WO2022162603A1 - Installation de traitement pour combustible hydrocarboné - Google Patents

Installation de traitement pour combustible hydrocarboné Download PDF

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Publication number
WO2022162603A1
WO2022162603A1 PCT/IB2022/050753 IB2022050753W WO2022162603A1 WO 2022162603 A1 WO2022162603 A1 WO 2022162603A1 IB 2022050753 W IB2022050753 W IB 2022050753W WO 2022162603 A1 WO2022162603 A1 WO 2022162603A1
Authority
WO
WIPO (PCT)
Prior art keywords
central
dielectric
magnets
housing
inlet
Prior art date
Application number
PCT/IB2022/050753
Other languages
English (en)
Inventor
Konstantin Vitalievich SLASTNIKOV
Original Assignee
BOLTENKOV, Evgenii Vladimirovich
CHABAN, Aleksey Sergeevich
GANIN, Sergei Aleksandrovich
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 BOLTENKOV, Evgenii Vladimirovich, CHABAN, Aleksey Sergeevich, GANIN, Sergei Aleksandrovich filed Critical BOLTENKOV, Evgenii Vladimirovich
Publication of WO2022162603A1 publication Critical patent/WO2022162603A1/fr

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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
    • C10G32/00—Refining of hydrocarbon oils by electric or magnetic means, by irradiation, or by using microorganisms
    • C10G32/02—Refining of hydrocarbon oils by electric or magnetic means, by irradiation, or by using microorganisms by electric or magnetic means
    • 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
    • C10G15/00—Cracking of hydrocarbon oils by electric means, electromagnetic or mechanical vibrations, by particle radiation or with gases superheated in electric arcs
    • C10G15/08—Cracking of hydrocarbon oils by electric means, electromagnetic or mechanical vibrations, by particle radiation or with gases superheated in electric arcs by electric means or by electromagnetic or mechanical vibrations
    • 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
    • C10G15/00—Cracking of hydrocarbon oils by electric means, electromagnetic or mechanical vibrations, by particle radiation or with gases superheated in electric arcs
    • C10G15/10—Cracking of hydrocarbon oils by electric means, electromagnetic or mechanical vibrations, by particle radiation or with gases superheated in electric arcs by particle radiation
    • 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
    • C10G31/00—Refining of hydrocarbon oils, in the absence of hydrogen, by methods not otherwise provided for

