EP1022391B1 - Procédé pour le recyclage de matériau contenant du goudron et/ou du bitume et comprenant d'aggrégat d'asphalte, au moyen d'une conversion thermique en combinaison avec la production d'asphalte - Google Patents

Procédé pour le recyclage de matériau contenant du goudron et/ou du bitume et comprenant d'aggrégat d'asphalte, au moyen d'une conversion thermique en combinaison avec la production d'asphalte Download PDF

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Publication number
EP1022391B1
EP1022391B1 EP00200082A EP00200082A EP1022391B1 EP 1022391 B1 EP1022391 B1 EP 1022391B1 EP 00200082 A EP00200082 A EP 00200082A EP 00200082 A EP00200082 A EP 00200082A EP 1022391 B1 EP1022391 B1 EP 1022391B1
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EP
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Prior art keywords
aggregate
asphalt
asphaltic
thermal conversion
tar
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Expired - Lifetime
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EP00200082A
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German (de)
English (en)
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EP1022391A1 (fr
Inventor
Henricus Johannes Nicolaas Antonius Bolk
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HEIJMANS INFRASTRUCTUUR BV
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HEIJMANS INFRASTRUCTUUR BV
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    • E—FIXED CONSTRUCTIONS
    • E01—CONSTRUCTION OF ROADS, RAILWAYS, OR BRIDGES
    • E01C—CONSTRUCTION OF, OR SURFACES FOR, ROADS, SPORTS GROUNDS, OR THE LIKE; MACHINES OR AUXILIARY TOOLS FOR CONSTRUCTION OR REPAIR
    • E01C19/00—Machines, tools or auxiliary devices for preparing or distributing paving materials, for working the placed materials, or for forming, consolidating, or finishing the paving
    • E01C19/02—Machines, tools or auxiliary devices for preparing or distributing paving materials, for working the placed materials, or for forming, consolidating, or finishing the paving for preparing the materials
    • E01C19/10—Apparatus or plants for premixing or precoating aggregate or fillers with non-hydraulic binders, e.g. with bitumen, with resins, i.e. producing mixtures or coating aggregates otherwise than by penetrating or surface dressing; Apparatus for premixing non-hydraulic mixtures prior to placing or for reconditioning salvaged non-hydraulic compositions
    • E01C19/1004—Reconditioning or reprocessing bituminous mixtures, e.g. salvaged paving, fresh patching mixtures grown unserviceable; Recycling salvaged bituminous mixtures; Apparatus for the in-plant recycling thereof
    • E—FIXED CONSTRUCTIONS
    • E01—CONSTRUCTION OF ROADS, RAILWAYS, OR BRIDGES
    • E01C—CONSTRUCTION OF, OR SURFACES FOR, ROADS, SPORTS GROUNDS, OR THE LIKE; MACHINES OR AUXILIARY TOOLS FOR CONSTRUCTION OR REPAIR
    • E01C19/00—Machines, tools or auxiliary devices for preparing or distributing paving materials, for working the placed materials, or for forming, consolidating, or finishing the paving
    • E01C19/02—Machines, tools or auxiliary devices for preparing or distributing paving materials, for working the placed materials, or for forming, consolidating, or finishing the paving for preparing the materials
    • E01C19/10—Apparatus or plants for premixing or precoating aggregate or fillers with non-hydraulic binders, e.g. with bitumen, with resins, i.e. producing mixtures or coating aggregates otherwise than by penetrating or surface dressing; Apparatus for premixing non-hydraulic mixtures prior to placing or for reconditioning salvaged non-hydraulic compositions
    • E01C19/1059—Controlling the operations; Devices solely for supplying or proportioning the ingredients
    • E01C19/1063—Controlling the operations

