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WO2008002186A1 - Installation de retraitement de déchets combustibles solides - Google Patents

Installation de retraitement de déchets combustibles solides Download PDF

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Publication number
WO2008002186A1
WO2008002186A1 PCT/RU2007/000201 RU2007000201W WO2008002186A1 WO 2008002186 A1 WO2008002186 A1 WO 2008002186A1 RU 2007000201 W RU2007000201 W RU 2007000201W WO 2008002186 A1 WO2008002186 A1 WO 2008002186A1
Authority
WO
WIPO (PCT)
Prior art keywords
pyrolysis
chamber
pipe
reactor
pyrolysis chamber
Prior art date
Application number
PCT/RU2007/000201
Other languages
English (en)
Russian (ru)
Inventor
Boris Nikolaevich Ulko
Dmitry Semenovich Strebkov
Farit Salikhovich Burganov
Original Assignee
Boris Nikolaevich Ulko
Strebkov Dmitrij S
Farit Salikhovich Burganov
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 Nikolaevich Ulko, Strebkov Dmitrij S, Farit Salikhovich Burganov filed Critical Boris Nikolaevich Ulko
Publication of WO2008002186A1 publication Critical patent/WO2008002186A1/fr

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Classifications

    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
    • F23G5/02—Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment
    • F23G5/027—Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment pyrolising or gasifying stage
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
    • C10B47/00—Destructive distillation of solid carbonaceous materials with indirect heating, e.g. by external combustion
    • C10B47/02—Destructive distillation of solid carbonaceous materials with indirect heating, e.g. by external combustion with stationary charge
    • C10B47/16—Destructive distillation of solid carbonaceous materials with indirect heating, e.g. by external combustion with stationary charge with indirect heating means both inside and outside the retorts
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
    • C10B49/00—Destructive distillation of solid carbonaceous materials by direct heating with heat-carrying agents including the partial combustion of the solid material to be treated
    • C10B49/02—Destructive distillation of solid carbonaceous materials by direct heating with heat-carrying agents including the partial combustion of the solid material to be treated with hot gases or vapours, e.g. hot gases obtained by partial combustion of the charge
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
    • C10B53/00—Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
    • C10B57/00—Other carbonising or coking processes; Features of destructive distillation processes in general
    • C10B57/02—Multi-step carbonising or coking processes
    • 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
    • C10G1/00—Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal
    • C10G1/06—Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal by destructive hydrogenation
    • 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
    • C10G1/00—Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal
    • C10G1/10—Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal from rubber or rubber waste
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
    • F23G5/08—Incineration of waste; Incinerator constructions; Details, accessories or control therefor having supplementary heating
    • F23G5/12—Incineration of waste; Incinerator constructions; Details, accessories or control therefor having supplementary heating using gaseous or liquid fuel
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
    • F23G5/24—Incineration of waste; Incinerator constructions; Details, accessories or control therefor having a vertical, substantially cylindrical, combustion chamber
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
    • F23G5/44—Details; Accessories
    • F23G5/46—Recuperation of heat
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23C—METHODS OR APPARATUS FOR COMBUSTION USING FLUID FUEL OR SOLID FUEL SUSPENDED IN  A CARRIER GAS OR AIR 
    • F23C2900/00—Special features of, or arrangements for combustion apparatus using fluid fuels or solid fuels suspended in air; Combustion processes therefor
    • F23C2900/9901—Combustion process using hydrogen, hydrogen peroxide water or brown gas as fuel
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G2201/00—Pretreatment
    • F23G2201/30—Pyrolysing
    • F23G2201/301—Treating pyrogases
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G2201/00—Pretreatment
    • F23G2201/30—Pyrolysing
    • F23G2201/302—Treating pyrosolids
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G2201/00—Pretreatment
    • F23G2201/70—Blending
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G2900/00—Special features of, or arrangements for incinerators
    • F23G2900/50001—Combination of two or more furnaces
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00—Technologies for the production of fuel of non-fossil origin
    • Y02E50/30—Fuel from waste, e.g. synthetic alcohol or diesel

