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WO2013039461A1 - Kiln for firing ceramic articles - Google Patents

Kiln for firing ceramic articles Download PDF

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Publication number
WO2013039461A1
WO2013039461A1 PCT/UA2012/000068 UA2012000068W WO2013039461A1 WO 2013039461 A1 WO2013039461 A1 WO 2013039461A1 UA 2012000068 W UA2012000068 W UA 2012000068W WO 2013039461 A1 WO2013039461 A1 WO 2013039461A1
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WO
WIPO (PCT)
Prior art keywords
gas
products
kiln
main channel
sections
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/UA2012/000068
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French (fr)
Russian (ru)
Inventor
Александр Юльевич ЛЕВЕСТАМ
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Individual
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Individual
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Publication of WO2013039461A1 publication Critical patent/WO2013039461A1/en
Anticipated expiration legal-status Critical
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Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F27FURNACES; KILNS; OVENS; RETORTS
    • F27BFURNACES, KILNS, OVENS OR RETORTS IN GENERAL; OPEN SINTERING OR LIKE APPARATUS
    • F27B5/00Muffle furnaces; Retort furnaces; Other furnaces in which the charge is held completely isolated
    • F27B5/06Details, accessories or equipment specially adapted for furnaces of these types
    • F27B5/14Arrangements of heating devices
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F27FURNACES; KILNS; OVENS; RETORTS
    • F27BFURNACES, KILNS, OVENS OR RETORTS IN GENERAL; OPEN SINTERING OR LIKE APPARATUS
    • F27B17/00Furnaces of a kind not covered by any of groups F27B1/00 - F27B15/00
    • F27B17/0008Open field furnace for burning bricks
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F27FURNACES; KILNS; OVENS; RETORTS
    • F27BFURNACES, KILNS, OVENS OR RETORTS IN GENERAL; OPEN SINTERING OR LIKE APPARATUS
    • F27B9/00Furnaces through which the charge is moved mechanically, e.g. of tunnel type; Similar furnaces in which the charge moves by gravity
    • F27B9/06Furnaces through which the charge is moved mechanically, e.g. of tunnel type; Similar furnaces in which the charge moves by gravity heated without contact between combustion gases and charge; electrically heated
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F27FURNACES; KILNS; OVENS; RETORTS
    • F27DDETAILS OR ACCESSORIES OF FURNACES, KILNS, OVENS OR RETORTS, IN SO FAR AS THEY ARE OF KINDS OCCURRING IN MORE THAN ONE KIND OF FURNACE
    • F27D99/00Subject matter not provided for in other groups of this subclass
    • F27D99/0001Heating elements or systems
    • F27D99/0033Heating elements or systems using burners
    • F27D99/0035Heating indirectly through a radiant surface
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F27FURNACES; KILNS; OVENS; RETORTS
    • F27DDETAILS OR ACCESSORIES OF FURNACES, KILNS, OVENS OR RETORTS, IN SO FAR AS THEY ARE OF KINDS OCCURRING IN MORE THAN ONE KIND OF FURNACE
    • F27D7/00Forming, maintaining or circulating atmospheres in heating chambers
    • F27D7/04Circulating atmospheres by mechanical means
    • F27D2007/045Fans
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P40/00Technologies relating to the processing of minerals
    • Y02P40/60Production of ceramic materials or ceramic elements, e.g. substitution of clay or shale by alternative raw materials, e.g. ashes

