CN1333087C - Heating furnace with regenerative burners and method of operating heating furnace - Google Patents
Heating furnace with regenerative burners and method of operating heating furnace Download PDFInfo
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- CN1333087C CN1333087C CNB2005100789386A CN200510078938A CN1333087C CN 1333087 C CN1333087 C CN 1333087C CN B2005100789386 A CNB2005100789386 A CN B2005100789386A CN 200510078938 A CN200510078938 A CN 200510078938A CN 1333087 C CN1333087 C CN 1333087C
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- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E20/00—Combustion technologies with mitigation potential
- Y02E20/34—Indirect CO2mitigation, i.e. by acting on non CO2directly related matters of the process, e.g. pre-heating or heat recovery
Abstract
A method of controlling a furnace pressure for preventing air from intruding to a heating furnace, a method of stable operation during low combustion load of heat regenerating burners and a method of measuring concentration of an atmospheric gas in a heating furnace are proposed. When the heat recovered with burners each attached with a heat regeneration body is used for heating the combustion air of burners at a combustion state, the suction ratio of the exhaust gas from the burners to the heat regeneration body is adjusted to control the furnace pressure in accordance with a combustion load on an entire heating furnace. The furnace pressure is controlled by adjusting the flow rate of dilution air in accordance with the temperature of the exhaust gas in the exhaust stack on the inlet side of a recuperator in the heating furnace and the combustion load on the heating furnace. When the extraction door of the heating furnace is opened, the flame for heating burners located in the lower region of the furnace extraction end is extended for the width of the opening in the lateral direction of the extraction port thereby shutting the intruding path of air from the extraction port with the burner flame, thereby suppressing the increase in the oxygen concentration in the furnace. In a case where the combustion load on the heat regeneration burners is small, a hot blow is supplied to a suction device for sucking the exhaust gas in the furnace from the burners through the heat regeneration body during a not-combustion state. When operation for the heating furnace is conducted while utilizing to the recovered heat for heating the combustion air of the burners during combustion state, a portion of the exhaust gas sucked from the burners is introduced into an analyzer to measure the concentration of ingredients in the exhaust gas.
Description
The application be that January 17 calendar year 2001 (preference day), application number are 01809247.0 the applying date, denomination of invention divides an application for the application for a patent for invention of " a kind of furnace pressure control method of process furnace ".
Technical field
This invention relates to the method for the furnace pressure of most suitably controlling process furnace.This invention relates to the method that the atmosphere of process furnace is controlled, particularly related to the oxygen concn rising that suppresses in the atmosphere.This invention relate to the working method of process furnace and process furnace with heat-accumulating burner, particularly be related to the working method of the paired burner alternate combustion of advantageously carrying out heat-accumulating burner and in this operation the direct process furnace of use.This invention relates to the measuring method and the process furnace of the atmosphere gas concentration in the process furnace.
Background technology
The process furnace of steel be think that strand with the steel billet of cogging factory roughing and continuous casting is rolled into the finished product and reheat to become to be suitable for this rolling specified temperature be that purpose is used.This process furnace is divided into batch-type process furnace and continuous furnace substantially.Owing to have merits and demerits separately, select to use according to its purpose.Continuous furnace is suitable for production in enormous quantities in recent years, so Steel Plant use this process furnace mostly.
Figure 1 shows that the typical example of the sectional view of continuous furnace.Generally the side of packing into from steel is made of preheating zone 1, heating zone 2 and soaking zone 3 successively.At least heating zone 2 and soaking zone 3 are heated to specified temperature by burner 4 and are incubated.The steel 5 that import preheating zone 1 from the fire door 1a that packs into move on carry road 6, are heated to specified temperature in soaking zone 3 then through heating zone 2, and the extraction fire door 3a of 3 outlet sides takes out of outside the stove from the soaking zone.The waste gas that burning produced by burner 4 is discharged to outside the stove from the flue 7 of the inlet side that is located at preheating zone 1.In addition, 7a is that interchanger and 7b that the waste gas sensible heat heat exchange with flue 7 becomes burner combustion to use with the sensible heat of air are the flue shutters that the control furnace pressure is used.
At this, continuous furnace must be heated to steel the temperature that is suitable for rolling process thereafter.If the temperature of the steel that continuous furnace heated is lower than the rolling suitable temp lower limit of regulation, then can rolling operation and quality product bring detrimentally affect.In addition, need temperature if the temperature of the steel of extracting out from process furnace is higher than, then the thermosteresis of continuous furnace is big, so in continuous furnace, it is important with the fuel of necessary minimum steel being heated to rolling suitable temp.And, also require in process furnace, to adjust heat-up time, so that in turn supply with the steel that heat from process furnace accordingly with the rolling cycle of rolling process.
In continuous furnace, the loss of the radiating capacity of thermosteresis, particularly heating zone is big.By in inlet, outlet side configuration preheating zone and the soaking zone of heating zone,, suppress thermosteresis like this with being divided into 3 zones in the stove.
Pack into the steel of continuous furnace, have the strand that is cooled to normal temperature and continuous casting back directly direct sending be just different to the hot charging stove material of rolling process etc. in the temperature of process furnace inlet side.Its Heating temperature is that height is different, and the treatment capacity of the steel that heat in process furnace also changes.Must be according to the temperature in this all condition control process furnace.The quantity combusted of increase and decrease burner is adjusted Heating temperature.At this moment, because the variation of burner combustion amount, furnace pressure changes.
