WO2001094241A1 - Tank for purifying liquid fuels using hydrogen peroxide - Google Patents

Tank for purifying liquid fuels using hydrogen peroxide Download PDF

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Publication number
WO2001094241A1
WO2001094241A1 PCT/CA2001/000015 CA0100015W WO0194241A1 WO 2001094241 A1 WO2001094241 A1 WO 2001094241A1 CA 0100015 W CA0100015 W CA 0100015W WO 0194241 A1 WO0194241 A1 WO 0194241A1
Authority
WO
WIPO (PCT)
Prior art keywords
tank
fuel
hydrogen peroxide
fuels
platform
Prior art date
Application number
PCT/CA2001/000015
Other languages
French (fr)
Inventor
Viva Marie Cundliffe
Original Assignee
Viva Marie Cundliffe
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Viva Marie Cundliffe filed Critical Viva Marie Cundliffe
Priority to AU26594/01A priority Critical patent/AU2659401A/en
Publication of WO2001094241A1 publication Critical patent/WO2001094241A1/en

Links

Classifications

    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G27/00—Refining of hydrocarbon oils in the absence of hydrogen, by oxidation
    • C10G27/04—Refining of hydrocarbon oils in the absence of hydrogen, by oxidation with oxygen or compounds generating oxygen
    • C10G27/12—Refining of hydrocarbon oils in the absence of hydrogen, by oxidation with oxygen or compounds generating oxygen with oxygen-generating compounds, e.g. per-compounds, chromic acid, chromates
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/24—Stationary reactors without moving elements inside