Definitions

  • the invention relates to the field of technology, namely, to continuous kilns and can be used for heat treatment of building ceramic products, in particular, hollow bricks and blocks.
  • the known device for the thermal treatment of ceramic hollow products is selected as the prototype (Appendix 1 - application, Appendix 2 - translation) and consists of a main channel filled products and a circulation channel with fans that provide gas circulation by taking gas from the main channel and returning it to the main channel from the opposite side.
  • a gas circulation system is created that improves the uniformity of the heat treatment of hollow products, but has the following disadvantages.
  • the device is tasked by improving the design of the furnace by introducing additional elements to provide a predetermined and controlled mode of heating, firing and cooling of products, which will ensure strict implementation of the firing technology and, accordingly, the quality of the fired products.
  • the next objective of the invention to the device is that in the furnace by the maximum degree of heat recovery of the products of combustion, steam and air to achieve maximum savings of thermal energy used for firing ceramic products.
  • the problem is solved in that in a kiln for firing ceramic products, including a main channel filled with products and a circulation channel with gas moving devices that circulate gas by taking gas from the main channel and returning it to the main channel from the opposite side, according to the invention , the furnace is divided into sections by partitions with holes.
  • transverse partitions with openings that are capable of passing through limited gas flow and prevent intensive mixing of gas along the length of the furnace.
  • the task set as the basis of the invention is also achieved by the fact that in the partitions between the sections of the furnace, guide elements are additionally made - dampers for creating a directed gas flow between the sections, cutting off part of the circulation stream of the previous section and feeding it to the next section.
  • dampers with adjustable tilt makes it possible to change the speed and direction of gas movement between sections.
  • an intense circulating gas flow is formed in the main channel, which ensures uniform temperature in each section in width and height in the working space of the main channel and a controlled gas flow along the main channel, which reduces the firing time while improving quality products.
  • the device of the kiln for firing ceramic products has another improvement, due to which an additional technical result is obtained.
  • the next task which is the basis of the invention is achieved by the fact that in the circulation channel of the furnace is additionally installed at least one heat exchanger.
  • the heat exchanger can additionally be equipped with a fan to provide the necessary gas flow rate.
  • FIG. 1 - shows a cross section of a kiln for firing ceramic products
  • FIG. 2 execution of transverse partitions with holes in the furnace in the context of figure 1 along the section aa,
  • FIG. 3 the execution of the guide elements in the furnace in the context of figure 1 along the section aa,
  • FIG. 4 execution of the heat exchanger in the furnace in the context of figure 1 along section A-A.
  • the kiln for firing ceramic products is shown in Fig. 1 and consists of an external casing 1, a main channel 2, which is filled with hollow products 3 and a circulation channel 4, separated from the main channel 2 by partitions 5 and necessary to create an intense circulating gas flow that helps to accelerate heat transfer .
  • Fans 6 are installed in the upper part of each section of the main channel 2, for gas extraction from the upper part of the main channel 2 and its supply to the lower part through the circulation channel 4.
  • transverse partitions 7 (Fig. 2) with holes 8, while in the case of a furnace with mechanical movement of hollow products 3, the transverse partitions 7 are made of two parts: a fixed part 7, blocking the circulation channel 4 and the movable part 1a (Fig. 1) moving together with hollow articles 3.
  • inlet 9 (Fig. 2) and exhaust 10 fans can be installed.
  • a heat exchanger 12 is additionally installed, which is additionally equipped with a fan 13.
  • Heating of products can take place from any source of heat: by burning fuel, using an electric heater, or in another way.
  • the design of the kiln for firing ceramic products is applicable both to furnaces with mechanical movement of products, and to furnaces with a fixed arrangement of products.
  • the kiln for ceramic works as follows.
  • the main channel 2 is filled with hollow products 3 either in each section separately - for furnaces with a fixed arrangement of products 3, or through the outer sections - for furnaces with mechanical movement of products 3.
  • the furnace has three zones: a heating, firing and cooling zone.
  • the processes of heat and mass transfer in the furnace are similar to the processes occurring in conventional tunnel and ring furnaces. In the proposed furnace due to the presence of fans 6, the intensity of heat and mass transfer is significantly increased.
  • the heat exchange between the gas medium of the furnace (coolant) and the void products 3 (Fig. 1) within each section is due to the multiple passage of gas around and through the void products 3 by taking gas from the top part of the main channel 2 by the fan 6 and feeding it through the circulation channel 4 to the lower part of the main channel 2.
  • the transfer of thermal energy between the sections (along the main channel 2) is carried out by moving the gas (coolant) through the holes 8 (figure 2) in the partitions 7.
  • the first way to optimize the heat transfer process between sections of the furnace is done by selecting the size of the holes 8 in the partitions 7, while the gas itself is moved by creating a pressure difference between the sections, for example, fans 9 and 10.
  • the second way to optimize the heat transfer process between the sections of the furnace is done by adjusting the slope shutters 11 (Fig. 3).
  • the steam generated in the furnace, as well as the combustion products (when using fuel), by the guide flaps 11 are supplied to the furnace section from which they are taken through the heat exchanger 12, while the incoming gases are cooled in the heat exchanger 12 and the steam is partially condensed, which provides heating of the hollow products 3 (not shown conditionally), filled into the furnace.
  • a fan 13 is used to ensure the necessary gas flow through it.
  • the steam-gas mixture can be supplied to the section from which it is taken to the heat exchanger 12, can be made through openings 8 without shutters 11 due to vacuum, created by the fan 13.

