EP2700875B1 - Procédé pour le traitement thermique de matériaux de démolition routiers contenant du PAK ou de boues pétrolières - Google Patents

Procédé pour le traitement thermique de matériaux de démolition routiers contenant du PAK ou de boues pétrolières Download PDF

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Publication number
EP2700875B1
EP2700875B1 EP13003705.4A EP13003705A EP2700875B1 EP 2700875 B1 EP2700875 B1 EP 2700875B1 EP 13003705 A EP13003705 A EP 13003705A EP 2700875 B1 EP2700875 B1 EP 2700875B1
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EP
European Patent Office
Prior art keywords
modules
fed
flue gases
burning device
rotary tube
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.)
Active
Application number
EP13003705.4A
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German (de)
English (en)
Other versions
EP2700875A1 (fr
Inventor
Uwe Neumann
Robert Leicht
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.)
Eisenmann SE
Original Assignee
Eisenmann SE
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Publication date
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Priority to PL13003705T priority Critical patent/PL2700875T3/pl
Publication of EP2700875A1 publication Critical patent/EP2700875A1/fr
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Publication of EP2700875B1 publication Critical patent/EP2700875B1/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
    • F23G5/20—Incineration of waste; Incinerator constructions; Details, accessories or control therefor having rotating or oscillating drums
    • 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
    • F23G5/14—Incineration of waste; Incinerator constructions; Details, accessories or control therefor having supplementary heating including secondary combustion
    • F23G5/16—Incineration of waste; Incinerator constructions; Details, accessories or control therefor having supplementary heating including secondary combustion in a separate 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
    • F23G5/40—Portable or mobile incinerators
    • 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
    • F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G2203/00—Furnace arrangements
    • F23G2203/60—Mobile furnace
    • F23G2203/601—Mobile furnace carried by a vehicle
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G2203/00—Furnace arrangements
    • F23G2203/70—Modular furnace
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G2209/00—Specific waste
    • F23G2209/12—Sludge, slurries or mixtures of liquids
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G2209/00—Specific waste
    • F23G2209/24—Contaminated soil; foundry sand

