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US4332626A Expired / Lapsed US ⏱️ 0.0 years remaining

Method for removing liquid residues from vessels by combustion

Assignee: PPG Industries Inc
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Filing: 1981-04-22
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Granted: 1982-06-01
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Expires: 2001-04-22
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Abstract

Abstract Oxidizable liquid organic chemical residues are removed from large vessels by a non-catalytic method comprising: a. heating the vessel by introducing a heat source and oxygen into the interior of the vessel, the emitted heat being sufficient to volatilize substantially all and decompose at least a portion of said oxidizable liquid organic chemical contaminating the interior of said vessel; b. exhausting from the vessel combustion gas resulting from the volatilization and decomposition of the liquid organic chemical during the heating step; c. filtering particulates from the combustion gas and decomposing with heat any volatilized organic chemical remaining in the combustion gas exhausted from the vessel; and d. venting to the atmosphere combustion gas essentially free of said particulates and oxidizable organic chemical.

Inventors

  • 👤 Oscar L. Hood
  • 👤 Irvin V. Lytton

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-27 07:31
CPC Classifications
B; B08; B08B; B08B9/00; B08B9/08

Claims Analysis

Total Claims: 18
Claim 1
Independent Claim 147 words
A non-catalytic method of decontaminating vessels used for storing, transporting, or processing oxidizable liquid organic chemicals, which comprises: a. introducing oxygen and a source of heat directly into the interior of the vessel, said vessel containing minor contaminating amounts of said liquid organic chemical, the heat emitted from said heat source being sufficient to heat the interior surfaces of the vessel to a temperature sufficient to volatilize substantially all and decompose at least a portion of said oxidizable liquid organic chemical contaminating the interior of said vessel, thereby to produce combustion gas within the vessel; b. exhausting from the vessel combustion gas resulting from step (a); c. filtering particulates from the exhausted combustion gas and decomposing with heat volatilized organic chemical remaining in the combustion gas exhausted from the vessel; and d. venting to the atmosphere combustion gas substantially free of said particulates and oxidizable organic chemical.
Claim 2
Dependent Claim 147 words
A non-catalytic method of decontaminating vessels used for storing, transporting, or processing oxidizable liquid organic chemicals, which comprises: a. introducing oxygen and a source of heat directly into the interior of the vessel, said vessel containing minor contaminating amounts of said liquid organic chemical, the heat emitted from said heat source being sufficient to heat the interior surfaces of the vessel to a temperature sufficient to volatilize substantially all and decompose at least a portion of said oxidizable liquid organic chemical contaminating the interior of said vessel, thereby to produce combustion gas within the vessel; b. exhausting from the vessel combustion gas resulting from step (a); c. filtering particulates from the exhausted combustion gas and decomposing with heat volatilized organic chemical remaining in the combustion gas exhausted from the vessel; and d. venting to the atmosphere combustion gas substantially free of said particulates and oxidizable organic chemical.
Claim 3
Dependent Claim 22 words
The method of claim 1 wherein the vessel is a large vessel having a capacity of from about 1,500 to 36,000 liters.
Claim 4
Dependent Claim 30 words
The method of claim 1 wherein the interior surfaces of the vessel are heated to from about 200° C. to about 650° C. for from about 1 to 24 hours.
Claim 5
Dependent Claim 20 words
The method of claim 3 wherein the oxidizable liquid chemical is alkyl lead, ethylene dibromide, ethylene dichloride, or vinyl chloride.
Claim 6
Dependent Claim 23 words
The method of claim 1 wherein the heat source is superheated air or a burner fueled by natural gas or liquid hydrocarbon fuel.
Claim 7
Dependent Claim 13 words
The method of claim 1 wherein the vessel is a railroad tank car.
Claim 8
Independent Claim 170 words
A method of decontaminating large vessels used for storing, transporting or processing liquid alkyl lead which comprises: a. introducing oxygen and a source of heat directly into the interior of the vessel, said vessel containing minor contaminating amounts of said liquid alkyl lead, the heat emitted from said heat source being sufficient to heat the interior surfaces of the vessel to a temperature sufficient to volatilize substantially all and decompose at least a portion of said alkyl lead contaminating the interior of said vessel, thereby to produce a combustion gas within the vessel; b. exhausting from the vessel combustion gas and lead dixoide particles resulting from the volatilization and decomposition of the alkyl lead during step (a); c. filtering lead dioxide particles and combustion gas exhausted from the vessel, thereby to separate said particles from the combustion gas; d. decomposing with heat alkyl lead remaining in the combustion gas exhausted from the vessel; and e. venting to the atmosphere combustion gas substantially free of lead dioxide particles and alkyl lead.
Claim 9
Independent Claim 170 words
A method of decontaminating large vessels used for storing, transporting or processing liquid alkyl lead which comprises: a. introducing oxygen and a source of heat directly into the interior of the vessel, said vessel containing minor contaminating amounts of said liquid alkyl lead, the heat emitted from said heat source being sufficient to heat the interior surfaces of the vessel to a temperature sufficient to volatilize substantially all and decompose at least a portion of said alkyl lead contaminating the interior of said vessel, thereby to produce a combustion gas within the vessel; b. exhausting from the vessel combustion gas and lead dixoide particles resulting from the volatilization and decomposition of the alkyl lead during step (a); c. filtering lead dioxide particles and combustion gas exhausted from the vessel, thereby to separate said particles from the combustion gas; d. decomposing with heat alkyl lead remaining in the combustion gas exhausted from the vessel; and e. venting to the atmosphere combustion gas substantially free of lead dioxide particles and alkyl lead.
Claim 10
Dependent Claim 22 words
The method of claim 7 wherein the alkyl lead is tetraethyl lead, tetramethyl lead or mixtures of tetraethyl lead and tetramethyl lead.
Claim 11
Independent Claim 32 words
The method of claims 7 or 8 wherein the interior surfaces of the vessel are heated to from about 200° C. to about 650° C. for from about 1 to 24 hours.
Claim 12
Dependent Claim 24 words
The method of claim 7 wherein the heat source is superheated air or a portable burner fueled by natural gas or liquid hydrocarbon fuel.
Claim 13
Dependent Claim 21 words
The method of claim 7 wherein a bag filter is used for filtering the exhausted lead dioxide particles and combustion gas.
Claim 14
Dependent Claim 23 words
The method of claim 11 wherein the bag filter is also used to filter flue gas derived from the manufacture of alkyl lead.
Claim 15
Independent Claim 20 words
The method of claims 1 or 4 wherein substantially all of the liquid organic chemical is decomposed in step (a).
Claim 16
Dependent Claim 26 words
The method of claim 7 wherein the vessel is selected from the group consisting of a railroad tank car, process vessel and a portable storage tank.
Claim 17
Dependent Claim 17 words
The method of claim 7 wherein substantially all of the alkyl lead is decomposed in step (a).
Claim 18
Dependent Claim 32 words
The method of claim 11, wherein a portion of the alkyl lead in the exhausted gas is decomposed by the action of a lead dioxide catalyst on the surface of the filter.

References Cited (Backward Citations)

US1040410A Cited
US1125930A Cited
US1901803A Cited
US2507685A Cited
US3219108A Cited
US3163134A Cited
US3428435A Cited
US3590756A Cited
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USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1985-05-31 1985-11-30 1986-06-01 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1989-05-31 1989-11-30 1990-06-01 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1993-05-31 1993-11-30 1994-06-01 $7700.00 Window Closed / Lapsed

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