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Furnace Details (AREA)
  • Tunnel Furnaces (AREA)

Abstract

The kiln for firing ceramic articles relates to a technical field, more specifically to continuous firing kilns and can be used for heat treating ceramic construction articles, in particular hollow bricks and blocks. The kiln for firing ceramic articles consists of a main channel (2) which is filled with the articles (3), and a circulation channel (4) with devices for the movement of a gas (6), which devices provide for the circulation of the gas by bleeding same from the main channel (2) and returning it to the main channel (2) from the opposite end. Furthermore, the firing kiln is divided into sections by partitions with openings. Also, the partitions between the sections are additionally provided with guide elements in the form of dampers (11) for generating a flow of gas between the sections. Additionally, a heat exchanger (12) equipped with a ventilator is situated in the circulation channel (4).

Description

Печь для обжига керамических изделий  Ceramic kiln

Область техники  Technical field

Изобретение относится к области техники, а именно, к обжиговым печам непрерывного действия и может использоваться для термической обработки строительных керамических изделий, в частности, пустотного кирпича и блоков.  The invention relates to the field of technology, namely, to continuous kilns and can be used for heat treatment of building ceramic products, in particular, hollow bricks and blocks.

Предшествующий уровень техники  State of the art

Известное устройство для термической обработки керамических пустотных изделий (патентная заявка WO 2008/063538 А2, МПК6 С04В 35/638, F27B 9/00) выбрано за прототип (дополнение 1 - заявка, дополнение 2 - перевод) и состоит из основного канала, заполняемого изделиями и циркуляционного канала с вентиляторами, обеспечивающими циркуляцию газа путём отбора газа из основного канала и возврата его в основной канал с противоположной стороны. Нужно отметить, что в известном устройстве для термической обработки пустотных изделий создаётся система циркуляции газа, которая улучшает равномерность термической обработки пустотных изделий, однако имеет следующие недостатки. The known device for the thermal treatment of ceramic hollow products (patent application WO 2008/063538 A2, IPC 6 C04B 35/638, F27B 9/00) is selected as the prototype (Appendix 1 - application, Appendix 2 - translation) and consists of a main channel filled products and a circulation channel with fans that provide gas circulation by taking gas from the main channel and returning it to the main channel from the opposite side. It should be noted that in the known device for the heat treatment of hollow products, a gas circulation system is created that improves the uniformity of the heat treatment of hollow products, but has the following disadvantages.

При созданной циркуляции газа в основном канале печи происходит и активное перемешивание потоков газа по всей длине канала, что исключает возможность нагрева, обжига и охлаждения пустотных изделий в строгом соответствии с технологией. Другим недостатком известного устройства является то, что вместе с продуктами горения из печи выводится пар, который образуется при испарении воды из загружаемых сырых изделий, при этом вместе с паром из печи выводится тепло, затраченное на парообразование. With the created gas circulation in the main channel of the furnace, there is an active mixing of gas flows along the entire length of the channel, which excludes the possibility of heating, firing and cooling of hollow products in strict accordance with technology. Another disadvantage of the known device is that, together with the combustion products, steam is removed from the furnace, which is formed during the evaporation of water from the loaded raw products, while the heat expended on steam generation is removed along with the steam from the furnace.

Раскрытие изобретения  Disclosure of invention

В основу изобретения на устройство поставлена задача путём усовершенствования конструкции печи за счёт введения дополнительных элементов обеспечить заданный и контролируемый режим нагревания, обжига и охлаждения изделий, что обеспечит строгое выполнение технологии обжига и соответственно качества обожжённых изделий.  The basis of the invention, the device is tasked by improving the design of the furnace by introducing additional elements to provide a predetermined and controlled mode of heating, firing and cooling of products, which will ensure strict implementation of the firing technology and, accordingly, the quality of the fired products.

Следующей задачей изобретения на устройство является то, что в печи путём максимальной степени рекуперации тепла продуктов горения, пара и воздуха достигнуть максимальной экономии тепловой энергии, идущей на обжиг керамических изделий. The next objective of the invention to the device is that in the furnace by the maximum degree of heat recovery of the products of combustion, steam and air to achieve maximum savings of thermal energy used for firing ceramic products.

