An improved process for the recovery of aromatic compounds from a mixture containing aromatic and non-aromatic compounds and method for retrofitting existing equipment for the same is provided. The improved process comprises the steps of recovering aromatic compounds via parallel operation of a hybrid extractive distillation/liquid-liquid extractor operation and variations thereof. Methods of quickly and economically retrofitting existing recovery process equipment for use with the improved aromatics recovery process are also disclosed.
Aromatics Separation Process And Method Of Retrofitting Existing Equipment For Same
An improved process for the recovery of aromatic compounds from a mixture containing aromatic and non-aromatic compounds and method for retrofitting existing equipment for the same is provided. The improved process comprises the steps of recovering aromatic compounds via parallel operation of a hybrid extractive distillation/liquid-liquid extractor operation and variations thereof. Methods of quickly and economically retrofitting existing recovery process equipment for use with the improved aromatic recovery process are also disclosed.
Process Of Removing Sulfur Compounds From Gasoline
A process for the removal of sulfur compounds from a hydrocarbon stream is disclosed. In a preferred embodiment, the process includes extractive distillation of a gasoline stream from a fluid catalytic cracker to reject olefins to a raffinate stream and simultaneously extract sulfur compounds to an extract stream.
Aromatics Separation Process And Method Of Retrofitting Existing Equipment For Same
An improved process for the recovery of aromatic compounds from a mixture containing aromatic and non-aromatic compounds and method for retrofitting existing equipment for the same is provided. The improved process comprises the steps of recovering aromatic compounds via parallel operation of a hybrid extractive distillation/liquid-liquid extractor operation and variations thereof. Methods of quickly and economically retrofitting existing recovery process equipment for use with the improved aromatics recovery process are also disclosed.
Mircea Cretoiu - Sugar Land TX, US Joseph C. Gentry - Houston TX, US Pradeep Pawar - Houston TX, US Song Wang - Houston TX, US
Assignee:
GTC Technology US, LLC - Houston TX
International Classification:
C07C 7/10
US Classification:
585833, 585834, 585864, 585867
Abstract:
Apparatuses and systems for removing heavy hydrocarbons from a solvent stream are disclosed herein. The apparatuses extract heavy hydrocarbons into light hydrocarbons and provide a solvent stream having the heavy hydrocarbons removed. Two water washing steps are used to remove residual solvent from the heavy hydrocarbon solution in light hydrocarbons. In some embodiments, the second water wash is used for processing subsequent batches of the solvent stream. The heavy hydrocarbons and solvent can be recovered and processed further. Methods for removing heavy hydrocarbons from a solvent stream are also disclosed herein.
Systems And Processes For The Production Of Isophthalic Acid And Terephthalic Acid
George A. Ball - Hampstead NC, US Joseph G. Gentry - Houston TX, US Joseph P. Weller - Angleton TX, US Zhongyi Ding - Katy TX, US Weihua Jin - Katy TX, US
International Classification:
C09K 3/00 B01J 8/00
US Classification:
25218212, 422187, 422129, 422630
Abstract:
Various embodiments of the present invention generally disclose systems and processes for the conversion of a feed stream comprising at least one C8 aromatic into a product stream comprising isophthalic acid and purified terephthalic acid (IPA/TA).
George A. Ball - Hampstead NC, US Joseph C. Gentry - Houston TX, US Joseph P. Weller - Angleton TX, US Zhongyi Ding - Katy TX, US John R.H. Wilson - Essex, GB Meritxell Guino - York, GB Weihua Jin - Katy TX, US
International Classification:
C07C 51/265 C09K 3/00 B01J 8/00
US Classification:
25218212, 562414, 422608
Abstract:
Various embodiments of the invention herein described generally relate to novel processes for the production of aromatic acids by fixed bed catalytic oxidation of aromatic compounds carrying at least one oxidizable substituent group attached directly to the carbon atom of the corresponding aromatic nucleus. In an embodiment, a novel oxidation process of the present invention comprises the steps of: a) catalytically oxidizing, with an oxidation catalyst, a liquid phase aromatic acid precursor in the presence of a gaseous oxygen source; b) separating a finished product; c) purging the solvent and the oxidation catalyst; d) optionally recycling at least a portion of the solvent into the oxidation reactor; e) recovering at least a portion of the oxidation catalyst; f) recharging the at least a portion of the oxidation catalyst over a solid recharging catalyst bed; and (g) feeding a reactivated oxidation catalyst to the oxidation reactor.
Process For Production Of Xylenes Through Integration Of Methylation And Transalkylation
Weihua Jin - Katy TX, US Joseph C. Gentry - Houston TX, US Mircea Cretoiu - Sugar Land TX, US
Assignee:
GTC Technology US LLC - Houston TX
International Classification:
C07C 6/06
US Classification:
585319
Abstract:
The inventive process is directed to the production of xylenes through integration of aromatics methylation and transalkylation. This integrated process maximizes the production of xylenes and eliminates or minimizes the production of benzene.