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WO2005087380A1 - Procede et installation de transformation et de reutilisation de materiaux de revetement de toit comprenant du bitume - Google Patents

Procede et installation de transformation et de reutilisation de materiaux de revetement de toit comprenant du bitume Download PDF

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Publication number
WO2005087380A1
WO2005087380A1 PCT/RU2005/000103 RU2005000103W WO2005087380A1 WO 2005087380 A1 WO2005087380 A1 WO 2005087380A1 RU 2005000103 W RU2005000103 W RU 2005000103W WO 2005087380 A1 WO2005087380 A1 WO 2005087380A1
Authority
WO
WIPO (PCT)
Prior art keywords
gas
bitumen
οτχοdοv
reagent
wastes
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/RU2005/000103
Other languages
English (en)
Russian (ru)
Inventor
Vyacheslav Nikolaevich Androsov
Staniclav Yurevich Filippov
Ryslan Alekseevich Lem
Karnil Grigorevich Tigay
Vladislav Nikolaevich Lihoded
Mihail Romanovich Urin
Roman Borisovich Kim
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.)
Obschestvo S Ogranichennoy Otvetstvennostyu 'slav-Sta Bitum'
Original Assignee
Obschestvo S Ogranichennoy Otvetstvennostyu 'slav-Sta Bitum'
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 Obschestvo S Ogranichennoy Otvetstvennostyu 'slav-Sta Bitum' filed Critical Obschestvo S Ogranichennoy Otvetstvennostyu 'slav-Sta Bitum'
Publication of WO2005087380A1 publication Critical patent/WO2005087380A1/fr
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

Links

Classifications

    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10C—WORKING-UP PITCH, ASPHALT, BITUMEN, TAR; PYROLIGNEOUS ACID
    • C10C3/00—Working-up pitch, asphalt, bitumen
    • C10C3/007—Working-up pitch, asphalt, bitumen winning and separation of asphalt from mixtures with aggregates, fillers and other products, e.g. winning from natural asphalt and regeneration of waste asphalt
    • 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
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B17/00—Recovery of plastics or other constituents of waste material containing plastics
    • B29B17/02—Separating plastics from other materials
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29K—INDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
    • B29K2095/00—Use of bituminous materials as moulding material
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29L—INDEXING SCHEME ASSOCIATED WITH SUBCLASS B29C, RELATING TO PARTICULAR ARTICLES
    • B29L2031/00—Other particular articles
    • B29L2031/10—Building elements, e.g. bricks, blocks, tiles, panels, posts, beams
    • B29L2031/108—Roofs
    • 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
    • Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00—Technologies for solid waste management
    • Y02W30/50—Reuse, recycling or recovery technologies
    • Y02W30/62—Plastics recycling; Rubber recycling