В заявленном устройстве задача решается тем, что в печи для обжига керамических изделий, включающей основной канал, заполняемый изделиями и циркуляционный канал с устройствами перемещения газа, обеспечивающими циркуляцию газа путём отбора газа из основного канала и возврата его в основной канал с противоположной стороны, согласно изобретению, печь разделена на секции перегородками с отверстиями. In the claimed device, the problem is solved in that in a kiln for firing ceramic products, including a main channel filled with products and a circulation channel with gas moving devices that circulate gas by taking gas from the main channel and returning it to the main channel from the opposite side, according to the invention , the furnace is divided into sections by partitions with holes.

Для устранения активного перемешивания газа, являющегося теплоносителем, по длине печи установлены поперечные перегородки с отверстиями, которые способны пропускать ограниченный поток газа и препятствовать интенсивному перемешиванию газа по длине печи. To eliminate active mixing of the gas, which is a coolant, transverse partitions with openings that are capable of passing through limited gas flow and prevent intensive mixing of gas along the length of the furnace.

Задача, поставленная в основу изобретения также достигается тем, что в перегородках между секциями печи дополнительно выполнены направляющие элементы - заслонки для создания направленного потока газа между секциями, отсекающие часть циркуляционного потока предыдущей секции и подающие его в последующую секцию. Выполнение заслонок с регулируемым наклоном даёт возможность изменения скорости и направления перемещения газа между секциями.  The task set as the basis of the invention is also achieved by the fact that in the partitions between the sections of the furnace, guide elements are additionally made - dampers for creating a directed gas flow between the sections, cutting off part of the circulation stream of the previous section and feeding it to the next section. The implementation of dampers with adjustable tilt makes it possible to change the speed and direction of gas movement between sections.

Таким образом, за счёт усовершенствования конструкции печи, в основном канале образуется интенсивный циркуляционный поток газа, что обеспечивает равномерность температур в каждой секции по ширине и высоте в рабочем пространстве основного канала и управляемый поток газа вдоль основного канала, что сокращает продолжительность обжига при одновременном повышении качества продукции.  Thus, by improving the design of the furnace, an intense circulating gas flow is formed in the main channel, which ensures uniform temperature in each section in width and height in the working space of the main channel and a controlled gas flow along the main channel, which reduces the firing time while improving quality products.

Устройство печи для обжига керамических изделий имеет и другое усовершенствование, благодаря чему, получается дополнительный технический результат.  The device of the kiln for firing ceramic products has another improvement, due to which an additional technical result is obtained.

Следующая задача, которая поставлена в основу изобретения достигается тем, что в циркуляционном канале печи дополнительно установлен, по крайней мере, один теплообменник.  The next task, which is the basis of the invention is achieved by the fact that in the circulation channel of the furnace is additionally installed at least one heat exchanger.

Чтобы вернуть тепло парообразования в технологический процесс - в зону нагрева изделий, необходимо этот пар или парогазовую смесь пропустить через теплообменник, который располагается в циркуляционном канале в зоне нагрева. В этом теплообменнике происходит не только охлаждение парогазовой смеси, но и конденсация пара. Таким образом, теплота конденсации и нагретой газовой смеси используется для нагрева изделий. To return the heat of vaporization to the process - to the heating zone of products, you need this steam or pass the gas-vapor mixture through a heat exchanger, which is located in the circulation channel in the heating zone. In this heat exchanger, not only the vapor-gas mixture is cooled, but also the condensation of the vapor. Thus, the heat of condensation and heated gas mixture is used to heat products.

Теплообменник дополнительно может быть оборудован вентилятором, для обеспечения необходимой скорости прохождения газа.  The heat exchanger can additionally be equipped with a fan to provide the necessary gas flow rate.

Использование данной совокупности существенных признаков, включая отличительные, позволяет по сравнению с прототипом:Using this combination of essential features, including distinctive features, allows, in comparison with the prototype:

- обеспечить заданный и контролируемый режим нагревания, обжига и охлаждения изделий; - provide a predetermined and controlled mode of heating, firing and cooling of products;

- достигнуть максимальной экономии тепловой энергии.  - achieve maximum heat energy savings.

