WO1995014562A1 - Procede de retraitement d'enveloppes de pneu use et son equipement de mise en ×uvre - Google Patents

Procede de retraitement d'enveloppes de pneu use et son equipement de mise en ×uvre Download PDF

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Publication number
WO1995014562A1
WO1995014562A1 PCT/BY1994/000003 BY9400003W WO9514562A1 WO 1995014562 A1 WO1995014562 A1 WO 1995014562A1 BY 9400003 W BY9400003 W BY 9400003W WO 9514562 A1 WO9514562 A1 WO 9514562A1
Authority
WO
WIPO (PCT)
Prior art keywords
steam
reactor
reprocessing
gas
cooler
Prior art date
Application number
PCT/BY1994/000003
Other languages
English (en)
Russian (ru)
Inventor
Boris Konstantinovich Muslin
Leonid Mikhailovich VINOGRÁDOV
Vladimir Mikhailovich Drozdov
Anatoly Zhoresovich Grebenkov
Gennady Ivanovich Zhuravsky
Original Assignee
Boris Konstantinovich Muslin
Vinogradov Leonid Mikhailovich
Vladimir Mikhailovich Drozdov
Anatoly Zhoresovich Grebenkov
Gennady Ivanovich Zhuravsky
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 Boris Konstantinovich Muslin, Vinogradov Leonid Mikhailovich, Vladimir Mikhailovich Drozdov, Anatoly Zhoresovich Grebenkov, Gennady Ivanovich Zhuravsky filed Critical Boris Konstantinovich Muslin
Publication of WO1995014562A1 publication Critical patent/WO1995014562A1/fr

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Classifications

    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J3/00—Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
    • C10J3/02—Fixed-bed gasification of lump fuel
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10K—PURIFYING OR MODIFYING THE CHEMICAL COMPOSITION OF COMBUSTIBLE GASES CONTAINING CARBON MONOXIDE
    • C10K1/00—Purifying combustible gases containing carbon monoxide
    • C10K1/04—Purifying combustible gases containing carbon monoxide by cooling to condense non-gaseous materials
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J2300/00—Details of gasification processes
    • C10J2300/09—Details of the feed, e.g. feeding of spent catalyst, inert gas or halogens
    • C10J2300/0913—Carbonaceous raw material
    • C10J2300/0946—Waste, e.g. MSW, tires, glass, tar sand, peat, paper, lignite, oil shale
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J2300/00—Details of gasification processes
    • C10J2300/16—Integration of gasification processes with another plant or parts within the plant
    • C10J2300/1687—Integration of gasification processes with another plant or parts within the plant with steam generation
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J2300/00—Details of gasification processes
    • C10J2300/16—Integration of gasification processes with another plant or parts within the plant
    • C10J2300/1696—Integration of gasification processes with another plant or parts within the plant with phase separation, e.g. after condensation