If furnace pressure is lower than stove external pressure, in then extraneous air is promptly packed fire door and extraction fire door intrusion stove into from the peristome of process furnace.If air is invaded in the stove, then temperature reduces in the stove, so increase the quantity combusted of burner.Gu unit consumption of fuel increases, cost is risen.If air is invaded in the stove, then the oxygen concn of furnace atmosphere rises, oxidation, nitrogenize or the decarburization etc. on the surfaces such as steel so promotion is packed in the stove.Its result causes that surface quality of steel reduces.
Therefore, must suitably control the interior pressure of process furnace.About furnace pressure control, various motions have been proposed.For example, the spy opens clear 61-119987 communique and has disclosed such method, promptly according to waste gas generating capacity in the stove, the setting furnace pressure of process furnace soaking zone is controlled to be malleation (being designated hereinafter simply as malleation) with respect to the stove external pressure, prevent from packing fire door and extract the fire door invading air out into.According to the method, the furnace pressure that with the landline in the stove is the upper area (hereinafter referred to as the top band) on boundary can be controlled to be malleation.But, under the little situation of the burning load of whole process furnace, be that the furnace pressure pressure outer with respect to stove of the lower region (hereinafter referred to as the bottom band) on boundary is negative pressure (hereinafter referred to as negative pressure) with landline in the stove.Prevent that positively from the underclearance invading air of pack into fire door and extraction fire door be difficult.These fire doors be difficult to positively to prevent from the engagement of broach shape ground closed, be called as V shape (extrafork) peristome and enter air.The V shape peristome of so-called broach shape is 3C place shown in Figure 14.
In addition, the spy opens flat 9-209032 communique and has disclosed such method, i.e. the top of soaking zone, and the furnace pressure flashboard in the flue that passes through by the waste gas that is located at process furnace according to the burning load amount of process furnace, is controlled furnace pressure best.But, burning load amount hour, the air-flow of flue (draft) is bigger than the pressure-losses that causes to the exhaust flow of flue in the stove.So-called air-flow is meant that heated gas produces buoyancy and becomes negative pressure in flue and stove.In this case, be difficult to utilize the furnace pressure flashboard to make and become malleation until the bottom band.Be difficult to positively prevent from fire door and the extraction fire door invading air of packing into.
The heat exchanger outlet side that Te Kaiping 7-316645 communique has disclosed at flue connects gas supplying tubing system, gases such as air is blown into the method for flue control furnace pressure.This method must newly be established gas blower and various pipe arrangement and Controlling System in order to control furnace pressure.There are cost of equipment height, the miscellaneous problem of its maintenance.And intricately is equipped with pipeline and sets up equipment around the process furnace, so there is not configuration space, is difficult to newly establish Controlling System.
Prevent in the air intrusion process furnace this considers it is very important with the operation of process furnace on quality product.For the technology that realizes this point has various motions.For example, open in the flat 11-172326 communique the spy and to have proposed such scheme, promptly extract a mouthful invading air out from process furnace in order to prevent, from stove in heating burner branch be opened near extracting out mouthful a nozzle ejection inflammable gas, the burning by at this moment consumes the oxygen in the invading air.
But, must near extracting mouth out, establish special-purpose inflammable gas jetting nozzle, need the flower installation cost.In addition, be effectively for the position top invading air that is provided with from jetting nozzle, but little for the effect that below, position invading air is set from this jetting nozzle.Because the furnace pressure of below is a negative pressure, so can not avoid air here to invading.Particularly be difficult to positively prevent from V shape peristome invading air.
In recent years, on continuous furnace, its heating source adopts heat-accumulating burner, carries out the heat in the waste gas is used in again the operation of process furnace preheating, that thermosteresis is few of the combustion air of burner.Fig. 2 A and Fig. 2 B are the examples of the structure of expression heat-accumulating burner.Shown in the example of Fig. 2 A and Fig. 2 B, heat-accumulating burner is by constituting with the lower section: a pair of burner 40a and the 40b that relatively dispose between the two side of the equal hot body 3 of process furnace; Outside stove, combustion air imported each burner and the waste gas in the stove is imported the dual-purpose path 41a and the 41b of stove external application by each burner; In illustrated example, be provided in the heat storage 42a and the 42b at the burner side opening place of each path.The a pair of burner of this heat-accumulating burner is alternately burnt.For example, shown in Fig. 2 A, 41a supplies with burner 40a with combustion air from the dual-purpose path, fueling 43a meanwhile, make burner 40a when burning, from sucking waste gas in stove with its burner 40b in opposite directions, this waste gas reclaims after the heat by heat storage 42b, import dual-purpose path 41b, be discharged to outside the stove.
Then, the burning running of conversion burner, and at this moment change the transforming valve 44 of dual- purpose path 41a and 41b, change with being connected of the conduit of above-mentioned air and waste gas after, shown in Fig. 2 B, with combustion air from dual-purpose path 41b, when supplying with burner 40b by heat storage 42b, lateral dominance is used in the heat that heat storage 42b is reclaimed in the technological process shown in the prior figures 2A, the preheated burning air, and this air is supplied with on the limit, fueling 43b makes burner 40b burning simultaneously.Simultaneously, from sucking waste gas in stove with its burner 40a in opposite directions, this waste gas reclaims by heat storage 42a after the heat, imports dual-purpose path 41a, and is discharged to outside the stove.