Definitions

  • the invention relates to the field of processing of combustible solid household and industrial waste, including polyethylene, plastics, food waste, fabrics, dry biomass, woodworking waste, sawdust, bark, etc., with obtaining diesel fuel, gasoline as final products, synthesis gas.
  • a device for processing solid waste is known [RF Patent N 2076272], containing a horizontally located housing, means for supplying raw materials and unloading coke residue, a heating chamber located on the outside of the housing with a furnace (high-temperature reactor) and means for supplying and burning fuel, air and output combustion products.
  • the installation is equipped with different-sized movable jumpers attached to the upper wall of the housing, dividing its internal volume into zones of drying, pyrolysis and afterburning.
  • the upper part of the afterburning zone is connected by an external channel to the lower part of the pyrolysis zone, the upper part of the pyrolysis zone is connected by an external channel to the lower part of the drying zone, and the upper part of the drying zone is connected by an external channel to the furnace.
  • the disadvantage of this device is that with the heterogeneity of the feedstock received for processing, there are significant fluctuations in the quantity and calorific value of gaseous products released during pyrolysis and then transferred to the furnace of the device. And since the thermal potential of products burned in the furnace, then transferred by flue gases to the pyrolysis zone through the wall of the device, is the source of the bulk of the thermal energy necessary for of the pyrolysis process, either the process attenuates at too low calorie content of the raw material, or, on the contrary, its excessive intensification at high calorific value, leading to uncontrolled "acceleration" of the process and an unaccounted temperature increase, which may result in structural failure.
  • a device for processing solid waste was selected [RF Patent Ns 2132997], containing a horizontal body, means for feeding waste (auger) and unloading coke residue.
  • a heating chamber connected to a high-temperature reactor with means for supplying and burning fuel and pyrolysis gas, air supply and output of combustion products.
  • the walls of the casing from the side of the heating chamber are equipped with movable partitions, the axis of rotation of which are perpendicular to the longitudinal axis of the casing, and their width is equal to or less than the gap between the walls of the casing and the heating chamber.
  • the distance between the axis of rotation of two adjacent partitions is equal to or less than their width.
  • Partitions are equipped with bimetallic rotary devices.
  • the flue gases generated in the furnace during fuel combustion pass through the heating chamber and the processed waste located in the housing is heated through the walls of the furnace.
  • the raw material is first dried, and then, as it warms up, it is pyrolyzed. Pyrolysis occurs in the presence of air, which is supplied by means of a special tool. Gaseous decomposition products enter a high-temperature reactor, replacing part of the fuel.
  • the position of the partitions is determined by the temperature inside the case. At low temperatures, partitions partially overlap the internal volume of the casing, forming labyrinth passages for the movement of pyrosynthesis gas, which is directed in countercurrent to the supplied raw materials.
  • the partitions occupy a position that does not impede the direct passage of gas through the internal volume of the chambers.
  • the main disadvantage of the prototype is that the resulting pyrosynthesis is used only for own needs to ensure the combustion process in the furnace. At the output of the device receive flue gases and coke and slag residue.
  • the basis of the invention is the task of ensuring the processing of combustible waste to produce marketable products - hydrocarbons, namely gasoline, diesel fuel, combustible gases, as well as solid carbon-containing fractions (carbon black, coke and slag residue).
  • the problem is solved by changing the design of the installation.
  • the plant for processing solid combustible waste includes a high-temperature reactor connected to a pyrolysis reactor.