Definitions

  • This 50-1250 barrel tank is a facility to Oxidize and Purify a variety of fuels using Hydrogen Peroxide (in 80% to 100%purity) before the fuel is sent to market.
  • the attachments and scheme are designed in an open air fashion so that the Hydrogen Peroxide can not cause a pressure buildup as it performs its oxidation process on the fuel.
  • the roof is designed to protect the contents of the tank from weather, and, hold sealed lighting for the work area.
  • the Grid Iron work area is of sufficient size ( covering about 25% of the top of the tank) to allow for two to three persons to perform the tank operations, which are to receive the barrels, measure the Hydrogen Peroxide, and operate the mixer as the Hydrogen Peroxide is added to the fuel.
  • the Fuel After the Fuel stands in the tank for 24 -48 hours, it will be suctioned out to a preliminary or final storage tank or taken on board a tanker truck for market. There will be a nominal amount of water and dust settled at the bottom of the subject tank, which will be hosed out of the tank at its lowest corner, and put into barrels, and shipped in water to a handling facility.
  • the tank will be constructed of a sufficiently strong combination of Re-bar concrete and Metallic or Plastic lining (non-reactive surfaces for the Hydrogen Peroxide). There will be a covered electric or gas motored lift shaft to the side of the tank for bringing the Hydrogen Peroxide barrels from ground level to above the top of the tank, where it will be administered to the fuel in measured quantities.
  • the tank will serve as a stand alone added facility to the refinery setting, and service bulk fuel handling systems prior, as in upstream, to commercial use and delivery of fuels, possibly including a permanganate treatment bed at this stage, prior to the finishing tank.
  • the tank will have a working platform from which the Hydrogen Peroxide can be administered in measured doses to the fuel in the tank as described in claim 1.
  • the tank's platform will serve as an access point for the separation of the fuel from the settled byproduct, accommodating a flexible polypropylene suction hose that connects to the transport truck, or an finished product tank, which will be needed after the fuel oxidation process is complete and unloading and storing of the fuel is required.
  • the roof of the tank will contain sealed lighting to illuminate the tank and the working platform, as in claim 3, and will be of a sufficient brightness to illuminate to the bottom of the tank.
  • the tank will have a moveable aluminum interior access ladder for access to the interior of the tank
  • the tank will have a top mounted slurry apparatus in the form of a plastic fan to stir the contents of the tank and mix the Hydrogen Peroxide safely, and the motor will be of a spark free rating and of sufficient power to repeatedly perform the mixing.
  • the tank will have a 3 degree sloped interior to one corner so that the byproduct can be hosed out of the tank with water, and will have a permanently mounted egress valve controlled from the lowest point of the tank floor.
  • the tank may have a catalyzing bed for the hydrogen peroxide located on the working platfo ⁇ n to catalyze the hydrogen peroxide prior to applying it into the tank to treat the fuel.
  • the tank will serve as a stand alone added facility to the refinery setting, and service bulk fuel handling systems prior, as in upstream, to commercial use and delivery of fuels.
  • the tank will have a working platform from which the Hydrogen Peroxide can be administered in measured doses to the fuel in the tank as described in claim 1.
  • the tank's platform will serve as an access point for the separation of the fuel from the settled byproduct, accommodating a flexible polypropylene suction hose that connects to the transport truck, or an finished product tank, which will be needed after the fuel oxidation process is complete and unloading and storing of the fuel is required.
  • the roof of the tank will contain sealed lighting to illuminate the tank and the working platform,as in claim 3, and will be of a sufficient brightness to illuminate to the bottom of the tank, and the roof will seal the tank chamber when dealing with volatile fuels such as JP4 gasoline, Aviation fuels, in order that these subject fuels will not evaporate into the environment.
  • the tank will have a moveable aluminum interior access ladder for access to the interior of the tank
  • the tank will have a top mounted slurry apparatus in the form of a plastic fan to stir the contents of the tank and mix the Hydrogen Peroxide safely, and the motor will be of a spark free rating and of sufficient power to repeatedly perform the mixing.
  • the tank will have a 3 degree sloped interior to one corner so that the byproduct can be hosed or distilled out of the tank, and will have a permanently mounted egress valve controlled from the lowest point of the tank floor.
  • the tank may have a catalyzing bed for the hydrogen peroxide located on the working platform to catalyze the hydrogen peroxide prior to applying it to the tank to treat the fuel.
  • the tank has a platform at the top from which comprises a delivery system of Hydrogen Peroxide to the fuel in the tank, which includes a non-reactive surface fan which is mounted from this platfonn to stir the petrochemical with the Hydrogen Peroxide.
  • the tank will contain an oxidation reaction between the fuel and the Hydrogen Peroxide.
  • the tank will have a full roof, but with partially opened walls above the fuel level to allow for ventilation and worker access.
  • the tank will have a sloped bottom where the reacted material (residium) removed from the fuel can settle.
  • the tank will have a water supply to it through the top or side of the tank comprising of a 2-4 inch hose or opening.
  • a valve at the bottom of the tank that may be opened from the exterior, and the by product of the oxidation can be flushed into barrels, or applied to a standard H2S Stripper and methane gas trapping apparatus, either using a stream of water from the water supply provided inside the tank, or flushing by ventillation as the fuel is treated.
  • the tank comprises a method of removing toxic nitrogens, sulfurs, methanes and fine metals and carbon particles from the fuel before it is taken into commercial use at the final stage tank, possibloy with an permanganate treatment bed, downstream to this tank.
  • the fuels to be treated by this intermediate tank are reframate gasoline, all grades of diesel, kerosene, aviation fuel, and liquid jet fuel.

Abstract

I claim as my invention, a 50-1250 barrel intermediate Aluminum or Plastic lined tank for mixing hydrocarbon fuels with hydrogen peroxide. The tank has a platform at the top from which comprises a delivery system of Hydrogen Peroxide to the fuel in the tank, which includes a non-reactive surface fan which is mounted from this platform to stir the petrochemical with the Hydrogen Peroxide. The tank will contain an oxidation reaction between the fuel and the Hydrogen Peroxide. The tank will have a full roof, but with partially opened walls above the fuel level to allow for ventilation and worker access. The tank will have a sloped bottom where the reacted material (residium) removed from the fuel can settle. The tank will have a water supply to it through the top or side of the tank comprising of a 2-4 inch hose or opening. To the side of the interior of the tank their will be a valve at the bottom of the tank that may be opened from the exterior, and the by product of the oxidation can be flushed into barrels, or applied to a standard H2S Stripper and methane gas trapping apparatus, either using a stream of water from the water supply provided inside the tank, or flushing by ventillation as the fuel is treated. The tank comprises a method of removing toxic nitrogens, sulfurs, methanes and fine metals and carbon particles from the fuel before it is taken into commercial use at the final stage tank, possibly with an permanganate treatment bed, downstream to this tank. The fuels to be treated by this intermediate tank are reframate gasoline, all grades of diesel, kerosene, aviation fuel, and liquid jet fuel.