Definitions

  • the present invention relates to a process for recycling tar and/or bitumen containing material, whereby said material comprises asphaltic aggregate, in an asphalt production plant, wherein the said material is thermally converted into hot gases and a hot mineral residue, which are supplied to a mixing plant for the production of asphalt.
  • the present invention also relates to an apparatus for carrying out the process.
  • asphalt material reclaimed from old pavement material is to an increasing extent used in the production of asphalt, often referred to as "recycling asphalt".
  • old asphalt contains valuable materials such as bitumen, which is a petroleum product, and mineral aggregates.
  • An example of a process for recycling of old asphalt is described in WO 85/05439.
  • reclaimed asphaltic aggregate is mixed with fresh bitumen and fresh mineral aggregate.
  • the reclaimed asphaltic aggregate is dried and heated in a so-called recycle dryer (a parallel drum), which requires a substantial supply of energy.
  • EP 216,316 describes a process for recycling asphaltic granulate.
  • the apparatus used comprises a drum dryer for drying minerals, a drum dryer for drying asphaltic granulate and a mixer in which the dried materials are mixed with filler and bitumen.
  • the gases from the dryer for drying asphaltic aggregate are directed to the dryer for drying minerals.
  • the object of the described process is not to oxidise or otherwise deteriorate the recycled bitumen material, but to heat it.
  • EP 437,990 describes a process for preparing bituminous asphalt products from recycled asphalt material and fresh minerals and bitumen.
  • the recycled asphaltic aggregate is dried and heated in a first drum and then introduced into a second drum where it is mixed with fresh mineral aggregate and fresh bitumen.
  • the object is to heat the recycled material and to avoid its thermal degradation.
  • DE 3723103 a method is described wherein recycled asphaltic material is heated and mixed with fresh bitumen and mineral aggregate. The object is also to reuse reclaimed asphaltic material without deterioration of the bitumen.
  • Tar containing asphalt has been used up to about 1991 (in the Netherlands).
  • Tar containing asphalt has the disadvantage that it contains polycyclic aromatic hydrocarbons (PAH's), which are harmful substances for which strict legal limitations apply. It is not allowed to recycle tar containing asphalt by hot mixing it with new asphalt, because then the PAH's could evaporate into the environment. Conventionally tar containing asphalt is therefore recycled in a cold manner as "mineral" aggregate in cement and/or bitumen-emulsion bound granular base course material. However, this is only a temporary solution because the harmful substances from the tar are not removed.
  • PAH's polycyclic aromatic hydrocarbons
  • the object of the present invention is to provide a process which allows the recycling of low quality tar and/or bitumen containing material which comprises asphaltic aggregate, such as tar containing asphalt or low quality bitumen containing asphalt. Another object is to recycle tar and/or bitumen containing material which comprises asphaltic aggregate in combination with the production of asphalt such that it results in saving of energy and starting materials. A further object is to provide a process for total recycling of asphalt in an efficient and economical manner.
  • the present invention provides a process for recycling of tar and/or bitumen containing material, whereby said material comprises asphaltic aggregate, according to claim 1.
  • recycling is meant to include re-using of reclaimed materials.
  • this term therefore includes thermal conversion of reclaimed asphalt and then using the residues and energy content for the production of asphalt, as well as mixing reclaimed asphalt together with new mineral aggregate and new bitumen to obtain a new asphalt product (“recycling asphalt”).
  • asphalt which at least in part contains fresh bitumen and which may also contain bitumen from reclaimed asphalt.
  • This term thus also includes the so-called recycling asphalt, which consists of both fresh bitumen and recycled bitumen.
  • the tar and/or bitumen containing material which is thermally converted comprises asphaltic aggregate.