  • the installation differs from the prototype in that the pyrolysis reactor is vertically oriented and has two coaxially located pyrolysis chambers. Both cameras are equipped with mixing devices.
  • the first pyrolysis chamber has an outer and inner coaxially located body with a slotted annular channel between them, which is a heating chamber and connected to a high-temperature reactor. The exit of the slotted annular channel is located inside the second pyrolysis chamber.
  • the first pyrolysis chamber in the bottom has a hopper with a lock chamber for collecting and withdrawing coke residue.
  • the first pyrolysis chamber In the upper part of the first pyrolysis chamber there is a pipe for supplying raw materials and a pipe for exiting the pyrolysis products, equipped with a shut-off valve. In the axial zone of the first pyrolysis chamber is located at least one longitudinally oriented pipe, the entrance of which is located in the bottom of the heating chamber. The outlet of the pipe is equipped with a fine atomizer and is located in the bottom of the second pyrolysis chamber. In the upper part of the second pyrolysis chamber there is a pipe for supplying sorted raw materials and a pipe for the output of pyrolysis products. In the bottom of the second pyrolysis chamber there is a hopper for withdrawing the coke residue.
  • Installation for processing solid combustible waste contains a high-temperature reactor 1, which is connected by a pipe 2 to the pyrolysis reactor.
  • the pyrolysis reactor consists of two coaxially located pyrolysis chambers, with a common vertically oriented cylindrical water-cooled casing (not shown in the Figure). In one installation, two pyrolysis reactors can be connected to one high-temperature reactor.
  • the first chamber 3 of the pyrolysis reactor has an outer casing 4 and an inner casing 5 coaxial to it (construction “glass in glass”). Between the housings 4, 5 there is a slotted annular cylindrical channel 6, which is a heating chamber of the first pyrolysis chamber and is connected by a pipe 2 to a high-temperature reactor 1.
  • a mixing device is located inside the first pyrolysis chamber 3 (the device itself is not shown, but its drive 7 is shown) .
  • a hopper 8 for collecting and withdrawing coke residue, equipped with a lock chamber.
  • a pipe 9 for supplying processed raw materials and a pipe 10 for outputting gaseous pyrolysis products.
  • the pipe 10 is equipped with an adjustable shut-off valve (not shown in the Figure).
  • a continuation of the housing 4 of the first chamber is the housing 11 of the second pyrolysis chamber 12, and the slotted annular channel 6 extends into the second pyrolysis chamber 13 into its bottom part.
  • a longitudinally oriented pipe 13 is placed along the axis or in the axial region of the first pyrolysis chamber 3. Its inlet is located at the bottom of the heating chamber and, thus, it is connected to the high-temperature reactor 1.
  • the outlet of the pipe 13 is equipped with a fine spray 14 and is located in the bottom of the second chamber 12palysis.
  • In the first chamber 3 pyrolysis can several longitudinally oriented pipes should be placed, just like the pipe 13.
  • the second pyrolysis chamber 12 like the first, is equipped with a mixing device (the device itself is not shown in the Figure, but its drive 15 is shown) and a hopper 16 for collecting and removing the coke residue.
  • a mixing device the device itself is not shown in the Figure, but its drive 15 is shown
  • a hopper 16 for collecting and removing the coke residue.
  • a pipe 17 for supplying sorted processed raw materials (solid combustible waste) and a pipe 18 for outputting the pyrolysis products.
  • a combustible mixture consisting mainly of combustible gas (methane) and air with an excess of fuel (oxygen excess coefficient is cH), 5-0.6) is fed to a high-temperature reactor 1, where at a temperature of 1400-1600 0 C combustion is carried out with the formation of a working fluid consisting of a mixture of gases: CO, CO 2 , H 2, N 2; and other gases.
  • the heated gases through the pipe 2 enter the slotted annular channel 6 between the walls of the first pyrolysis chamber, which is the heating chamber. At the same time, the heated gas stream rushes into the pipe 13.
  • the internal volume of the first pyrolysis chamber is uniformly heated by radial counter flows: from the walls to the longitudinal axis and from the axial pipe 13 to the walls.
