Patent US4935320A successfully refreshed from Google Patents.
Patent US4094816A successfully refreshed from Google Patents.
← Back to Patent Explorer
US4094816A Expired / Lapsed US ⏱️ 0.0 years remaining

Method for stabilizing a phosphorus-vanadium-oxygen complex catalyst

Assignee: Standard Oil Co
•
Filing: 1976-12-22
•
Granted: 1978-06-13
•
Expires: 1996-12-22
📄 Original PDF 🌐 Google Patents 🔄 Sync Now

Abstract

Abstract The present disclosure relates to a method for the stabilization of certain phosphorus-vanadium-oxygen complex catalysts by the repetitive reactivation of such catalysts using a specified class of reactivating agents. The present method is specifically applicable to the stabilization of phosphorus-vanadium-oxygen complex catalysts which are suitable for the production of maleic anhydride from aromatic or aliphatic feed streams. In a specific instance, the stabilization process incorporates passing a feed stream of an aliphatic hydrocarbon and oxygen over a phosphorus-vanadium-oxygen catalyst to cause it to deactivate, thereafter contacting the deactivated catalyst with a specified class of reactivating agents and thereafter repeating this sequence at least once. This process tempers the catalyst so it deactivates at a lower rate and is improved in its performance.

Inventors

  • 👤 Walter Partenheimer

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-07 09:23
CPC Classifications
C; C07; C07C; C07C51/00; C07C51/16; C07C51/21; C07C51/215; B; B01; B01J; B01J23/00; B01J23/90; B01J23/94; B01J27/00; B01J27/28; B01J27/285; C07C51/25; Y; Y02; Y02P; Y02P20/00; Y02P20/50; Y02P20/584; Y10; Y10S; Y10S502/00; Y10S502/50