Definitions

  • Iz ⁇ b ⁇ e ⁇ enie ⁇ n ⁇ si ⁇ sya ⁇ s ⁇ eds ⁇ vam ⁇ e ⁇ e ⁇ ab ⁇ i ⁇ ve ⁇ - dy ⁇ ⁇ d ⁇ v, s ⁇ de ⁇ zhaschi ⁇ ⁇ ezinu and m ⁇ zhe ⁇ by ⁇ is ⁇ lz ⁇ van ⁇ ⁇ eimusches ⁇ venn ⁇ for ⁇ e ⁇ e ⁇ ab ⁇ i izn ⁇ shenny ⁇ av ⁇ m ⁇ bilny ⁇ tires and ⁇ a ⁇ zhe d ⁇ ugi ⁇ s ⁇ de ⁇ zhaschi ⁇ vys ⁇ m ⁇ le ⁇ ulya ⁇ nye uglev ⁇ - d ⁇ dnye s ⁇ edineniya ⁇ myshlenny ⁇ ⁇ d ⁇ v.
  • a known installation contains a reagent, a cooler and a condensate of gas-like products, a separator of a condensate, a device for discharging
  • ⁇ Devices for the implementation of such a process containing a cooler and a condenser for gas discharges, are a separator - 4 - vyg ⁇ uz ⁇ i and ⁇ azdeleniya ⁇ ve ⁇ d ⁇ g ⁇ ⁇ s ⁇ a ⁇ a and ⁇ a ⁇ zhe incinerator chas ⁇ i ⁇ luchaem ⁇ g ⁇ ⁇ i ⁇ i ⁇ lize ene ⁇ ge ⁇ iches ⁇ g ⁇ gas and nag ⁇ eva ⁇ ab ⁇ chey s ⁇ edy ⁇ ea ⁇ a, ⁇ vy ⁇ du of ⁇ azde- li ⁇ elya ⁇ ndensa ⁇ a ⁇ v ⁇ de ⁇ d ⁇ lyuchen ⁇ ladi ⁇ el, ⁇ d ⁇ lyuchen- 5 ny ⁇ g ⁇ eyuschey s ⁇ ne ⁇ vy ⁇ du gaz ⁇ b ⁇ azny ⁇ of ⁇ du ⁇ v
  • Thermal regeneration which is conveniently implemented due to the particularities of the installation scheme, saves energy costs, and especially saves the cost of utilization.
  • the device for unloading unit 3 is installed in the lower part of unit 1 and is equipped with a monitoring system.
  • the unit is equipped with a capacity of 13, which is connected to
  • the sensor 14 has been installed in the process. - 7 -
  • the inventive installation works as follows. 5 Processed, worn-out, automotive flash drives are loaded into the process 1 through the unloading device. C, igniting step 11 and turning on the circulation of the operating body with pump 12. To speed up
  • the heating of the process can be used for an additional heating, for example, the combustion of gas from the system of the boiler or from the other source of heating (non-charge). Due to the use of a steam appliance in the form of a working body, the unloading of a loaded reaction means there is a risk of
  • Hydrocarbons are sold in tank 13 and sent to the user or for further processing. If you need to be in the dividend separator 6, you may have organized a separate sale of carbohydrates, as well as doing so at a time. From the separator 6 separator, with the help of pump 12, it will return to the control unit for the transfer of the steam. 4 The 4-water cooler is supplied with food and cigarettes, and in the setting of 10, the appliance is restarted at a predetermined temperature of 400 ... 700 degrees. C. After 2 ...
  • EXAMPLE 1 REACT 1 through an LOADING device 2 LOAD the worn out bulk in a quantity of 1000 kg.
  • the pressure of the steam in process 1 is controlled by the indications of the pressure gauge (maintains a pressure of 10 5 Pa). There is a good condition for steam, which is necessary to go to process 1, so that you can get 1000 kg of food to start working,
  • the transmitter is in operation 1 of which controls the indications of sensor 14.
  • Gaseous products mixed with water are condensed in a condensate 5.
  • the claimed method is distinguished by the relatively best technological processes, environmental protection. Operating costs per unit réelle--35 processed raw materials are exchanged than in known processes. - eleven -
  • the inventive installation can be created on the available in the industrial technological base.
  • the equipment is commercially available with the most modern specialized installations, including the installation, Consequently- Consequently- Consequently- Consequently- Consequently- Consequently- Consequently- ⁇ ⁇ ⁇ ⁇ ⁇ ⁇ till ⁇ tillley kmangex

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Combustion & Propulsion (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)

Abstract

L'invention concerne des moyens de retraitement de déchets industriels solides contenant du caoutchouc, et notamment de retraitement de pneus usés d'automobiles. Afin de réduire l'impact du retraitement des déchets sur l'environnement, et d'en améliorer l'efficacité, on charge des enveloppes de pneus usés d'automobiles dans un réacteur (1) par un dispositif de chargement (2). Le réacteur (1) est chauffé à la température voulue comprise entre 400 et 700 °C, les jets (11) étant allumés et une pompe (12) faisant démarrer le flux de circulation autour de la pièce à traiter. Une fois que la température dans le réacteur (1) a atteint 400 °C, les composés de masse moléculaire élevée subissent une conversion par l'élimination des hydrocarbures volatils lesquels, avec la vapeur, pénètrent dans le refroidisseur (4). Lorsqu'il quitte le refroidisseur le mélange de vapeur et de gaz pénètre dans le condenseur (5) où les fractions de vapeur et d'hydrocarbures lourds se condensent. Le liquide se stabilise et se sépare en couches dans le séparateur (6) de condensat. Le mélange gazeux est reconduit dans le système en partie jusqu'à un dispositif consommateur, et en partie vers les jets (11). Une fois le liquide stabilisé en couches, il est évacué du séparateur (6) de condensat. Les hydrocarbures pénètrent dans une cuve (13) et sont dirigés vers un dispositif consommateur ou envoyés pour retraitement. L'eau provenant du séparateur (6) de condensat est réintroduite dans le circuit par une pompe (12) afin de produire une vapeur surchauffée. L'eau est chauffée et bout dans le refroidisseur (4) des gaz produits dans la pyrolyse, la vapeur résultante est surchauffée dans l'unité (10) jusqu'à une température voulue comprise entre 400 et 700 °C. Un résidu solide reste dans le réacteur (1) sous la forme d'un cordon de métal et de pyrocarbone poreux. Le réacteur est refroidi et dépressurisé à l'aide du dispositif de déchargement (3). Les résidus solides sont transportés par un convoyeur (8) jusqu'à un séparateur magnétique (7) séparant les impuretés métalliques. Le pyrocarbone fini pénètre dans la trémie de réception (9).
PCT/BY1994/000003 1993-11-25 1994-11-24 Procede de retraitement d'enveloppes de pneu use et son equipement de mise en ×uvre WO1995014562A1 (fr)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
BY01018-01 1993-11-25
BY1018 1993-11-25