Definitions

  • the invention relates to a method according to claim 1.
  • a plant of the type mentioned, with which this required treatment can take place, is in the DE 10 2009 025 361 B4 described. This plant is stationarily positioned near an asphalt mixing plant. Thus, in Germany z. For example, each one central system a federal state as a catchment area. For treatment, the PAK-containing road-breaking material from the entire catchment area is transported to the stationary facility. This leads to a high transport wall. To set up the known system, a foundation is needed, which makes costly changes to the installation as well as a finally required dismantling of the plant.
  • Oil sludge can basically be disposed of by essentially identical procedures. With regard to their seizure and especially the location of the seizure, they may have similar problems as described above for road-breaking material. This is the case, for example, when an oil pipeline breaks.
  • Object of the present invention is to provide a system of the type mentioned in such a way that the costs associated with their creation, operation and possibly demolition costs are reduced.
  • the logistics structure is compared with the prior art vice versa: While in the latter the roadside material or oil sludge is transported to the stationary, central processing plant, according to the invention, the treatment plant moves to the place of Eduktanfalls.
  • the inventive concept of the mobile plant in comparison to a stationary system has a significant potential savings in the field of transport volumes and thus the transport costs.
  • the installation, changes in the installation and disassembly of the system according to the invention require a maximum of the use of a crane.
  • the mobile system can be converted quickly, if this z. B. is required for reasons of space. It can also be operated at temporarily assigned locations and can be removed after the execution of the process task with little effort.
  • the modules used according to the invention can be replaced variably and quickly in the event of changes in the process control or modernization measures.
  • the invention is characterized in that it additionally has a module, in which the components required for the supply of the other modules, in particular a generator, tanks for operating media such as water, gas, compressed air, fuel are summarized. While the construction of a stationary plant is not possible at every location, since a basic infrastructure with respect to the supply streams is a prerequisite, in this preferred embodiment of the invention, the mobile plant can be operated at any construction site, as they are with respect to the supply of the corresponding energy sources and media self-sufficient. This provides a high degree of availability and security for the plant operator.
  • At least a part of the modules are connected to each other via shape-changing tubes or hoses. This facilitates the repositioning of the modules, if this is necessary, for example, in the further movement or the change of a construction site for reasons of space.
  • a flue gas cooler is advantageously arranged to protect the filter.
  • FIG. 1 The plant shown here and designated overall by the reference numeral 1 is intended for mobile use at various construction sites, to which it can be transported by means of low-loaders on roads.
  • Appendix 1 includes all the essential components necessary to carry out the above mentioned DE 10 2009 025 361 B4 described method are determined. Because of the functioning of the installed system, reference is made to this document, unless otherwise stated below. These components are divided into four modules 2, 3, 4, 5, which are supported by trailers 6, 7, 8, 9. The trailer 6, 7, 8, 9 with the components constructed thereon can be connected in a known manner with a tractor for transport.
  • modules 2, 3, 4, 5 depends on the size of the system; In general, four modules 2, 3, 4, 5 are adequate as shown. For systems with smaller or larger capacity, fewer or more modules can be used.
  • a filling container 10 is constructed, the automatically or manually supplied PAH-containing material that in FIG. 1 is shown schematically and provided with the reference numeral 11.
  • the filling container 10 represents a feeding station in the terminology of the claims.
  • the PAH-containing material enters a rotary kiln 13, where it is thermally processed in a known manner.
  • the trailer 7 of the second module 3 carries a cyclone 16, via a flexible pipe or hose connection 17, the flue gases from the rotary kiln 13 of the first module 2 are supplied.
  • the cyclone 16 is in FIG. 1 presented in his working position, in which he has a considerable height. It can be folded for transport about an axis 18 in an approximately horizontal position.
  • the freed from residual solids in the cyclone 16 flue gases are supplied via a pipe 19 to a Nachbrenn driven 20, in which any remaining unwanted organic components are burned. If necessary, the afterburner 20, similar to the cyclone 16, can be folded down when this is necessary for transport.
  • the corresponding axis is not shown in FIG.
  • a flue gas cooler 21 is constructed, to which the hot flue gases are supplied via a flexible tube or hose connection 22, which leave the afterburner 20 of the second module 3.
  • the flue gases are produced by injecting water or with help a heat exchanger is cooled to a suitable low temperature and then via a line 23 of a filter device, in the illustrated embodiment, a fabric filter 24, respectively.
  • the latter is also located on the trailer 8 of the third module 4.
  • a suction fan 25 on the trailer 8 finally pulls the cooled flue gases from the fabric filter 24 and sets the entire flow upstream system components under negative pressure.
  • the extracted from the suction fan 25 flue gases which are now cleaned according to the requirements of the 17th BimSchV a (public regulation in Germany), can be discharged through a chimney 26 in the outside atmosphere.
  • the third module 5 of the system 1 comprises, supported by its trailer 9, all those components which are required to supply the process-active components on the three modules 2, 3, 4. This is especially true for components that are required for power, such as a generator 27, which is essential in particular at construction sites that are far away from the public power supply. Of course, in addition a connection option for the network can be present. Other tanks 27, 28, 29, 30 contain auxiliary media, such as. As air, gas, water or diesel fuel.
  • FIG. 1 shown plant 1 with the help of four, each a module 2, 3, 4, 5 carrying low loaders spent at the site.
  • each a module 2, 3, 4, 5 carrying low loaders spent at the site.
  • the various modules 2, 3, 4, 5 are then placed on site, the arrangement largely taking place in accordance with the available spatial conditions.
  • the system 1 is made ready by the various compounds, in particular the flexible pipe or hose connections 17, 22 and the electrical connections are made. Then, the operation can begin in principle the same way as in the DE 10 2009 025 361 B4 is described.
  • One difference, however, is that it dispenses with the generation of heat from the resulting flue gases and instead the flue gases are cooled while losing the corresponding heat. This is simply due to the fact that there are generally no customers for this heat on site at the construction site.
  • the heat stuck in the flue gases of the rotary kiln 13 and / or the afterburner 20 may be used to preheat the oxidizing air. This can be done for example with the aid of the flue gas cooler 21, the fresh air for this purpose air is supplied, which is supplied after heating with cooling of the flue gases to the rotary kiln 13 and / or the post-combustion device 20.
  • the mobile plant 1 can follow this site, so that the transport routes are always very short.
  • FIG. 2 is a plant for the thermal treatment of PAH-containing roadbreak shown, the only difference is that it is not intended for the exclusive road transport on low loaders but possibly also for transport by train or ship or other trucks.
  • the trailer 6, 7, 8 are replaced by platforms 106, 107, 108, which are each on four legs and which may also be accommodated in containers.
  • the plant corresponds to the FIG. 2 in the function and structure of the individual modules and the connections between them and those of Annex 1 of the FIG. 1 , Corresponding parts are therefore in FIG. 2 denoted by the same reference numeral plus 100.

