sieves, especially metalloalumin... | 05/29/2007 |
| 7199068 | Reactive distillation alkylation process including in situ catalyst regeneration A unified process which couples a unique in situ catalyst regeneration process with a continuous reactive distillation under pressure for the alkylation of light aromatic hydrocarbons such as benzene with C2–C30 olefins using a solid acid alk... | 04/03/2007 |
| 7038100 | Aromatics alkylation The present invention provides a process for producing an alkylaromatic compound comprising the step of contacting an alkylatable aromatic compound with an alkylating agent under alkylation conditions in the presence of a alkylation catalyst comprising phosphorus an... | 05/02/2006 |
| 6979394 | Alkylaromatic process with catalyst regeneration A process for producing a product aromatic compound is disclosed which uses an on-stream alkylation reactor and an off-stream alkylation reactor, and in which at least a portion of the feed aromatic compound in the effluent stream of off-stream alkylation reactor un... | 12/27/2005 |
| 6555722 | Countercurrent alkylation process A countercurrent process for the alkylation of aromatic materials with olefins which takes place in a multi-bed system. The aromatic material is in the liquid phase; the olefin in the gaseous phase; and the catalyst in the solid phase. The olefinic materi... | 04/29/2003 |
| 6544408 | Process and installation for the production of aromatic compounds in a fixed bed Process for the production of aromatic compounds, such as reforming, that uses at least one fixed catalyst bed with a base of platinum and 0.08% rhenium. In said process, before moving onto the bed, the feedstock undergoes a heat exchange with the effluen... | 04/08/2003 |
| 6479721 | Alkylation process operating at low olefin ratios A process for the alkylation of aromatics with olefins using a solid catalyst is disclosed, wherein the olefin ratio and/or the maximum olefin concentration in the alkylation catalyst, bed is maintained less than an upper limit. Such operation can decreas... | 11/12/2002 |
| 6395947 | Method for preparing diarylethane A method for preparing diarylethane is disclosed. Alkylation is carried out in a continuous type process at 100-300° C. under a pressure of 1-45 kg/cm2 G in the presence of a solid acid catalyst while a reactant mixture comprising alpha-methyl... | 05/28/2002 |
| 6255549 | Method for producing low bromine number fraction A fraction of low bromine number mainly containing a styrenic compound/aromatic compound adduct can be attained, by feeding reaction materials of a styrenic compound and an aromatic compound to a fixed-bed flow reactor packed with a solid acid catalyst in... | 07/03/2001 |
| 6156949 | Selective pseudocumene production by xylene methylation There is provided a process for shape selective xylene methylation that involves contacting a feedstream which includes xylene and methanol under alkylation conditions, with a low activity catalyst. Xylene conversions of at least 15% at methanol utilizati... | 12/05/2000 |
| 6123836 | Process for the removal of acid compounds from a hydrocarbon stream Process for the removal of acid compounds contained in a hydrocarbon process stream by passing the process stream through a fixed bed of an adsorption material at conditions where the acid compounds adsorb on the material and withdrawing a purified hydroc... | 09/26/2000 |
| 5939597 | Fluid bed process for para-xylene production Para-xylene is produced by toluene methylation by charging toluene and a methylating agent to a fluidized bed of catalyst at a rate sufficient to maintain the fluidized bed in a turbulent sub-transport flow regime, reacting the toluene with the methylatin... | 08/17/1999 |
| 5856606 | Turbulent bed solid catalyst hydrocarbon alkylation process Paraffins or other hydrocarbons are alkylated in a process featuring a reaction zone containing a pool of liquid maintained at its boiling point and containing a suspended solid catalyst, which allows the heat of reaction to vaporize a portion of the liqu... | 01/05/1999 |
| 5847255 | Gas phase alkylation-liquid phase transalkylation process Process for the production of ethylbenzene by alkylation over a silicalite alkylation catalyst with the subsequent transalkylation of diethylbenzene with the alkylation catalyst and conditions selected to retard xylene production and also heavies producti... | 12/08/1998 |
| 5847254 | Alkylation of benzene to form linear alkylbenzenes using fluorine-containing mordenites This invention is directed to a fluorine-containing mordenite catalyst and use thereof in the manufacture of linear alkylbenzene (LAB) by alkylation of benzene with an olefin. The olefin may have from about 10 to 14 carbons. The fluorine-containing morden... | 12/08/1998 |
| 5789640 | Aromatic hydrocarbons alkylation and liquid-solid circulating fluidized bed for alkylation Disclosed is a process for continuous alkylation of aromatics or their derivatives in the presence of a solid acid catalyst in a liquid-solid circulating fluidized bed system, said system comprising a liquid-solid cocurrent upflow reactor, a sedimentation... | 08/04/1998 |