  • Metals, stones, glass, dry plaster, sand, clay, etc. are preliminarily separated from solid waste, leaving combustible household waste intended for processing in the first pyrolysis chamber 3.
  • the purified raw materials are ground. The load goes from above through the nozzle 9. When strewn, the raw material falls on the blades of the mixing device and is further loosened and crushed.
  • the temperature inside the first chamber 3 of pyrolysis reaches 400 ° - 500 0 C, and the pressure is 0.1-2.0 MPa, and is determined by the adjustment of the shut-off valve.
  • the first pyrolysis chamber 3 high-speed heating of combustible raw materials occurs, accompanied by the destruction of high molecular weight components of the raw materials.
  • the resulting gaseous pyrolysis products when the specified pressure is reached in the chamber are discharged through the pipe 10, because its shut-off valve is triggered. Further processing of the obtained gas phase of the pyrolysis products is carried out by traditional methods and is not the subject of the present invention.
  • the solid coke-ash residues formed are poured into the hopper 8 and removed from it as they accumulate. In this case, the raw materials continue to be fed to the first chamber 3 for processing continuously.
  • the increased pressure created in the chamber 3 accelerates the dry pyrolysis process, improves the heat exchange between the walls of the reactor and the raw material, as well as within the volume of the raw material itself, since the mass density increases per unit volume.
  • the pyrolysis process is accelerated and improved, the process of intensification of the pyrolysis of the feedstock occurs, which improves the quality of the liquid fraction of diesel fuel.
  • the pyrolysis process occurs without contact with the working fluid.
  • pyrolysis of the sorted raw material takes place, which is supplied from the upper pipe 17. When strewn, the raw material falls onto the blades of the mixing device and is further loosened and crushed.
  • the raw materials in the second chamber use polyethylene waste and wood waste (eg sawdust), while the amount of wood waste is at least 30%.
  • the pyrolysis process occurs in the presence of hydrogen, which is present in the working fluid coming from a finely dispersed atomizer 14 and a slotted annular gap 6.
  • gasoline and diesel fuel are formed up to 80% of the mass of processed raw materials and up to 11% of pyrolysis gas the rest is carbon black (carbon black).
  • the raw materials in the second chamber 12 is fed continuously and the pyrolysis process is continuous.
  • the temperature in the second chamber 12 is slightly lower - 390-430 0 C.
  • the heating and supply of the products of the high-temperature reactor is carried out by annular blasting from the bottom along the chamber walls (from the annular slot gap of the first chamber), and also introduced by blasting from the atomizer 14 at the end of the pipe 13.
  • pyrolysis occurs intensive movement of raw materials, both due to mechanical mixing, and due to the impact of turbulent gas flows. Pyrolysis occurs in a fluidized bed. Gaseous pyrolysis products from the second chamber
  • test results are summarized in tables.
  • the temperature in the pyrolysis chamber is 400 0 C, the pressure is atmospheric, and there is no working fluid (hydrogen) in the chamber.
  • the temperature in the chamber is 400 0 C, the pressure is atmospheric, and there is no working fluid (hydrogen) in the chamber.
  • the temperature in the chamber is 450 ° C, the pressure is atmospheric, and there is no working fluid (hydrogen) in the chamber.
  • the temperature in the second chamber is 360 0 C, the pressure is 0.2 MPa.
  • the pyrolysis process was similar in contact with the working fluid, i.e. in the presence of hydrogen.
  • the pyrolysis process was similar in contact with the working fluid, i.e. in the presence of hydrogen.
  • the two-chamber design of the pyrolysis reactor allows the processing of solid household and industrial waste with various physicochemical characteristics.
  • the output is marketable products - hydrocarbons, namely, gasoline, diesel fuel, combustible gases, and solid carbon fractions
  • Kaliningrad in which out of 1000 tons of the daily waste rate, 10% is wood waste and polyethylene waste. From this amount of solid combustible waste, you can get 80 tons of high-quality gasoline and diesel fuel.

