WO1983001677A1 - Heating device for open kilns with revolving fire and method for implementing such device - Google Patents
Heating device for open kilns with revolving fire and method for implementing such device Download PDFInfo
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- WO1983001677A1 WO1983001677A1 PCT/FR1982/000175 FR8200175W WO8301677A1 WO 1983001677 A1 WO1983001677 A1 WO 1983001677A1 FR 8200175 W FR8200175 W FR 8200175W WO 8301677 A1 WO8301677 A1 WO 8301677A1
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- Prior art keywords
- partitions
- fuel
- gas stream
- partition
- heating device
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Classifications
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- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B35/00—Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products
- C04B35/515—Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products based on non-oxide ceramics
- C04B35/52—Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products based on non-oxide ceramics based on carbon, e.g. graphite
- C04B35/528—Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products based on non-oxide ceramics based on carbon, e.g. graphite obtained from carbonaceous particles with or without other non-organic components
- C04B35/532—Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products based on non-oxide ceramics based on carbon, e.g. graphite obtained from carbonaceous particles with or without other non-organic components containing a carbonisable binder
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F27—FURNACES; KILNS; OVENS; RETORTS
- F27B—FURNACES, KILNS, OVENS, OR RETORTS IN GENERAL; OPEN SINTERING OR LIKE APPARATUS
- F27B5/00—Muffle furnaces; Retort furnaces; Other furnaces in which the charge is held completely isolated
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F27—FURNACES; KILNS; OVENS; RETORTS
- F27B—FURNACES, KILNS, OVENS, OR RETORTS IN GENERAL; OPEN SINTERING OR LIKE APPARATUS
- F27B13/00—Furnaces with both stationary charge and progression of heating, e.g. of ring type, of type in which segmental kiln moves over stationary charge
- F27B13/06—Details, accessories, or equipment peculiar to furnaces of this type
- F27B13/12—Arrangements of heating devices
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- 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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P10/00—Technologies related to metal processing
- Y02P10/25—Process efficiency
Definitions
- the counter-current heating device which is the subject of the invention relates to so-called baking ovens with rotating fire, in which a set of chambers, often arranged in two parallel lines, is heated by gases brought to high temperature, which circulate in hollow partitions.
- These partitions which divide the rooms into compartments are themselves arranged in several rows parallel to each other and also to the lignas of rooms.
- the partitions of the same line are connected together, at their ends, to allow gases to pass through them in series.
- the products to be heated are piled up in the compartments and receive heat by conduction through the walls of the partitions.
- Such ovens are used, in particular, for cooking carbonaceous products, such as, for example, the carbon anodes of aluminum electrolysis cells.
- the carbon products are protected from oxidation by a thick layer of carbon material in small grains, which covers them and fills all the free spaces.
- the compartments remain open at the top.
- the heating of the partitions in the so-called cooking zone is carried out by means of fuel injection means placed at the top of these partitions.
- a jet of fuel such as a heavy fuel oil or a combustible gas, is thus introduced into a stream of oxidizing gas preheated beforehand, the jet of fuel or gas being oriented in the direction of flow of this oxidizing gas.
- the partitions include baffles making it possible to circulate the gases in a zig zag fashion, from top to bottom, then from bottom to top and so on.
- the heating device for a baking oven open with a rotating fire which is the subject of the invention, makes it possible to avoid or reduce the. partitions overheating in the lower area. It includes means of injecting a liquid, gaseous or even solid fuel into the interior of an oxidizing gas stream, the fuel jet (s) being oriented against the current, that is to say in a direction opposite to the direction displacement of the oxidizing gas stream.
- the invention also relates to a process which makes it possible to better distribute the deformations of the bricks which constitute the partitions, so as to prolong the life of the latter.
- Figure 1 plan view of part of a cooking oven open to rotating fire, of known type.
- Figure 2 elevation and sectional view of the oven partitions of Figure 1.
- Figure 3 elevation and sectional view of the usual arrangement of injectors on a partition of a rotary fire oven of known type.
- Figure 4 elevation view in section of the counter-current arrangement according to the invention, of the injectors on the partition of Figure 3.
- FIG. 1 which partially reproduces FIG. 1 of the cited patent
- a rotary fire baking oven comprising 60 chambers, or sections, arranged in two parallel rows of 30 chambers, 28 of which are visible on the figure.
- Each room includes six compartments side by side such as (1) in which the products to be cooked covered with a filling material are placed.
- hollow partitions such as. (2) are arranged in a line so that the gases can pass in series through the partitions forming part of the same line.
- a loop pipe (3) makes it possible to connect the gas circuits from one row to the other.
- the heating and cooling cycle of the products is carried out thanks to a so-called rotating light system which applies to a group of chambers arranged in series, in which a certain number of chambers are in preheating, some in cooking and, finally, some in cooling.
- the location of such a group in the set of chambers, which constitutes the oven, is determined by the respective connection points of the cold air inlet pipe (K), of the row of heating burners (L ) and, finally, the exhaust gas exhaust pipe (M). After a holding time of the order of 16 to 48 hours, the connection points of the air inlet (K) and outlet, burnt gas (M) pipes and the row of burners (L). This movement is carried out in the direction of travel of the air and the burnt gases. As. As shown in Figure 1, several rotating lights can run through the rooms of the same oven at the same rate.
- Figure 2 shows in section what happens inside a row of partitions forming part of the same group of rooms.
- the cold air which is introduced through the pipe (4) at the separation between the partitions (A) and (B), crosses the partition (B), then the following two ( C) and (D), which correspond to cooling chambers, which gradually heat it up.
- this air stream which has thus been preheated to around 500 ° C, passes from the partition (D) to the partition (E), an injector (5) sends a jet of fuel into this vein, in the same direction as the direction of flow of the vein
- This jet enters the partition (E) by burning on contact with very hot air which flows through this partition.
- the combustion gases pass through the partitions of the chambers (F), (G) and (H), preheating them and, finally, exit through the pipe (6) which evacuates the gases towards the chimney.
- FIG. 3 represents a hollow partition (7) comparable in principle to the partitions of FIGS. 1 and 2, which has been arranged so as to favor the heat exchanges between its walls and the gases which flow through its internal volume. Attempts have been made to obtain a gas sweep of the walls over the entire height and length of the partition. For this, there are, in the intermediate hollow space of the partition (7), vertical baffles (8), (9) and (10) sandwiched between the two large walls of the partition. These baffles therefore force the gas stream coming from the preceding partition, which enters through the connection orifice (11), to traverse the partition in a zig zag direction according to the arrows to finally exit through the orifice (12) for connection to the partition next.
- the combustion continues over a greater or lesser length of course, then the hot gases continue their zigzag course to the outlet orifice.
- a thermoelectric couple (16) for regulating the temperature is generally placed out of the direct view of the flame, behind the baffle (8) in the vicinity of the top of the cell.
- a second injector (17) is placed in the zone where the gas flow descends towards the bottom of the partition between the baffles (9) and (10). It is, in turn, regulated by a thermoelectric couple (18) separated from the burner by the partition (10). In certain cases, the thermoelectric couple (16) is eliminated and it is the thermoelectric couple (18) which regulates the two injectors (13) and (17). Tests have shown that such an arrangement of baffles, as well as injectors and their regulating torques, gives relatively favorable results with regard to the efficiency of heat exchanges, between the hot gases and the products contained in the compartments. .ts, by conduction through the cell walls.
- the temperature reached in the upper zones of the compartments is no longer sufficient for correct cooking of the products.
- the temperature measurements carried out inside the partitions by means of couples making it possible to record the temperatures reached simultaneously in several locations distributed in these partitions, revealed temperature differences of up to 150 ° C. or more between the top and the bottom of these partitions, the maximum temperatures always being reached at the bottom of the partitions, in the zones situated in the extension of the axis of the injectors.