Описание чертежей  Description of drawings

Описание печи для обжига керамических изделий подтверждается чертежами, где на:  The description of the kiln for firing ceramic products is confirmed by the drawings, where:

фиг. 1 - изображён поперечный разрез печи для обжига керамических изделий,  FIG. 1 - shows a cross section of a kiln for firing ceramic products,

фиг. 2 - исполнение поперечных перегородок с отверстиями в печи в разрезе фиг.1 по сечению А- А,  FIG. 2 - execution of transverse partitions with holes in the furnace in the context of figure 1 along the section aa,

фиг. 3 - исполнение направляющих элементов в печи в разрезе фиг.1 по сечению А- А,  FIG. 3 - the execution of the guide elements in the furnace in the context of figure 1 along the section aa,

фиг. 4 - исполнение теплообменника в печи в разрезе фиг.1 по сечению А- А.  FIG. 4 - execution of the heat exchanger in the furnace in the context of figure 1 along section A-A.

Изобретение подробно описывается со ссылками на чертежи. Печь для обжига керамических изделий показана на фиг.1 и состоит из внешнего корпуса 1, основного канала 2, который заполняется пустотными изделиями 3 и циркуляционного канала 4, отделённого от основного канала 2 перегородками 5 и необходимого для создания интенсивного циркуляционного потока газа, способствующего ускорению теплообмена. В верхней части каждой секции основного канала 2 установлены вентиляторы 6, для отбора газа из верхней части основного канала 2 и подачи его в нижнюю часть через циркуляционный канал 4. The invention is described in detail with reference to the drawings. The kiln for firing ceramic products is shown in Fig. 1 and consists of an external casing 1, a main channel 2, which is filled with hollow products 3 and a circulation channel 4, separated from the main channel 2 by partitions 5 and necessary to create an intense circulating gas flow that helps to accelerate heat transfer . Fans 6 are installed in the upper part of each section of the main channel 2, for gas extraction from the upper part of the main channel 2 and its supply to the lower part through the circulation channel 4.

По всей длине печь разделена на секции поперечными перегородками 7 (фиг. 2) с отверстиями 8, при этом в случае выполнения печи с механическим перемещением пустотных изделий 3 поперечные перегородки 7 выполняются из двух частей: неподвижной части 7, перегораживающей циркуляционный канал 4 и подвижной части 1а (фиг.1), перемещающейся вместе с пустотными изделиями 3.  The entire length of the furnace is divided into sections by transverse partitions 7 (Fig. 2) with holes 8, while in the case of a furnace with mechanical movement of hollow products 3, the transverse partitions 7 are made of two parts: a fixed part 7, blocking the circulation channel 4 and the movable part 1a (Fig. 1) moving together with hollow articles 3.

Для обеспечения направленного перемещения газа внутри печи между секциями могут быть установлены приточные 9 (фиг. 2) и вытяжные 10 вентиляторы. To ensure the directed movement of gas inside the furnace between the sections, inlet 9 (Fig. 2) and exhaust 10 fans can be installed.

В поперечных перегородках 7 (фиг. 3) с отверстиями 8 дополнительно выполнены направляющие элементы - заслонки 1 1 с регулируемым наклоном, при этом отверстия 8 выполняются по размерам заслонок 11 и в этом случае необходимость установки вентиляторов 9 и 10 отсутствует. В циркуляционном канале 4 (фиг. 4) дополнительно установлен теплообменник 12, который дополнительно оборудован вентилятором 13. In the transverse partitions 7 (Fig. 3) with openings 8, guide elements are additionally made - shutters 1 1 with an adjustable slope, while the openings 8 are made according to the dimensions of the shutters 11 and in this case there is no need to install fans 9 and 10. In the circulation channel 4 (Fig. 4), a heat exchanger 12 is additionally installed, which is additionally equipped with a fan 13.

Нагревание изделий может проходить от любого источника тепла: путём сжигания топлива, применения электрического нагревателя или другим способом.  Heating of products can take place from any source of heat: by burning fuel, using an electric heater, or in another way.

Исполнение печи для обжига керамических изделий применимо как к печам с механическим перемещением изделий, так и к печам с неподвижным расположением изделий.  The design of the kiln for firing ceramic products is applicable both to furnaces with mechanical movement of products, and to furnaces with a fixed arrangement of products.

Вариант осуществления изобретения  An embodiment of the invention

Печь для обжига керамических изделий работает следующим образом.  The kiln for ceramic works as follows.