  • asphaltic aggregate is meant tar-free or tar-containing asphalt reclaimed from (old) asphalt pavement. This means that the asphaltic aggregate can contain reclaimed tar containing asphalt pavement, but also aged (oxidized) bitumen containing asphalt pavement and/or contaminated, for instance with hydrocarbons, bitumen containing asphalt pavement.
  • the tar and/or bitumen containing material which comprises asphaltic aggregate are other tar and bitumen containing materials, such as roof cuttings. Further, any other organic material which is combustible can be added, provided that the residues after conversion do not disturb the asphalt production process.
  • the tar and/or bitumen containing material which comprises asphaltic aggregate comprises more than 30 % by weight, more preferably more than 50 % by weight, most preferably more than 80 % by weight of asphaltic aggregate.
  • thermal conversion any process which converts the tar and/or bitumen containing material under the influence of heat to substances which are less or not harmful to the environment. This process therefore does not involve just heating the recycled material but converts it into different substances.
  • the thermal conversion is for instance an incineration process.
  • the thermal conversion process is preferably a process which allows to control the temperature of the gas stream discharged from the process.
  • the thermal conversion apparatus is preferably a fluidised bed reactor, more preferably a toroidal fluidised bed reactor.
  • Such toroidal fluidised bed reactors are available under the tradename TORBED from Torftech, UK and are described in EP-A-0 068 853, which is incorporated by reference.
  • the use of such a thermal conversion process makes it possible to recycle tar containing asphalt, without the risk of PAH's remaining in the discharge streams of the process.
  • the process control of the thermal conversion apparatus depends on the starting materials used. Specific conditions such as temperature can readily be determined by a skilled person.
  • the tar and/or bitumen containing material which comprises asphaltic aggregate is first thermally converted which results in a hot gas stream and a mineral residue which was contained in the asphalt
  • the mineral residue resulting from the thermal conversion is clean and environmentally safe.
  • the big advantage of using asphaltic aggregate in this process is that the mineral residue obtained after the thermal conversion of the asphaltic aggregate already has a composition suitable for use in asphalt. It can be transferred directly to the aggregate dryer because it does not disturb the composition of the asphalt.
  • the inherent heat of the tar or bitumen containing materials is re-used.
  • the tar or bitumen itself is fuel for the thermal conversion process, hence this process requires little energy supply.
  • the thermal conversion process results in a stream of hot gases and hot mineral residue which can be used advantageously in the asphalt production process.
  • the asphalt production plant to which the hot gases and hot mineral residue are supplied can be a batch type asphalt mixing plant or a continuous asphalt mixing plant, such as a drum mixer. These asphalt mixing plants can be of conventional design.
  • the hot mineral residue obtained after thermal conversion is preferably transferred to the aggregate dryer, which is used to dry and heat fresh mineral aggregate.
  • the aggregate dryer can be of conventional design.
  • the hot mineral residue can be transferred to the aggregate dryer with or without intermediate storage.
  • Preferably the hot mineral residue is not stored. This allows use of the energy of the hot mineral residue in the aggregate dryer. Part or all of the hot gases obtained after thermal conversion can also be directed to the aggregate dryer.
  • the asphalt production plant can also comprise a device for heating and drying asphaltic aggregate, preferably a parallel drum, sometimes referred to as a recycle dryer.
  • This device serves to heat and dry asphaltic aggregate before mixing it with fresh mineral aggregate and fresh bitumen.
  • the device makes it possible to recycle not-contaminated bitumen containing asphalt of high quality. It is not allowed to supply low quality materials (contaminated) such as tar containing asphalt to a device for heating and drying asphaltic aggregate due to legal restrictions.