Description

A LARGE INTEGRATABLE HYDROGEN PEROXIDE INTERMEDIATE STAGE
TANK FOR THE PURPOSE OF PURIFYING COMMERCIAL FUELS USING UNTREATED HYDROGEN PEROXIDE IN FUELS
This 50-1250 barrel tank is a facility to Oxidize and Purify a variety of fuels using Hydrogen Peroxide (in 80% to 100%purity) before the fuel is sent to market. The attachments and scheme are designed in an open air fashion so that the Hydrogen Peroxide can not cause a pressure buildup as it performs its oxidation process on the fuel. The roof is designed to protect the contents of the tank from weather, and, hold sealed lighting for the work area. The Grid Iron work area is of sufficient size ( covering about 25% of the top of the tank) to allow for two to three persons to perform the tank operations, which are to receive the barrels, measure the Hydrogen Peroxide, and operate the mixer as the Hydrogen Peroxide is added to the fuel. After the Fuel stands in the tank for 24 -48 hours, it will be suctioned out to a preliminary or final storage tank or taken on board a tanker truck for market. There will be a nominal amount of water and dust settled at the bottom of the subject tank, which will be hosed out of the tank at its lowest corner, and put into barrels, and shipped in water to a handling facility. The tank will be constructed of a sufficiently strong combination of Re-bar concrete and Metallic or Plastic lining (non-reactive surfaces for the Hydrogen Peroxide). There will be a covered electric or gas motored lift shaft to the side of the tank for bringing the Hydrogen Peroxide barrels from ground level to above the top of the tank, where it will be administered to the fuel in measured quantities.
-Fuel intake pipe (permanent or flexible) for filling tank with fuel.
2-sloped floor of aluminum or plastic lined tank
3-byproduct egress pipe with release valve
4-lift shaft for barrels of Hydrogen peroxide from ground level to top of tank
5-roof over reception area for hydrogen peroxide barrels
6-exterior access ladder to working area
J-interior access ladder
8-hose of fresh water supply to hose out bottom of tank
9-exterior of tank
10-roof of tank with full sealed lighting for work area and tank
11 -steel girded walking and working platform above fuel and tank floor.
12-shaft to mixing fan to mix fuel and hydrogen peroxide
13-plastic or permanent sump-hose to remove treated fuel to tank truck or pipeline
14-Grid iron platform for receiving Hydrogen Peroxide barrels above tank
15-Grid iron Platform for miscellaneous storage, work, and supervision above tank
16-Strapping to wrap around H202 barrels and attach barrels to lift device. I claim as my invention:
1) A 50-1250 barrel tank facility to purify fuels in a bulk process in accordance with practices required in the oil and gas industry, as a an intermediate facility to perform the fuel treatment with Hydrogen Peroxide on Jp4 gas, regular gasoline, diesel, kerosene, aviation fuel, and liquid jet fuel.
2) As in Claim 1 The tank will serve as a stand alone added facility to the refinery setting, and service bulk fuel handling systems prior, as in upstream, to commercial use and delivery of fuels, possibly including a permanganate treatment bed at this stage, prior to the finishing tank.
3) The tank will have a working platform from which the Hydrogen Peroxide can be administered in measured doses to the fuel in the tank as described in claim 1.
4) As in claim 3 ,the tank's platform will serve as an access point for the separation of the fuel from the settled byproduct, accommodating a flexible polypropylene suction hose that connects to the transport truck, or an finished product tank, which will be needed after the fuel oxidation process is complete and unloading and storing of the fuel is required.
5) The roof of the tank will contain sealed lighting to illuminate the tank and the working platform, as in claim 3, and will be of a sufficient brightness to illuminate to the bottom of the tank.
6) The tank as in claims 1,2,3,4,5 will have a fixed exterior access ladder to the platform.
7)As in claim 6, The tank will have a moveable aluminum interior access ladder for access to the interior of the tank
8) As in claim 3, the tank will have a top mounted slurry apparatus in the form of a plastic fan to stir the contents of the tank and mix the Hydrogen Peroxide safely, and the motor will be of a spark free rating and of sufficient power to repeatedly perform the mixing.
9) As in Claim 1, The tank will have a 3 degree sloped interior to one corner so that the byproduct can be hosed out of the tank with water, and will have a permanently mounted egress valve controlled from the lowest point of the tank floor.