- the device and the method according to the invention make it possible to reduce the temperature differences as well as the deformations of the partitions in a simple and effective manner.
- the heating device for a baking oven open with a revolving fire comprises hollow partitions, inside which circulates an oxidizing gas stream as well as injection means introducing a fuel into this gas stream, one at least one of these injection means being oriented so as to direct a jet of fuel against the flow of the oxidizing gas stream.
- the invention also relates to a method which makes it possible to prolong the life of the heating partitions of a baking oven open to a rotating fire, in which the length of the flame which forms at the outlet of the injector (s) is reduced. fuel placed at the upper part of these partitions, by guiding the oxidizing gas stream inside each of these partitions, so that its direction of movement is opposite to that of the fuel jets for at least part of the heating time of these partitions.
- FIG. 4 represents, without limitation, an embodiment of the new device according to the invention.
- the partition (19), whose baffles (20), (21) and (22) are arranged in the same way as in the case of the partition (7), is traversed in a zig zag by a gaseous vein which enters the partition through the orifice (23), then travels in the direction of the arrows to the outlet orifice (24) which connects the partition (19) to the partition (25).
- a fuel injector (26) which passes through the cover (27) of the partition (19), sends a jet of heavy fuel directed up and down in the area between the baffles (20) and (21), area in which the gas stream goes from bottom to top.
- thermoelectric torque for controlling and / or regulating the temperature (28) is placed at the upper part of the zone between the baffles (21) and (22), so that, thanks to the low position of the baffle ( 21), it is in view of at least part of the flame resulting from the combustion of the fuel projected from the injector (26).
- a second injector 29
- This injector is also arranged, as shown in Figure 4, so that the direction of the jet of fuel it projects, is oriented against the current of the gas stream which rises from bottom to top.
- the operation of this second injector (29) is controlled and / or regulated by a second thermoelectric couple (31), which is placed at the upper part of the next partition (25) in contact with the gas stream which leaves the partition ( 19) through the orifice (24).
- the bottom of the partitions reaches an average temperature of 1295 ° C. In fact, in many cases, this temperature exceeds 1300 ° C, and this is a cause of deformation by creep, which greatly reduces the service life.
- the average temperature is 120 ° C lower, while in the middle, this temperature is only slightly lower than the bottom.
- the bottom temperature exceeds by more than 120 ° C that which is fixed as a setpoint for regulation, which takes away from this regulation all the precision that is expected of it.
- the use of the device according to the invention makes it possible to increase the life of the partitions of these ovens by approximately 30%. Indeed, the deformation of the partitions by creep generally makes it necessary to replace them, in the case of cooking carbonaceous products, at time intervals of the order of two years.
- the use of the injection device according to the invention makes it possible to provide for an average increase of six to eight months in the life span of the birds, which represents a significant saving.
- thermocouple being isolated from the flames by a baffle, does not take into account this radiation which, on the other hand, directly affects the surrounding bricks. Against the current, on the other hand, the thermocouple is exposed to the flame, so it can receive its radiation directly.
- the flame can have a heat radiation as high as that of a fuel flame.
- the position of the thermocouple offering the exposure to the flame that allows the counter current is decisive for the precision and the sensitivity of the regulation.
- gas injectors which, in one or the other of the two positions, give a fairly little difference in temperature distribution
- the position of the injectors is changed at regular time intervals.
- one light can always be operated in one position and the other in the opposite position.
- the part of the partitions, which is the most subject to deformation is, in fact, that which is located directly under the injectors.
- the recommended arrangement then makes it possible to distribute the thermal action of the flames coming from the injectors over the whole of the partition. This results in a slowing of the deformation of the partitions over time.
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- Organic Chemistry (AREA)
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- Structural Engineering (AREA)
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- Muffle Furnaces And Rotary Kilns (AREA)
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- Vertical, Hearth, Or Arc Furnaces (AREA)
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Abstract
The heating device according to the invention relates to open kilns with revolving fire, comprising an assembly of chambers heated by gases which circulate in hollow partition walls (19, 25) which subdivide said chambers into compartments. The production of the hot gases is provided by fuel injection means (26, 29) arranged at the upper portion of the partition walls in counter current (26, 29) of the combustive gas stream, thereby allowing to improve considerably the distribution of the temperature and the regulation precision. The device applies particularly to the firing of carbon anodes used in cells for the electrolysis of aluminum.
Description
DISPOSITIF DE CHAUFFAGE POUR FOURS DE CUISSON OUVERTS A FEU TOURNANT ET PROCEDE DE MISE EN OEUVRE DE CE DISPOSITIF HEATING DEVICE FOR OPEN COOKING OVENS WITH ROTATING FIRE AND METHOD FOR IMPLEMENTING THE SAME
Le dispositif de chauffage à contre-courant, qui fait l'objet de l'in vention, concerne les fours de cuisson dits ouverts à feu tournant, dans lesquels un ensemble de chambres, souvent disposées en deux lignes parallèles, est chauffé' par des gaz portés à température élevée, qui circulent dans des cloisons creuses. Ces cloisons qui divisent les chambres en compartiments sont elles-mêmes disposées en plusieurs files parallèles entre elles et aussi aux lignas de chambres.The counter-current heating device which is the subject of the invention relates to so-called baking ovens with rotating fire, in which a set of chambers, often arranged in two parallel lines, is heated by gases brought to high temperature, which circulate in hollow partitions. These partitions which divide the rooms into compartments are themselves arranged in several rows parallel to each other and also to the lignas of rooms.
Les cloisons d'une même file sont reliées entre elles, à leurs extrémités, pour permettre aux gaz de les parcourir en série. Les produits à chauffer sont entassés dans les compartiments et reçoivent la chaleur par conduc tion à travers les parois des cloisons. De tels fours sont utilisés, en particulier, pour la cuisson des produits carbonés, tels que, par exemple, les anodes en carbone des cellules d'électrolyse de l'aluminium. Dans chaque compartiment, les produits carbonés sont protégés de l'oxydation par une épaisse couche de matière carbonée en petits grains, qui les recouvre et remplit tous les espaces libres. Les compartiments restent ouverts à la partie supérieure.The partitions of the same line are connected together, at their ends, to allow gases to pass through them in series. The products to be heated are piled up in the compartments and receive heat by conduction through the walls of the partitions. Such ovens are used, in particular, for cooking carbonaceous products, such as, for example, the carbon anodes of aluminum electrolysis cells. In each compartment, the carbon products are protected from oxidation by a thick layer of carbon material in small grains, which covers them and fills all the free spaces. The compartments remain open at the top.
L'une des difficultés importantes qu'on rencontre dans l'exploitation de tels fours est la réalisation, de façon reproductible, d'un cycle de chauf fage et de refroidissement des produits, qui permette leur' cuisson dans les conditions optimales. On connaît généralement bien le cycle de température qu'il convient d'imposer aux produits pour les cuire, mais la difficulté est d'obtenir que les produits, placés dans les différentes zones de chaque compartiment, subissent effectivement un cycle de température proche du cycle optimal.One of the major difficulties encountered in the operation of such ovens is the carrying out, in a reproducible manner, of a heating and cooling cycle of the products, which allows them to be cooked under optimal conditions. The temperature cycle that should be imposed on the products in order to cook them is generally well known, but the difficulty is to obtain that the products, placed in the different zones of each compartment, effectively undergo a temperature cycle close to the cycle. optimal.