  • part or all of the hot gases obtained after thermal conversion can be directed to the device for heating and drying asphaltic aggregate.
  • the process according to the present invention preferably also includes the steps of classifying the dried and heated aggregate according to particle size using a suitable sizing screen arrangement and mixing a metered quantity of the classified aggregate with a metered amount of bitumen. To this mixture dried and heated asphaltic aggregate obtained in the parallel drum can be added.
  • an apparatus for recycling asphalt comprising an apparatus for thermal conversion of a tar and/or bitumen containing material, whereby the said material comprises asphaltic aggregate, according to claim 11.
  • the present invention further provides a batch type apparatus for the production of asphalt according to claim 12.
  • this apparatus preferably contains an aggregate dryer as described above and means for transferring the hot mineral residue obtained after thermal conversion to the aggregate dryer and/or means for transferring hot gases to the aggregate dryer.
  • the batch type apparatus also includes a parallel drum for heating and drying asphaltic aggregate as described above and means for directing part or all of the hot gases obtained after thermal conversion to the parallel drum.
  • the batch type apparatus can comprise means for directing part or all of the hot gases from the parallel drum to the aggregate dryer.
  • the batch type apparatus can further include a cold feed hopper for storing starting mineral aggregate.
  • the apparatus includes a plurality of cold feed hoppers for storing aggregate of various size to be used in producing the final mix.
  • the same means can be used to transfer mineral residue from the thermal conversion apparatus, optionally after intermediate storage, to the aggregate dryer.
  • the aggregate dryer is of conventional design and can be a large elongated drum having a burner directed into one end, with the aggregate being fed therethrough from the other end, and providing rotation of the drum with flights for mixing the aggregate material with the hot gases and causing it to be dried.
  • the hot and dried aggregate can be transported to the sizing screen arrangement by means of a transfer belt, elevator or other suitable means.
  • the sizing screen arrangement serves to classify the preheated and dried aggregate into various particle sizes and is connected to a system for holding the graded material.
  • the sizing screen arrangement may be provided in any suitable form to separate the aggregate into any suitable number of size ranges as desired.
  • the batch type apparatus may also include an asphaltic aggregate storage silo (cold feeder) and means for transporting the asphaltic aggregate, for instance a conveyor belt or other transfer means, to the parallel drum where it is dried and heated.
  • the parallel drum is of conventional design.
  • the heated asphaltic aggregate can be transported directly to the weighing hopper but can also be stored in an intermediate storage silo.
  • the batch type apparatus may also include storage silo's for storing hot mineral aggregate to serve as a buffer.
  • the batch type apparatus may further include a weighing hopper for weighing the heated aggregate and optionally (heated) asphaltic aggregate.
  • the proportion of mineral aggregate and reclaimed asphalt discharged into the weighing hopper may be controlled according to the grade or mix required in the final batch.
  • Bitumen may be added to the mix from a suitable bitumen storage tank or other facility.
  • the bitumen preferably is added to the mix in a suitable mixing chamber.
  • Filler materials such as fine material or powder may also be added to the mixing chamber or elsewhere.
  • An associated filler tank or silo may be provided for this purpose. Fines may be collected by extraction from exhaust gas of the aggregate dryer and used to provide at least part of the filler. Extraction may be by means of a bag filter or fabric filter for example.
  • the mineral residue and hot gases obtained after thermal conversion can also be supplied to a continuous asphalt mixing plant.