Definitions

  • the invention is available for the reprocessing of materials, in particular for the processing and disposal of consumer bituminous products.
  • the resulting bituminous composition is discharged for further use, and it is destroyed, for example, it burns or ends up at 21:10 a.m. ⁇ 3/10 ⁇ 12 12.27.2002; ⁇ ⁇ ⁇ 02/28610, class ⁇ 29 ⁇ 17/02 ⁇ 11 11.04.2002; ⁇ 10046156, class C 10 ⁇ 3/10 ⁇ 17 17.02.1998).
  • the main disadvantages of the waste of the technology are the incomplete separation of the bulk of the basic energy, low economic efficiency and high energy consumption. With this, the known processes of processing and disposal of the bitumen-containing waste products are aimed at utilizing the bitumen, and the materials that have been processed are not used.
  • bitumen liquefied in the products of the consumers, is used for products of the consumer group (additives), the modified bitumen (with additives) is used for the production of products.
  • Gas soot can be used in the manufacture of rubber products, as the dye is used in industrial applications and, in general, is used as a cigarette P ⁇ sle vshlavleniya bi ⁇ uma and ⁇ myv ⁇ i eg ⁇ in ⁇ as ⁇ v ⁇ i ⁇ ele and / or ⁇ azbavi ⁇ ele ⁇ s ⁇ ae ⁇ sya ⁇ a ⁇ nnaya ⁇ sn ⁇ va ⁇ veln ⁇ g ⁇ ma ⁇ e ⁇ iala, ⁇ aya chas ⁇ ichn ⁇ szhigae ⁇ sya ( ⁇ .e.
  • the reagent bitumen uses kerosin or is used for diesel fuel at a ratio of 1: 2.
  • the unit also has a gas plant for trapping and sedimenting soot and filtering devices for gas and a gas source
  • the capacity of the working camera does not exceed 300 liters.
  • the unit is equipped with a fan or pump for the outlet of a typical gas.
  • the gas separator contains, at a lower size, 15 voltages, the size of the cells is 1-5 mm.
  • the capacity of the gas unit is at least 6 m.
  • ⁇ el for ⁇ as ⁇ lavleniya bi ⁇ uma is ⁇ lzuyuschiysya in us ⁇ an ⁇ v ⁇ e for ⁇ susches ⁇ vleniya s ⁇ s ⁇ ba ⁇ e ⁇ e ⁇ ab ⁇ i and u ⁇ ilizatsii ⁇ velnzh bi ⁇ um ⁇ s ⁇ de ⁇ zhaschi ⁇ ⁇ d ⁇ v, s ⁇ de ⁇ zhi ⁇ ⁇ ab ⁇ chuyu ⁇ ame ⁇ u and ⁇ chnuyu Part with ⁇ a ⁇ ub ⁇ m for ⁇ v ⁇ da ⁇ chn ⁇ g ⁇ gas and ⁇ ab ⁇ chaya ⁇ ame ⁇ a provided yacheis ⁇ y g ⁇ iz ⁇ n ⁇ aln ⁇ y ⁇ e ⁇ eg ⁇ d ⁇ y for u ⁇ lad ⁇ i ⁇ velny ⁇ ⁇ d ⁇ v, ⁇ a ⁇ ub ⁇ m for ⁇ v ⁇ da ⁇ as ⁇ lavlenn ⁇ g ⁇ bi ⁇ uma,
  • boilers 1 for melting bitumen and a hollow compartment 2 for reducing the pressure of the outlet of the typical gas compared to the pressure in the boiler.
  • the soot catcher 5 is connected to the filter device 7. When the soot catcher 5 is removed, the filter 6 can be turned off, for example, by switching off. Smoke is discharged from boiler 1, goes to room 2 and goes on to smoke 3, exhausted by ventilator 8. The following is necessary. Before processing, the waste products are cut into parts (chopped) into a machine, such as a guillotine or with a knife blade. Household appliances are cut in parts with sizes of 300x300 mm and stacked in boilers for 150-200 kg. Larger sizes and weights are due to the available capacity.
  • Household appliances may be assembled in briquettes, and may be stacked in boilers without first-time equipment and accessories.
  • the process is heated for about 2 hours before the temperature is 100-110 ° C, and partial removal of the device is subject to physical and / or moisture.
  • the base uses a contactless carrier, which is poured directly into the boiler.
  • a commercially available product uses processed oils and / or low-level inoculants (fuel oil and other products), and an industrial process.
  • Part ⁇ d ⁇ v za ⁇ ladyvae ⁇ sya in ⁇ chnuyu ⁇ l ⁇ v Part 18 ( ⁇ ig.4, 4a) ⁇ aches ⁇ ve ⁇ chn ⁇ g ⁇ ma ⁇ e ⁇ iala szhigae ⁇ sya and, thus ⁇ em d ⁇ s ⁇ igae ⁇ sya e ⁇ n ⁇ miya ene ⁇ g ⁇ esu ⁇ s ⁇ v ⁇ i ⁇ e ⁇ miches ⁇ y ⁇ b ⁇ ab ⁇ e not ⁇ s ⁇ avlyaya ⁇ dy, ⁇ ye ⁇ ebuyu ⁇ d ⁇ lni ⁇ eln ⁇ g ⁇ unich ⁇ zheniya and / or ⁇ nse ⁇ vatsii.
  • an indi- vidual process occurs when the temperature of the product is not shut down. However, for the period of the industrial transition - around 1 hour, up to 80% of moisture is removed. After that, the temperature rises to 180-235 ° ⁇ (the third stage).
  • a large temperature device is available for melting the bitumen and separating it from the base in a capacity of not more than 300 liters of the specified mass for a minimum of 30-60 min.
