WO2011027042A1 - Methode de caracterisation de la combustion dans des lignes de cloisons d'un four a chambres a feu(x) tournant(s) - Google Patents
Methode de caracterisation de la combustion dans des lignes de cloisons d'un four a chambres a feu(x) tournant(s) Download PDFInfo
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- WO2011027042A1 WO2011027042A1 PCT/FR2009/051682 FR2009051682W WO2011027042A1 WO 2011027042 A1 WO2011027042 A1 WO 2011027042A1 FR 2009051682 W FR2009051682 W FR 2009051682W WO 2011027042 A1 WO2011027042 A1 WO 2011027042A1
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- combustion
- partitions
- line
- incomplete
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Classifications
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F27—FURNACES; KILNS; OVENS; RETORTS
- F27D—DETAILS OR ACCESSORIES OF FURNACES, KILNS, OVENS, OR RETORTS, IN SO FAR AS THEY ARE OF KINDS OCCURRING IN MORE THAN ONE KIND OF FURNACE
- F27D19/00—Arrangements of controlling devices
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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
- F27B13/14—Arrangement of controlling, monitoring, alarm or like devices
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F27—FURNACES; KILNS; OVENS; RETORTS
- F27D—DETAILS OR ACCESSORIES OF FURNACES, KILNS, OVENS, OR RETORTS, IN SO FAR AS THEY ARE OF KINDS OCCURRING IN MORE THAN ONE KIND OF FURNACE
- F27D21/00—Arrangements of monitoring devices; Arrangements of safety devices
- F27D21/04—Arrangements of indicators or alarms
Definitions
- Fire (s) turning (s) for the firing of carbonaceous blocks, more particularly carbon anodes and cathodes for the production by electrolysis of aluminum, and the invention more particularly relates to a method characterizing combustion in partition lines of such a chamber furnace.
- Fire furnaces (x) rotating (s) for baking anodes are described in particular in the following patent documents: US 4,859,175, WO 91/19147, US 6,339,729, US 6,436,335 and CA 2550880, to which reference will be made for more details about them.
- FIGS. 1 and 2 respectively showing a schematic plan view of the structure of a furnace (x) rotating (s) and open chambers, at two lights in this example, for Figure 1, and a partial perspective view and cutaway cross-section showing the internal structure of such an oven, for Figure 2.
- the baking oven (FAC) 1 comprises two parallel casings or bays 1a and 1b, extending along the longitudinal axis XX along the length of the oven 1 and each comprising (e) a succession of transverse chambers 2 (perpendicular to the axis XX), separated from each other by transverse walls 3.
- Each chamber 2 is constituted, in its length, that is to say in the transverse direction of the furnace 1, by the juxtaposition, alternately, of 4 cells, open at their upper part, to allow the loading of the carbonaceous blocks to be cooked and the unloading of the cooled cooked blocks, and in which are stacked the carbonaceous blocks 5 to be embedded in a carbonaceous dust, and hollow-walled hollow heating partitions 6, generally kept spaced apart by transverse spacers 6a.
- the hollow partitions 6 of a chamber 2 are in the longitudinal extension (parallel to the major axis XX of the furnace 1) of the hollow partitions 6 of the other chambers 2 of the same span 1a or 1b, and the hollow partitions 6 are in communication with each other through skylights 7 at the upper part of their longitudinal walls, facing longitudinal passages formed at this level in the transverse walls 3, so that the hollow partitions 6 form rows of longitudinal partitions, arranged parallel to the XX axis of the furnace and in which will circulate gaseous fluids (combustion air, combustible gases and gases and combustion fumes) for preheating and cooking the anodes 5, and then cooling.
- gaseous fluids combustion air, combustible gases and gases and combustion fumes
- the hollow partitions 6 further include baffles 8, to elongate and distribute more uniformly the path of the combustion gases or fumes, and these hollow partitions 6 are provided at their upper part with openings 9, called “openings", closable by removable covers and arranged in an oven crown block 1.
- the two bays 1a and 1b of the furnace 1 are placed in communication at their longitudinal ends by turning flues 10, which make it possible to transfer the gaseous fluids from one end of each line of hollow partitions 6 of a span 1 a or 1b at the end of the line of corresponding hollow partitions 6 on the other bay 1b or 1a, so as to form substantially rectangular loops of hollow partition lines 6.
- fire advance (x) furnaces consists in causing a flame front to move from one chamber 2 to another which is adjacent during a cycle, each chamber 2 undergoing successively stages of preheating, forced heating, fire, then cooling (natural then forced).
- the firing of the anodes 5 is carried out by one or more lights or groups of lights (two groups of lights being represented in FIG. 1, in a position in which one extends, in this example, over thirteen chambers 2 of the span 1a and the other on thirteen chambers 2 of the span 1b) which move cyclically from chamber 2 to chamber 2.