Publications (1)

Publication Number Publication Date
WO1995014562A1 true WO1995014562A1 (fr) 1995-06-01

Family

ID=4083644

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/BY1994/000003 WO1995014562A1 (fr) 1993-11-25 1994-11-24 Procede de retraitement d'enveloppes de pneu use et son equipement de mise en ×uvre

Country Status (1)

Country Link
WO (1) WO1995014562A1 (fr)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2002038350A1 (fr) * 2000-11-09 2002-05-16 Dmitry Viktorovich Aristarkhov Procede de transformation de dechets de caoutchouc
WO2005102639A1 (fr) 2004-04-26 2005-11-03 Krivoruchko, Evgeny Petrovich Procede de retraitement thermique de pneus uses et dispositif correspondant
WO2006123970A2 (fr) * 2005-05-19 2006-11-23 Aleksey Viktorovich Matveev Procede de transformation de dechets caoutchoutes ou d'un melange de dechets caoutchoutes et polymeres et installation de mise en oeuvre du procede
WO2008030137A1 (fr) * 2007-01-10 2008-03-13 Konstanta, Obschestvo S Ogranichennoy Otvetstvennostyu Procédé et dispositif de traitement de déchets de caoutchouc
WO2015087235A1 (fr) * 2013-12-09 2015-06-18 Kassel Harry Dean Recyclage de matériaux contenant des hydrocarbures

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2255165A1 (fr) * 1973-12-24 1975-07-18 Fuji Kasui Eng Co Ltd
DE3244130A1 (de) * 1982-03-05 1983-09-15 SAVA KRANJ, industrija gumijevih, usnjenih in kemičnih izdelkov n.o.sol.o., 64000 Kranj Verfahren zur kontinuierlichen verarbeitung von grob granuliertem altgummi zu einem sekundaeren gummirohstoff
SU1698074A1 (ru) * 1989-05-05 1991-12-15 Харьковское специальное конструкторско-технологическое бюро "Машприборпластик" Способ переработки отходов термопластов
SU1763210A1 (ru) * 1990-09-10 1992-09-23 Институт Химии Дальневосточного Отделения Ан Ссср Установка дл переработки политетрафторэтилена

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2255165A1 (fr) * 1973-12-24 1975-07-18 Fuji Kasui Eng Co Ltd
DE3244130A1 (de) * 1982-03-05 1983-09-15 SAVA KRANJ, industrija gumijevih, usnjenih in kemičnih izdelkov n.o.sol.o., 64000 Kranj Verfahren zur kontinuierlichen verarbeitung von grob granuliertem altgummi zu einem sekundaeren gummirohstoff
SU1698074A1 (ru) * 1989-05-05 1991-12-15 Харьковское специальное конструкторско-технологическое бюро "Машприборпластик" Способ переработки отходов термопластов
SU1763210A1 (ru) * 1990-09-10 1992-09-23 Институт Химии Дальневосточного Отделения Ан Ссср Установка дл переработки политетрафторэтилена

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2002038350A1 (fr) * 2000-11-09 2002-05-16 Dmitry Viktorovich Aristarkhov Procede de transformation de dechets de caoutchouc
WO2005102639A1 (fr) 2004-04-26 2005-11-03 Krivoruchko, Evgeny Petrovich Procede de retraitement thermique de pneus uses et dispositif correspondant
EP1785248A1 (fr) * 2004-04-26 2007-05-16 Krivoruchko, Evgeny Petrovich Procede de retraitement thermique de pneus uses et dispositif correspondant
EP1785248A4 (fr) * 2004-04-26 2007-10-24 Krivoruchko Evgeny Petrovich Procede de retraitement thermique de pneus uses et dispositif correspondant
WO2006123970A2 (fr) * 2005-05-19 2006-11-23 Aleksey Viktorovich Matveev Procede de transformation de dechets caoutchoutes ou d'un melange de dechets caoutchoutes et polymeres et installation de mise en oeuvre du procede
WO2006123970A3 (fr) * 2005-05-19 2007-01-18 Aleksey Viktorovich Matveev Procede de transformation de dechets caoutchoutes ou d'un melange de dechets caoutchoutes et polymeres et installation de mise en oeuvre du procede
WO2008030137A1 (fr) * 2007-01-10 2008-03-13 Konstanta, Obschestvo S Ogranichennoy Otvetstvennostyu Procédé et dispositif de traitement de déchets de caoutchouc
WO2015087235A1 (fr) * 2013-12-09 2015-06-18 Kassel Harry Dean Recyclage de matériaux contenant des hydrocarbures

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