Dans le cas de la cuisson des anodes en carbone, il est, en particulier, important que celles-ci soient portées à une température maximale d'au moins environ 1100°C pour obtenir les caractéristiques physico-chimiques souhaitées. Une surchauffe 'éventuelle des anodes placées dans les zones les plus chaudes peut entraîner une modification des caractéristiques physiques de celles-ci, par rapport aux caractéristiques de celles cuites
à des températures moins élevées. Il en résulte une hétérogénéité des caractéristiques des lots d'anodes cuites obtenues, qui a, comme on le sait, des conséquences très défavorables sur les conditions de fonctionnement des cellules d'électrolyse de l'aluminium sur lesquelles seront montées les anodes. De plus, les surchauffes non contrôlées provoquent une détérioration accélérée des réfractaires et il en résulte une déformation rapide des cloisons de chauffage, dont la durée est ainsi réduite de façon très notable.In the case of cooking carbon anodes, it is in particular important that they are brought to a maximum temperature of at least about 1100 ° C. in order to obtain the desired physicochemical characteristics. Possible overheating of the anodes placed in the hottest zones can lead to a modification of the physical characteristics of these, compared to the characteristics of those cooked at lower temperatures. This results in a heterogeneity of the characteristics of the batches of cooked anodes obtained, which, as is known, has very unfavorable consequences on the operating conditions of the aluminum electrolysis cells on which the anodes will be mounted. In addition, uncontrolled overheating causes accelerated deterioration of the refractories and this results in rapid deformation of the heating partitions, the duration of which is thus reduced very significantly.
De la façon la plus générale, le chauffage des cloisons dans la zone dite de cuisson, est effectué grâce à des moyens d'injection de combustible placés à la partie supérieure de ces cloisons.In the most general manner, the heating of the partitions in the so-called cooking zone is carried out by means of fuel injection means placed at the top of these partitions.
Un jet de combustible, tel qu'un fuel lourd ou un gaz combustible, est ainsi introduit dans un courant de gaz comburant préchauffé au préalable, le jet de fuel ou de gaz étant orienté dans le sens d'écoulement de ce gaz comburant.A jet of fuel, such as a heavy fuel oil or a combustible gas, is thus introduced into a stream of oxidizing gas preheated beforehand, the jet of fuel or gas being oriented in the direction of flow of this oxidizing gas.
Dans de nombreux cas, les cloisons comportent des chicanes permettant de faire circuler les gaz en zig zag, de haut en bas, puis de bas en haut et ainsi de suite.In many cases, the partitions include baffles making it possible to circulate the gases in a zig zag fashion, from top to bottom, then from bottom to top and so on.
L'expérience a montré que ce mode de chauffage des cloisons entraînait une surchauffe de la partie inférieure de celles-ci. Une telle surchauffe comme cela vient d'être dit, a pour conséquences, d'une part, une hétérogénéité des caractéristiques physiques des anodes qui sont cuites dans les chambres et, d'autre part, une déformation accélérée des cloisons dans la zone la plus chargée, qui réduit de façon très importante leur durée de vie.Experience has shown that this method of heating the partitions leads to overheating of the lower part thereof. Such overheating, as has just been said, has, on the one hand, a heterogeneity of the physical characteristics of the anodes which are baked in the chambers and, on the other hand, an accelerated deformation of the partitions in the most charged, which significantly reduces their lifespan.
On a donc recherché la possibilité d'éviter une telle surchauffe de ces cloisons dans la zone inférieure et, aussi, celle d'obtenir, une meilleure répartition des contraintes de déformation de ces cloisons afin de prolonger leur durée de vie de façon importante.We therefore sought the possibility of avoiding such overheating of these partitions in the lower zone and, also, that of obtaining a better distribution of the deformation stresses of these partitions in order to extend their service life significantly.
Le dispositif de chauffage pour four de cuisson ouvert à feu tournant, qui fait l'objet de l'invention, permet d'éviter ou de réduire la. surchauffe des cloisons dans la zone inférieure. Il comporte des moyens
d'injection d'un combustible liquide, gazeux ou même solide à l'intérieu d'une veine gazeuse comburante, le ou les jets de combustible étant orientés à contre-courant, c'est-à-dire dans un sens opposé au sens de déplacement de la veine gazeuse comburante.The heating device for a baking oven open with a rotating fire, which is the subject of the invention, makes it possible to avoid or reduce the. partitions overheating in the lower area. It includes means of injecting a liquid, gaseous or even solid fuel into the interior of an oxidizing gas stream, the fuel jet (s) being oriented against the current, that is to say in a direction opposite to the direction displacement of the oxidizing gas stream.
La description et les figures ci-après permettront de mieux comprendre les caractéristiques des dispositifs de chauffage des fours de cuisson ouverts à feu tournant, utilisés en général, et celles du nouveau dispositif de chauffage qui fait l'objet de l'invention. Comme on le verra par ailleurs, l'invention concerne aussi un procédé qui permet de mieux répartir les déformations des briques qui constituent les cloisons, de façon à prolonger la durée de vie de celles-ci.The description and the figures below will make it possible to better understand the characteristics of the heating devices of baking ovens open with rotating fire, used in general, and those of the new heating device which is the subject of the invention. As will be seen moreover, the invention also relates to a process which makes it possible to better distribute the deformations of the bricks which constitute the partitions, so as to prolong the life of the latter.
Figure 1 : vue en plan d'une partie d'un four de cuisson ouvert à feu tournant, de type connu.Figure 1: plan view of part of a cooking oven open to rotating fire, of known type.
Figure 2 : vue en élévation et en coupe des cloisons du four de la figure 1 . Figure 3 : vue en élévation et en coupe de la disposition habituelle des injecteurs sur une cloison d'un four à feu tournant de type connu.Figure 2: elevation and sectional view of the oven partitions of Figure 1. Figure 3: elevation and sectional view of the usual arrangement of injectors on a partition of a rotary fire oven of known type.
Figure 4 : vue en élévation et en coupe de la disposition à contre-couran suivant l'invention, des injecteurs sur la cloison de la figure 3.Figure 4: elevation view in section of the counter-current arrangement according to the invention, of the injectors on the partition of Figure 3.
Le brevet US. 2 699 931 décrit, comme le montre la figure 1 (qui reproduit partiellement la figure 1 du brevet cité) un four de cuisson à feu tournant comprenant 60 chambres, ou sections, disposées en deux rangées parallèles de 30 chambres, dont 28 sont visibles sur la figure. Chaque chambre comprend six compartiments côte à côte tels que (1) dans lesquels on place les produits à cuire recouverts par une matière de remplissage. Entre les compartiments, des cloisons creuses telles .que (2) sont disposées en file de façon que les gaz puissent parcourir en série les cloisons faisant partie d'une même file. En extrémité, une canalisation de bouclage (3) permet de raccorder les circuits de gaz d'une rangée à l'autre.The US patent. 2,699,931 describes, as shown in FIG. 1 (which partially reproduces FIG. 1 of the cited patent) a rotary fire baking oven comprising 60 chambers, or sections, arranged in two parallel rows of 30 chambers, 28 of which are visible on the figure. Each room includes six compartments side by side such as (1) in which the products to be cooked covered with a filling material are placed. Between the compartments, hollow partitions such as. (2) are arranged in a line so that the gases can pass in series through the partitions forming part of the same line. At the end, a loop pipe (3) makes it possible to connect the gas circuits from one row to the other.
En exploitation, le cycle de chauffage puis refroidissement des produits
s'effectue grâce à un système dit de feu tournant qui s'applique à un groupe de chambres disposées en série, dans lequel un certain nombre de chambres sont en préchauffage, quelques-unes en cuisson et, enfin, quelques-unes en refroidissement.In operation, the heating and cooling cycle of the products is carried out thanks to a so-called rotating light system which applies to a group of chambers arranged in series, in which a certain number of chambers are in preheating, some in cooking and, finally, some in cooling.