- Each fire or group of lights is composed of five successive zones A to E, which are, as shown on FIG. 1 for the fire of the span 1b, and of the downstream upstream with respect to the flow direction of the gaseous fluids in the hollow partition lines 6, and in the opposite direction to the cyclic chamber displacements in bedroom :
- a preheating zone comprising, referring to the light of span 1a, and taking into account the direction of rotation of the lights indicated by the arrow at the turning flue 10 at the end of the furnace 1 at the top of Figure 1:
- a suction ramp 1 1 equipped, for each hollow partition 6 of the chamber 2 above which this suction ramp extends, with a system for measuring and regulating the flow rate of the gases and combustion fumes by line of hollow partitions 6,
- this system may comprise, in each suction pipe 1 1 a which is integral with the suction ramp 1 1 and opening into the latter, on the one hand, and, secondly, engaged in the opening 9 of one respectively of the hollow partitions 6 of this chamber 2, an adjustable shutter pivoted by a shutter actuator, for the flow control, and a flowmeter 12, slightly upstream, in the pipe 1 1 a corresponding, a temperature sensor (thermocouple) 13 for measuring the temperature of the exhaust combustion fumes, and
- a preheating measurement ramp 15 substantially parallel to the suction ramp 1 1 upstream of the latter, generally above the same chamber 2, and equipped with temperature sensors (thermocouples) and pressure sensors to prepare the static depression and the temperature prevailing in each of the hollow partitions 6 of this chamber 2 in order to be able to display and adjust this depression and this temperature of the preheating zone;
- a heating zone comprising:
- each heating ramp 16 - several identical heating ramps 16, two or, preferably, three, as shown in Figure 1; each equipped with burners or fuel injectors (liquid or gaseous) and temperature sensors (thermocouples), each of the ramps 16 extending above one of the chambers respectively of a corresponding number of adjacent chambers 2 , so that the injectors of each heating ramp 16 are engaged in the openings 9 of the hollow partitions 6 to inject the fuel therein;
- a natural blowing or cooling zone comprising:
- a so-called "zero point” ramp 17 extending above chamber 2 immediately upstream of that below the most upstream heating ramp 16, and equipped with pressure sensors for measuring the prevailing pressure in each of the hollow partitions 6 of this chamber 2, in order to be able to adjust this pressure as indicated below, and -
- a forced cooling zone which extends over three chambers 2 upstream of the blowing ramp 1 8, and which comprises, in this example, two parallel cooling ramps 1 9, each equipped with motorcycle fans and pipes blowing air blowing ambient air into the hollow partitions 6 of the corresponding chamber 2; and E) A working zone, extending upstream of the cooling ramps 1 9 and allowing charging and deflection of the anodes 5, and the maintenance of the rooms 2.
- the heating of the oven 1 is thus provided by the heating ramps 1 6, the injectors of the burners are introduced through the openings 9 into the hollow walls 6 of the chambers 2 concerned.
- the blowing ramp 1 8 and the cooling ramp (s) 1 9 comprise combustion air insufflation pipes supplied by motorcycle fans, these pipes being connected, through the openings 9, to the hollow partitions 6 of the chambers 2 concerned.
- the suction ramp 1 1 is available to extract the combustion gases and fumes, referred to collectively as "combustion fumes", which circulate in hollow partition lines 6.
- the heating and cooking of the anodes 5 are ensured both by the combustion of the fuel (gaseous or liquid) injected, in a controlled manner, by the heating ramps 1 6, and, to a substantially equal extent, by the combustion of materials.
- volatile (such as polycyclic aromatic hydrocarbons) pitch diffused by the anodes 5 in the cells 4 of the chambers 2 in preheating zones and heating, these volatile materials, largely combustible, diffused into the cells 4 can flow into the two hollow partitions 6 adjacent by passages formed in these partitions, to ignite in these two partitions, thanks to residual combustion air present at this level, among the combustion fumes in these hollow partitions 6.
- the air circulation and combustion fumes is performed along the lines of hollow partitions 6, and a negative pressure imposed downstream of the heating zone B by the suction ramp 1 1 at the downstream end of the preheating zone A, to control the flow of combustion fumes inside the hollow partitions 6, while the air from the cooling zones C and D, thanks to the ramps of 1 9, and especially at the blowing ramp 1 8, is preheated in the hollow partitions 6, cooling the anodes 5 cooked in the adjacent cells 4, during its journey and serves as an oxidizer when it reaches the zone of heating B.
- the control method of the FAC 1 essentially comprises the temperature and / or pressure regulation of the preheating zones A, heating B and natural blowing or cooling C of the oven 1 according to predefined setpoint laws.