By for example carrying out the alternate combustion of burner shown in above Fig. 2 A and Fig. 2 B every tens of second repeatedly, can carry out the few furnace operation of thermosteresis.
At this, attraction to the waste gas of discharging from the burner in non-when burning, for example shown in Fig. 2 A and Fig. 2 B, end at the path 45 that attracts by heat storage 42a or 42b from burner 40a or 40b sets for example by the suction device 8 that attracts fan to constitute, drive this suction device 8, just attract the waste gas of discharging from burner.
But, in the operation of the process furnace that uses above heat-accumulating burner, after beginning to carry out burner combustion to reach design temperature during and (or) atmosphere gas in the stove is controlled to be under the situation of the low-temperature region about 800 ℃, attract out and the temperature of waste gas by heat storage also reduces from burner.Its result, at the waste gas outlet side and connected above-mentioned path 45 places of heat storage, moisture and sulphur content contained in the waste gas condense.The liquid that produces because of condensing, be the waste gas outlet side that so-called water of condensation often is trapped in heat storage.Under this state, the burning running of conversion burner and when becoming state of combustion, water of condensation is sneaked into the result in the combustion air, the problem of bringing combustion flame temperature to descend.The reduction of the combustion flame temperature that causes because of water of condensation reduces the thermo-efficiency of process furnace, and the situation that hinders the low temperature running is also arranged.
In addition, be provided with on the process furnace of a plurality of heat-accumulating burners, will coming out to become cryogenic waste gas by heat storage from burner, to import the path of suction device longer.Often water of condensation not only produces at the heat storage outlet side, also produces in above-mentioned path way.The water of condensation that produces on this path can corrode the impeller of suction device.During contained solid-state part abrasive damage impeller, can develop into great accident in the water of condensation.Therefore, now, the process furnace with heat-accumulating burner is carried out continually the inspection of waste gas suction device.In addition, frequent increase of repairing required expense such as the impeller replacing of suction device also is a problem.
For above-mentioned variety of issue, open in the flat 10-30812 communique the spy and to have disclosed device shown in Figure 3 about water of condensation.The waste gas that makes (for example the soaking zone 3) in the process furnace is by in the bypass pipe 51 inflow exhaust gas pipe arrangement roads 50, and this bypass pipe is arranged with the path branch that discharges out of the furnace by burner 40a and waste gas pipe arrangement road 50.Having disclosed by such method just to make the temperature in the waste gas pipe arrangement road 50 remain on more than the dew point of waste gas.
But, for the temperature that makes the thickness of steel product direction is even, can not carry out high loading incendiary occasion etc. with producing equipment failure in the occasion of spending the long period to heat with lower temperature, must make burner combustion with extremely low load.In this case, that make that suction device (fan) is reduced to its attraction power for example is not 10% result who turns round, and tends to make the running instability of suction device.Can not stably obtain rotating fluid with the whole blade of fan, produce the position that can not obtain rotating fluid because of stall.So, not only be difficult to make the waste gas traffic attraction that sucks from burner to keep certain, and blade can produce abnormal vibrations, the breakage of blade meeting sometimes.
As mentioned above, though the spy opens the variety of issue that the described technology of flat 10-30812 communique has solved the water of condensation about with low load combustion the time, do not solve the running problem of unstable of suction device.In addition, because described exhaust pipe 50 of this communique and bypass pipe 51 have control valve separately, so also have its control complicated problems.
For the surface of being pined for steel adding of continuous furnace maintains good state, the atmosphere of strictly controlling in the stove is important.For example, the oxygen concn of furnace atmosphere rises, interior material-to-be-heated surface oxidation, nitrogenize or the decarburizations etc. such as steel of stove that then promote to pack into, if directly be rolled, then surface quality of products reduces.For improving or keeping quality product, the oxygen concn that must suppress furnace atmosphere rises.Therefore, the oxygen concn of correctly measuring furnace atmosphere is important.
Except oxygen concn, to carbon monoxide in the furnace atmosphere and oxynitride etc. too, it is important correctly measuring its concentration.Nitrogen is influential to the nitrogenize of steel surface, and carbon monoxide can be used to detect the incomplete combustion of burner, and oxynitride is to consider in the management of environment discharge standard value.
At this, open in the clear 62-40312 communique the spy and to have disclosed following method, be about to measure the various gauge heads that oxygen concn and carbon monoxide concentration are used in the process furnace and be set as the mode that moves freely,, come the air ratio of Correction and Control burner by obtaining mean intensity value in several mensuration concentration that locates.
But, in order to measure concentration, must newly establish drive system and Controlling System, so the cost of equipment height.Have problems such as maintenance is miscellaneous, and the process furnace intricately is equipped with pipeline and optional equipment class,, is difficult to newly establish drive system and Controlling System so most applications is not have configuration space.