L'emplacement d'un tel groupe dans l'ensemble de chambres, qui constitue le four est déterminé par les points de raccordement respectifs de la canalisation d'arrivée d'air froid (K), de la rangée de brûleurs de chauffage (L) et, enfin, de la canalisation d'extraction des gaz brûlés (M). Après un temps de maintien de l'ordre de 16 à 48h, on déplace d'une chambre les points de raccordement des canalisations d'arrivée d'air (K) et de départ, des gaz brûlés (M) ainsi que la rangée de brûleurs (L). Ce déplacement est effectué dans le sens de parcours de l'air et des gaz brûlés. Comme. le montre la figure 1, plusieurs feux tournants peuvent parcourir les chambres d'un même four à la même cadence.The location of such a group in the set of chambers, which constitutes the oven, is determined by the respective connection points of the cold air inlet pipe (K), of the row of heating burners (L ) and, finally, the exhaust gas exhaust pipe (M). After a holding time of the order of 16 to 48 hours, the connection points of the air inlet (K) and outlet, burnt gas (M) pipes and the row of burners (L). This movement is carried out in the direction of travel of the air and the burnt gases. As. As shown in Figure 1, several rotating lights can run through the rooms of the same oven at the same rate.
La figure 2 représente en coupe ce qui se passe à l'intérieur d'une file de cloisons faisant partie d'un même groupe de chambres. On voit qu'une partie au moins de l'air froid qui est introduit par la canalisation (4) au niveau de la séparation entre les cloisons (A) et (B), traverse la cloison (B), puis les deux suivantes (C) et (D), qui correspondent à des chambres en refroidissement, ce qui l'échauffé progressivement. Au moment où cette veine d'air, qui a été ainsi préchauffée vers500°C, passe de la cloison (D) à la cloison (E), un injecteur (5) envoie dans cette veine un jet de fuel, dans le même sens que le sens d'écoulement de la veine Ce jet pénètre dans la cloison (E) en brûlant au contact de l'air très chaud qui parcourt cette cloison. Au-delà, les gaz de combustion traversent les cloisons des chambres (F), (G) et (H), en les préchauffant et, enfin, sortent par la canalisation (6) qui évacue les gaz en direction de la cheminée.Figure 2 shows in section what happens inside a row of partitions forming part of the same group of rooms. We see that at least part of the cold air which is introduced through the pipe (4) at the separation between the partitions (A) and (B), crosses the partition (B), then the following two ( C) and (D), which correspond to cooling chambers, which gradually heat it up. When this air stream, which has thus been preheated to around 500 ° C, passes from the partition (D) to the partition (E), an injector (5) sends a jet of fuel into this vein, in the same direction as the direction of flow of the vein This jet enters the partition (E) by burning on contact with very hot air which flows through this partition. Beyond, the combustion gases pass through the partitions of the chambers (F), (G) and (H), preheating them and, finally, exit through the pipe (6) which evacuates the gases towards the chimney.
On comprend qu'avec une disposition des brûleurs telle qu'elle est représentée sur la figure 2, il soit très difficile d'obtenir une certaine homogénéité de température de la cloison dans laquelle se produit la combustion, compte tenu de l'étroitesse relative de l'espace réservé au passage des gaz à l'intérieur de la cloison. Il est, du reste, indiqué dans le brevet cité que, pour mieux répartir les températures, on peut envisager de disposer, à l'intérieur des cloisons, des chicanes permettant
de faire circuler les gaz suivant un parcours tortueux.It will be understood that with an arrangement of the burners as shown in FIG. 2, it is very difficult to obtain a certain temperature uniformity of the partition in which combustion takes place, taking into account the relative narrowness of the space reserved for the passage of gases inside the partition. It is, moreover, indicated in the cited patent that, to better distribute the temperatures, it is possible to envisage having, inside the partitions, baffles allowing to circulate the gases following a tortuous course.
La figure 3 représente une cloison creuse (7) comparable dans son princi pe aux cloisons des figures 1 et 2, qui a été aménagée de façon à favori ser les échanges de chaleur entre ses parois et les gaz qui parcourent son volume intérieur. On a cherché à obtenir un balayage des parois par les gaz sur toute la hauteur et la longueur de la cloison. Pour cela, on dispose, dans l'espace creux intermédiaire de la cloison (7), des chicanes verticales (8), (9) et (10) enserrées entre les deux grandes parois de la cloison. Ces chicanes obligent donc la veine gazeuse provenant de la cloison précédente, qui entre par l'orifice de raccordement (11), à parcourir la cloison en zig zag suivant les flèches pour sortir finalement par l'orifice (12) de raccordement à la cloison suivante.FIG. 3 represents a hollow partition (7) comparable in principle to the partitions of FIGS. 1 and 2, which has been arranged so as to favor the heat exchanges between its walls and the gases which flow through its internal volume. Attempts have been made to obtain a gas sweep of the walls over the entire height and length of the partition. For this, there are, in the intermediate hollow space of the partition (7), vertical baffles (8), (9) and (10) sandwiched between the two large walls of the partition. These baffles therefore force the gas stream coming from the preceding partition, which enters through the connection orifice (11), to traverse the partition in a zig zag direction according to the arrows to finally exit through the orifice (12) for connection to the partition next.
L'injecteur (13), qui traverse le couvercle (14) de la cloison, pulvérise un jet de fuel dirigé de haut en bas, qui s'enflamme au contact de l'air chaud qui, après avoir pénétré par l'orifice (11), se dirige vers le bas grâce à la chicane (8) et à la paroi (15) de la cellule. Suivant les caractéristiques du fuel utilisé, la combustion se poursuit sur une longueur de parcours plus ou moins grande, puis les gaz chauds continuent leur parcours en zig zag jusqu'à l'orifice de sortie. Un couple thermoélectrique (16) de régulation de la température est généralement disposé hors de la vue directe de la flamme, derrière la chicane (8) au voisinage du haut de la cellule. Dans bien des cas, pour améliorer la réparti- tion du chauffage, un deuxième injecteur (17) est placé dans la zone où le flux gazeux redescend en direction du fond de la cloison entre les chicanes (9) et (10). Il est, à son tour, régulé par un couple thermoélectrique (18) séparé du brûleur par la cloison (10). Dans certains cas, le couple thermoélectrique (16) est supprimé et c'est le couple thermoélectrique (18) qui régule les deux injecteurs (13) et (17). Les essais ont montré qu'une telle disposition des chicanes, ainsi que des injecteurs et de leurs couples de régulation, donnait des résultats relativement favorables en ce qui concerne l'efficacité des échanges thermiques, entre les gaz chauds et les produits contenus dans les compartimen.ts, par conduction à travers les parois des cellules.The injector (13), which passes through the cover (14) of the partition, sprays a jet of fuel directed from top to bottom, which ignites on contact with hot air which, after having penetrated through the orifice ( 11), goes downwards thanks to the baffle (8) and the wall (15) of the cell. Depending on the characteristics of the fuel used, the combustion continues over a greater or lesser length of course, then the hot gases continue their zigzag course to the outlet orifice. A thermoelectric couple (16) for regulating the temperature is generally placed out of the direct view of the flame, behind the baffle (8) in the vicinity of the top of the cell. In many cases, to improve the distribution of the heating, a second injector (17) is placed in the zone where the gas flow descends towards the bottom of the partition between the baffles (9) and (10). It is, in turn, regulated by a thermoelectric couple (18) separated from the burner by the partition (10). In certain cases, the thermoelectric couple (16) is eliminated and it is the thermoelectric couple (18) which regulates the two injectors (13) and (17). Tests have shown that such an arrangement of baffles, as well as injectors and their regulating torques, gives relatively favorable results with regard to the efficiency of heat exchanges, between the hot gases and the products contained in the compartments. .ts, by conduction through the cell walls.