- the combustion fumes extracted from the fires by the suction ramps 1 1 are collected in a flue gas duct 20, for example a cylindrical duct partially shown in FIG. 2, with a flue gas flue 21 that can have a U-shaped shape. (see dotted line in FIG. 1) or able to go around the furnace, and whose outlet 22 directs the combustion fumes sucked and collected to a smoke treatment center (CTF) not shown because it is not part of the furnace. invention.
- CTF smoke treatment center
- the current conduct of ovens of this type favors the supply of fuel (liquid or gaseous fuel) heating ramps 1 6 independently of draft depression conditions and aeraulic conditions in the partitions 6, where it can result in incomplete combustion in a significant number, or even a high number, of the partition lines 6.
- fuel liquid or gaseous fuel
- This results in high operating costs of the furnace, not only because of the overconsumption of fuel, but also because of clogging of the ducts and suction ducts that lead to the capture by the deposits of unburnt, deposits which represent in addition a potential risk of ignition and drift of the cooking process.
- the problem underlying the invention is, in general, to improve the continuous optimization of the operation of such ovens, in order to reduce operating costs and prevent the risk of fire and drift of the cooking process, and to this end, the invention proposes a method or a method for characterizing the combustion in the partition lines of a chamber furnace called "rotating fire") for the cooking of carbon blocks, by analysis of the value of at least one image parameter of the overall content of unburned in the combustion gases and residual air from said partition lines and collected in a suction ramp of said oven, said furnace comprising a succession of preheating chambers, heating, natural cooling and forced cooling, arranged in series along the longitudinal axis of the furnace, each chamber being constituted by the juxtaposition, transversely to said longitudinal axis nal and alternately, cells in which are arranged carbon blocks to cook and hollow heating partitions, in communication and aligned with the partitions of the other rooms, parallel to the longitudinal axis of the furnace, in lines of partitions in which circulate cooling and combustion air and combustion gases, said suction ramp
- the method according to the invention further comprises at least one previous step, so-called preselection of the partition lines likely to be in an incomplete combustion situation, and making it possible to limit the number of injection stop tests, in said step of successive tests of total fuel injection stoppage, to only lines of preselected partitions, and consisting in calculating, for each line of partitions of rank n, a combustion ratio, equal to the ratio of the quantity of combustion air available to the quantity of fuel injected into said line of partitions of rank n , to define empirically a so-called stoichiometric limit ratio from measurements of said image parameter of the unburned content in the combustion gases collected at the outlet of a line of standard partitions, representative of the best state of the oven partition lines, and so that this stoichiometric ratio corresponds to a measured threshold of said image parameter below which combustion is considered incomplete, to compare the combustion ratio of all the lines of partitions with a
- the identification of the partition lines in an incomplete combustion situation is advantageously preceded by a pre-selection of the partition lines likely to be in this incomplete combustion situation, thanks to the calculations, on the one hand, of the combustion ratio for each of the furnace partition lines, and, on the other hand, of said stoichiometric ratio, empirically defined from measurements of the image parameter in a standard partition line, chosen as being representative of the best state of the partition lines and finally by comparing each combustion ratio to the stoichiometric ratio, to deduce which (s) is or are the line or lines of combustion, in which or which combustion may be considered incomplete.
- the combustion ratio (RCcIn) in said step of preselecting the incomplete combustion partition lines, can be calculated in a line of partition walls.
- row n being proportional to the square root of the static draw depression measured in the preheating zone for said line of partitions considered, and inversely proportional to the sum of the fuel injection power of the injectors of the heating ramps operating on the same line of partitions of rank n.
- the combustion ratio of the row of partitions of rank n can be easily calculated by applying the following formula: where Pi and P 7 are the pressures measured in the n-row partitions of the chambers respectively in communication with the suction ramp and the so-called "zero point" ramp in the natural cooling zone, N is the number of heating ramps , generally equal to 2 or 3, and InjHRi is the total injection power in the rank n partition of the injectors of the heating ramp of rank i, where i varies from 1 to N.
- the image parameter of the overall content of unburned in the combustion gases is chosen as the image parameter.
- the carbon monoxide (CO) content which is measured, to determine said stoichiometric ratio, in the suction pipe of said suction ramp which is connected to the partition of the standard partition line in the first chamber of preheating, said threshold of this image parameter corresponding to the stoichiometric ratio being about 500 ppm of CO measured at said suction pipe, which corresponds, under the standard operating conditions of this type of furnace, to a level of 1000 ppm of CO at the point of combustion.
- the process of the invention can be implemented without it is necessary to implement a specific detection and / or measurement apparatus, but only by using measurement data already available, because provided by sensors of a detection instrumentation already installed on such furnaces, the implementation of the method of the invention being carried out only through a software module that can simply and easily be integrated into the current programs for driving such ovens.