  • Continuous mixing plants generally can be divided into two categories. In the first type mineral aggregate is heated and dried in a drum dryer. The heated and dried aggregate is then discharged into a separate mixing device, such as a pugmill. Bitumen is then introduced into the mixer along with the mineral aggregate and is thoroughly mixed, the resulting new asphalt being discharged from the other end of the mixer.
  • the mineral residue obtained after thermal conversion can be added to the fresh mineral aggregate in the dryer.
  • the hot gases can be supplied to the dryer.
  • drum mixer In the second type of continuous mixing plant, the so-called drum mixer, the drying and mixing processes are both carried out in a single rotating drum.
  • Mineral aggregate is added at the top of the rotating drum.
  • a burner is mounted in the upper end to heat and dry the mineral aggregate.
  • Bitumen is introduced into the drum downstream of the burner. The heated and dried aggregate and the bitumen are then mixed in the bottom portion of the drum, and the new asphalt is discharged out the lower end of the drum.
  • the mineral residue obtained after thermal conversion can be introduced into the drum together with fresh mineral aggregate.
  • the hot gases can be introduced at any point in the drum, but are preferably introduced near the burner.
  • drum mixers can also be used for recycling old asphalt.
  • asphaltic aggregate is generally introduced into the drum mixer downstream of the burner.
  • fresh aggregate is supplied to a cold feed hopper 1.
  • the aggregate is transferred by conveyor belts 2, 3 and 4 to the aggregate dryer 5.
  • the heated and dried aggregate is transported to a sizing screen arrangement 7 by means of a hot elevator 6.
  • the aggregate dryer 5 is further connected to a dust filter system which consists of a pre-separator 22 and a fabric filter 23.
  • the dust filter system is connected to an exhauster 27 and a stack 28 for discharging the gases from the dryer.
  • the fabric filter 23 is also connected to an exhauster 24, filtered dust storage 25 and filtered dust dosage silo 26 which are used to meter the filtered dust and to transport it to the filler weighing hopper 19.
  • the pre-separator 22 is connected to elevator 6, for transporting the separated material to the sizing screen arrangement 7.
  • the apparatus also includes an asphaltic aggregate feeder 12 connected to a conveyor belt 13 and elevator 14 to transport asphaltic aggregate to the parallel drum 34.
  • the parallel drum 34 is connected to an exhauster 31 for transporting the gases of the parallel drum 34 to the aggregate dryer 5.
  • the dried and heated asphaltic aggregate is transported to an intermediate storage silo 15.
  • the asphaltic aggregate is transferred by means of screw conveyor 16 to the weighing hopper 9.
  • the weighing hopper 9 is also connected to holding bin for heated mineral aggregate 8.
  • the holding bin 8 receives the heated mineral aggregate from the sizing screen arrangement 7, which contains a screen overflow 37 and a screen exhaust 30 (connected to pre-separator 22).
  • asphaltic aggregate and mineral aggregate from weighing hopper 9 are mixed with additives provided by opening 20, fillers and additives from filler weighing hopper 19 and bitumen.
  • the bitumen is stored in storage tank 17 and transferred via bitumen dosage device 18 to the mixer 10. If desired modified bitumen can be added at 33 and via modified bitumen dosage device 36.
  • the filler material is stored in filler storage silo 21. Additives are supplied to weighing hopper 19 by means of dosage unit 35. From mixer 10 the asphalt is conveyed to the asphalt storage silo 11 from where it can be transported to customers (29).
  • the apparatus further contains a control room 32 having the plant controls.
  • Thermal conversion of tar and/or bitumen containing materials which comprise asphaltic aggregate takes place in thermal conversion apparatus 38.
  • the tar and/or bitumen containing material which comprise asphaltic aggregate is transferred to the thermal conversion apparatus 38 from a storage silo (not shown).
  • mineral residue obtained after conversion of the tar and/or bitumen containing materials which comprise asphaltic aggregate is transferred 39 to the aggregate dryer 5.
  • the gases obtained in the thermal conversion apparatus 38 are directed to the parallel drum 34 and/or to the aggregate dryer 5.