  • Boilers 19 are made from metal, and it is therefore very important to choose the correct thickness of the metal for the typical part of 18 shipments.
  • An advantageous variant of the boiler performance is in the form of cylindrical gears, and this cylinder is also very large ⁇ dna ⁇ ⁇ ma ⁇ ab ⁇ chey chas ⁇ i ⁇ la not ⁇ g ⁇ anichena ⁇ a ⁇ im vsh ⁇ lneniem and m ⁇ zhe ⁇ by ⁇ as lyub ⁇ g ⁇ ⁇ ela v ⁇ ascheniya, na ⁇ ime ⁇ ⁇ ela v ⁇ ascheniya ⁇ a ⁇ etsii ( ⁇ niches ⁇ aya ⁇ ve ⁇ n ⁇ s ⁇ ) ⁇ ela v ⁇ ascheniya ⁇ lu ⁇ uga (s ⁇ e ⁇ iches ⁇ aya ⁇ ve ⁇ n ⁇ s ⁇ ) ⁇ ela v ⁇ ascheniya ⁇ iv ⁇ y v ⁇ g ⁇ ⁇ yad ⁇ a (elli ⁇ iches ⁇ aya or ⁇ vaya ⁇ ve ⁇ n ⁇ s ⁇ ) and ⁇ . ⁇ .
  • Each soot trap camera contains a set of 9 (Fig. 2, 2a), it is installed, but at least 15, it is small that it is 20-25
  • the size of the switch is 10 times lower than the height of the camera and mounted on the upper and lower walls of the camera in a shuffle box, while avoiding one another.
  • each gas chamber has a capacity of at least 6 m for 9 significant reduction in exhaust flow rate, and the cell sizes are selected with the best capture of soot and free air intake, when the cell is blocked with soot.
  • the input is 11 and the transition is 12 and, respectively, the output is 13, but the P ⁇ i ⁇ zhdenii che ⁇ ez sazheulavliva ⁇ el smoke ⁇ s ⁇ u ⁇ ae ⁇ in ⁇ e ⁇ vuyu ⁇ ame ⁇ u che ⁇ ez v ⁇ dn ⁇ e ⁇ ve ⁇ s ⁇ ie 11 ⁇ tsa sazheulavliva ⁇ elya and nagne ⁇ aemy ven ⁇ ilya ⁇ m che ⁇ ez se ⁇ cha ⁇ ye ⁇ e ⁇ eg ⁇ d ⁇ i and sv ⁇ b ⁇ dnye ⁇ dy, ⁇ di ⁇ ⁇ ⁇ iv ⁇ l ⁇ zhn ⁇ y s ⁇ en ⁇ e where na ⁇ di ⁇ sya ⁇ e ⁇ e ⁇ dn ⁇ e ⁇ ve ⁇ s ⁇ ie 12 v ⁇ v ⁇ uyu ⁇ ame ⁇ u where ⁇ a ⁇ im same ⁇ b ⁇ az ⁇ m smoke ⁇ di ⁇ che ⁇
  • soot trap In the case of the soot trap being installed as one-piece, instead of the transition to the installed one, the second-hand drive is installed. All soot is trapped and held for 10% of the process and is used in the process In this case, for the extraction of soot, the camcorder contains bulbs on the outside and the outside (not shown). Cleaned in the soot trap 5 (Fig. 1) soot the gas through the filter 6 is discharged into the filter device 7, where it is cleaned and disposed of in the exhaust gas.
  • bitumen-containing products is carried out for 2-4 hours, the bitumen is melted and runs to the bottom of the boiler, which was transferred to the boiler.
  • the molten bitumen 21 (Figs. 4, 4a)
  • the molten bitumen is drained for further use.
  • Bitumen is poured into commercial containers and disposed of to a cooling unit, for example, by means of a wait. After draining the melted bitumen, the boilers are relieved, and then the remaining base and waste are cleaned (including inclusions).
  • the internal working part of the boiler is completed in the form of an external part of the business.
  • the remaining base and garbage can be placed in metal containers of 200 l;
  • a predominant embodiment of the system is that a small amount of liquid is used or is used with diesel (1).
  • the processed mass must not be delivered at 140 ° ⁇ .
  • stir the resulting mass at a temperature of at least 90 ° C and often use it for cleaning.
  • part of the mass is returned to the technological process, and partly is used to make the voluminous materials on the basis of the type "Endulin".
  • the liquid phase merges with the following filtering and is used to make the bio varnish series ⁇ .
  • this method of processing and disposing of biosafety products does not replace the inoperative material. All material obtained in the process of processing the waste gas must be disposed of.
  • the proposed method is more eco-friendly than the known ones, t. ⁇ . It uses all materials that are received by the consumer in the process of using bitumen-friendly products, which used to be used to by-pass and the source of non-polluting products.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Civil Engineering (AREA)
  • Structural Engineering (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Analytical Chemistry (AREA)
  • Materials Engineering (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Organic Chemistry (AREA)
  • Architecture (AREA)
  • Processing Of Solid Wastes (AREA)
  • Crystals, And After-Treatments Of Crystals (AREA)

