Richard C. Stell - Houston TX, US Jennifer L. Bancroft - Houston TX, US Arthur R. DiNicolantonio - Seabrook TX, US Subramanian Annamalai - Houston TX, US James N. McCoy - Houston TX, US Paul F. Keusenkothen - Houston TX, US George Stephens - Humble TX, US John R. Messinger - Kingwood TX, US James Mitchell Frye - Houston TX, US Nick G. Vidonic - Seabrook TX, US George J. Balinsky - Kingwood TX, US
Assignee:
ExxonMobil Chemical Patents Inc. - Houston TX
International Classification:
C07C 4/04 C07C 4/02
US Classification:
585652, 585658
Abstract:
A process for cracking hydrocarbon feedstock containing resid comprising: heating the feedstock, mixing the heated feedstock with a fluid and/or a primary dilution steam stream to form a mixture, flashing the mixture to form a vapor phase and a liquid phase which collect as bottoms and removing the liquid phase, separating and cracking the vapor phase, and cooling the product effluent. The process comprises at least two of the following conditions: (1) maintaining the bottoms under conditions to effect at least partial visbreaking; (2) reducing or eliminating partial vapor condensation during flashing by adding a heated vaporous diluent to dilute and superheat the vapor; (3) partially condensing the vapor within said flash/separation vessel by contacting with a condenser; (4) decoking internal surfaces and associated piping of the flash/separation vessel with air and steam; (5) utilizing a flash/separation vessel having an annular, inverted L-shaped baffle; and (6) regulating temperature in furnace tube banks used for heating by utilizing a desuperheater and/or an economizer. An apparatus for carrying out the process is also provided.
Process And Apparatus For Cracking Hydrocarbon Feedstock Containing Resid
Richard C. Stell - Houston TX, US George J. Balinsky - Kingwood TX, US James N. McCoy - Houston TX, US Paul F. Keusenkothen - Houston TX, US
Assignee:
ExxonMobil Chemical Patents Inc. - Houston TX
International Classification:
C07C 4/04
US Classification:
585647, 585652
Abstract:
A process for cracking hydrocarbon feedstock containing resid comprising: heating the feedstock, mixing the heated feedstock with a fluid and/or a primary dilution steam stream to form a mixture, flashing the mixture to form a vapor phase and a liquid phase which collect as bottoms and removing the liquid phase, separating and cracking the vapor phase, and cooling the product effluent, wherein the bottoms are maintained under conditions to effect at least partial visbreaking. The visbroken bottoms may be steam stripped to recover the visbroken molecules while avoiding entrainment of the bottoms liquid. An apparatus for carrying out the process is also provided.
Process And Apparatus For Cracking Hydrocarbon Feedstock Containing Resid To Improve Vapor Yield From Vapor/Liquid Separation
Richard C. Stell - Houston TX, US Jennifer L. Bancroft - Houston TX, US Arthur R. Dinicolantonio - Seabrook TX, US Subramanian Annamalai - Houston TX, US James N. McCoy - Houston TX, US Paul F. Keusenkothen - Houston TX, US George Stephens - Humble TX, US John R. Messinger - Kingwood TX, US James Mitchell Frye - Houston TX, US Nick G. Vidonic - Seabrook TX, US George J. Balinsky - Kingwood TX, US
A process for cracking hydrocarbon feedstock containing resid comprising: heating the feedstock, mixing the heated feedstock with a fluid and/or a primary dilution steam stream to form a mixture, flashing the mixture to form a vapor phase and a liquid phase which collect as bottoms and removing the liquid phase, separating and cracking the vapor phase, and cooling the product effluent. The process comprises at least two of the following conditions: (1) maintaining the bottoms under conditions to effect at least partial visbreaking; (2) reducing or eliminating partial vapor condensation during flashing by adding a heated vaporous diluent to dilute and superheat the vapor; (3) partially condensing the vapor within said flash/separation vessel by contacting with a condenser; (4) decoking internal surfaces and associated piping of the flash/separation vessel with air and steam; (5) utilizing a flash/separation vessel having an annular, inverted L-shaped baffle; and (6) regulating temperature in furnace tube banks used for heating by utilizing a desuperheater and/or an economizer. An apparatus for carrying out the process is also provided.