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  • Engineering & Computer Science (AREA)
  • Architecture (AREA)
  • Civil Engineering (AREA)
  • Structural Engineering (AREA)
  • Road Paving Machines (AREA)
  • Working-Up Tar And Pitch (AREA)
  • Road Paving Structures (AREA)
  • Compositions Of Macromolecular Compounds (AREA)

Claims (14)

  1. Procédé de recyclage d'un matériau contenant du goudron et/ou du bitume, dans lequel ledit matériau comprend un agrégat d'asphalte, caractérisé par la conversion thermique dudit matériau en un résidu minéral et en gaz chauds et l'acheminement du résidu minéral et des gaz chauds vers une usine de production d'asphalte.
  2. Procédé selon la revendication 1, dans lequel le matériau contenant du goudron et/ou du bitume, dans lequel ledit matériau comprend un agrégat d'asphalte, comprend plus de 30% en poids, de préférence plus de 50% en poids d'agrégat d'asphalte.
  3. Procédé selon la revendication 1 ou 2, dans lequel la conversion thermique est effectuée de manière à obtenir un courant régulé de gaz chauds.
  4. Procédé selon l'une quelconque des revendications précédentes, dans lequel la conversion thermique est effectuée dans un réacteur à lit fluidisé.
  5. Procédé selon l'une quelconque des revendications précédentes, dans lequel l'usine de production d'asphalte est une installation de mélange d'asphalte du type discontinu.
  6. Procédé selon la revendication 5, dans lequel l'installation de mélange d'asphalte du type discontinu comprend un sécheur d'agrégats pour chauffer et sécher l'agrégat minéral, caractérisé en ce que le résidu minéral obtenu après conversion thermique est transféré au sécheur d'agrégats.
  7. Procédé selon la revendication 6, dans lequel une partie ou la totalité des gaz chauds obtenus après conversion thermique est envoyée au sécheur d'agrégats.
  8. Procédé selon l'une quelconque des revendications 5 à 7, dans lequel l'installation de mélange d'asphalte du type discontinu comprend un dispositif, de préférence un tambour parallèle, pour chauffer et sécher un agrégat d'asphalte, caractérisé en ce qu'une partie ou la totalité des gaz chauds obtenus après conversion thermique est envoyée audit dispositif.
  9. Procédé selon l'une quelconque des revendications 1 à 4, dans lequel l'installation de production d'asphalte est une installation de mélange d'asphalte du type continu.
  10. Procédé selon la revendication 9, dans lequel l'agrégat d'asphalte est acheminé à l'installation de mélange d'asphalte du type continu de manière à obtenir un produit constitué essentiellement de 100% d'asphalte recyclé.
  11. Appareil pour le recyclage de l'asphalte, caractérisé en ce qu'il comprend un appareil pour la conversion thermique d'un matériau contenant du goudron et/ou du bitume, dans lequel ledit matériau comprend un agrégat d'asphalte, en un résidu minéral chaud et en gaz chauds; et un moyen de transfert du résidu minéral chaud et des gaz chauds à une installation de production d'asphalte
  12. Appareil du type discontinu pour la production d'asphalte, comprenant un sécheur d'agrégats (5) pour le chauffage et le séchage d'un agrégat minéral; un dispositif à tamis de calibrage (7) pour classifier l'agrégat séché et chauffé en fonction de la taille particulaire; un moyen pour le transfert de l'agrégat minéral séché et chauffé au dispositif à tamis de calibrage (6); une trémie de pesage (9) et un mélangeur (10) pour mélanger l'agrégat classifié au bitume; caractérisé en ce qu'il comprend en outre un appareil pour la conversion thermique d'un matériau contenant du goudron et/ou du bitume, dans lequel ledit matériau comprend un agrégat d'asphalte, en un résidu minéral chaud et en gaz chauds (38); et un moyen (39) pour le transfert du résidu minéral chaud obtenu après conversion thermique au sécheur d'agrégats (5) et un moyen pour envoyer une partie ou la totalité des gaz chauds après conversion thermique au sécheur d'agrégats (5).
  13. Appareil selon la revendication 12, comprenant en outre un dispositif, de préférence un tambour parallèle (34), pour chauffer et sécher un agrégat d'asphalte; un moyen (16) pour transférer l'agrégat d'asphalte séché et chauffé à la trémie de pesage (9) et au mélangeur (10); un moyen (40) pour envoyer une partie ou la totalité des gaz chauds obtenus après conversion thermique au dispositif pour chauffer et sécher l'agrégat d'asphalte (34).
  14. Appareil selon la revendication 13, comprenant en outre un moyen (31) pour envoyer une partie ou la totalité des gaz chauds du dispositif pour chauffer et sécher l'agrégat d'asphalte au sécheur d'agrégats (5).
EP00200082A 1999-01-11 2000-01-11 Procédé pour le recyclage de matériau contenant du goudron et/ou du bitume et comprenant d'aggrégat d'asphalte, au moyen d'une conversion thermique en combinaison avec la production d'asphalte Expired - Lifetime EP1022391B1 (fr)