Заполнение основного канала 2 пустотными изделиями 3 производится либо в каждую секцию отдельно - для печей с неподвижным расположением изделий 3, либо через крайние секции - для печей с механическим перемещением изделий 3. Печь имеет три зоны: зону нагрева, обжига и охлаждения. Процессы тепло-массообмена в печи подобны процессам, происходящим в обычных туннельных и кольцевых печах. В предлагаемой печи благодаря наличию вентиляторов 6 интенсивность тепло-массообмена значительно повышается.  The main channel 2 is filled with hollow products 3 either in each section separately - for furnaces with a fixed arrangement of products 3, or through the outer sections - for furnaces with mechanical movement of products 3. The furnace has three zones: a heating, firing and cooling zone. The processes of heat and mass transfer in the furnace are similar to the processes occurring in conventional tunnel and ring furnaces. In the proposed furnace due to the presence of fans 6, the intensity of heat and mass transfer is significantly increased.

Теплообмен между газовой средой печи (теплоносителем) и пустотными изделиями 3 (фиг. 1) в пределах каждой секции осуществляется благодаря многократному прохождению газа вокруг и через пустотные изделия 3 путём отбора газа из верхней части основного канала 2 вентилятором 6 и подачи его через циркуляционный канал 4 в нижнюю часть основного канала 2. Перенос тепловой энергии между секциями (вдоль основного канала 2) осуществляется перемещением газа (теплоносителя) через отверстия 8 (фиг.2) в перегородках 7. The heat exchange between the gas medium of the furnace (coolant) and the void products 3 (Fig. 1) within each section is due to the multiple passage of gas around and through the void products 3 by taking gas from the top part of the main channel 2 by the fan 6 and feeding it through the circulation channel 4 to the lower part of the main channel 2. The transfer of thermal energy between the sections (along the main channel 2) is carried out by moving the gas (coolant) through the holes 8 (figure 2) in the partitions 7.

Первый способ оптимизации процесса теплообмена между секциями печи выполняется путём подбора размера отверстий 8 в перегородках 7, при этом само перемещение газа осуществляется путём создания разности давлений между секциями, например, вентиляторами 9 и 10. Второй способ оптимизации процесса теплообмена между секциями печи выполняется путём регулирования наклона заслонок 11 (фиг. 3).  The first way to optimize the heat transfer process between sections of the furnace is done by selecting the size of the holes 8 in the partitions 7, while the gas itself is moved by creating a pressure difference between the sections, for example, fans 9 and 10. The second way to optimize the heat transfer process between the sections of the furnace is done by adjusting the slope shutters 11 (Fig. 3).

Образующийся в печи пар, а также продукты горения (при использовании топлива) направляющими заслонками 11 (фиг. 4) подаются в секцию печи, из которой осуществляется их отбор через теплообменник 12, при этом в теплообменнике 12 происходит охлаждение входящих газов и частичная конденсация пара, что обеспечивает нагрев пустотных изделий 3 (условно не показаны), заполненных в печь. При большом перепаде давления в теплообменнике 12 для обеспечения прохождения через него необходимого потока газа используется вентилятор 13. При использовании вентилятора 13 подвод парогазовой смеси к секции, из которой производится её отбор в теплообменник 12, может производится через отверстия 8 без заслонок 11 за счёт разряжения, создаваемого вентилятором 13. Промышленная применимость The steam generated in the furnace, as well as the combustion products (when using fuel), by the guide flaps 11 (Fig. 4) are supplied to the furnace section from which they are taken through the heat exchanger 12, while the incoming gases are cooled in the heat exchanger 12 and the steam is partially condensed, which provides heating of the hollow products 3 (not shown conditionally), filled into the furnace. With a large pressure drop in the heat exchanger 12, a fan 13 is used to ensure the necessary gas flow through it. When using a fan 13, the steam-gas mixture can be supplied to the section from which it is taken to the heat exchanger 12, can be made through openings 8 without shutters 11 due to vacuum, created by the fan 13. Industrial applicability

Приведённые сведения подтверждают то, что усовершенствованная печь для обжига керамических изделий промышленно применима с использованием разных вариантов исполнения. В результате применения предлагаемых решений получены качественно обожжённые изделия за счёт строгого выполнения технологии обжига при минимальных энергетических затратах. Опытно-экспериментальный образец печи для обжига керамический изделий изготовлен, эксплуатационные характеристики которой подтвердили достижение желаемого технического результата.  The above information confirms that the advanced ceramic kiln is industrially applicable using different versions. As a result of the application of the proposed solutions, high-quality calcined products were obtained due to the strict implementation of the firing technology with minimal energy costs. A pilot sample of a ceramic products kiln was manufactured, the operational characteristics of which confirmed the achievement of the desired technical result.