Process And Apparatus For Cracking Hydrocarbon Feedstock Containing Resid
Richard C. Stell - Houston TX, US George J. Balinsky - Kingwood TX, US James N. McCoy - Houston TX, US Paul F. Keusenkothen - Houston TX, US
Assignee:
ExxonMobil Chemical Patents Inc. - Houston TX
International Classification:
B01J 10/00 C07C 4/02
US Classification:
422188, 422187, 585648
Abstract:
A process for cracking hydrocarbon feedstock containing resid comprising: heating the feedstock, mixing the heated feedstock with a fluid and/or a primary dilution steam stream to form a mixture, flashing the mixture to form a vapor phase and a liquid phase which collect as bottoms and removing the liquid phase, separating and cracking the vapor phase, and cooling the product effluent, wherein the bottoms are maintained under conditions to effect at least partial visbreaking. The visbroken bottoms may be steam stripped to recover the visbroken molecules while avoiding entrainment of the bottoms liquid. An apparatus for carrying out the process is also provided.
Process And Apparatus For Cracking Hydrocarbon Feedstock Containing Resid
A process for cracking hydrocarbon feedstock containing resid comprising: heating the feedstock, mixing the heated feedstock with a fluid and/or a primary dilution steam stream to form a mixture, flashing the mixture to form a vapor phase and a liquid phase which collect as bottoms and removing the liquid phase, separating and cracking the vapor phase, and cooling the product effluent, wherein the bottoms are maintained under conditions to effect at least partial visbreaking. The visbroken bottoms may be steam stripped to recover the visbroken molecules while avoiding entrainment of the bottoms liquid. An apparatus for carrying out the process is also provided.
Process For The Hydrogenation Of Aromatic Hydrocarbons
George J. Balinsky - Randolph NJ Omer Biceroglu - Sarnia, CA Joe S. Lin - Torrance CA
Assignee:
Exxon Research and Engineering Co. - Florham Park NJ
International Classification:
C10G 4500 C10G 4554 C07C 510
US Classification:
208143
Abstract:
A noble metal-containing zeolitic catalyst having cracking activity and hydrogenation activity is pretreated by contacting the catalyst with a nitrogen-containing compound to decrease the cracking activity of the catalyst followed by treatment with hydrogen to recover the hydrogenation activity of the catalyst. The pretreated catalyst is used in a process for the hydrogenation of aromatic hydrocarbons.
Magnetically Stabilized Bed, Temperature, Partial Pressure Swing, Hydrogen Recovery Process
Walter H. Hatch - Summit NJ George J. Balinsky - Baton Rouge LA Steve Ackerman - Randolph NJ
Assignee:
Exxon Research & Engineering Co. - Florham Park NJ
International Classification:
B01D 5319
US Classification:
55 60
Abstract:
An adsorption process for the recovery of hydrogen from a feed gas or vapor which contains hydrogen in admixture with one or more hydrocarbon components, alone or in admixture with non-hydrocarbon components. Particulate adsorbent solids are provided with a magnetizable component, or components, and circulated between an adsorption zone in which hydrogen is concentrated in the off gas by contact of the adsorbent solids with the feed, and hydrogen recovered, and a desorption zone in which the exhausted solids are regenerated. Within the adsorption zone the feed is countercurrently contacted with the solids at relatively low temperature to selectively adsorb hydrocarbon, and perhaps other non-hydrogen components. The solids are formed into a moving, fluidized bed, and magnetically stabilized to suppress gross solids circulation while hydrocarbons are adsorbed from the feed. Occluded hydrogen is subsequently displaced from the particulate adsorbent solids with hydrocarbons, and the hydrocarbon enriched particulate adsorbent solids are then transported to the desorption zone.