- the method according to the present application can be completed by the fact that after the characterization steps for identifying and to select the partition lines in incomplete combustion, it is possible to implement at least one subsequent step called optimization of combustion.
- such an optimization of the combustion can consist in automatically modifying control parameters in the zones of preheating, heating and / or natural cooling of the oven, in order to balance the stoichiometric ratio RS combustion air on fuel, in order to recover a complete combustion situation, which can be defined simply by passing the value of said image parameter under a parameterizable threshold.
- the method of the present application can be advantageously such that, following said optimization step, at least one complementary step of characterization of the combustion as defined above, in the lines of non-preselected partitions, as also indicated above, among the partition lines assumed to be incomplete combustion, is activated if at least one step of optimizing the combustion as mentioned above did not recover a complete combustion situation.
- FIGS. 1 and 2 are respectively a schematic plan view of the structure of a furnace with two rotating lights and open chambers, and a partial perspective view and cross section with tearing representing the internal structure of such an oven,
- FIG. 3 is a double graph showing the evolution, on the one hand, of the measured CO (in ppm) and, on the other hand, of the percentage of residual oxygen in the fumes collected at the suction pipe of the same line of partitions, according to the total injection power, in the partition line, expressed as a percentage of the maximum installed power, according to three values different from the static draft depression measured at the preheating measurement ramp associated with the first preheating chamber of the oven;
- FIG. 4 is a characterization curve of the combustion in a line of walls of rank n, indicating the measured CO content (in ppm) per line of partitions as a function of the combustion ratio RC C i n ;
- FIG. 5 is a diagram representing, on the abscissa, the notation of the combustion in a row of partitions of rank n by the note NC C
- FIG. 6 is a diagram corresponding to an example of a total fuel injection stop test successively in three rows of partitions ⁇ , ⁇ , and ⁇ , and representing, on the ordinate, the value of the total measured CO content. (in ppm) in the suction ramp as a function of time (expressed in minutes), and showing, for the first line of partitions tested, a reduction in the overall measured CO content, due to the test, greater than one indicative threshold of an incomplete combustion state in this line of partitions a.
- the method of the invention relates to a combustion characterization loop in the partition lines 6 of the furnace 1 by analysis of the total content of carbon monoxide (CO), or any other image parameter of the unburned content, in the fumes collected at the suction ramp 1 1 of a furnace fire 1, where this total CO content is measured by the CO-analyzer-detector 1 4 in the manifold of the suction ramp 1 1 (see Figure 2), and the combustion characterization method in the partition lines 6 comprises a first step of estimating the quality of combustion in each of the rows of partitions 6 and preselection of partition lines estimated in incomplete combustion state, then classification of the partition lines using a rating system, to select partition lines considered incomplete combustion, and defined according to the ratio of the combustion air to the fuel available in each line of partitions 6 and a stoichiometric ratio RS empirically defined by measurements in a line of partitions 6 one, representative of the best state of the rows of walls of the furnace.
- CO carbon monoxide
- This first step of the combustion characterization method makes it possible to preselect lines of partitions 6 which are estimated to be incomplete combustion if their so-called combustion ratio RC, which is the ratio of the combustion air to the fuel available for each line of partitions. 6 considered, is lower than the stoichiometric RS ratio presented above.
- This step of preselecting the partition lines estimated in incomplete combustion is immediately followed by a step of selecting the rows of partitions 6 considered incomplete combustion by classification, according to a rating system of the combustion quality in the partition lines which is based, as already said, on the principle of stoichiometry of the ratio of the amount of combustion air to the amount of fuel available in each line of partitions.
- the maximum amount of fuel that can be injected at a given moment in a line of partitions 6 depends on the air flow in this line of partitions, or the level of static depression measured in this line partitions at the same time. Below the stoichiometric ratio, combustion is incomplete, and some of the fuels present in the line of partitions no longer burn completely, giving rise to the formation of carbon monoxide (CO).
- CO carbon monoxide
- This threshold phenomenon is better perceived by the consideration of FIG. 3, representing, by 3 continuous curves, the CO content measured in ppm by a CO analyzer 14 in the suction pipe 11a (see FIG. a line of partitions considered, as a function of the quantity of fuel injected, expressed as total injection power in said line of partitions considered, and evaluated as a percentage of the maximum installed power, the three continuous curves of CO measurements being established each for one respectively of three different static draw draws in the considered partition line and respectively corresponding to three phantom curves indicative of the percentage of residual oxygen in the flue gases collected in the suction pipe of 1 1 a of the suction ramp January 1 considered, these three different static depressions being measured by the preheating ramp 15 at the level of the pre first chamber 2 preheating.