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Organic Chemistry (AREA)
  • Materials Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Combustion & Propulsion (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Wood Science & Technology (AREA)
  • Processing Of Solid Wastes (AREA)

Abstract

L'invention appartient au domaine du retraitement de déchets combustibles. Le mélange combustible, constitué principalement d'un gaz combustible et d'air, est injecté dans un réacteur à haute température (1) dans lequel s'effectuent la combustion et la formation d'un fluide de travail. Les gaz chauffé sont acheminés via une canalisation (2) dans un canal annulaire à fente (6) disposé entre les parois d'une première chambre de pyrolyse et fonctionnant comme une chambre de chauffage. Simultanément, le flux de gaz chauffé se dirige dans un tuyau (13) tout en réchauffant le volume interne de la première chambre de pyrolyse (3). Les produits gazeux de pyrolyse, qui se forment pendant ce processus, sont évacués via une tubulure (10), et les résidus solides sont acheminés dans une trémie (8). Simultanément, une pyrolyse des matières premières triées, acheminée depuis la tubulure supérieure (17), se produit dans une deuxième chambre (12). Les matières premières tombent sur les pales d'un mélangeur. Le processus de pyrolyse s'effectue en absence d'hydrogène présent dans le fluide de travail, qui provient d'un atomiseur à dispersion fine (14) et d'un intervalle annulaire à fente (6). Les produits gazeux de pyrolyse sont évacués d'une deuxième chambre (12) via une tubulure (18), et les résidus solides sont évacués via une trémie (16). L'invention permet de retraiter des déchets industriels possédant des caractéristiques physico-chimiques différentes.
PCT/RU2007/000201 2006-06-28 2007-04-24 Installation de retraitement de déchets combustibles solides WO2008002186A1 (fr)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
RU2006123042/03A RU2316696C1 (ru) 2006-06-28 2006-06-28 Установка для переработки горючих твердых отходов
RU2006123042 2006-06-28

Publications (1)

Publication Number Publication Date
WO2008002186A1 true WO2008002186A1 (fr) 2008-01-03

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RU (1) RU2316696C1 (fr)
WO (1) WO2008002186A1 (fr)

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CN107062257A (zh) * 2017-01-13 2017-08-18 安徽未名鼎和环保有限公司 一种双调节式垃圾高效处理系统
WO2018227949A1 (fr) * 2017-06-14 2018-12-20 上海王甘环保科技集团有限公司 Chaudière mère-enfant de gazéification pour la cokéfaction, la production d'acier, la coulée et la production d'énergie
US10636724B2 (en) 2017-05-09 2020-04-28 Panasonic Intellectual Property Management Co., Lttd. Mount structure

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CN106765147A (zh) * 2017-01-13 2017-05-31 安徽未名鼎和环保有限公司 一种稳定高效的垃圾处理系统

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RU23875U1 (ru) * 2002-02-12 2002-07-20 Общество с ограниченной ответственностью "Промышленные реакторы" Реактор для переработки углеводородного сырья

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RU2098718C1 (ru) * 1994-12-22 1997-12-10 Акционерное общество закрытого типа "НОВЕК" Устройство для сжигания горючих веществ с твердыми компонентами
RU2132997C1 (ru) * 1998-05-29 1999-07-10 Двоскин Григорий Исакович Устройство для переработки твердых отходов
JP2000329327A (ja) * 1999-05-19 2000-11-30 Hiroshi Kuwajima 焼却炉
RU23875U1 (ru) * 2002-02-12 2002-07-20 Общество с ограниченной ответственностью "Промышленные реакторы" Реактор для переработки углеводородного сырья

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WO2018227948A1 (fr) * 2017-06-14 2018-12-20 上海王甘环保科技集团有限公司 Chaudière mère-enfant de gazéification pour production d'énergie, alimentée au charbon, destinée à être utilisée dans un porte-avions à roues géantes

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