Claims Analysis

Total Claims: 31
Claim 1
Independent Claim 250 words
A method for stabilizing a phosphorus-vanadium-oxide catalyst having an atomic ratio of phosphorus to vanadium in the range of about 0.5 to 5, which comprises: (A) Contacting said catalyst at deactivation conditions including a temperature in the range of from about 350° to 600° C. with a gaseous mixture containing molecular oxygen for a period of greater than about 1 hour; (B) Contacting said catalyst with an effective amount of a material selected from the group consisting of: (1) Molecular chlorine or fluorine or mixtures thereof; (2) Halides of fluorine, chlorine, bromine or iodine being in the vapor state above about 250° C. at atmospheric pressure represented by the following formula: C(X).sub.n where each X is a selected halide and n is an integer from 1 to 4, any remaining radicals being hydrogen or mixtures thereof; (3) Organic halides of fluorine, chlorine, bromine or iodine being in the vapor state above about 250° C. at atmospheric pressure represented by the formula: R(X.sub.1).sub.m where R is alkane, alkene or alkyne of straight or branched structure having at least two carbon atoms and X 1 is independently a primary, secondary, or tertiary halide and m is an integer of from 1 to about 20 consistent with the number of carbon atoms of said structure or mixtures; (4) hydrogen halides; or mixtures thereof at reactivation conditions including a temperature in the range of from about 300° to about 500° C.; and (c) repeating the sequence of steps (A) and (B) at least once.
Claim 2
Independent Claim 250 words
A method for stabilizing a phosphorus-vanadium-oxide catalyst having an atomic ratio of phosphorus to vanadium in the range of about 0.5 to 5, which comprises: (A) Contacting said catalyst at deactivation conditions including a temperature in the range of from about 350° to 600° C. with a gaseous mixture containing molecular oxygen for a period of greater than about 1 hour; (B) Contacting said catalyst with an effective amount of a material selected from the group consisting of: (1) Molecular chlorine or fluorine or mixtures thereof; (2) Halides of fluorine, chlorine, bromine or iodine being in the vapor state above about 250° C. at atmospheric pressure represented by the following formula: C(X).sub.n where each X is a selected halide and n is an integer from 1 to 4, any remaining radicals being hydrogen or mixtures thereof; (3) Organic halides of fluorine, chlorine, bromine or iodine being in the vapor state above about 250° C. at atmospheric pressure represented by the formula: R(X.sub.1).sub.m where R is alkane, alkene or alkyne of straight or branched structure having at least two carbon atoms and X 1 is independently a primary, secondary, or tertiary halide and m is an integer of from 1 to about 20 consistent with the number of carbon atoms of said structure or mixtures; (4) hydrogen halides; or mixtures thereof at reactivation conditions including a temperature in the range of from about 300° to about 500° C.; and (c) repeating the sequence of steps (A) and (B) at least once.
Claim 3
Dependent Claim 29 words
The method of claim 1 further characterized in that said gaseous mixture includes a hydrocarbon selected from the group consisting of methane, ethane, propane, n-butane, n-butene or mixtures thereof.
Claim 4
Dependent Claim 24 words
The method of claim 2 further characterized in that said hydrocarbon is selected from the group consisting of n-butane and n-butene or mixtures thereof.
Claim 5
Dependent Claim 50 words
The method of claim 1 further characterized in that said material of step (B) comprises a meterial represented by the following formula: C(X).sub.n where each X is independently a halide of chlorine, fluorine or bromine and n is an integer of from 1 to 4, any remaining radicals being hydrogen.
Claim 6
Dependent Claim 32 words
The method of claim 1 further characterized in that said material of step (B) is selected from the group consisting of carbon tetrachloride, carbon trichloride, carbon dichloride or methylchloride or mixtures thereof.
Claim 7
Dependent Claim 17 words
The method of claim 5 further characterized in that said material of step (B) comprises carbon tetrachloride.
Claim 8
Dependent Claim 24 words
The method of claim 1 further characterized in that said deactivation conditions include temperature in the range of from about 380° to 520° C.
Claim 9
Dependent Claim 22 words
The method of claim 1 further characterized in that the sequence of steps (A) and (B) is repeated at least three times.
Claim 10
Independent Claim 262 words