- the curves 23, 24 and 25 of the CO content measured (in ppm) to said suction pipe 11a by varying the total injection power from 10% to about 30% of the maximum power installed, with a draw static depression respectively of -140 Pa, -120 Pa and -70 Pa respectively correspond to the curves in phantom lines 26, 27 and 28 indicating the corresponding variation (in continuous reduction) of the percentage of residual oxygen, as indicated on the right ordinate axis of Figure 3, respectively for the same drawdown depressions.
- the curves of the measured CO 23, 24 and 25 to the suction pipe 11 1 has said line of partitions 6 are little different from each other, and indicate low CO contents (substantially less than 500 ppm), corresponding to a combustion considered complete, while for values of the total injection power greater than 15% of the maximum installed power, the three CO 23, 24 and 25 measuring curves diverge from one another with slopes that are initially increasing and then substantially constant, but as important as the draft depression is small in absolute value.
- the three measurement curves of CO 23, 24 and 25 give results greater than 1000 ppm, which corresponds to a combustion even more incomplete as the draft depression is low in absolute value.
- the curves 26, 27 and 28 indicating the variation of the percentage of residual oxygen are decreasing with a negative slope substantially constant and little different from one curve to another.
- a combustion ratio RC C i n is defined which gives the ratio of the quantity of fuel injected into said line of partition walls of rank n to the quantity of fuel. combustion air available in this same line of partitions of rank n.
- the amount of combustion air available in the line of partitions of rank n corresponds to the air flow in this line of partitions of rank n, which can be estimated by the calculation of the square root of the static draft depression in this line. of partitions of rank n, measured in the preheating zone A by the preheating measurement ramp 15 (see FIG. 1).
- the quantity of fuel injected into the same line of partitions of rank n can be directly obtained by summing the powers of the injectors that operate on the same line of partitions.
- formula (1) expressing the ratio or combustion ratio of this line of partitions of rank n may be the following: where P1 and P7 are the pressures measured in the line of partitions of rank n at the chambers 2 in communication respectively with the suction ramp 1 1 for P1, in the preheating zone A, and with the "point 0" ramp 1 7 in the natural cooling zone C, and where N is the number of heating ramps 1 6, in general equal to 2 or 3, and InjH Ri is the sum of the injector injection powers of the heating ramp 1 6 of rank i where i varies from 1 to N (2 or 3) in the row partition line not.
- the combustion ratio RCcIn in a line of partitions of rank n is proportional to the square root of the static draft depression measured in the preheating zone A for this line of partitions 6 considered and inversely proportional to the sum of the powers of the injecting fuel injector heating ramps 1 6 operating on the same line of partitions 6 of rank n.
- FIG. 4 represents, for this row of partitions 6 of rank n, a shaded and curved zone 29, which corresponds to the envelope of the different measurement points of the CO measured in ppm with the corresponding suction pipe 11a. of the variation of the corresponding combustion ratio RCcIn.
- the threshold value of RC below which the combustion is estimated to be incomplete, that is to say the value of said stoichiometric ratio RS, is empirically defined by observation of the value of CO in a line of partitions representative of the best state oven partitions.
- a pre-selection of the rows of partitions 6 likely to be in an incomplete combustion situation is further specified that the CO content, chosen in this embodiment as an image parameter of the overall content of unburned in the combustion gases , is measured, for determining the stoichiometric ratio RS, in that of the suction pipes 1 1 a of the suction ramp 1 1 which is connected to that of the partitions 6 which is at the intersection of the line of standard partitions and the first preheating chamber 2, the threshold of the CO content corresponding to the stoichiometric ratio RS being about 500 ppm of CO measured at this suction pipe 11a, which corresponds, under standard conditions of operation of this type of furnace 1, at a level of 1000 ppm CO at the point of combustion.
- the combustion ratio RCcIn From calculation of the combustion ratio RCcIn, it is also deduced, at least for the lines of partitions 6 estimated in incomplete combustion by comparison of their combustion ratio RCcIn with the stoichiometric ratio RS, but preferably for all the rows of partitions 6 of the furnace 1, a note for classifying the partition lines in descending order from the one with the most incomplete combustion to the one with the least incomplete combustion, or even the most complete if all the partition lines are noted, for example by a system of notation from 0 to 20, defined such that beyond the value 10, the stoichiometric limit is exceeded and combustion is considered incomplete in the corresponding line of partitions.
- a classification of the pre-selected partition lines as being in incomplete combustion in the manner described above consists in classifying these partition lines in the order from that in which combustion is most incomplete to that in which combustion is the less incomplete by applying the scoring system of the partition lines according to which any line of partitions 6 of rank n is assigned a classification note NCcIn given by the following formula (2):
- NC C in 20 - 10 (- ⁇ )
- RCcIn and RS are the previously defined ratios, namely respectively the combustion ratio in the n-rank partition and the stoichiometric ratio.