In addition, Te Kaiping 9-53120 communique has disclosed such process furnace, it is inboard and at the downside of slideway promptly to extract the furnace wall of side out at process furnace, along the stove cross direction spaced walls is set, and has oxymeter and atmosphere gas is discharged to the vapor pipe of stove external application between this spaced walls and extraction wing furnace wall.Disclosed in this process furnace top and carried out the flow control in the vapor pipe with above-mentioned oxymeter mensuration oxygen concn, limit.
But,, must insert gauge head from furnace bottom or furnace wall in order to measure with the oxymeter that is located at spaced walls and extract out between the wing furnace wall.If insert gauge head from furnace bottom, then because iron sheet etc. fall and pile up, gauge head produces damaged and stops up, so be difficult to carry out for a long time the high concentration determination of reliability.In addition, if insert gauge head from the furnace wall, then gauge head is exposed to the high-temperature area in the stove and produces bending, and measuring point can misplace and maybe can produce damage.
Summary of the invention
One of purpose of the present invention is to propose a kind of air that can positively prevent and invades the furnace pressure control method in the process furnace.
The intrusion of the air of inventors when becoming negative pressure in the stove is studied with great concentration.Air is invaded in the stove from pack into fire door and extraction fire door two sides.As shown in Figure 1, be provided with flue 7 in the back of the fire door 1a that packs into.The air of invading from the fire door 1a that packs into directly is extracted in the flue 7 and is discharged to outside the stove.Distinguished the air of invading from the fire door 1a that packs into be difficult to become cause that oxygen concn in the stove rises and stove in the major reason of temperature reduction.In the stove oxygen concn rise and stove in temperature reduce, it is important avoiding from extraction fire door invading air.Therefore, draw such opinion, it is very important promptly suitably controlling the furnace pressure that is provided with the soaking zone of extracting fire door out.
In addition, as mentioned above, control furnace pressure by the flashboard that switching is located in the flue, this is difficult to make the furnace pressure of the conveying road lower zone of soaking zone to become malleation especially under the less situation of burning load.This is because the generating capacity of waste gas reduces, and the pressure-losses of the waste gas in the stove before discharging from flue reduces, in addition, in stove more downwards, air-flow is big more.Furnace pressure distribute relatively along with to the process furnace below near and reduce gradually, at the bottom band, compare with the pressure-losses of waste gas, air-flow increases, and becomes negative pressure easily.
The heating source of continuous furnace uses heat-accumulating burner, can carry out the heat in the waste gas is used to again furnace operation combustion air, that thermosteresis is few of preheating burner.Furnace pressure control for the process furnace that uses heat-accumulating burner is studied.Found that particularly the lower region in the soaking zone uses under the situation of heat-accumulating burner as heating source,, can carry out strict furnace pressure control, so finished the present invention by utilizing the distinctive mechanism of heat-accumulating burner.
That is, the present invention is a kind of furnace pressure control method of utilizing heat-accumulating burner, it is characterized in that, on the process furnace that uses heat-accumulating burner, according to the burning load of whole process furnace, regulate the waste gas attraction rate that is drawn onto heat storage from above-mentioned burner, control the furnace pressure of soaking zone.
In addition; inventors have carried out discovering the interchanger that is located in the flue in order to protect with keen determination for the method that burning load hour also can make the furnace pressure of the conveying road lower zone of soaking zone become malleation, can utilize the diluent air control furnace pressure of the heat exchanger entrance side of supplying with flue.
Promptly; the present invention is a kind of furnace pressure control method of process furnace; it is characterized in that; disposing interchanger at the flue that the waste gas in process furnace guiding stove is outer on the way, when being the combustion air of burner, be not subjected to the infringement of high-temperature atmosphere in order to protect interchanger with the heating source of the pre-heat supply process furnace of this interchanger; when the heat exchanger entrance side of flue is supplied with diluent air; according to the spent air temperture of heat exchanger entrance side and the burning load of process furnace, regulate the flow of diluent air, the control furnace pressure.
One of purpose of the present invention is to propose a plan from extracting fire door method of invading air in process furnace out for preventing definitely.In addition, one of purpose of the present invention is to provide the process furnace of this method use.
The intrusion of the air of inventors when becoming negative pressure in the stove is studied with keen determination, distinguish in this case, air is invaded in the stove from pack into fire door and extraction fire door two sides, but as shown in Figure 1, owing to be provided with flue 7 in the back of the fire door 1a that packs into, so in the direct suction flue 7 of air of invading from the fire door of packing into and discharge out of the furnace, state this can not become cause that oxygen concn in the stove rises and stove in the major cause of temperature reduction.Thereby, in the stove oxygen concn rise and stove in temperature reduce, it is important avoiding from extracting a mouth invading air out.Therefore, recognize that it is important positively cutting off the air intrusion at the extraction end.
Even one of purpose of the present invention is under the less situation of the burning load of heat-accumulating burner, the working method of the process furnace that the running of waste gas suction device also can be stable proposes a plan.In addition, one of purpose of the present invention is to provide the process furnace that the working method of this process furnace is used.
Inventors reduce the burning load of heat-accumulating burner, the suction device of waste gas is had to for example less than 10% load running the time, improving the method mirror meaning ground of the operating load of this suction device studies, discovery is very favourable from the flue outside the waste gas guiding stove of process furnace is imported suction device with waste gas, thereby has finished the present invention.