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Processing Of Solid Wastes (AREA)
  • Treatment Of Sludge (AREA)
  • Muffle Furnaces And Rotary Kilns (AREA)
  • Waste-Gas Treatment And Other Accessory Devices For Furnaces (AREA)

Claims (4)

  1. Procédé de fonctionnement d'une installation de traitement thermique de matériau de démolition routier contenant des HAP ou de boues d'hydrocarbures, laquelle installation présente les composants suivants :
    a) une station d'alimentation (10; 110) de matériau de démolition routier préalablement broyé ou de boues d'hydrocarbures (11 ; 111) ;
    b) un four tubulaire rotatif (13 ; 113) dans lequel le matériau de démolition routier (11 ; 111) ou les boues d'hydrocarbures sont brûlés avec apport d'air d'oxydation ;
    c) un séparateur de poussières (16 ; 116) auquel sont amenés les gaz de fumée qui sont produits dans le four tubulaire rotatif (13 ; 113) ;
    d) un dispositif de post-combustion (20 ; 120) auquel sont amenés les gaz de fumée qui quittent le séparateur de poussières (16 ; 116) ;
    e) un dispositif de filtrage (24 ; 124) auquel sont amenés les gaz de fumée provenant du dispositif de post-combustion (20 ; 120) ;
    caractérisé en ce que
    f) les composants de l'installation (10, 13, 16, 20, 24 ; 110, 113, 116, 120, 124) selon les caractéristiques a) à e) sont répartis entre une pluralité de modules (2, 3, 4; 102, 103, 104) qui présentent tous un poids et des dimensions qui leur permettent d'être transportés individuellement sur des remorques surbaissées ou des camions ;
    g) les modules (2, 3, 4 ; 102, 102, 104) sont installés à proximité géographique du lieu de production du matériau de démolition routier contenant des HAP ou des boues d'hydrocarbures ;
    h) les modules (2, 3, 4 ; 102, 103, 104) sont reliés entre eux au moins en partie au moyen de tubes ou tuyaux de forme variable (17, 22 ; 117, 122) ;
    i) une fois l'activité terminée, les modules (2, 3, 4 ; 102, 103, 104) sont séparés les uns des autres à un premier lieu de production et transportés vers un prochain lieu de production ;
    k) un module supplémentaire (5 ; 105) étant utilisé, dans lequel sont regroupés les composants nécessaires à l'alimentation des autres modules (2, 3, 4 ; 102, 103, 104), à savoir un groupe électrogène (27 ; 127), des réservoirs (28, 29, 30, 31 ; 128, 129, 130, 131) pour des fluides de service tels que eau, gaz, air comprimé, carburant.
  2. Procédé selon la revendication 1, caractérisé en ce que les composants de l'installation (10, 13, 16, 20, 24; 110, 113, 116, 120, 124) selon les caractéristiques a) à e) sont répartis entre quatre modules (2, 3, 4, 5 ; 102, 103, 104, 105).
  3. Procédé selon l'une des revendications précédentes, caractérisé en ce qu'un refroidisseur de gaz de fumée (21 ; 121) est disposé entre le dispositif de post-combustion (20 ; 120) et le dispositif de filtrage (24 ; 124).
  4. Procédé selon l'une des revendications précédentes, caractérisé en ce que la chaleur contenue dans les gaz de fumée du four tubulaire rotatif (13 ; 113) et/ou du dispositif de post-combustion (20 ; 120) est utilisée au moins en partie pour préchauffer l'air d'oxydation amené au four tubulaire rotatif (13 ; 113) et/ou au dispositif de post-combustion (20 ; 120).
EP13003705.4A 2012-08-24 2013-07-24 Procédé pour le traitement thermique de matériaux de démolition routiers contenant du PAK ou de boues pétrolières Active EP2700875B1 (fr)