- FIG. 5 The result of such a notation is shown, by way of example, in FIG. 5, in which the NCcIn notes are indicated by round dots on a continuous curve which crosses three hatched rectangular zones, one of which extends between the grades 0 and 10 on the abscissa and between 0 and the incomplete combustion threshold of 500 ppm measured CO, for the complete combustion partition lines, a second zone 31 of which extends on the abscissa between the notes 10 and 12 and on the ordinate between the values of 500 and 1000 ppm measured CO, for one or more line (s) of incomplete combustion walls, and finally whose third zone 32 extends for the grades greater than 12 on the abscissa and a CO measured greater than 1000 ppm on the ordinate, for any line of partitions in combustion very incomplete and therefore critical.
- the NCcIn notes are indicated by round dots on a continuous curve which crosses three hatched rectangular zones, one of which extends between the grades 0 and 10 on the abscissa and between 0 and the incomplete combustion
- the lines of closions considered in incomplete combustion are thus selected as having a grade greater than 10, which are then each subjected to a step of identification of the incomplete combustion partition lines, using a complete fuel injection stop test for a specified period and in succession on the fuel lines selected partitions, starting with the one with the highest rating and performing the test successively on the partition lines whose burn scores are in descending order.
- FIG. 6 diagrammatically represents the unfolding of the fuel injection total stopping test successively on three rows of partitions of rank ⁇ , ⁇ and ⁇ , the combustion notes NC of which are progressively decreasing.
- the overall CO content measured in ppm in the manifold of the suction manifold 1 1 is represented on the ordinate by the CO detector 14 (see FIG. 2), and, on the abscissa, the every minute Curve 33 represents the evolution over time of the overall CO content measured in the manifold of the suction manifold 1 1.
- the row of partitions 6 of rank at the total stop of the fuel supply of injectors is controlled by heating ramps 16 operating on this line of partitions a, by an almost instantaneous break, starting from from an initial value (for the total stop test) of fuel injection rate to a zero flow, which corresponds to the left side with downward arrow of the rectangle "a", symbolizing the feed control fuel injectors from this line of bulkheads during this total injection stop test.
- the injection is stopped for a time interval t1 t2 sufficient for the measurement of the CO content to stabilize before the time t2 of the end of the total injection cutoff.
- the curve 33 of the CO content shows a drop to a stabilized value of, for example, 500 ppm during the interval t1 t2, so that it is possible to measure the ACO value corresponding to the difference between the initial value at time t1 and the final value at time t2 of the CO content due to this interruption of supply. Then, at time t2, the fuel supply of this line of partitions a is restored to its initial value, as symbolized on the right side of the rectangle "a" of Figure 6, by the rising arrow.
- a time interval t2 t3 elapses, of a duration slightly greater than or substantially equal to the interval t1 t2, itself of the order of 2 minutes, to start at time t3, the same test total stop of fuel injection on the line of partitions of rank ⁇ , knowing that, during the execution of a test of total stop on a line of particular partitions, no modification is controlled on the course of the cooking process in all the other lines of partitions.
- the duration of the second test, on the line of partitions ⁇ , corresponding to the interval t3 t4, is the same as the duration t1 t2, and the curve 33 of the CO content, which is returned, after the end of the test on the line of partitions a, at a normal level, marks, as a result of the test on the line of partitions ⁇ , a limited reduction in the CO content measured following the total injection stop in the line of partitions ⁇ during the interval t3 t4.
- the total fuel injection stop test is therefore conducted, line of partitions per line of partitions, on the partition lines previously selected by their NC combustion rating. It is essential that no action be commanded on the lines of partitions 6 other than the one in total injection stop test, during the complete duration of this test, so as not to disturb the characterization of the combustion. This characterization indeed depends on the calculation of the variation of the measured CO content between the initial moment of the test and the final moment, while noting that the measurements of CO content always remain global. The sharp downward inflection then the rise of the curve 33 in FIG. 6 thus reflect the impact of the total fuel injection stoppage in the partition line a on the CO content in the collector. of the intake manifold 1 1, which therefore takes into account the flue gas extracted from all the walls of the oven walls.
- this value of X depends in particular on the number of partitions 6 per chamber 2 of the oven, as well as the accuracy of measurement and detection threshold values of the CO detector 14, in particular. In general, X% is selected in a range of 5% to 10%.
- the characterization system implementing the method of the invention must be able to detect at least one partition of rank n among 9 partitions 6 where the combustion tends to become incomplete.
- Such a step may consist in modifying, preferably automatically, control parameters in at least one of the natural cooling zones C, heating B and preheating A, in order, as far as possible, to balance the combustion ratios on the stoichiometric ratio of combustion air on fuel, to recover a complete combustion situation in as many as possible of the partition lines, this transition to a complete combustion situation that can be defined by the passage of the measured value of the CO content, or by passing the value of at least one other image parameter of the overall unburned content in the combustion gases, below a parameterizable threshold.