A method for stabilizing a phosphorus-vanadium-oxide catalyst having an atomic ratio of phosphorus to vanadium in the range of about 0.5 to 5, which comprises: (A) Contacting said catalyst at deactivating conditions including a temperature in the range of from about 350° to 600° C. with a gaseous mixture containing molecular oxygen and a hydrocarbon having less than about ten carbon atoms per molecule for a period of greater than about 1 hour. (B) Contacting said catalyst with an effective amount of a material selected from the group consisting of: (1) Molecular chlorine or fluorine or mixtures thereof; (2) Halides of fluorine, chlorine, bromine or iodine being in the vapor state above about 250° C. at atmospheric pressure represented by the following formula: C(X).sub.n where each X is a selected halide and n is an integer from 1 to 4, any remaining radicals being hydrogen or mixtures thereof; (3) Organic halides of fluorine, chlorine, bromine or iodine being in the vapor state above about 250° C. at atmospheric pressure represented by the formula: R(X.sub.1).sub.m where R is alkane, alkene or alkyne of straight or branched structure having at least two carbon atoms and X 1 is independently a primary, secondary, or tertiary halide and m is an integer of from 1 to about 20 consistent with the number of carbon atoms of said structure or mixtures; (4) Hydrochloric acid; or mixtures thereof at reactivation conditions including a temperature in the range of from about 300° to about 500° C.; and (c) repeating the sequence of steps (A) and (B) at least once.
Claim 11
Independent Claim 262 words
A method for stabilizing a phosphorus-vanadium-oxide catalyst having an atomic ratio of phosphorus to vanadium in the range of about 0.5 to 5, which comprises: (A) Contacting said catalyst at deactivating conditions including a temperature in the range of from about 350° to 600° C. with a gaseous mixture containing molecular oxygen and a hydrocarbon having less than about ten carbon atoms per molecule for a period of greater than about 1 hour. (B) Contacting said catalyst with an effective amount of a material selected from the group consisting of: (1) Molecular chlorine or fluorine or mixtures thereof; (2) Halides of fluorine, chlorine, bromine or iodine being in the vapor state above about 250° C. at atmospheric pressure represented by the following formula: C(X).sub.n where each X is a selected halide and n is an integer from 1 to 4, any remaining radicals being hydrogen or mixtures thereof; (3) Organic halides of fluorine, chlorine, bromine or iodine being in the vapor state above about 250° C. at atmospheric pressure represented by the formula: R(X.sub.1).sub.m where R is alkane, alkene or alkyne of straight or branched structure having at least two carbon atoms and X 1 is independently a primary, secondary, or tertiary halide and m is an integer of from 1 to about 20 consistent with the number of carbon atoms of said structure or mixtures; (4) Hydrochloric acid; or mixtures thereof at reactivation conditions including a temperature in the range of from about 300° to about 500° C.; and (c) repeating the sequence of steps (A) and (B) at least once.
Claim 12
Dependent Claim 26 words
The method of claim 9 further characterized in that said hydrocarbon is selected from the group consisting of methane, ethane, propane, n-butane, n-butene or mixtures thereof.
Claim 13
Dependent Claim 24 words
The method of claim 10 further characterized in that said hydrocarbon is selected from the group consisting of n-butane and n-butene or mixtures thereof.
Claim 14
Dependent Claim 50 words
The method of claim 9 further characterized in that said material of step (B) comprises a material represented by the following formula: C(X).sub.n where each X is independently a halide of chlorine, fluorine or bromine and n is an integer of from 1 to 4, any remaining radicals being hydrogen.
Claim 15
Dependent Claim 32 words
The method of claim 9 further characterized in that said material of step (B) is selected from the group consisting of carbon tetrachloride, carbon trichloride, carbon dichloride or methylchloride or mixtures thereof.
Claim 16
Dependent Claim 17 words
The method of claim 13 further characterized in that said material of step (B) comprises carbon tetrachloride.
Claim 17
Dependent Claim 25 words
The method of claim 9 further characterized in that said temperature of step (A) is in the range of from about 380° to 520° C.
Claim 18
Dependent Claim 22 words
The method of claim 9 further characterized in that the sequence of steps (A) and (B) is repeated at least three times.
Claim 19
Independent Claim 166 words
A method for stabilizing a phosphorus-vanadium-oxide catalyst having pentavalent phosphorus and vanadium with an average valence in the range of from about 3.9 to about 4.5, an atomic ratio in the range of from about 1 to 2, which comprises: (A) contacting said catalyst at deactivation conditions including a temperature in the range of about 350° to 540° C. with a gaseous mixture containing molecular oxygen and a hydrocarbon having less than about seven carbon atoms per molecule for a period of greater than about one hour; (B) contacting said catalyst with an effective amount of a material selected from the group consisting of methyl chloride, carbon dichloride, carbon trichloride, or carbon tetrachloride or mixtures thereof, at reactivation conditions including a temperature in the range of from about 300° to about 500° C; (c) contacting said catalyst with steam at a temperature in the range of from about 400° to 500° C; and (D) repeating the sequence of steps (A), (B) and (C) at least once.
Claim 20
Independent Claim 166 words
