WO1992006331A1 - Procede de destruction thermique de composes liquides toxiques et organiques gaseux - Google Patents

Procede de destruction thermique de composes liquides toxiques et organiques gaseux Download PDF

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Publication number
WO1992006331A1
WO1992006331A1 PCT/SU1990/000229 SU9000229W WO9206331A1 WO 1992006331 A1 WO1992006331 A1 WO 1992006331A1 SU 9000229 W SU9000229 W SU 9000229W WO 9206331 A1 WO9206331 A1 WO 9206331A1
Authority
WO
WIPO (PCT)
Prior art keywords
pressure
zone
gas
organic compounds
gazοοbρaznyχ
Prior art date
Legal status (The legal status 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 status listed.)
Ceased
Application number
PCT/SU1990/000229
Other languages
English (en)
Russian (ru)
Inventor
July Abramovich Kolbanovsky
Evgeny Ivanovich Goncharov
Alexandr Stepanovich Grigoriev
Valery Vasilievich Demidjuk
Viktor Stepanovich Schipachev
Nikolai Alfredovich Plate
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Institut Neftekhimicheskogo Sinteza Imeni A V Topchieva
AV Topchiev Institute of Petrochemical Synthesis
Original Assignee
Institut Neftekhimicheskogo Sinteza Imeni A V Topchieva
AV Topchiev Institute of Petrochemical Synthesis
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 Institut Neftekhimicheskogo Sinteza Imeni A V Topchieva, AV Topchiev Institute of Petrochemical Synthesis filed Critical Institut Neftekhimicheskogo Sinteza Imeni A V Topchieva
Priority to PCT/SU1990/000229 priority Critical patent/WO1992006331A1/fr
Publication of WO1992006331A1 publication Critical patent/WO1992006331A1/fr
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

Links

Classifications

    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G7/00—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals
    • F23G7/06—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of waste gases or noxious gases, e.g. exhaust gases
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G7/00—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals
    • F23G7/008—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals for liquid waste

Definitions

  • P ⁇ edshes ⁇ vuyuschiG u ⁇ en ⁇ e ⁇ ni ⁇ i ⁇ sh ⁇ izves ⁇ n ⁇ ⁇ azlichnye s ⁇ s ⁇ by ⁇ e ⁇ miches ⁇ g ⁇ ⁇ S unich ⁇ zheniya ⁇ sichny ⁇ ⁇ ganiches ⁇ i ⁇ s ⁇ edineny, na ⁇ ime ⁇ , za ⁇ ina (iz ⁇ il ⁇ v ⁇ g ⁇ e ⁇ i ⁇ a me ⁇ il ⁇ s ⁇ n ⁇ G: ⁇ isl ⁇ y) iu ⁇ e ⁇ .: ⁇ i ⁇ lnza.
  • the process is not prone to atmospheric pressure because of the hazardous components: these are ovens.
  • the foreign currency is no more than 99,996 ⁇ .
  • the non-hazardous operation of the exhaust gas is 20% higher than the previous one due to a low concentration.
  • the invention has the task of disassembling a thermally disassembled liquid and gas discharges of the
  • i ⁇ ⁇ azdelenie in ⁇ m, s ⁇ g- lasn ⁇ ⁇ z ⁇ b ⁇ e ⁇ en ⁇ yu, szh ⁇ ganie vedu ⁇ ⁇ ⁇ dde ⁇ zhanii ⁇ ⁇ ea ⁇ tsi ⁇ nn ⁇ : z ⁇ ne ⁇ em ⁇ e ⁇ a ⁇ u ⁇ y in in ⁇ e ⁇ ale 1500-35001, pressure ⁇ in ⁇ e ⁇ vale 0.5-10 ⁇ LPa and ⁇ b ⁇ azuyuschiesya gaz ⁇ b- ⁇ aznye ⁇ du ⁇ y ⁇ Y ⁇ DYA ⁇ OF ⁇ ea ⁇ tsi ⁇ nn ⁇ z ⁇ ny with ⁇ ⁇ y ⁇ ,
  • the method may have been used for any toxic and supercomposite organic :: :: sarc, soman, ⁇ ⁇ :: :: :: :: ::: ::: ::: :::::::::::::::::::::::::::::::::::::::::::::::::::::::::::::::::::::::::::::::::::::::::::::::::::::::::::::::::::::::::::::::::::::::::::::::::::::::::::::::::::::::::::::::::::::::::::::::::::::
  • Residual residual concentration of annihilating compounds in a few dozen Residual residual concentration of annihilating compounds in a few dozen.
  • the pressure in the long-range operation is not necessary to maintain in the range of 0.1-5 ⁇ .Pa and at least twice as low as for the
  • the range of residence is divided by
  • the oxidizing agent is supplied to the first reactive zone to be dealt with with a coefficient of excess that is between 0.5-1.5.
  • the reactive area is also provided with liquid fuel, taken with the help of the eliminated connections for 9: 1 odical connections.
  • the mixture is natural and is in good condition 8: 2 with an acid with an excess of the oxidizing agent I. I-supports the temperature of 35%. ⁇ . pressure 12 ⁇ . ⁇ a ⁇ at the time of the inactivation of the reagents 5- " ⁇ "* 3 s.
  • the obtained gas-derived products are withdrawn from the reaction with the reaction,
  • Example 4 25 Reactivate the type of oxygen, through fats, they give LOW. ⁇ '' With an acid (oxidizer) with an excess of 1.2. Reactivate the temperature of 2500 II and a pressure of 5 ° C. For both time and time of reacting, react 3 " ⁇ 0 ""3 sec.
  • the chemical type delivers a mixture of kerosene and LSD in a volumetric mixture of 1: 9 and 5% acid (excess) to the mixture through oxygen.
  • they support the tempera. a pressure of 2200 ⁇ and a pressure of 5 riona ⁇ and the duration of the residence of the agent 2- ⁇ 0 ⁇ in s.
  • the resulting gaseous products - discharges very quickly, the same local speed of sound, and 10 discharges the product, where there is no waste ⁇ ⁇ m ⁇ ea ⁇ e ⁇ dde ⁇ zhivayu ⁇ ⁇ em ⁇ e ⁇ a ⁇ u ⁇ u 1200 ⁇ and a pressure of 2 ⁇ Pa ⁇ i v ⁇ emeni ⁇ ebyvaniya gaz ⁇ b ⁇ azny ⁇ ⁇ du ⁇ ⁇ G 2-5.
  • Gaseous products are sent to the separation.