- the method according to the present application proposes at least one additional stage of characterization of the combustion, which is carried out by applying the total injection stop test to those of the partition lines which do not have were preselected, in accordance with the demand method, among the partition lines assumed to be incomplete combustion only because their RC combustion ratio was calculated lower than the stoichiometric RS ratio.
- this additional characterization step makes it possible to identify partitions whose stoichiometric conditions are satisfactory, having an NC combustion rating of less than 10, in the example of the notation system previously described, but whose physical conditions generate problems. of combustion, because partitions are deformed, pinched or plugged more or less completely.
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Priority Applications (7)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP09745074.6A EP2475948B1 (fr) | 2009-09-07 | 2009-09-07 | Methode de caracterisation de la combustion dans des lignes de cloisons d'un four a chambres a feu(x) tournant(s) |
CN200980161301.XA CN102597678B (zh) | 2009-09-07 | 2009-09-07 | 用于描述具有旋转点火膛的炉子的多排隔墙中的燃烧特性的方法 |
AU2009352124A AU2009352124B2 (en) | 2009-09-07 | 2009-09-07 | Method for characterizing the combustion in lines of partitions of a furnace having rotary firing chamber(s) |
PCT/FR2009/051682 WO2011027042A1 (fr) | 2009-09-07 | 2009-09-07 | Methode de caracterisation de la combustion dans des lignes de cloisons d'un four a chambres a feu(x) tournant(s) |
CA2772693A CA2772693C (fr) | 2009-09-07 | 2009-09-07 | Methode de caracterisation de la combustion dans des lignes de cloisons d'un four a chambres a feu(x) tournant(s) |
RU2012113704/02A RU2500961C1 (ru) | 2009-09-07 | 2009-09-07 | Способ определения характеристик горения в линиях перегородок многокамерной печи с вращающимся пламенем |
ZA2012/01211A ZA201201211B (en) | 2009-09-07 | 2012-02-17 | Method for characterizing the combustion in lines of partitions of a furnace having rotary firing chamber(s) |
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PCT/FR2009/051682 WO2011027042A1 (fr) | 2009-09-07 | 2009-09-07 | Methode de caracterisation de la combustion dans des lignes de cloisons d'un four a chambres a feu(x) tournant(s) |
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PCT/FR2009/051682 WO2011027042A1 (fr) | 2009-09-07 | 2009-09-07 | Methode de caracterisation de la combustion dans des lignes de cloisons d'un four a chambres a feu(x) tournant(s) |
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EP (1) | EP2475948B1 (fr) |
CN (1) | CN102597678B (fr) |
AU (1) | AU2009352124B2 (fr) |
CA (1) | CA2772693C (fr) |
RU (1) | RU2500961C1 (fr) |
WO (1) | WO2011027042A1 (fr) |
ZA (1) | ZA201201211B (fr) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2013034840A1 (fr) | 2011-09-08 | 2013-03-14 | Solios Carbone | Dispositif et procédé d'optimisation de la combustion dans des lignes de cloisons d'un four à chambres pour la cuisson de blocs carbonés |
WO2015049428A1 (fr) * | 2013-10-02 | 2015-04-09 | Solios Carbone | Procede d'injection de combustible gazeux dans un four a chambres a feu(x) tournant(s) |
FR3012590A1 (fr) * | 2013-10-31 | 2015-05-01 | Solios Carbone | Procede de regulation d'un four a chambres a feu(x) tournant(s) pour la cuisson de blocs carbones |
CN115187607A (zh) * | 2022-09-14 | 2022-10-14 | 山东鑫亚格林鲍尔燃油系统有限公司 | 一种基于图像处理的喷油器喷雾形态检测方法 |
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US4284404A (en) * | 1979-02-05 | 1981-08-18 | Genevois Jean L | Continuous ring baking furnaces of the Hoffmann type |
FR2600152A1 (fr) * | 1986-06-17 | 1987-12-18 | Pechiney Aluminium | Dispositif et procede d'optimisation de la combustion dans les fours a chambres pour la cuisson de blocs carbones |
US6027339A (en) * | 1998-06-11 | 2000-02-22 | Aluminium Pechiney | Ring furnace with central tubular flow |
