Hydrodealkylation processes

a technology of hydrodealkylation and process, applied in chemical/physical/physical-chemical processes, chemical/physical/physical-chemical processes, and preparation of oxygen-containing compounds, etc., can solve the problems of metal dusting, no longer existintiori protection, and sulfur interference in the carburization reaction, so as to reduce sulfide corrosion, improve product value, and increase sulfur levels

Inactive Publication Date: 2004-06-08
CHEVRON PHILLIPS CHEMICAL CO LP
View PDF135 Cites 5 Cited by
  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Benefits of technology

Additionally, it has been found that certain preferred coatings are sulfur-tolerant, for example, the tin-based protective layers can tolerate up to 200 ppm sulfur. The protective layers eliminate the need to presulfide the metallurgy, reduce sulfide corrosion and improve product values and waste disposal due to induced levels of sulfur. Chromium-, Sb- and Ge-based protective layers can tolerate even higher sulfur levels, up to 5 or more wt. %. Most preferably, the layers can tolerate the respective amounts of sulfur for a period of at least 200, preferably at least 400, and most preferably 600 hours without degrading to an extent that carburization will occur, resulting in shut-down of the system due to excessive coking.

Problems solved by technology

Somehow, the sulfur interferes with the carburization reaction.
But with low sulfur systems or with sulfur outages, this inherent protection no longer exists especially when the system is exposed to high temperatures such as in thermal hydrodealkylation.
The problems associated with carburization include coking, carburization of system metallurgy, and metal dusting.
The excessive "metal-dusting" adds active metal particulates to the system, which particulates provide additional sites for coke formation in the system.
Coking is generally not a problem which must be addressed in hydrodealkylation processes, but this significant source of calm formation due to the absence of sulfur in reactor feedstreams excessively aggravates the problem.
As a result, a premature coke-plugging of the reactor system occurs which can lead to a premature shut-down of the system.
However, the addition of sulfur increases production cost and process complexity.
Moreover, at high temperatures coking and carburization will still occur even when sulfur is added to the feed.

Method used

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
View more

Image

Smart Image Click on the blue labels to locate them in the text.
Viewing Examples
Smart Image
  • Hydrodealkylation processes
  • Hydrodealkylation processes
  • Hydrodealkylation processes

Examples

Experimental program
Comparison scheme
Effect test

example 1

A thermal hydrodealkylation reactor made of 0.25 inch OD 316 stainless steel seamless pipe 8.75 inches long was prepared by cleaning the surfaces of the reactor exposed to the hydrodealkylation reaction with soap and water, and drying with an organic solvent. The reactor was then coated by pouring a tin paint into one end of the reactor, draining the excess, pouring the tin paint into the other end of the reactor, draining the excess, and then reducing the tin paint coating at approximately 1050.degree. F. for approximately 40 hours. The tin paint used for, coating the reactor was prepared by mixing together by weight 7 parts Tin Ten Cem (Mooney Chemical, Co.), 6 parts isopropyl alcohol, 14 parts tin powder (1-5 microns) and 14 parts stannic oxide (-325 mesh) and 5% Fe.sub.2 O.sub.3 in paint mixture. Toluene at 24 .mu.l / min was fed into the reactor with nitrogen at 20 cc / min for approximately 596 hours of operation at 1400.degree. F. No plugging occurred but operational problems in ...

example 2

A thermal hydrodealkylation reactor was prepared as described in Example 1 except that no Fe.sub.2 O.sub.3 was used in the paint. Into the reactor which was maintained at 1250.degree. F. and 100 psig, toluene at 25 .mu.l / min and hydrogen at 20 cc / mm were introduced for approximately 88 hours of operation. Then, the temperature was raised to 1400.degree. F. The reaction was continued until approximately 303 hours of operation occurred. No plugging of the reactor occurred.

example 3

A thermal hydrodealkylation reactor was prepared as described in Example 1. The reactor was preheated and maintained at a temperature of 1400.degree. F. Toluene at 25 .mu.l / min was fed into the reactor with hydrogen at 10 cc / min. The reactor pressure was maintained at approximately 100 psig. The reaction was allowed to proceed for at least 597 hours before changing the feed to n-hexane. No plugging of the reactor occurred during approximately 600 hours of operation. See FIG. 2 which is a photograph of the reactor cut open to show that no plugging occurred.

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to view more

PUM

PropertyMeasurementUnit
temperaturesaaaaaaaaaa
temperaturesaaaaaaaaaa
temperaturesaaaaaaaaaa
Login to view more

Abstract

Carburization and metal-dusting while hydrodealkylating a hydrodealkylatable hydrocarbon are reduced even in the substantial absence of added sulfur.

Description

BACKGROUND OF THE INVENTIONThe present invention rotates to an improved technique for the hydrodealkylation of a hydrodealkylatable hydrocarbon, particularly under conditions of low sulfur, which minimizes carburization thus preventing premature plant shut-downs.The hydrodealkylation of hydrodealkylatable hydrocarbons such as alkyl aromatics has been practiced for many years. The principal processes involve the conversion of toluene and like alkyl-substituted benzenes to benzene and various byproducts. Such processes are either catalytic or non-catalytic in nature. The catalytic processes employ one or more catalysis that promote the conversion of the alkyl aromatic compounds to benzene and the remaining alkyl. The non-catalytic processes typically employ heat and pressure to promote the conversion of the alkyl aromatic compounds to benzene and the remaining alkyl.Some conventional catalytic hydrodealkylation processes employ Group VIII metals such as Rh and Pt supported on an alumi...

Claims

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to view more

Application Information

Patent Timeline
no application Login to view more
Patent Type & Authority Patents(United States)
IPC IPC(8): B01J19/00B01J19/02C07C2/64C07C2/86C07C4/00C07C4/04C07C5/48C07C2/00C07C4/08C07C4/16C07C5/327C07C5/00C07C6/00C07C6/12C10G75/00
CPCB01J19/0026B01J19/02B01J2219/0236B01J2219/024B01J2219/0286C07C2/00C07C2/64C07C2/864C07C4/04C07C4/08C07C4/16C07C5/327C07C5/48C07C6/123C10G75/00C07C15/00C07C15/08C07C15/46C07C11/02
Inventor HEYSE, JOHN V.MULASKEY, BERNARD F.INNES, ROBERT A.HAGEWIESCHE, DANIEL P.CANNELLA, WILLIAM J.KRAMER, DAVID C.
Owner CHEVRON PHILLIPS CHEMICAL CO LP
Who we serve
  • R&D Engineer
  • R&D Manager
  • IP Professional
Why Eureka
  • Industry Leading Data Capabilities
  • Powerful AI technology
  • Patent DNA Extraction
Social media
Try Eureka
PatSnap group products