10) As in claims 1, 2, 3, and 4, the tank may have a catalyzing bed for the hydrogen peroxide located on the working platfoπn to catalyze the hydrogen peroxide prior to applying it into the tank to treat the fuel.
AMENDED CLAIMS
[received by the International Bureau on 04 September 2001 (04.09.01); original claims 1-10 amended (1 page)]
I claim as my invention:
1) A 50-1250 barrel tank facility to purify fuels in a bulk process in accordance with practices required in the oil and gas industry, as a an intermediate facility to perform the fuel treatment with Hydrogen Peroxide on Jp4 gas, regular gasoline, diesel, kerosene, aviation fuel, and liquid jet fuel, and crushed coal.
2) As in Claim 1 The tank will serve as a stand alone added facility to the refinery setting, and service bulk fuel handling systems prior, as in upstream, to commercial use and delivery of fuels.
3) The tank will have a working platform from which the Hydrogen Peroxide can be administered in measured doses to the fuel in the tank as described in claim 1.
4) As in claim 3, the tank's platform will serve as an access point for the separation of the fuel from the settled byproduct, accommodating a flexible polypropylene suction hose that connects to the transport truck, or an finished product tank, which will be needed after the fuel oxidation process is complete and unloading and storing of the fuel is required.
5) The roof of the tank will contain sealed lighting to illuminate the tank and the working platform,as in claim 3, and will be of a sufficient brightness to illuminate to the bottom of the tank, and the roof will seal the tank chamber when dealing with volatile fuels such as JP4 gasoline, Aviation fuels, in order that these subject fuels will not evaporate into the environment.
6) The tank as in claims 1,2,3,4,5 will have a fixed exterior access ladder to the platform.
7)As in claim 6, The tank will have a moveable aluminum interior access ladder for access to the interior of the tank
8) As in claim 3, the tank will have a top mounted slurry apparatus in the form of a plastic fan to stir the contents of the tank and mix the Hydrogen Peroxide safely, and the motor will be of a spark free rating and of sufficient power to repeatedly perform the mixing.
9) As in Claim 1, The tank will have a 3 degree sloped interior to one corner so that the byproduct can be hosed or distilled out of the tank, and will have a permanently mounted egress valve controlled from the lowest point of the tank floor.
10) As in claims 1,2,3, and 4, the tank may have a catalyzing bed for the hydrogen peroxide located on the working platform to catalyze the hydrogen peroxide prior to applying it to the tank to treat the fuel.
I claim as my invention, a 50 -1250 barrel intermediate Aluminum or Plastic lined tank for mixing hydrocarbon fuels with hydrogen peroxide. The tank has a platform at the top from which comprises a delivery system of Hydrogen Peroxide to the fuel in the tank, which includes a non-reactive surface fan which is mounted from this platfonn to stir the petrochemical with the Hydrogen Peroxide. The tank will contain an oxidation reaction between the fuel and the Hydrogen Peroxide. The tank will have a full roof, but with partially opened walls above the fuel level to allow for ventilation and worker access. The tank will have a sloped bottom where the reacted material (residium) removed from the fuel can settle. The tank will have a water supply to it through the top or side of the tank comprising of a 2-4 inch hose or opening. To the side of the interior of the tank their will be a valve at the bottom of the tank that may be opened from the exterior, and the by product of the oxidation can be flushed into barrels, or applied to a standard H2S Stripper and methane gas trapping apparatus, either using a stream of water from the water supply provided inside the tank, or flushing by ventillation as the fuel is treated. The tank comprises a method of removing toxic nitrogens, sulfurs, methanes and fine metals and carbon particles from the fuel before it is taken into commercial use at the final stage tank, possibloy with an permanganate treatment bed, downstream to this tank. The fuels to be treated by this intermediate tank are reframate gasoline, all grades of diesel, kerosene, aviation fuel, and liquid jet fuel.
PCT/CA2001/000015 2000-06-05 2001-01-08 Tank for purifying liquid fuels using hydrogen peroxide WO2001094241A1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
AU26594/01A AU2659401A (en) 2000-06-05 2001-01-08 Tank for purifying liquid fuels using hydrogen peroxide