Par contre, de sérieuses difficultés ont été rencontrées pour obtenir verticalement une répartition homogène des températures et, plus
particulièrement, dans le cas d'un chauffage au fuel. Habituellement, on observe les températures les plus élevées au fond des cloisons et, les plus basses, au sommet. Il est clair que, dans ces conditions, les produits placés au fond atteignent un degré de cuisson plus élevé que ceux du sommet. D'autre part, en ce qui concerne les parois des cloisons, on a observé des déformations très importantes par fluage des structures en briques réfractaires qui les constituent, au voisinage du fond, c'està-dire dans la région où les briques supportent la charge de tout 1'empilement.On the other hand, serious difficulties have been encountered in obtaining a uniform temperature distribution vertically and, more particularly in the case of oil heating. Usually, the highest temperatures are observed at the bottom of the partitions and, the lowest, at the top. It is clear that, under these conditions, the products placed at the bottom reach a higher degree of cooking than those at the top. On the other hand, with regard to the walls of the partitions, very significant deformations have been observed by creep of the refractory brick structures which constitute them, in the vicinity of the bottom, that is to say in the region where the bricks support the load of the whole stack.
Si on veut éviter de telles déformations en abaissant la température de réglage, on constate que, dans bien des cas, la température atteinte dans les zones supérieures des compartiments n'est plus suffisante pour une cuisson correcte des produits. Les mesures de température effectuées à l'intérieur des cloisons, au moyen de couples permettant d'enregistrer les températures atteintes simultanément dans plusieurs emplacements répartis dans ces cloisons, ont fait apparaître des écarts de température pouvant atteindre 150°C ou davantage entre le haut et le bas de ces cloisons, les températures maximales étant toujours atteintes dans le fond des cloisons, dans les zones situées dans le prolongement de l'axe des injecteurs. On a recherché la possibilité de réduire de façon très importante les écarts de température existant entre les zones supérieures et inférieures des cloisons, sans apporter de modifications notables à la structure proprement dite de ces cloisons creuses, structure qui résulte d'une optimisation progressive basée sur une longue expérience.If one wishes to avoid such deformations by lowering the setting temperature, it can be seen that, in many cases, the temperature reached in the upper zones of the compartments is no longer sufficient for correct cooking of the products. The temperature measurements carried out inside the partitions, by means of couples making it possible to record the temperatures reached simultaneously in several locations distributed in these partitions, revealed temperature differences of up to 150 ° C. or more between the top and the bottom of these partitions, the maximum temperatures always being reached at the bottom of the partitions, in the zones situated in the extension of the axis of the injectors. We looked for the possibility of very significantly reducing the temperature differences existing between the upper and lower zones of the partitions, without making significant modifications to the structure proper of these hollow partitions, structure which results from a progressive optimization based on long experience.
Le dispositif et le procédé suivant l'invention permettent de réduire les écarts de température ainsi que les déformations des cloisons de façon simple et efficace.The device and the method according to the invention make it possible to reduce the temperature differences as well as the deformations of the partitions in a simple and effective manner.
Le dispositif de chauffage pour four de cuisson ouvert à feu tournant, suivant l'invention comporte des cloisons creuses, à l'intérieur desquelles circule une veine gazeuse comburante ainsi que des moyens d'injection introduisant un combustible dans cette veine gazeuse, l'un au moins de ces moyens d'injection étant orienté de façon à diriger un jet de combustible à contre courant de la veine gazeuse comburante.
L'invention concerne aussi un procédé qui permet de prolonger la durée de vie des cloisons chauffantes d'un four de cuisson ouvert à feu tournant, dans lequel on diminue la longueur .de la flamme qui se forme à la sortie du ou des injecteurs de combustible placés à la partie supérieu re de ces cloisons, en guidant la veine gazeuse comburante à l'intérieur de chacune de ces cloisons, de façon que son sens de déplacement soit opposé à celui du ou des jets de combustible pendant au moins une partie du temps de chauffage de ces cloisons.The heating device for a baking oven open with a revolving fire, according to the invention comprises hollow partitions, inside which circulates an oxidizing gas stream as well as injection means introducing a fuel into this gas stream, one at least one of these injection means being oriented so as to direct a jet of fuel against the flow of the oxidizing gas stream. The invention also relates to a method which makes it possible to prolong the life of the heating partitions of a baking oven open to a rotating fire, in which the length of the flame which forms at the outlet of the injector (s) is reduced. fuel placed at the upper part of these partitions, by guiding the oxidizing gas stream inside each of these partitions, so that its direction of movement is opposite to that of the fuel jets for at least part of the heating time of these partitions.
La figure 4 représente, de façon non limitative, un mode de réalisation du nouveau dispositif selon l'invention. La cloison (19), dont les chicanes (20), (21) et (22) sont disposées de la même façon que dans le cas de la cloison (7), est parcourue en zig zag par une veine gazeuse qui entre dans la cloison par l'orifice (23), puis la parcourt suivant le sens des flèches jusqu'à l'orifice de sortie (24) qui raccorde la cloison (19) à la cloison (25). Un injecteur de combustible (26), qui traverse le couvercle (27) de la cloison (19), envoie un jet de fuel lourd dirigé de haut en bas dans la zone comprise entre les chicanes (20) et (21), zone dans laquelle la veine gazeuse se dirige de bas en haut. Le couple thermoélectrique de contrôle et/ou de régulation de la température (28) est placé à la partie supérieure de la zone comprise entre les chicanes (21) et (22), de façon que, grâce à la position basse de la chicane (21), il soit en vue d'une partie au moins de la flamme résultant de la combustion du combustible projeté à partir de l'injecteur (26).FIG. 4 represents, without limitation, an embodiment of the new device according to the invention. The partition (19), whose baffles (20), (21) and (22) are arranged in the same way as in the case of the partition (7), is traversed in a zig zag by a gaseous vein which enters the partition through the orifice (23), then travels in the direction of the arrows to the outlet orifice (24) which connects the partition (19) to the partition (25). A fuel injector (26), which passes through the cover (27) of the partition (19), sends a jet of heavy fuel directed up and down in the area between the baffles (20) and (21), area in which the gas stream goes from bottom to top. The thermoelectric torque for controlling and / or regulating the temperature (28) is placed at the upper part of the zone between the baffles (21) and (22), so that, thanks to the low position of the baffle ( 21), it is in view of at least part of the flame resulting from the combustion of the fuel projected from the injector (26).
Comme le montre également la figure 4, il est possible de placer dans la même cloison un deuxième injecteur (29), dans la zone comprise entre la chicane (22) et la paroi (30), qui sépare la cloison (19) de la cloison suivante (25). Cet injecteur est également disposé, comme le montre la figure 4, de façon que le sens du jet de combustible qu'il projette, soit orienté à contre courant de la veine gazeuse qui remonte de bas en haut. Le fonctionnement de ce deuxième injecteur (29) est contrôlé et/ou régulé par un deuxième couple thermoélectrique (31), qui est placé à la partie supérieure de la cloison suivante (25) en contact avec la veine gazeuse gui sort de la cloison (19) par l'orifice (24).As also shown in Figure 4, it is possible to place in the same partition a second injector (29), in the area between the baffle (22) and the wall (30), which separates the partition (19) from the next partition (25). This injector is also arranged, as shown in Figure 4, so that the direction of the jet of fuel it projects, is oriented against the current of the gas stream which rises from bottom to top. The operation of this second injector (29) is controlled and / or regulated by a second thermoelectric couple (31), which is placed at the upper part of the next partition (25) in contact with the gas stream which leaves the partition ( 19) through the orifice (24).
Des essais pratiques d'exploitation ont été effectués sur un même four de cuisson à feu tournant, comportant des chambres équipées de cloisons
du type représenté aux figures 3 et 4, et comportant soit des dispositifs classiques d'injection de combustible dans les cloisons des chambres en cuisson, comme ceux représentés à la figure 3, soit, au contraire, des dispositifs d'injection à contre courant suivant l'invention, comme ceux représentés à la figure 4. Le combustible utilisé était un fuel lourd. Les cloisons avaient environ 4,5 m de hauteur et 5 m de longueur pour une largeur intérieure de 0,250 m.Practical operating tests were carried out on the same baking oven on a rotating fire, comprising chambers equipped with partitions of the type represented in FIGS. 3 and 4, and comprising either conventional devices for injecting fuel into the partitions of the cooking chambers, like those represented in FIG. 3, or, on the contrary, injection devices against the current the invention, like those shown in FIG. 4. The fuel used was a heavy fuel. The partitions were approximately 4.5 m high and 5 m long with an internal width of 0.250 m.