Definitions

  • the invention relates to the treatment of liquids and gases, in particular hydrocarbon fuels according to claim 1 .
  • a magnetogravity separator containing a magnet system is known.
  • a separation chamber is installed in the magnet system.
  • the chamber is filled with ferromagnetic liquid.
  • the separator is equipped with a separating plate.
  • the separator has a device for removing the light fraction (RU200543).
  • the reactor contains a cylindrical dielectric body 19.
  • the vessel has dielectric inlet and outlet fittings.
  • the source of the magnetic field is generated by pairs of magnets with the same poles facing each other.
  • the reactor has a dielectric profiled seal with centripetal notches.
  • One of the magnets has an outlet opening in the centre of the magnet.
  • One of the flanges is connected to the intake port.
  • the reactor contains a cylindrical fuel line pipe.
  • the electric field source of the reactor is in the form of an asymmetrical capacitor. (EA035654).
  • the downside low efficiency, as centripetal rotation is not maintained over the entire length of the reactor; electrical pulses with only one parameter.
  • the task is to ensure non-thermal (without heating the medium) cracking.
  • the task is to remove particles with a size of 0.1 to 0.25 micron.
  • the technical result is the generation of a centripetal movement of the medium.
  • the centripetal movement of the medium is generated over the entire length of the large and small diameter part of the central conductor element.
  • the result is an increase in the processing time of the medium.
  • the result is an improvement in the quality of handling the medium.
  • the medium has a multiple path of movement around and along the rod.
  • Fig. 1 is a general view of the magnetic gravity separator
  • Fig. 2 is a longitudinal section through the magnetic gravity separator
  • Fig. 3 is a top view of the magnetic gravity separator
  • Fig. 4 is a cross-sectional view showing in particular a petal brake
  • Fig. 5 shows a separate schematic representation of the bypass with position 10 (three-way valve) corresponding to position 5 (outlet). Position 11 (three-way valve) corresponds to position 6 (inlet);
  • Fig. 6 shows a schematic diagram of a non-thermal fission reactor.
  • the hydrocarbon fuel treatment plant consists of a magnetic gravity separator.
  • the plant also consists of a non-thermal fission reactor.
  • the magnetogravity separator contains an inlet 6 and an outlet 5.
  • the inlet 6 and the outlet 5 can be designed in any known technical manner.
  • the separator contains a non-magnetic housing 1 , a cover 14 and a magnetic field source.
  • the magnetic field source is in the form of a rod 8.
  • the removable rod 8 is magnetised longitudinally along its entire length with several N-S pole pairs.
  • the inlet 6 and the outlet 5 are connected to the bypass 9.
  • the inlet 6 is equipped with centrifugal guide ports.
  • the inner cavity forms a toroidal structure.
  • the toroidal structure is bounded by the petal brake 7, the housing walls 2 and the rod 8.
  • the process medium enters through the inlet 6 of the bottom flange 1 into the cavity on the centripetal trajectory.
  • the working medium forms a toroidal structure in the interior of the magnetic gravity separator.
  • the toroidal structure is formed between the housing walls 2, the petal brake 7 and the rod 8.
  • the toroidal structure rotates in two planes.
  • the toroidal structure is in the effective zone of the magnetic field and the earth's gravity.
  • Paramagnetic particles are in the toroidal structure in the working environment.
  • the paramagnetic particles rotate. In the process, the particles repeatedly repeat their trajectory in two planes.
  • the particles are deposited on the rod 8.
  • the rod has several poles. Large particles are deposited under the influence of centripetal acceleration. Fine particles are deposited by gravity.
  • the working medium is decelerated by the petal brake 7.
  • the cover 14 is fixed to the flange 3 with the screw connection 12 via the O-ring seal 13.
  • the magnetic rod 8 is fixed inside the cover 14.
  • the cover is perforated.
  • the magnetic rod 8 is fastened by means of the sleeve 4 with a screw connection.
  • the fittings for inlet 6 and outlet 5 are connected to bypass 9 via three-way valves 11 and 10.
  • the forward condenser contains a central conductive element 20.
  • the element 5 is designed as a tube with variable cross-section.
  • the tube with variable cross-section can consist of several elements.
  • the elements can be connected to each other by means of a screw connection.
  • the elements may be joined by welding or by any other means known in the art.
  • the second conductive element 21 is in the form of a metal strip.
  • the metal strip is wound onto the central conducting element 20 via a dielectric 7.
  • the input and the output of the central conducting element 20 are pro- vided with dielectric connecting elements 23.
  • the connecting elements may be fittings.
  • the connecting elements 3 are connected to the three-way valves via a bypass.
  • the conductive elements have a larger diameter.
  • the magnets face each other and have identical poles.
  • a profile element 25 is located between the magnets 24.
  • the profile element 25 has a profile formed by notches. The notches define the centripetal acceleration of the medium from the edge to the centre of the magnets 24. In the centre of the magnet 24 there is an opening for an outlet 5.
  • the hole is placed on the side of the part with the smaller diameter of the central conducting element 20.
  • the central conducting element 20 has a spirally wound element 17 made of a non-magnetic material (e.g. non-magnetic metal wire).
  • the housing 1 is made of dielectric material.
  • the housing is usefully made of impact resistant material.
  • the housing is filled with dielectric material 18 on the inside.
  • the central conductor element 20 and the second conductor element 21 form a coaxial structure.
  • the central conductive element 20 and the conductive element 21 are surrounded by a dielectric housing 1.
  • the housing may have covers 2.
  • Liquid or gas is introduced into the central conducting element 20. Through the profiled element 25, the liquid or gas receives a centripetal acceleration from the edge to the centre of the magnets 24. The liquid or gas enters the part of the central conducting element 20 with the smaller diameter through the outlet opening 11.
  • the spirally wound element 17 maintains the spiral centripetal motion. The movement is maintained until it leaves the central conducting element 20.
  • a high pressure zone is formed in the working fluid.
  • a discharge zone is also formed in the central part of the central conducting element 20.
  • the formation process is the key factor. The process has a catalytic effect on the medium at the boundary between the different pressure zones.
  • the measure aims to ensure high performance of the proposed technical solution.
  • Two units supply the reactor with power.
  • One unit sets the frequency and the other does the amplification and shaping of the pulse waveform to supply the pass capacitor.
  • the other does the amplification and pulse shaping to supply the pass capacitor.
  • Rare earth magnets can be used as a magnetic field source or electromagnets.
  • a light and/or colour indicator can be installed to monitor the operation of the unit. The indicator is mounted on the outside of the housing 1.
  • the hydrocarbon fuel is treated under the influence of overpressure along the edge of the centripetal zone.
  • the outflow zone (low pressure) in the centre is also treated.
  • the fuel oil is in the presence of magnetic and modulated electric fields.
  • the fields provide the necessary energy for this process.
  • the energy leads to a radical chain mechanism of C-C bond breaking.
  • the molecules of the paraffinic, naphthenic, alkylaromatic and high-boiling unsaturated hydrocarbons of the crude oil break. C-H bonds in low molecular weight paraffin and other hydrocarbons are also broken. The process leads to the achievement of the claimed technical effect.
  • At least one, more preferably two power supply units 15 are provided, which are preferably arranged within the housing 1.
  • an electrical connection 16 for an electrical power source is provided, preferably in a bottom or top cover 14.
  • the invention may relate to an apparatus for treating hydrocarbon fuels, characterized by a magneto gravity separator operatively connectable to a non-thermal fission reactor.
  • the apparatus comprises an inlet 6, an outlet 5, a non-magnetic housing (1), a cover (14), and a magnetic field source having the shape of a rod 8, a petal brake (-s), the rod (8) being removable and extending longitudinally along its entire length magnetized with a plurality of N-S pole pairs, the inlet 6 and outlet 5 being connected by a bypass (9), the inlet being provided with centrifugal fittings, and the inner cavity forming a toroidal structure.
  • the apparatus is provided in that the non-thermal fission reactor contains a dielectric shell the housing is filled with dielectric material 18 the source of the magnetic field are the magnets 24 whose poles are opposite each other the housing 1 contains a capacitor the central conductive element 20 is designed as a tube with an alternating cross-section a second conductive element 21 has the form of a metal strip the metal strip is wound onto the central conductive element 20 the metal strip is wound through a dielectric the inlet 6 and the outlet 5 of the central conducting element 20 are provided with dielectric connecting elements 23 the elements are connected by a bypass 9 magnets 24 are located at the opposite ends of the part 22 with the larger diameter of the central conducting element 20 the magnets 24 face each other with their identical poles there is a profile element 25 between the magnets the magnet 24 has an opening in the middle the opening is on the side with the smaller diameter of the central conductor element 20 the part of the central conductor element 20 with the smaller diameter has a wound coil 17 the wound coil 17 is made of non-magnetic material the dielectric body 19,
  • the apparatus is provided in that at least one, preferably two power supply units 15 are provided, which are preferably arranged within the housing 1.
  • an electrical connection 16 for an electrical power source is provided, preferably in a bottom or top cover 14.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Physics & Mathematics (AREA)
  • Electromagnetism (AREA)
  • Mechanical Engineering (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Microbiology (AREA)
  • Health & Medical Sciences (AREA)
  • Toxicology (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)