One of purpose of the present invention is that the method for utilizing existing equipment can correctly heat the concentration determination of the composition gas in the furnace atmosphere is proposed a plan.Another object of the present invention is to provide the process furnace of the concentration determination of the composition gas that can heat in the furnace atmosphere.
In the furnace operation of using heat-accumulating burner, be to heat by for example carrying out the technological process shown in Fig. 2 A and Fig. 2 B repeatedly every tens of seconds, realize the few furnace operation of thermosteresis.
In the furnace operation of using this heat-accumulating burner, attract owing to carry out the waste gas of heat-accumulating burner at a high speed, so on a large scale, attract to be distributed in the waste gas on the stove cross direction.Inventors are conceived to this phenomenon, discovery is reproduced furnace atmosphere well by waste gas in the stove of heat-accumulating burner attraction, the waste gas that heat-accumulating burner attracted is carried out the mensuration of constituent concentration if die, then can correctly measure the constituent concentration of furnace atmosphere, thereby finish the present invention.
Main points of the present invention are as follows.
1. furnace pressure control method of utilizing heat-accumulating burner, it is characterized in that, has the preheating zone, heating zone and soaking zone also are provided with on the process furnace of array heat-accumulating burner, this heat-accumulating burner is as the thermal source of soaking zone, the paired burner of heat storage is set up in configuration relatively, each that makes heat-accumulating burner alternately burnt to burner, and when not burning, attract waste gas in the stove from burner, waste gas is imported above-mentioned heat storage, with the heat recuperation in the waste gas in heat storage, the combustion air of the burner the when heat that is reclaimed is used for heating flame, when carrying out the operation of process furnace, regulate the waste gas attraction rate that sucks heat storage from above-mentioned burner according to the burning load of whole process furnace, the furnace pressure of control soaking zone.
2. the furnace pressure control method of a process furnace; it is characterized in that; in way, be provided with interchanger with the flue outside the guiding of the waste gas in the process furnace stove; when being the combustion air of burner with the heating source of the pre-heat supply process furnace of this interchanger; in order to protect interchanger not to be subjected to the infringement of high-temperature atmosphere; when the heat exchanger entrance side of flue is supplied with diluent air, regulate the flow of diluent air, control furnace pressure according to the burning load of the spent air temperture of heat exchanger entrance side and process furnace.
3. the atmosphere control method of a process furnace, it is characterized in that, when opening the extraction fire door of process furnace, several heating that are provided in this process furnace are controlled with the burning of burner independently with heating among the burner, that be configured in the lower region of stove extraction end, the flame of this burner is prolonged along this A/F on the width of extracting mouth out, cut off from extracting the intrusion road of mouthful invading air out with burner flame, suppress the rising of oxygen concn in the stove.
4. the atmosphere control method of a process furnace is characterized in that, in 3, in the stove inboard of the heating that is configured in stove extraction end with burner, be provided with axial spaced walls from the furnace bottom, form upstream, make from extract mouthful above-mentioned upstream of air admission of invading out along this spaced walls.
5. the atmosphere control method of a process furnace is characterized in that, in 3 or 4, makes to be configured in heating that stove extracts end out with the burner running of burning under low air ratio condition.
6. furnace operation method with heat-accumulating burner, it is characterized in that, have on the process furnace of heat-accumulating burner that relatively sets the subsidiary paired burner that heat storage arranged as heating source, each that makes heat-accumulating burner alternately burnt to burner, and the burner during from non-burning attracts the waste gas in the stove, waste gas is imported above-mentioned heat storage, with the heat recuperation in the waste gas in heat storage, the combustion air of the burner the when Btu utilization of this recovery is come heating flame, when carrying out the operation of process furnace, under the less situation of the burning load of heat-accumulating burner, with the warm-air supply suction device, this suction device is used for attracting waste gas in the stove from the burner in above-mentioned non-when burning by heat storage.
7. in the working method of the process furnace described in 6, it is characterized in that hot blast is with the waste gas in the flue outside the guiding of the waste gas in the process furnace stove.
8. the measuring method of atmosphere gas concentration in the process furnace, it is characterized in that, have on the process furnace of heat-accumulating burner that relatively sets the subsidiary paired burner that heat storage arranged as heating source, each that makes heat-accumulating burner alternately burnt to burner, and the burner during from non-burning attracts the waste gas in the stove, waste gas is imported above-mentioned heat storage, with the heat recuperation in the waste gas in heat storage, the combustion air of the combustion mouth the when heat of this recovery is used for heating flame, when carrying out furnace operation, to import analyzer from a part of waste gas that above-mentioned burner attracts, the constituent concentration in the waste gas will be measured.
9. the measuring method of the atmosphere gas concentration in the process furnace is characterized in that, the component concentration measuring value of the waste gas that attracts from heat-accumulating burner in 8 is used as the typical value of the constituent concentration of the band in the process furnace that is provided with this heat-accumulating burner.
10. process furnace, have relatively set the subsidiary paired burner that heat storage arranged several heat-accumulating burners as heating source, each that makes this heat-accumulating burner alternately burnt to burner, and the burner during from non-burning attracts waste gas in the stove, waste gas is imported above-mentioned heat storage, with the heat recuperation in the waste gas in heat storage, the combustion air of the burner the when heat of this recovery is used for heating flame, the process furnace of operating like this, it is characterized in that the heat-accumulating burner that is configured in the lower region of process furnace extraction end at least has the independently combustion control system that separates with other heat-accumulating burner.