FR2918164A1 (fr) * | 2007-06-29 | 2009-01-02 | Solios Environnement Sa | Procede de surveillance d'un conduit des fumees reliant un four de cuisson de blocs carbones a un centre de traitement des fumees |
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SU877285A1 (ru) * | 1979-08-17 | 1981-10-30 | Запорожский индустриальный институт | Устройство дл дожигани летучих веществ |
FR2616525B1 (fr) * | 1987-06-09 | 1989-09-08 | Pechiney Aluminium | Dispositif et procede d'obturation des cloisons d'un four a chambres a feu tournant destine a la cuisson de blocs carbones |
CN101172652B (zh) * | 2007-10-29 | 2012-03-21 | 贾绍才 | 矾矿钙法步进式焙烧方法及焙烧炉 |
-
2009
- 2009-09-07 RU RU2012113704/02A patent/RU2500961C1/ru not_active IP Right Cessation
- 2009-09-07 EP EP09745074.6A patent/EP2475948B1/fr active Active
- 2009-09-07 CN CN200980161301.XA patent/CN102597678B/zh not_active Expired - Fee Related
- 2009-09-07 WO PCT/FR2009/051682 patent/WO2011027042A1/fr active Application Filing
- 2009-09-07 CA CA2772693A patent/CA2772693C/fr not_active Expired - Fee Related
- 2009-09-07 AU AU2009352124A patent/AU2009352124B2/en not_active Ceased
-
2012
- 2012-02-17 ZA ZA2012/01211A patent/ZA201201211B/en unknown
Patent Citations (4)
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US4284404A (en) * | 1979-02-05 | 1981-08-18 | Genevois Jean L | Continuous ring baking furnaces of the Hoffmann type |
FR2600152A1 (fr) * | 1986-06-17 | 1987-12-18 | Pechiney Aluminium | Dispositif et procede d'optimisation de la combustion dans les fours a chambres pour la cuisson de blocs carbones |
US6027339A (en) * | 1998-06-11 | 2000-02-22 | Aluminium Pechiney | Ring furnace with central tubular flow |
FR2918164A1 (fr) * | 2007-06-29 | 2009-01-02 | Solios Environnement Sa | Procede de surveillance d'un conduit des fumees reliant un four de cuisson de blocs carbones a un centre de traitement des fumees |
Non-Patent Citations (1)
Title |
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BEACH DAVID ET AL: "Proven control philosophy and operation for anode baking process", LIGHT METALS,, 1 January 2007 (2007-01-01), pages 953 - 957, XP009103395, ISSN: 0147-0809 * |
Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2013034840A1 (fr) | 2011-09-08 | 2013-03-14 | Solios Carbone | Dispositif et procédé d'optimisation de la combustion dans des lignes de cloisons d'un four à chambres pour la cuisson de blocs carbonés |
CN103930741A (zh) * | 2011-09-08 | 2014-07-16 | 索里斯卡彭公司 | 优化焙烧碳块用环形炉隔墙线路中燃烧的方法和装置 |
RU2600607C2 (ru) * | 2011-09-08 | 2016-10-27 | Солиос Карбон | Устройство и способ оптимизации горения в линиях перегородок многокамерной печи для обжига углеродистых блоков |
WO2015049428A1 (fr) * | 2013-10-02 | 2015-04-09 | Solios Carbone | Procede d'injection de combustible gazeux dans un four a chambres a feu(x) tournant(s) |
FR3012590A1 (fr) * | 2013-10-31 | 2015-05-01 | Solios Carbone | Procede de regulation d'un four a chambres a feu(x) tournant(s) pour la cuisson de blocs carbones |
WO2015063396A1 (fr) | 2013-10-31 | 2015-05-07 | Solios Carbone | Procede de regulation d'un four a chambres a feu(x) tournant(s) pour la cuisson de blocs carbones |
RU2682077C2 (ru) * | 2013-10-31 | 2019-03-14 | Фив Солиос | Способ регулирования многокамерной печи с поворотным пламенем для обжига углеродных блоков |
CN115187607A (zh) * | 2022-09-14 | 2022-10-14 | 山东鑫亚格林鲍尔燃油系统有限公司 | 一种基于图像处理的喷油器喷雾形态检测方法 |
CN115187607B (zh) * | 2022-09-14 | 2022-11-22 | 山东鑫亚格林鲍尔燃油系统有限公司 | 一种基于图像处理的喷油器喷雾形态检测方法 |
Also Published As
Publication number | Publication date |
---|---|
AU2009352124B2 (en) | 2014-05-01 |
EP2475948A1 (fr) | 2012-07-18 |
RU2012113704A (ru) | 2013-10-20 |
AU2009352124A1 (en) | 2012-03-08 |
ZA201201211B (en) | 2013-05-29 |
RU2500961C1 (ru) | 2013-12-10 |
CA2772693A1 (fr) | 2011-03-10 |
CA2772693C (fr) | 2017-01-03 |
EP2475948B1 (fr) | 2014-12-10 |
CN102597678A (zh) | 2012-07-18 |
CN102597678B (zh) | 2014-08-20 |
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