Abstract

La présente invention concerne un appareil pour le traitement de combustibles hydrocarbonés, caractérisé par un séparateur gravitationnel magnétique pouvant être relié de manière fonctionnelle à un réacteur de fission non thermique.
PCT/IB2022/050753 2021-01-29 2022-01-28 Installation de traitement pour combustible hydrocarboné WO2022162603A1 (fr)

Applications Claiming Priority (4)

Application Number Priority Date Filing Date Title
RURU2021102130 2021-01-29
RURU2021102129 2021-01-29
RU2021102129 2021-01-29
RU2021102130 2021-01-29

Publications (1)

Publication Number Publication Date
WO2022162603A1 true WO2022162603A1 (fr) 2022-08-04

Family

ID=80218398

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/IB2022/050753 WO2022162603A1 (fr) 2021-01-29 2022-01-28 Installation de traitement pour combustible hydrocarboné

Country Status (1)

Country Link
WO (1) WO2022162603A1 (fr)

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20170190984A1 (en) * 2014-03-21 2017-07-06 Galexum Technologies Ag A method of cracking and/or demulsification of hydrocarbons and/or fatty acids in emulsions
RU200543U1 (ru) * 2020-08-06 2020-10-28 Закрытое акционерное общество "ИТОМАК" Магнитогравитационный сепаратор
RU2766847C1 (ru) * 2021-01-29 2022-03-16 Болтенков Евгений Владимирович Реактор нетермического крекинга

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20170190984A1 (en) * 2014-03-21 2017-07-06 Galexum Technologies Ag A method of cracking and/or demulsification of hydrocarbons and/or fatty acids in emulsions
RU200543U1 (ru) * 2020-08-06 2020-10-28 Закрытое акционерное общество "ИТОМАК" Магнитогравитационный сепаратор
RU2766847C1 (ru) * 2021-01-29 2022-03-16 Болтенков Евгений Владимирович Реактор нетермического крекинга

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