11. a process furnace is characterized in that, in 10, and process furnace extract out and to sandwich between the fire door on the position with heat-accumulating burner of combustion control system independently, be provided with axial spaced walls from the furnace bottom.
12. process furnace, to have relatively set the subsidiary paired burner that heat storage arranged several heat-accumulating burners as heating source, each that makes this heat-accumulating burner alternately burnt to burner, and the burner during from non-burning attracts waste gas in the stove, waste gas is imported above-mentioned heat storage, with the heat recuperation in the waste gas in heat storage, the combustion air of the burner the when heat of this recovery is used for heating flame, the process furnace of operating like this, it is characterized in that, burner from non-burning the time, attract the end of the path of waste gas in this process furnace to be provided with suction device by heat storage, be provided with the pipeline that hot blast is imported suction device by open and close valve at the suction device inlet side of this path.
13. the process furnace described in 12 is characterized in that, pipeline is connected with the outer flue of stove that the waste gas in the process furnace is led, and guiding is as the waste gas in the process furnace of hot blast.
14. a process furnace in 12 or 13, is provided with interchanger at the upstream side of the pipeline of flue.
15. process furnace, to have relatively set the subsidiary paired burner that heat storage arranged several heat-accumulating burners as heating source, make this heat-accumulating burner each burner is alternately burnt, and the burner during from non-burning attracts waste gas in the stove, waste gas is imported above-mentioned heat storage, with the heat recuperation in the waste gas in heat storage, the combustion air of the burner the when heat of this recovery is used for heating flame, the process furnace of operating like this, it is characterized in that, burner from non-burning the time, discharge in the way of the path of waste gas in this process furnace the analyzer that is provided with the gauge head of gathering a part of waste gas and the constituent concentration of the waste gas gathered is measured by heat storage.
Description of drawings
Fig. 1 is the figure of the structure of expression continuous furnace.
Fig. 2 A is the figure of the structure of expression heat-accumulating burner.
Fig. 2 B is the figure of the structure of expression heat-accumulating burner.
Fig. 3 is the figure of the waste gas drain passageway of the existing process furnace of expression.
Fig. 4 is the figure of the waste gas drain passageway of expression process furnace of the present invention.
Fig. 5 is the figure of the structure of expression continuous furnace used in the present invention.
Fig. 6 is the figure of the relation of expression waste gas attraction rate and furnace pressure.
Fig. 7 is the figure of the relation of expression furnace pressure and invading air amount.
Fig. 8 is the figure of the structure of expression continuous furnace used in the present invention.
Fig. 9 is the figure of the relation of expression Flow-rate adjustment valve opening of diluent air and furnace pressure.
Figure 10 is the figure of the relation of oxygen concn in expression furnace pressure control method and furnace pressure and the stove.
Figure 11 is the figure of the relation of expression furnace pressure control method and furnace pressure.
Figure 12 is the figure of the relation of oxygen concn in expression furnace pressure control method and the stove.
Figure 13 is the figure of expression heating with configuration in the stove of burner.
Figure 14 is the figure of the extraction mouth of expression process furnace.
Figure 15 is the figure that the expression process furnace is extracted near the airflow of end out.
Figure 16 is that expression is heated with the air ratio of burner and the figure of the relation of the quantity combusted that enters air.
Figure 17 is the figure of expression from the drain passageway of the waste gas of heat-accumulating burner discharge.
Figure 18 is the in all sorts of ways measured value of the interior oxygen concn of mensuration stove and the figure that the interior average oxygen concentration of stove compares.
Embodiment
Below, with reference to accompanying drawing method of the present invention is described in detail.Fig. 5 represents the continuous furnace that the inventive method is directly used.This process furnace is substantially the same with stove shown in Figure 1.But, be at least at bottom configuration array Fig. 2 A and the heat-accumulating burner 40a shown in Fig. 2 B and the example of 40b on the conveying road 5 of soaking zone 3.In Fig. 5, comprise that the symbol of dual-purpose path and heat storage and 40a and 40b represent.The operation of this process furnace, according to the burning load of whole process furnace, adjusting is controlled furnace pressure from the waste gas attraction rate in above-mentioned burner 40a and 40b suction heat storage 42a and the 42b.Specifically, it is characterized in that the furnace pressure control of bottom band is become malleation.
Promptly, the operation of above-mentioned process furnace, with the furnace pressure meter actual measurement furnace pressure that is arranged on the bottom, soaking zone, according to the target furnace pressure, with the exhaust gas flow of Flow-rate adjustment valve regulation by the heat storage of heat-accumulating burner, control waste gas attraction rate like this, is controlled to be the target furnace pressure with bottom band, the particularly furnace pressure of bottom, soaking zone.
Fig. 6 represents the relation of waste gas attraction rate and furnace pressure.The expression aforesaid method, the furnace pressure of the bottom, soaking zone when regulating waste gas attraction rate and the relation of waste gas attraction rate according to burning load.The relation that waste gas attraction rate and furnace pressure roughly are inversely proportional to.By regulating waste gas attraction rate, can strictly control furnace pressure.So-called waste gas attraction rate means the exhausted air quantity of heat-accumulating burner suction and the ratio of the exhausted air quantity that burning produced of heat-accumulating burner.By just obtaining with the actual measurement of the exhaust gas flow meter on the exhaust pipeline that is arranged on heat-accumulating burner exhaust gas flow.