| 5777187 | Two-step process for alkylation of benzene to form linear alkylbenzenes This invention is directed to a fluorine-containing mordenite catalyst and use thereof in the manufacture of linear alkylbenzene (LAB) by alkylation of benzene with an olefin. The olefin may have from about 10 to 14 carbons. The fluorine-containing morden... | 07/07/1998 |
| 5648579 | Continuous alkylation of aromatics using solid catalysts; prevention of catalyst deactivation using a pulsed feed reactor A novel continuous process for the preparation of alkylated benzenes effected by solid catalysts which become deactivated under alkylation conditions uses a single catalyst zone for both reaction and catalyst flushing to prevent deactivation. The process ... | 07/15/1997 |
| 5395513 | Fluid bed catalytic upgrading of reformate A continuous process for upgrading reformate feedstock or the like to reduce benzene content and increase octane fuel rating. The improved process comprises maintaining a fluidized bed of regenerable acid solid medium pore zeolite catalyst particles in a ... | 03/07/1995 |
| 5262576 | Method for the alkylation of organic aromatic compounds A method and apparatus for conducting a catalytic distillation process is provided which allows for maintaining a liquid level in selected portions of the catalyst bed. Three particular processes disclosed are the production of methyl tertiary butyl ether... | 11/16/1993 |
| 5210348 | Process to remove benzene from refinery streams A substantially benzene-free product suitable for gasoline blending is formed from a benzene-containing refinery stream. At least about 30% of the benzene initially present in the stream is catalytically alkylated with C2 -C4 olefins... | 05/11/1993 |
| 5113031 | Aromatic alkylation process A process for the catalytic distillation production of alkylated aromatic compounds is provided wherein the vapor pressure of the olefin may be increased while maintaining the same olefin feed rate and aromatic to olefin ratio. In one embodiment a side st... | 05/12/1992 |
| 4950831 | Coupling process An alkene is coupled with an aromatic hydrocarbon having an active hydrogen on a saturated alpha-carbon in the presence of an unsupported alkali metal as a catalyst under high shear agitation conditions. In preferred embodiments of the invention, the alke... | 08/21/1990 |
| 4540831 | Mixed-phase hydrocarbon conversion process employing total overhead condenser A process is disclosed for performing an exothermic reaction such as the etherification of isobutylene with methanol. The feed is charged to a vertical reaction zone containing a solid catalyst. Heat released by the exothermic reaction partially vaporizes... | 09/10/1985 |
| 4292457 | Alkylation of aromatic hydrocarbons A new crystalline borosilicate comprises a molecular sieve material having the following composition in terms of mole ratios of oxides: wherein M is at least one cation, n is the valence of the cation, Y is a value within the range of 4 to about 600, and Z is ... | 09/29/1981 |
| 4134734 | Detergent alkylation reactor A unitary reactor system for the alkylation of benzene with olefins. The hydrocarbon reactants are sprayed horizontally from a plurality of openings in a number of vertical conduits which extend upward into a lower portion of the vessel. The conduits are ... | 01/16/1979 |
| 4072729 | Simulated moving bed reaction process A continuous catalytic reaction and catalyst reactivation process is performed using a simulated moving catalyst bed to effect simultaneously in different zones of a multi-zone fixed catalyst bed an alkylation reaction of olefinic and aromatic reactants a... | 02/07/1978 |
| 4051191 | Solid phosphoric acid catalyzed alkylation of aromatic hydrocarbons A process for the alkylation of aromatic hydrocarbons using a solid phosphoric acid catalyst in which liquid phosphoric acid is removed from the bottoms stream of the rectification column to which the alkylation zone effluent is charged. The acid is remov... | 09/27/1977 |
| 4049739 | Simulated moving bed alkylation process A continuous catalytic alkylation reaction and catalyst reactivation process is carried out using a simulated moving catalyst bed to effect simultaneously in different zones of a multi-zone, fixed catalyst bed, an alkylation reaction and a reactivation of... | 09/20/1977 |
| 4049738 | Selective production of para-xylene Process for the selective production of para-xylene by methylation of toluene in the presence of a catalyst comprising the crystalline aluminosilicate zeolite ZSM-23.... | 09/20/1977 |
| 4049737 | Propylation of toluene Propylation of toluene with selective production of cymene is accomplished by vapor phase reaction of toluene and propylene at a temperature between about 400° and about 600° F. in the presence of a catalyst comprising a crystalline aluminosilicate zeol... | 09/20/1977 |