Les essais comparatifs de cuisson de produits carbonés ont montré que, toutes choses égales par ailleurs, les températures des parois des cloisons sont beaucoup mieux réparties en utilisant le nouveau dispositif d'injection à contre courant suivant l'invention.The comparative tests for cooking carbonaceous products have shown that, all other things being equal, the temperatures of the walls of the partitions are much better distributed using the new injection device against the current according to the invention.
Les mesures de température ont été effectuées au voisinage de l'axe des injecteurs dans la paroi réfractaire de la cloison, en haut de celle-ci, à mi-hauteur et en bas. Le tableau ci-après donne les résultats obtenus :The temperature measurements were carried out in the vicinity of the axis of the injectors in the refractory wall of the partition, at the top thereof, halfway up and at the bottom. The table below gives the results obtained:
On voit que, dans le dispositif classique, le bas des cloisons atteint une température moyenne de 1295°C. En fait, dans bien des cas, cette température dépasse 1300°C, et ceci est une cause de déformation par fluage, qui réduit de façon très importante la durée de vie. Dans le haut de la cloison, la température moyenne est inférieure de 120°C, tandis que, au milieu, cette température est seulement légèrement inférieure à celle du bas. On constate aussi que la température du fond dépasse de plus de 120°C celle qui est fixée comme consigne à la régulation, ce qui enlève à cette régulation toute la précision que l'on attend d'elle. We see that, in the conventional device, the bottom of the partitions reaches an average temperature of 1295 ° C. In fact, in many cases, this temperature exceeds 1300 ° C, and this is a cause of deformation by creep, which greatly reduces the service life. At the top of the partition, the average temperature is 120 ° C lower, while in the middle, this temperature is only slightly lower than the bottom. We also note that the bottom temperature exceeds by more than 120 ° C that which is fixed as a setpoint for regulation, which takes away from this regulation all the precision that is expected of it.
Au contraire, dans le cas du fonctionnement à contre courant, les températures des cloisons, en haut et en bas, sont pratiquement égales, tandis qu'à mi-hauteur, la température est supérieure d'environ une centaine de degrés. Une telle répartition des températures est beaucoup plus favorable. En effet, la partie basse de la tloison, dans laquelle les briques supportent la plus forte charge, se trouve alors à une température plus faible qu'à mi-hauteur, et résiste donc beaucoup mieux au fluage. Par ailleurs, la zone supérieure, qui est généralement trop froide, se trouve à une température au moins égale à celle du fond, ce qui est particulièrement favorable pour l'homogénéité de la cuisson. Enfin, on a constaté que la disposition adoptée pour les thermocouples de régulation, exposant ceux-ci à une partie des flammes d'injection, améliore considérablement la précision et la sensibilité de l'équipement de régulation.On the contrary, in the case of counter-current operation, the temperatures of the partitions, above and below, are practically equal, while at mid-height, the temperature is approximately one hundred degrees higher. Such a distribution of temperatures is much more favorable. Indeed, the lower part of the partition, in which the bricks support the highest load, is then at a lower temperature than at mid-height, and therefore resists creep much better. Furthermore, the upper zone, which is generally too cold, is at a temperature at least equal to that of the bottom, which is particularly favorable for the homogeneity of the cooking. Finally, it has been found that the arrangement adopted for regulating thermocouples, exposing them to part of the injection flames, considerably improves the precision and sensitivity of the regulating equipment.
Les essais ont montré que l'utilisation du dispositif suivant l'invention permet d'augmenter de 30 % environ la durée de vie des cloisons de ces fours. En effet, la déformation des cloisons par fluage rend généralement nécessaire leur remplacement, dans le cas de la cuisson des produits carbonés, à des intervalles de temps de l'ordre de deux années. L'utilisation du dispositif d'injection suivant l'invention permet de prévoir une augmentation moyenne de six à huit mois de la durée de vie des d'oisons, ce qui représente une économie importante.Tests have shown that the use of the device according to the invention makes it possible to increase the life of the partitions of these ovens by approximately 30%. Indeed, the deformation of the partitions by creep generally makes it necessary to replace them, in the case of cooking carbonaceous products, at time intervals of the order of two years. The use of the injection device according to the invention makes it possible to provide for an average increase of six to eight months in the life span of the birds, which represents a significant saving.
Cet avantage de l'injection à contre courant est particulièrement important quand on utilise des fuels lourds du type de celui qui correspond à l'essai décrit. En effet, lorsqu'on injecte de tels fuels dans le sens du courant gazeux, la surchauffe des bas de cloisons est particulièrement
élevée. Ceci est dû à la combustion lente de ces fuels dont la température de vaporisation est élevée. L'effet du contre courant qui freine considérablement la chute des gouttelettes de fuel est particulièrement sensible. D'autre part, dans le cas du fuel, une grande partie de la chaleur est émise par le rayonnement de la flamme.This advantage of injection against the current is particularly important when using heavy fuels of the type which corresponds to the test described. Indeed, when injecting such fuels in the direction of the gas flow, the overheating of the bottom of the partitions is particularly high. This is due to the slow combustion of these fuels whose vaporization temperature is high. The effect of the counter current, which considerably slows the fall of fuel droplets, is particularly noticeable. On the other hand, in the case of fuel oil, a large part of the heat is emitted by the radiation of the flame.
Dans le cas de la disposition classique, le thermocouple étant isolé des flammes par une chicane, ne prend pas en compte ce rayonnement qui, par contre, affecte directement les briques environnantes. A contre courant, par contre, le thermocouple est exposé à la flamme, il peut ainsi recevoir, de façon directe, son rayonnement.In the case of the conventional arrangement, the thermocouple being isolated from the flames by a baffle, does not take into account this radiation which, on the other hand, directly affects the surrounding bricks. Against the current, on the other hand, the thermocouple is exposed to the flame, so it can receive its radiation directly.
L'avantage de l'injection à contre courant suivant l'invention, quoique moins important, est également observé dans le cas de l'injection de fuels plus légers, et aussi, quoique de façon nettement moins sensible, dans le cas de l'injection de combustibles gazeux tels que, par exemple, le gaz naturel. Dans le cas du gaz naturel, le problème posé par la vaporisation lente des gouttelettes d'hydrocarbures n'existe pas en effet, et l'on observe verticalement une distribution des températures plus régulière.The advantage of the injection against the current according to the invention, although less significant, is also observed in the case of the injection of lighter fuels, and also, although clearly less appreciably, in the case of the injection of gaseous fuels such as, for example, natural gas. In the case of natural gas, the problem posed by the slow vaporization of the droplets of hydrocarbons does not in fact exist, and a more regular distribution of temperatures is observed vertically.
Cependant, suivant le type d' injecteur à gaz utilisé, la flamme peut avoir un rayonnement calorifique aussi élevé que celui d'une flamme de fuel. Dans ce cas, la position du thermocouple offrant l'exposition à la flamme que permet le contre courant, est décisive pour la précision et la sensibilité de la régulation.However, depending on the type of gas injector used, the flame can have a heat radiation as high as that of a fuel flame. In this case, the position of the thermocouple offering the exposure to the flame that allows the counter current, is decisive for the precision and the sensitivity of the regulation.