In addition, furnace pressure, by the adjusting of above-mentioned waste gas attraction rate, preferably the furnace pressure with the bottom, soaking zone is controlled in 0～0.5mmAq scope.If the furnace pressure of bottom, soaking zone is controlled at more than the 0.5mmAq, then the furnace pressure on top, soaking zone is too high, and furnace gas blows out outside stove, can damage the extraction fire door.Unit consumption of fuel also improves.
Fig. 8 represents the continuous furnace that the inventive method is directly used.This process furnace is substantially the same with the structure of process furnace shown in Figure 1.This process furnace has following structure, and promptly waste gas surpasses on the heat resisting temperature of heat exchanger 7a in limited time in the stove of delivery heat exchanger 7a, diluent air 8 is supplied with the inlet side of the heat exchanger 7a of flues 7, with protection heat exchanger 7a.
In the operation of the process furnace of this structure, except when spent air temperture surpasses the heat resisting temperature of heat exchanger 7a, also supply with diluent air 8 when the furnace pressure of 3 particularly bottom is lower than target value in the soaking zone.It is characterized in that, by supplying with the diluent air 8 of regulation flow, the furnace pressure control of the lower region of soaking zone 3 is become malleation.
That is, as shown in Figure 8, furnace pressure measured value PI and the target furnace pressure (malleation) that the furnace pressure meter 3b with the lower region that is arranged on soaking zone 3 measures compared with arithmetical unit 9a.According to its result, at first carry out the aperture setting of the flashboard 7b of furnace pressure control usefulness, thereby carry out furnace pressure control by arithmetical unit 9a.
At this usually in the operation, with arithmetical unit 9b to being that the heat resisting temperature upper limit of heat exchanger 7a compares with the waste gas target temperature of this position with the temperature measuring value T.I of the thermometer 7c mensuration of the heat exchanger 7a inlet side that is located at flue 7.If temperature measuring value T.I is near the heat resisting temperature upper limit of heat exchanger 7a, the then instruction of sending according to arithmetical unit 9b gives suitable rotation speed of the fan and Flow-rate adjustment valve opening respectively to Air Blast fan 8a and the flow control valve 8b that supplies with diluent air 8 usefulness.Supply with flue 7 by the diluent air 8 that will stipulate flow, diluent air 8 is sneaked in the waste gas, the spent air temperture that just will import interchanger 7a is reduced to allowed band.When temperature measuring value T.I equates with above-mentioned target temperature, fan attachment rotating speed and flow rate regulating valve aperture.
In addition, in above-mentioned common operation, for example the burning load of burner reduces, the furnace pressure measured value P.I that furnace pressure meter 3b measures departs from objectives furnace pressure and when becoming suction side, give suitable rotation speed of the fan and Flow-rate adjustment valve opening by arithmetical unit 9a respectively to Air Blast fan 8a and flow control valve 8b, the diluent air 8 of regulation flow is supplied with flue 7, so that furnace pressure rises.That is, when diluent air 8 was supplied with flue 7, by the gas flow increase of flue 7, so the pressure-losses of flue 7 increases, furnace pressure rose.Its result can avoid the furnace pressure of the lower region of soaking zone 3 to become negative pressure.When furnace pressure measured value P.I equates with above-mentioned target furnace pressure, fan attachment rotating speed and Flow-rate adjustment valve opening.
Fig. 9 represents the relation of furnace pressure of the lower region of the Flow-rate adjustment valve opening of diluent air 8 and soaking zone 3.By the Flow-rate adjustment of diluent air 8, the span of control of furnace pressure is very big.Even under the little situation of the burning load of burner, also can easily make the furnace pressure of the lower region of soaking zone 3 become malleation by supplying with diluent air 8.And, owing to utilize existing equipment, need not carry out new facility investment.
On continuous furnace shown in Figure 1, several heating in being provided in its stove are with among the burner 4, to be provided in stove extract out end lower region heating with burner 40 adopt with other heating with the different independently Controlling System of burner 4, control the burning that burner 40 is used in this heating independently.
Here, the burning in the process furnace is used burner 4 as shown in figure 13, and relatively setting paired 4a and 4b between the two side of process furnace is general example.Heating for the lower region that is configured in stove extraction end also is configured burner 40a and 40b in couples with burner 40.
For the material that is heated that process furnace heated is extracted out outside the stove, when opening the extraction fire door 3a of process furnace, the burning with burner 40a and 40b is heated in control independently.Shown in Fig. 2 A and Fig. 2 B, open heating and extracting out with the burner flame of burner 40a and 40b on the width of mouthful 3b with extending extracting fire door 3a out along the A/F running of burning.If form like this along the burner flame of the A/F of extracting mouthful 3b out, then enter air in the stove from extracting mouthful 3b out, at first cut off by burner flame, can not further enter in the stove.And the oxygen in the invading air is fallen by this burner consumed by fire, so the rising of oxygen concn in the stove that can avoid causing because of invading air.