Priority Applications (1)

Application Number Priority Date Filing Date Title
EP00200082A EP1022391B1 (fr) 1999-01-11 2000-01-11 Procédé pour le recyclage de matériau contenant du goudron et/ou du bitume et comprenant d'aggrégat d'asphalte, au moyen d'une conversion thermique en combinaison avec la production d'asphalte

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
EP99200069 1999-01-11
EP99200069 1999-01-11
EP00200082A EP1022391B1 (fr) 1999-01-11 2000-01-11 Procédé pour le recyclage de matériau contenant du goudron et/ou du bitume et comprenant d'aggrégat d'asphalte, au moyen d'une conversion thermique en combinaison avec la production d'asphalte

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EP1022391A1 EP1022391A1 (fr) 2000-07-26
EP1022391B1 true EP1022391B1 (fr) 2004-05-12

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EP (1) EP1022391B1 (fr)
AT (1) ATE266772T1 (fr)
DE (1) DE60010533T2 (fr)
DK (1) DK1022391T3 (fr)

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DE102006009205B3 (de) * 2006-02-24 2007-06-06 Carsten Schaumburg Verfahren und Vorrichtung zum Erwärmen eines bituminösen Mischguts
EP2412783A1 (fr) 2010-07-30 2012-02-01 Physitron GmbH Dispositif et procédé de séparation de mélanges comprenant de l'huile ou des bitumes et des additifs
CN103758011B (zh) * 2014-01-21 2016-01-20 沧州市市政工程股份有限公司 厂拌冷再生泡沫沥青混合料生产系统
CN104032650B (zh) * 2014-05-09 2017-08-15 南阳市亚龙筑路机械制造有限公司 沥青混合料温拌再生设备
CN105507121B (zh) * 2015-12-31 2017-10-31 徐州徐工筑路机械有限公司 一种智能沥青料输送装置及其路面养护车
JP7017834B2 (ja) * 2018-03-09 2022-02-09 日工株式会社 アスファルトプラントの骨材貯蔵ビンの骨材貯蔵量表示方法
CN108708250B (zh) * 2018-07-04 2024-01-05 河南亚龙智能装备有限公司 一种废旧沥青混合料全再生设备
CN108867249B (zh) * 2018-07-25 2023-12-05 福建省铁拓机械股份有限公司 一种多功能连续式沥青混合料生产设备及其生产方法
DE102018213210A1 (de) 2018-08-07 2020-02-13 Fraunhofer-Gesellschaft zur Förderung der angewandten Forschung e.V. Verfahren zur Reinigung mineralischer Feststoffe und Holzmaterialien, Vorrichtung für dieses Verfahren und deren Verwendung
DE102019008187A1 (de) 2019-11-26 2021-05-27 Grenzebach Bsh Gmbh Verfahren und Anordnung zur Behandlung von Straßenaufbruchmaterial
CN111041944B (zh) * 2019-12-31 2021-10-22 三一汽车制造有限公司 清料方法、清料装置和一体式沥青搅拌站
DE102020002533A1 (de) 2020-04-27 2021-10-28 Grenzebach Bsh Gmbh Schachtofen zur Behandlung von Straßenaufbruchmaterial
CN113332906A (zh) * 2021-05-20 2021-09-03 漳州新立基沥青有限公司 一种高效节能的改性沥青加工装置

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DE60010533D1 (de) 2004-06-17
EP1022391A1 (fr) 2000-07-26
ATE266772T1 (de) 2004-05-15
DK1022391T3 (da) 2004-06-28
DE60010533T2 (de) 2005-08-25

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