Dans le cas où sont utilisée des injecteurs à gaz qui, dans l'une ou l'autre des deux positions, donnent une répartition des températures assez peu différente, il est cependant intéressant, pour prolonger la durée de vie des cloisons, d'utiliser simultanément les deux modes de combustion, les injecteurs étant disposés alternativement dans le sens du courant ou à contre courant.In the case where gas injectors are used which, in one or the other of the two positions, give a fairly little difference in temperature distribution, it is however advantageous, in order to prolong the service life of the partitions, to use simultaneously the two combustion modes, the injectors being arranged alternately in the direction of the current or against the current.
Dans le cas où le four comporte un seul feu, on modifie à intervalles de temps réguliers la position des injecteurs.
Dans le cas d'un four à plusieurs feux, on peut faire fonctionner systématiquement un feu dans une position, et l'autre, dans la position contraire. La partie des cloisons, qui est la plus sujette aux déformations, est, en effet, celle qui se trouve directement sous les injecteurs. La disposition préconisée permet alors de répartir l'action thermique des flammes issues des injecteurs sur l'ensemble de la cloison. Il en résulte un ralentissement de la déformation des cloisons dans le temps.In the case where the oven has only one fire, the position of the injectors is changed at regular time intervals. In the case of an oven with several lights, one light can always be operated in one position and the other in the opposite position. The part of the partitions, which is the most subject to deformation, is, in fact, that which is located directly under the injectors. The recommended arrangement then makes it possible to distribute the thermal action of the flames coming from the injectors over the whole of the partition. This results in a slowing of the deformation of the partitions over time.
D'autres modes de réalisation du dispositif d'injection à contre courant pour four de cuisson ouvert à feu tournant peuvent être envisagés, qui ne sortent pas du domaine de l'invention. De même, de nombreux procédés peuvent être envisagés pour utiliser ce dispositif' dans des conditions permettant une meilleure répartition des températures dans ce type de four, une moindre déformation des cloisons chauffantes, ou encore une meilleure répartition des déformations de ces cloisons conduisant à une plus grande durée de vie de celles-ci. Tous ces procédés' font également partie de l'invention.
Other embodiments of the counter-current injection device for a baking oven open with a rotating fire can be envisaged, which do not depart from the field of the invention. Likewise, numerous methods can be envisaged for using this device under conditions allowing a better distribution of temperatures in this type of oven, less deformation of the heating partitions, or even a better distribution of the deformations of these partitions leading to a more long service life of these. All these methods are also part of the invention.
Claims
REVENDICATIONS
1°/ - Dispositif de chauffage pour four de cuisson ouvert à feu tournant, comportant des cloisons creuses (19,25) à l'intérieur desquelles circule une veine gazeuse comburante, des moyens d'injection (26, 29) introduisant un combustible dans cette veine gazeuse, caractérisé en ce que, au moins un moyen d'injection (26, 29) est orienté de façon à diriger un jet de combustible à contre courant de la veine gazeuse comburante.1 ° / - Heating device for a baking oven open with a rotating fire, comprising hollow partitions (19,25) inside which circulates an oxidizing gas stream, injection means (26, 29) introducing a fuel into this gas stream, characterized in that at least one injection means (26, 29) is oriented so as to direct a jet of fuel against the current of the oxidizing gas stream.
2°/ - Dispositif de chauffage suivant renvendication 1, caractérisé en ce que le moyen d'injection est disposé à la partie supérieure d'une cloison (19) et dirige un jet de combustible vers le bas.2 ° / - Heating device according to claim 1, characterized in that the injection means is disposed at the upper part of a partition (19) and directs a jet of fuel downwards.
3°/ - Dispositif de chauffage suivant revendication 1 ou 2, caractérisé en ce que le combustible est gazeux, liquide ou solide.3 ° / - Heating device according to claim 1 or 2, characterized in that the fuel is gaseous, liquid or solid.
4°/ - Dispositif de chauffage suivant l'une des revendications 1 à 3, caractérisé en ce que la veine gazeuse est guidée à l'intérieur d'-une cloison creuse par des chicanes (20, 21, 22).4 ° / - Heating device according to one of claims 1 to 3, characterized in that the gas stream is guided inside a hollow partition by baffles (20, 21, 22).
5°/ - Dispositif de chauffage suivant l'une des revendications 1 à 4, caractérisé en ce qu'un moyen de contrôle et/ou de réglage de la température (28,31) est disposé en vue d'une partie au moins de la flamme produite par la combustion.5 ° / - Heating device according to one of claims 1 to 4, characterized in that a means for controlling and / or adjusting the temperature (28,31) is arranged for at least part of the flame produced by combustion.
6°/ Procédé permettant de prolonger la durée de vie des cloisons chauffantes d'un four, de cuisson ouvert à feu tournant, caractérisé en ce que l'on diminue la longueur de la flamme qui se forme à la sortie du ou des injecteurs de combustible placés à la partie supérieure de ces cloisons, en guidant la veine gazeuse comburante à l'intérieur de chacune.de ces cloisons, de façon que son sens de déplacement soit opposé à celui du ou des jets de combustible pendant au moins une partie du temps de chauffage de ces cloisons.6 ° / Method for extending the life of the heating partitions of an oven, cooking open to rotating fire, characterized in that one decreases the length of the flame which is formed at the outlet of the injector (s) fuel placed at the upper part of these partitions, guiding the oxidizing gas stream inside each of these partitions, so that its direction of movement is opposite to that of the fuel jets for at least part of the heating time of these partitions.
7°/ - Procédé suivant la revendication 6, caractérisé en ce que, au cours de la durée de vie des cloisons chauffantes, on déplace le ou les injecteurs de combustible de façon que le ou les jets de combustible soient dirigés tantôt dans le sens du courant de la veine gazeuse comburante,
tantôt à contre courant de celle-ci.7 ° / - A method according to claim 6, characterized in that, during the life of the heating partitions, the fuel injector (s) is moved so that the fuel jets are directed in the direction of current of the oxidizing gas stream, sometimes against the current of it.
8°/ - Anodes en carbone pour cellules d'électrolyse de l'aluminium cuites par le procédé suivant l'invention.
8 ° / - Carbon anodes for aluminum electrolysis cells baked by the process according to the invention.