Priority Applications (1)

Application Number Priority Date Filing Date Title
PL13003705T PL2700875T3 (pl) 2012-08-24 2013-07-24 Sposób termicznego uzdatniania zawierającego WWA materiału z rozbiórki dróg albo osadów olejowych

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DE102012016882.9A DE102012016882B4 (de) 2012-08-24 2012-08-24 Verfahren zum Betreiben einer Anlage zur thermischen Aufbereitung von PAK-haltigem Straßenaufbruchmaterial oder von Ölschlämmen

Publications (2)

Publication Number Publication Date
EP2700875A1 EP2700875A1 (fr) 2014-02-26
EP2700875B1 true EP2700875B1 (fr) 2015-07-15

Family

ID=48876997

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Application Number Title Priority Date Filing Date
EP13003705.4A Active EP2700875B1 (fr) 2012-08-24 2013-07-24 Procédé pour le traitement thermique de matériaux de démolition routiers contenant du PAK ou de boues pétrolières

Country Status (6)

Country Link
US (1) US20140057221A1 (fr)
EP (1) EP2700875B1 (fr)
DE (1) DE102012016882B4 (fr)
ES (1) ES2547234T3 (fr)
HU (1) HUE027875T2 (fr)
PL (1) PL2700875T3 (fr)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR3065721B1 (fr) * 2017-04-28 2022-07-22 F M I Process Sa Installation compacte pour l'incineration de boues
DE102019008187A1 (de) * 2019-11-26 2021-05-27 Grenzebach Bsh Gmbh Verfahren und Anordnung zur Behandlung von Straßenaufbruchmaterial
DE102020123078A1 (de) 2020-09-03 2022-03-03 Pakexa AG Verfahren zum Aufbereiten von bitumen- und/oder teerhaltigen Feststoffen

Family Cites Families (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1934219U (de) * 1965-12-29 1966-03-10 Becker & Co Fritz Vorrichtung zur veraschung von muell.
FR2245915B3 (fr) * 1973-09-28 1976-08-27 Bazin Claudine
US5619936A (en) * 1993-05-28 1997-04-15 Kleen Soil Technologies, L.C. Thermal desorption unit and processes
US5743196A (en) * 1996-09-03 1998-04-28 Beryozkin; Vladimir Mobile waste incinerator
HN1998000031A (es) * 1997-06-11 1999-06-10 Basf Ag Metodo y aparatos mejorados para recuperar la energia de desechos mediante combustion de los mismos hornos industriales .
US6276306B1 (en) * 2000-08-03 2001-08-21 Michael L. Murphy Apparatus for recovering hydrocarbons from granular solids
US6352040B1 (en) * 2000-11-22 2002-03-05 Randall P. Voorhees Mobile armored incinerator
EP1785202A1 (fr) * 2005-11-11 2007-05-16 Roman Daub Dispositif et procédé pour nettoyer des matières contaminées
US8691166B2 (en) * 2008-01-08 2014-04-08 Carbonxt Group Limited System and method for activating carbonaceous material
DE102009025361B4 (de) 2009-06-18 2012-03-01 Eisenmann Ag Verfahren und Anlage zur Aufbereitung von Straßenaufbruchmaterial

Also Published As

Publication number Publication date
US20140057221A1 (en) 2014-02-27
EP2700875A1 (fr) 2014-02-26
DE102012016882B4 (de) 2014-07-03
PL2700875T3 (pl) 2015-12-31
HUE027875T2 (hu) 2016-10-28
DE102012016882A1 (de) 2014-03-27
ES2547234T3 (es) 2015-10-02

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