Claims

Формула Formula Печь для обжига керамических изделий, включающая основной канал, заполняемый изделиями и циркуляционный канал с устройствами перемещения газа, обеспечивающими циркуляцию газа путём отбора газа из основного канала и возврата его в основной канал с противоположной стороны, отличающаяся тем, что печь разделена на секции перегородками с отверстиями.  A kiln for firing ceramic products, including a main channel filled with products and a circulation channel with gas transfer devices that provide gas circulation by taking gas from the main channel and returning it to the main channel from the opposite side, characterized in that the furnace is divided into sections by openings with openings . Печь по п.1, отличающаяся тем, что в перегородках между секциями дополнительно выполнены направляющие элементы для создания потока газа между секциями. The furnace according to claim 1, characterized in that in the partitions between the sections additionally made guide elements for creating a gas flow between the sections. Печь по п.1 , отличающаяся тем, что в циркуляционном канале дополнительно установлен, по крайней мере, один теплообменник. The furnace according to claim 1, characterized in that at least one heat exchanger is additionally installed in the circulation channel. Печь по п.З, отличающаяся тем, что теплообменник дополнительно оборудован вентилятором.  The furnace according to claim 3, characterized in that the heat exchanger is additionally equipped with a fan.
PCT/UA2012/000068 2011-09-16 2012-07-06 Kiln for firing ceramic articles Ceased WO2013039461A1 (en)

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UAA201111074 2011-09-16

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP3348943A1 (en) * 2017-01-11 2018-07-18 Wishing Star Marble Co. Ltd. Device and method for optimizing natural stone
CN108931142A (en) * 2018-05-25 2018-12-04 永济市海军新型墙材有限公司 A kind of energy-saving process method and device of energy-saving sintering kiln
RU231774U1 (en) * 2024-10-29 2025-02-11 Общество с ограниченной ответственностью "КРИП ТЕХНО" WORKING CHAMBER FOR FIRE-BURNT OF SILICON CARBIDE POWDER MIXTURE

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
SU1560960A1 (en) * 1987-03-03 1990-04-30 С.А.Вдовиченко и П.М.Анисимов Oven for firing carbonaceous materials
SU1686286A1 (en) * 1989-02-07 1991-10-23 Предприятие П/Я М-5409 Chamber furnace for calcination of carbon blanks
RU2015477C1 (en) * 1991-04-01 1994-06-30 Научно-исследовательский и проектно-конструкторский институт металлургической теплотехники цветной металлургии и огнеупоров Carbon article kiln
RU2069828C1 (en) * 1991-11-06 1996-11-27 Норск Хюдро, А.С. Annular sectional kiln for carbon blanks
WO2008063538A2 (en) * 2006-11-21 2008-05-29 Corning Incorporated Method and apparatus for thermally debinding a ceramic cellular green body

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
SU1560960A1 (en) * 1987-03-03 1990-04-30 С.А.Вдовиченко и П.М.Анисимов Oven for firing carbonaceous materials
SU1686286A1 (en) * 1989-02-07 1991-10-23 Предприятие П/Я М-5409 Chamber furnace for calcination of carbon blanks
RU2015477C1 (en) * 1991-04-01 1994-06-30 Научно-исследовательский и проектно-конструкторский институт металлургической теплотехники цветной металлургии и огнеупоров Carbon article kiln
RU2069828C1 (en) * 1991-11-06 1996-11-27 Норск Хюдро, А.С. Annular sectional kiln for carbon blanks
WO2008063538A2 (en) * 2006-11-21 2008-05-29 Corning Incorporated Method and apparatus for thermally debinding a ceramic cellular green body

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP3348943A1 (en) * 2017-01-11 2018-07-18 Wishing Star Marble Co. Ltd. Device and method for optimizing natural stone
CN108931142A (en) * 2018-05-25 2018-12-04 永济市海军新型墙材有限公司 A kind of energy-saving process method and device of energy-saving sintering kiln
RU231774U1 (en) * 2024-10-29 2025-02-11 Общество с ограниченной ответственностью "КРИП ТЕХНО" WORKING CHAMBER FOR FIRE-BURNT OF SILICON CARBIDE POWDER MIXTURE

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