Abstract

L'invention appartient au domaine de la réutilisation de matériaux et notamment de la transformation et de réutilisation de déchets contenant du bitume. Selon l'invention, les déchets sont broyés puis chargés dans une cuve de fusion de bitume et de séparation du bitume de son substrat en carton en présence d'un caloporteur liquide de contact. Pendant le réchauffement, on évacue les gaz de brûlage sous pression depuis la partie brûleur de la cuve via un boîtier destiné à réduire la pression des gaz de brûlage, par une conduite à destination d'un séparateur de gaz destiné à la capture et à la sédimentation de la suie. Le gaz est ensuite envoyé dans un dispositif de filtrage dans lequel il est purifié et éjecté dans l'atmosphère sous la forme d'air purifié. Le bitume fondu et la masse de carton sont extraits de la cuve de fusion et refroidis jusqu'à une température ne dépassant pas 140 °C, après quoi la masse de carton est rincée dans un réactif qui dissout le bitume puis utilisée pour fabriquer des matériaux de revêtement de toit et/ou en tant que combustible. La phase liquide qui reste après le rinçage est utilisée en tant que base dans la fabrication de laques à partir du bitume. La suie est utilisée au moins dans la fabrication d'articles techniques en caoutchouc ou en tant que colorant, ou en tant que pigment dans la fabrication de laques et de peintures. En outre, l'invention concerne une installation destinée à la mise en oeuvre de ce procédé. Elle comprend un séparateur de gaz, un dispositif de filtrage de gaz et une cuve de fusion de bitume, qui font partie de l'installation. Cette solution technique assure l'optimisation d'un processus de transformation sans déchets et écologiquement propre des déchets de matériaux de toiture contenant du bitume; elle augment la productivité et permet de réduire au minimum les dépenses matérielles et énergétiques, de réduire le temps de transformation, simplifie le procédé et diminue la consommation de matériaux utilisés dans l'installation.
PCT/RU2005/000103 2004-03-11 2005-03-10 Procede et installation de transformation et de reutilisation de materiaux de revetement de toit comprenant du bitume Ceased WO2005087380A1 (fr)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
RU2004107099 2004-03-11
RU2004107099A RU2244731C1 (ru) 2004-03-11 2004-03-11 Способ и установка для переработки и утилизации кровельных битумосодержащих материалов

Publications (1)

Publication Number Publication Date
WO2005087380A1 true WO2005087380A1 (fr) 2005-09-22

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Country Link
RU (1) RU2244731C1 (fr)
WO (1) WO2005087380A1 (fr)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2015199562A1 (fr) 2014-06-26 2015-12-30 Laboratorium Czystych Technologii Acren Sp. Z O.O. Procédé de recyclage de déchets de matériaux d'hydroisolation

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
RU2348470C1 (ru) * 2007-07-03 2009-03-10 Вячеслав Иванович Зотов Способ и установка для получения битума из устаревших кровельных материалов
EA012322B1 (ru) * 2008-12-17 2009-08-28 Александр Ефимович Голиков Способ переработки битумных кровельных материалов и комплекс для его осуществления
WO2012015336A1 (fr) * 2010-07-29 2012-02-02 Kovalev Sergey Ivanovich Procédé de réparation sans déchets d'une couverture de toit composite bitume / polymère
RU2500787C2 (ru) * 2011-10-05 2013-12-10 Общество с ограниченной ответственностью "Грани" Способ переработки битумных кровельных материалов
RU2700499C1 (ru) * 2018-11-01 2019-09-17 Федеральное государственное бюджетное образовательное учреждение высшего образования "Ивановская пожарно-спасательная академия Государственной противопожарной службы Министерства Российской Федерации по делам гражданской обороны, чрезвычайным ситуациям и ликвидации последствий стихийных бедствий" ФГ Способ переработки битумсодержащих отходов