A method for stabilizing a phosphorus-vanadium-oxide catalyst having pentavalent phosphorus and vanadium with an average valence in the range of from about 3.9 to about 4.5, an atomic ratio in the range of from about 1 to 2, which comprises: (A) contacting said catalyst at deactivation conditions including a temperature in the range of about 350° to 540° C. with a gaseous mixture containing molecular oxygen and a hydrocarbon having less than about seven carbon atoms per molecule for a period of greater than about one hour; (B) contacting said catalyst with an effective amount of a material selected from the group consisting of methyl chloride, carbon dichloride, carbon trichloride, or carbon tetrachloride or mixtures thereof, at reactivation conditions including a temperature in the range of from about 300° to about 500° C; (c) contacting said catalyst with steam at a temperature in the range of from about 400° to 500° C; and (D) repeating the sequence of steps (A), (B) and (C) at least once.
Claim 21
Dependent Claim 42 words
The method of claim 17, step (A) further characterized in that said hydrocarbon comprises normal butane, the temperature is in the range of from about 400° to about 540° C. and the contacting is a period of greater than about three hours.
Claim 22
Dependent Claim 30 words
The method of claim 17, step (B) further characterized in that said material comprises carbon tetrachloride and the temperature is in the range of from about 400° to 500° C.
Claim 23
Dependent Claim 29 words
The method of claim 17, step (C) further characterized in that said steam contact takes place at a temperature in the range of from about 400° to 500° C.
Claim 24
Dependent Claim 101 words
The method of claim 17 further characterized in that: in step (A) the hydrocarbon comprises normal butane, the temperature is in the range of from about 500° to about 540° C. and the contacting is a period of greater than about three hours; in step (B) said material comprises carbon tetrachloride and the temperature is in the range of from about 400° to 500° C; in step (C) said steam contact takes place at a temperature in the range of from about 400° to 500° C; and the sequence of steps (A), (B) and (C) is repeated at least three times.
Claim 25
Independent Claim 121 words
A method for stabilizing a phosphorus-vanadium-oxide catalyst having an atomic ratio of phosphorus to vanadium in the range of from about 0.5 to about 5 and containing an atomic ratio of zinc to vanadium of from about 0.01 to about 0.3 which method comprises: (A) contacting said catalyst at a temperature above about 370° C. with a gas containing molecular oxygen and a hydrocarbon selected from the group consisting of normal butane, normal butene-1, normal butene-2, butadiene, benzene or mixtures thereof for greater than about one hour; (B) contacting said catalyst with carbon tetrachloride at a temperature in the range of from about 300° to about 500° C; and (C) repeating the sequence of steps (A) and (B) at least once.
Claim 26
Independent Claim 121 words
A method for stabilizing a phosphorus-vanadium-oxide catalyst having an atomic ratio of phosphorus to vanadium in the range of from about 0.5 to about 5 and containing an atomic ratio of zinc to vanadium of from about 0.01 to about 0.3 which method comprises: (A) contacting said catalyst at a temperature above about 370° C. with a gas containing molecular oxygen and a hydrocarbon selected from the group consisting of normal butane, normal butene-1, normal butene-2, butadiene, benzene or mixtures thereof for greater than about one hour; (B) contacting said catalyst with carbon tetrachloride at a temperature in the range of from about 300° to about 500° C; and (C) repeating the sequence of steps (A) and (B) at least once.
Claim 27
Dependent Claim 28 words
The method of claim 22 further characterized in that said step (B) takes place at a temperature in the range of from about 350° to about 450° C.
Claim 28
Dependent Claim 43 words
The method of claim 22 further characterized in that the hydrocarbon of step (A) is selected from the group consisting of normal butane, normal butene-1, normal butene-2, butadiene or mixtures thereof and is present at below about 1.7 volume percent of the gas.
Claim 29
Dependent Claim 29 words
The method of claim 22 further characterized in that the phosphorus is pentavalent and the vanadium has a valence in the range of from about 4 to about 4.5.
Claim 30
Dependent Claim 32 words
The method of claim 22 further characterized in that from about 0.1 to about 10 percent by weight based on active catalyst of carbon tetrachloride contacts the catalyst in each step (B).
Claim 31
Dependent Claim 19 words
The method of claim 22 further characterized in that steps (A) and (B) are repeated at least three times.

References Cited (Backward Citations)

US4020174A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1981-06-12 1981-12-12 1982-06-13 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1985-06-12 1985-12-12 1986-06-13 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1989-06-12 1989-12-12 1990-06-13 $7700.00 Window Closed / Lapsed

Assigned Categories & Tags

No categories assigned to this patent yet.

Assign Category Tag