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
CA2,310,839 2000-06-05
CA 2310839 CA2310839A1 (en) 2000-06-05 2000-06-05 A large integratable hydrogen peroxide intermediate stage or stand alone tank for the purpose of purifying fuels using high strength hydrogen peroxide in fuels

Publications (1)

Publication Number Publication Date
WO2001094241A1 true WO2001094241A1 (en) 2001-12-13

Family

ID=4166389

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/CA2001/000015 WO2001094241A1 (en) 2000-06-05 2001-01-08 Tank for purifying liquid fuels using hydrogen peroxide

Country Status (3)

Country Link
AU (1) AU2659401A (en)
CA (1) CA2310839A1 (en)
WO (1) WO2001094241A1 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
ES2283178A1 (en) * 2005-03-08 2007-10-16 Carinox, S.A. Elevator for sample taking material in vertical storage tanks, has two frames, where frame is provided to pay attention to ground and other frame is in vertical alignment at extreme superiority of tank

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109173334B (en) * 2018-09-30 2021-02-02 苏州格燊制药设备工程技术有限公司 A draw jar for medicament production

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2210542A (en) * 1938-12-10 1940-08-06 Union Oil Co Process of removing phenols from mineral oils
US4197744A (en) * 1978-08-14 1980-04-15 Overstreet Robbie J Gas safety roof gauging control hatch adapter
US4490833A (en) * 1980-09-12 1984-12-25 Hoxan Corporation X-Ray photographic inspecting device
US4589565A (en) * 1984-01-03 1986-05-20 Spivey Bruce T Portable liquid storage tank
US4776581A (en) * 1986-07-24 1988-10-11 Shepherdson Donalda G Exercise apparatus
CA2164072A1 (en) * 1995-11-29 1997-05-30 Earl Gingras Method of removing iron sulfide from oil
WO1997048647A1 (en) * 1996-06-18 1997-12-24 Amec Australia Pty. Ltd. Waste water treatment plant

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2210542A (en) * 1938-12-10 1940-08-06 Union Oil Co Process of removing phenols from mineral oils
US4197744A (en) * 1978-08-14 1980-04-15 Overstreet Robbie J Gas safety roof gauging control hatch adapter
US4490833A (en) * 1980-09-12 1984-12-25 Hoxan Corporation X-Ray photographic inspecting device
US4589565A (en) * 1984-01-03 1986-05-20 Spivey Bruce T Portable liquid storage tank
US4776581A (en) * 1986-07-24 1988-10-11 Shepherdson Donalda G Exercise apparatus
CA2164072A1 (en) * 1995-11-29 1997-05-30 Earl Gingras Method of removing iron sulfide from oil
WO1997048647A1 (en) * 1996-06-18 1997-12-24 Amec Australia Pty. Ltd. Waste water treatment plant

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
ES2283178A1 (en) * 2005-03-08 2007-10-16 Carinox, S.A. Elevator for sample taking material in vertical storage tanks, has two frames, where frame is provided to pay attention to ground and other frame is in vertical alignment at extreme superiority of tank

Also Published As

Publication number Publication date
CA2310839A1 (en) 2001-09-11
AU2659401A (en) 2001-12-17

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