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SU107997A1 (ru) * 1955-12-12 1956-11-30 Г.И. Фефербойм Битумонагнетатель
SU145964A1 (ru) * 1961-05-22 1961-11-30 Л.С. Заглодин Печь дл термической переработки твердых топлив
GB1210471A (en) * 1967-02-11 1970-10-28 Kloeckner Humboldt Deutz Ag An apparatus for storing thermoplastic, bituminous binding agents
US4330340A (en) * 1978-03-07 1982-05-18 Carlton Wayne H Process to recycle bituminous roofing refuse into solid fuel and other energy-related products
SU1674911A1 (ru) * 1989-05-03 1991-09-07 И.И.Жмуров и И.В.Жамков Сепаратор дл очистки газов
RU2094623C1 (ru) * 1995-05-26 1997-10-27 Иван Иванович Кутыш Фильтрующий элемент с петлевым движением отработавших газов
RU2117532C1 (ru) * 1993-01-14 1998-08-20 Всеволод Вениаминович Тарнов Способ извлечения битума из кровельных материалов и установка для его реализации
RU2188696C1 (ru) * 2001-05-28 2002-09-10 Закрытое акционерное общество "Промышленная компания Элина" Способ мокрой очистки воздуха и устройство для его реализации
RU2195475C2 (ru) * 2001-11-15 2002-12-27 Акционерное общество закрытого типа Центральный научно-исследовательский проектно-экспериментальный институт организации, механизации и технической помощи строительству Способ выплавки битума из отходов битумных рулонных материалов

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CA1211063A (fr) * 1983-09-13 1986-09-09 Robert D. De Calonne Methode d'emploi et d'elimination des bouilles d'extraction a l'eau chaude des sables bitumineux
SU1329803A1 (ru) * 1985-11-11 1987-08-15 Всесоюзный Институт По Проектированию Объектов Газовой Промышленности "Союзгазпроект" Устройство дл фильтрации газа
SU1465124A1 (ru) * 1987-02-06 1989-03-15 МВТУ им.Н.Э.Баумана Центробежный сажеуловитель
SU1669551A1 (ru) * 1989-07-19 1991-08-15 Брестский инженерно-строительный институт Способ переработки кровельных материалов

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
SU107997A1 (ru) * 1955-12-12 1956-11-30 Г.И. Фефербойм Битумонагнетатель
SU145964A1 (ru) * 1961-05-22 1961-11-30 Л.С. Заглодин Печь дл термической переработки твердых топлив
GB1210471A (en) * 1967-02-11 1970-10-28 Kloeckner Humboldt Deutz Ag An apparatus for storing thermoplastic, bituminous binding agents
US4330340A (en) * 1978-03-07 1982-05-18 Carlton Wayne H Process to recycle bituminous roofing refuse into solid fuel and other energy-related products
SU1674911A1 (ru) * 1989-05-03 1991-09-07 И.И.Жмуров и И.В.Жамков Сепаратор дл очистки газов
RU2117532C1 (ru) * 1993-01-14 1998-08-20 Всеволод Вениаминович Тарнов Способ извлечения битума из кровельных материалов и установка для его реализации
RU2094623C1 (ru) * 1995-05-26 1997-10-27 Иван Иванович Кутыш Фильтрующий элемент с петлевым движением отработавших газов
RU2188696C1 (ru) * 2001-05-28 2002-09-10 Закрытое акционерное общество "Промышленная компания Элина" Способ мокрой очистки воздуха и устройство для его реализации
RU2195475C2 (ru) * 2001-11-15 2002-12-27 Акционерное общество закрытого типа Центральный научно-исследовательский проектно-экспериментальный институт организации, механизации и технической помощи строительству Способ выплавки битума из отходов битумных рулонных материалов

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2015199562A1 (fr) 2014-06-26 2015-12-30 Laboratorium Czystych Technologii Acren Sp. Z O.O. Procédé de recyclage de déchets de matériaux d'hydroisolation

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