Landscapes

  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Heterocyclic Carbon Compounds Containing A Hetero Ring Having Nitrogen And Oxygen As The Only Ring Hetero Atoms (AREA)

Abstract

Le procédé consiste à acheminer un agent d'oxydation ainsi que des composés liquides toxiques et organiques gaseux dans une zone de réaction, à brûler ces composés à une température comprise entre 1500 et 3500 K et à une pression comprise entre 0,5 et 10 MPa, et à décharger les produits gaseux obtenus de la zone de réaction à une vitesse égale à la vitesse du son locale, entraînant leur séparation.
PCT/SU1990/000229 1990-10-02 1990-10-02 Procede de destruction thermique de composes liquides toxiques et organiques gaseux Ceased WO1992006331A1 (fr)

Priority Applications (1)

Application Number Priority Date Filing Date Title
PCT/SU1990/000229 WO1992006331A1 (fr) 1990-10-02 1990-10-02 Procede de destruction thermique de composes liquides toxiques et organiques gaseux

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
PCT/SU1990/000229 WO1992006331A1 (fr) 1990-10-02 1990-10-02 Procede de destruction thermique de composes liquides toxiques et organiques gaseux

Publications (1)

Publication Number Publication Date
WO1992006331A1 true WO1992006331A1 (fr) 1992-04-16

Family

ID=21617707

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/SU1990/000229 Ceased WO1992006331A1 (fr) 1990-10-02 1990-10-02 Procede de destruction thermique de composes liquides toxiques et organiques gaseux

Country Status (1)

Country Link
WO (1) WO1992006331A1 (fr)

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2208968A1 (en) * 1972-12-01 1974-06-28 Gallo Pierre Rubbish incinerator without offensive smoke - for organic, halogenated, mineral or metallic materials
DE3128903A1 (de) * 1981-07-22 1983-03-03 L. & C. Steinmüller GmbH, 5270 Gummersbach "verfahren zum eintragen von additiv in einen reaktionsgasstrom"
US4530292A (en) * 1984-04-06 1985-07-23 Tricil Limited Treatment of acidic organic and alkaline inorganic wastes
US4681045A (en) * 1986-07-21 1987-07-21 William F. Cosulich Associates, P.C. Treatment of flue gas containing noxious gases
US4852504A (en) * 1988-06-20 1989-08-01 First Aroostook Corporation Waste fuel incineration system

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2208968A1 (en) * 1972-12-01 1974-06-28 Gallo Pierre Rubbish incinerator without offensive smoke - for organic, halogenated, mineral or metallic materials
DE3128903A1 (de) * 1981-07-22 1983-03-03 L. & C. Steinmüller GmbH, 5270 Gummersbach "verfahren zum eintragen von additiv in einen reaktionsgasstrom"
US4530292A (en) * 1984-04-06 1985-07-23 Tricil Limited Treatment of acidic organic and alkaline inorganic wastes
US4681045A (en) * 1986-07-21 1987-07-21 William F. Cosulich Associates, P.C. Treatment of flue gas containing noxious gases
US4852504A (en) * 1988-06-20 1989-08-01 First Aroostook Corporation Waste fuel incineration system

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