Priority Applications (6)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
HU8345A HU195881B (en) | 1981-10-29 | 1982-10-27 | Heating equipment for open combustion furnaces of circulation firing |
HU8345A HUT43712A (en) | 1981-10-29 | 1982-10-27 | Heating equipment for open combustion furnaces of circulation firing |
BR8207946A BR8207946A (en) | 1981-10-29 | 1982-10-27 | HEATING DEVICE FOR OPEN COOKING OVENS WITH ROTARY FLAME AND APPLICATION PROCESS FOR THIS DEVICE |
DE8282903243T DE3271846D1 (en) | 1981-10-29 | 1982-10-27 | Heating device for open kilns with revolving fire and method for implementing such device |
NO83832349A NO158238C (en) | 1981-10-29 | 1983-06-28 | PROCEDURE FOR EXTENDING THE OPERATING LIFE OF THE HEATED WALLS IN AN APEN BURN OVEN AND A DEVICE FOR IMPLEMENTING THE PROCEDURE. |
IN742/MAS/85A IN166179B (en) | 1981-10-29 | 1985-09-23 |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR81/20613811029 | 1981-10-29 | ||
FR8120613A FR2515799B1 (en) | 1981-10-29 | 1981-10-29 | HEATING DEVICE FOR OPEN BAKING OVENS WITH A ROTATING FIRE AND METHOD FOR IMPLEMENTING THE SAME |
Publications (1)
Publication Number | Publication Date |
---|---|
WO1983001677A1 true WO1983001677A1 (en) | 1983-05-11 |
Family
ID=9263659
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/FR1982/000175 WO1983001677A1 (en) | 1981-10-29 | 1982-10-27 | Heating device for open kilns with revolving fire and method for implementing such device |
Country Status (24)
Country | Link |
---|---|
US (1) | US4504219A (en) |
EP (1) | EP0091935B1 (en) |
JP (1) | JPS58501785A (en) |
KR (1) | KR840002096A (en) |
AU (1) | AU547624B2 (en) |
BR (1) | BR8207946A (en) |
CA (1) | CA1200449A (en) |
DE (1) | DE3271846D1 (en) |
ES (2) | ES516906A0 (en) |
FR (1) | FR2515799B1 (en) |
GR (1) | GR77696B (en) |
HR (1) | HRP920436A2 (en) |
HU (2) | HUT43712A (en) |
IN (2) | IN157081B (en) |
IS (1) | IS1239B6 (en) |
MX (1) | MX157445A (en) |
NO (1) | NO158238C (en) |
NZ (1) | NZ202267A (en) |
OA (1) | OA07242A (en) |
PL (1) | PL134949B1 (en) |
RO (1) | RO87865A (en) |
SI (1) | SI8212408A (en) |
WO (1) | WO1983001677A1 (en) |
YU (1) | YU240882A (en) |
Families Citing this family (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR920004473B1 (en) * | 1986-06-17 | 1992-06-05 | 알루미늄 뻬쉬니 | Apparatus and process for optimising combustion in chamber type furnace for baking carbonaceous blocks |
FR2600151B1 (en) * | 1986-06-17 | 1988-08-26 | Pechiney Aluminium | ADJUSTABLE NIPPLE PIPES FOR CARBON BLOCK COOKING OVENS |
FR2777072B1 (en) * | 1998-04-03 | 2000-05-19 | Pechiney Aluminium | METHOD AND DEVICE FOR REGULATING ROTATING FIRE COOKING OVENS |
US7104789B1 (en) * | 2005-03-17 | 2006-09-12 | Harbison-Walker Refractories Company | Wall structure for carbon baking furnace |
DE102009046937B4 (en) * | 2009-11-20 | 2019-12-05 | Innovatherm Prof. Dr. Leisenberg Gmbh + Co. Kg | Method and device for the production of anodes |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE693298C (en) * | 1935-05-22 | 1940-07-05 | Alfred Ruemcke | Monitoring device for pressure-fired furnace systems, especially brick kilns |
US2699931A (en) * | 1951-08-06 | 1955-01-18 | Kaiser Aluminium Chem Corp | Heat treatment of shaped bodies |
FR1404628A (en) * | 1964-05-22 | 1965-07-02 | Pechiney | New baking oven with rotating fire |
US3975149A (en) * | 1975-04-23 | 1976-08-17 | Aluminum Company Of America | Ring furnace |
Family Cites Families (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5013288A (en) * | 1973-06-08 | 1975-02-12 | ||
US4040778A (en) * | 1975-04-09 | 1977-08-09 | Refractory Services International Limited | Baking pit furnaces |
US4382778A (en) * | 1981-09-04 | 1983-05-10 | Noranda Mines Limited | Method and apparatus for reducing excess air inleakage into an open ring-type carbon baking furnace |
-
1981
- 1981-10-29 FR FR8120613A patent/FR2515799B1/en not_active Expired
-
1982
- 1982-10-22 NZ NZ202267A patent/NZ202267A/en unknown
- 1982-10-23 IN IN1265/CAL/82A patent/IN157081B/en unknown
- 1982-10-25 IS IS2759A patent/IS1239B6/en unknown
- 1982-10-25 GR GR69632A patent/GR77696B/el unknown
- 1982-10-26 PL PL1982238736A patent/PL134949B1/en unknown
- 1982-10-27 SI SI8212408A patent/SI8212408A/en unknown
- 1982-10-27 DE DE8282903243T patent/DE3271846D1/en not_active Expired
- 1982-10-27 HU HU8345A patent/HUT43712A/en unknown
- 1982-10-27 US US06/515,042 patent/US4504219A/en not_active Expired - Lifetime
- 1982-10-27 EP EP82903243A patent/EP0091935B1/en not_active Expired
- 1982-10-27 JP JP57503258A patent/JPS58501785A/en active Pending
- 1982-10-27 YU YU02408/82A patent/YU240882A/en unknown
- 1982-10-27 WO PCT/FR1982/000175 patent/WO1983001677A1/en active IP Right Grant
- 1982-10-27 HU HU8345A patent/HU195881B/en not_active IP Right Cessation
- 1982-10-27 MX MX194945A patent/MX157445A/en unknown
- 1982-10-27 AU AU90533/82A patent/AU547624B2/en not_active Expired
- 1982-10-27 BR BR8207946A patent/BR8207946A/en not_active IP Right Cessation
- 1982-10-28 CA CA000414412A patent/CA1200449A/en not_active Expired
- 1982-10-28 ES ES516906A patent/ES516906A0/en active Granted
- 1982-10-29 KR KR1019820004879A patent/KR840002096A/en unknown
- 1982-10-29 OA OA57835A patent/OA07242A/en unknown
-
1983
- 1983-05-28 RO RO83111098A patent/RO87865A/en unknown
- 1983-06-28 NO NO83832349A patent/NO158238C/en not_active IP Right Cessation
- 1983-08-10 ES ES524850A patent/ES8404498A1/en not_active Expired
-
1985
- 1985-09-23 IN IN742/MAS/85A patent/IN166179B/en unknown
-
1992
- 1992-09-23 HR HR920436A patent/HRP920436A2/en not_active Application Discontinuation
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE693298C (en) * | 1935-05-22 | 1940-07-05 | Alfred Ruemcke | Monitoring device for pressure-fired furnace systems, especially brick kilns |
US2699931A (en) * | 1951-08-06 | 1955-01-18 | Kaiser Aluminium Chem Corp | Heat treatment of shaped bodies |
FR1404628A (en) * | 1964-05-22 | 1965-07-02 | Pechiney | New baking oven with rotating fire |
US3975149A (en) * | 1975-04-23 | 1976-08-17 | Aluminum Company Of America | Ring furnace |
Also Published As
Publication number | Publication date |
---|---|
OA07242A (en) | 1984-04-30 |
DE3271846D1 (en) | 1986-07-31 |
MX157445A (en) | 1988-11-23 |
KR840002096A (en) | 1984-06-11 |
FR2515799A1 (en) | 1983-05-06 |
FR2515799B1 (en) | 1986-04-04 |
NO832349L (en) | 1983-06-28 |
IN157081B (en) | 1986-01-11 |
IN166179B (en) | 1990-03-24 |
AU547624B2 (en) | 1985-10-24 |
HUT43712A (en) | 1987-11-30 |
RO87865B (en) | 1985-10-31 |
EP0091935A1 (en) | 1983-10-26 |
PL238736A1 (en) | 1983-06-06 |
RO87865A (en) | 1985-11-30 |
HRP920436A2 (en) | 1995-08-31 |
YU240882A (en) | 1985-03-20 |
IS2759A7 (en) | 1983-04-30 |
SI8212408A (en) | 1995-08-31 |
JPS58501785A (en) | 1983-10-20 |
ES524850A0 (en) | 1984-05-01 |
ES8401612A1 (en) | 1983-12-01 |
EP0091935B1 (en) | 1986-06-25 |
NZ202267A (en) | 1986-03-14 |
ES516906A0 (en) | 1983-12-01 |
CA1200449A (en) | 1986-02-11 |
ES8404498A1 (en) | 1984-05-01 |
HU195881B (en) | 1988-07-28 |
NO158238C (en) | 1988-08-03 |
BR8207946A (en) | 1983-09-20 |
IS1239B6 (en) | 1986-11-03 |
NO158238B (en) | 1988-04-25 |
GR77696B (en) | 1984-09-25 |
AU9053382A (en) | 1983-05-18 |
US4504219A (en) | 1985-03-12 |
PL134949B1 (en) | 1985-09-30 |
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