Particularly as shown in figure 14, the extraction fire door that has the V shape peristome 3c of comb teeth shape in the bottom of extracting mouthful 3b out, enter air from this V shape peristome 3c easily, so extract the heating of the lower region of end out to cut off air intrusion path with the burner flame of burner 40a and 40b be very effective to be configured in stove.In addition, heating makes independent heating get final product to the burning control that the stove cross direction extends with the burner flame of burner with the occasion that burner does not dispose in pairs.
At this, the formation position of the burner flame of burner 40a and 40b is used in heating, on the furnace superintendent direction, and in burner flame does not touch the scope of the works of extracting mouthful bottom out, and preferably as best one can near extracting mouth out.In addition, on the short transverse of stove, burner flame is in the position that can block the V shape peristome, and is preferably in the scope at the bottom of the contact oven not.
In addition, as shown in figure 15, be preferably in the stove inboard of heating, be provided with from the axial spaced walls 8 of furnace bottom with burner 40a and 40b, and with the burner flame partition air admission path of heating with burner 40a and 40b.
Here, the pressure distribution in the stove is the boundary to carry road 6 as shown in figure 15, and the top pressure (be substantially normal atmosphere) outer with respect to stove is malleation, but the bottom is a negative pressure.That is, in stove, it is big more to arrive the below air-flow more usually, so furnace pressure presents such distribution, along with downwards near and reduce.On such process furnace, all zones becomes malleation in the stove if make, and then the stove internal upper part reaches than higher pressure, the result, and furnace gas can be from each peristome ejection.Therefore, control, make carrying that furnace pressure equates with normal atmosphere on the height location on road 6 with flashboard 7b (with reference to Fig. 1).
Particularly flow to conveying 6 bottoms, road from the air that V shape peristome 3c invades from extracting mouthful 3b out, the burner flame that major part is heated with burner 40a and 40b sucks.Because it is low temperature that invading air is compared with temperature in the stove, so shown in dotted line in Figure 15, the part of invading air flows into to the direction of sneaking into furnace bottom.Because this invading air flows into from rear side deep in stove of heating with burner 40a and 40b, so though amount is few, invade in the stove easily.
If establish spaced walls 8, then be spaced apart wall 8 with the air of the rear side intrusion of burner 40a and 40b and block from above-mentioned heating.Here be heated gradually and become, arrive the barotropic field of carrying 6 tops, road, so be discharged to outside the stove from conveying 6 tops, road along the upwelling of spaced walls 8.Like this, also can prevent in its intrusion stove for the air of invading with burner 40a and 40b rear side from heating.
In addition, when cutting off air and invade path with the burner flame of burner 40a and 40b, preferably make heating with burner 40a and the 40b running of under the condition of hanging down air ratio, burning with heating.The heating that Figure 16 represents to extract out end with the air of the air ratio of burner and intrusion in the relation of this heating with the quantity combusted on the burner.As known in the figure, if heating uses the air ratio of burner to descend, then invading air increases with the quantity combusted on the burner in heating.If make heating with burner 40a and the 40b running of under low air ratio condition, burning, can make then that mouthful airborne oxygen of 3b intrusion is direct to burn and consume from extracting out, be effective to making furnace atmosphere remain on low oxygen concentration.In addition, the size of spaced walls 8 between the stove two side in the scope of not disturbing the e Foerderanlage class in the stove, increases the height on furnace bottom, is favourable to cutting off invading air and forming upstream.
Fig. 4 represents to be directly used in the waste gas drain passageway of the continuous furnace of the inventive method.To the path 45 of suction device shown in Figure 48 and flue 7, be provided with pipeline 10 by heat storage 42a or 42b from the burner 40a shown in Fig. 2 A and Fig. 2 B or 40b.Be characterised in that,, be provided with the pipe arrangement road 10 that the waste gas in the flue 7 is imported suction device 8 by open and close valve 9 at the inlet side of suction device 8 and between with the flue 7 outside the guiding of the waste gas in the process furnace stove.On path 45, at the inlet side of suction device 8, the upstream side of the connection section of pipeline 10 is provided with under meter 45a, is used for measuring from burner sucking the waste gas traffic attraction, judges the switching time of open and close valve 9.In addition, be provided with flow control valve 45b between the connection section of pipeline 10 and path 45 and suction device 8, being used for the total Flow-rate adjustment is specified amount.
On process furnace with above waste gas drain passageway, burning load at heat-accumulating burner reduces, make under for example the state of suction device 8 less than 10% load running, the open and close valve 9 of above-mentioned pipeline 10 is opened, with suction device 8 inlet sides of the importing of the waste gas in the flue 7 path 45, the operating load of suction device 8 is increased.
Specifically, when the waste gas in the flue 7 are imported path 45, make the upper limit of waste gas and the durable temperature of the particularly impeller that is no more than suction device 8 by the mixed spent air temperture of the low temperature waste gas of heat storage in the flue.Select the caliber of pipeline 10, the flow of control waste gas makes the pressure-losses of waste gas in the flue of mixing point and the low temperature waste gas by heat storage equate simultaneously, mix waste gas is imported suction device 8 again.
By this operation, can realize making the operating load of suction device 8 for example to rise to more than 10% the above-mentioned variety of issue in the time of can solving utmost point low load combustion simply.
Then, when the traffic attraction of burner surpasses necessary minimum flow, the supply by waste gas in the flue of pipeline 10 is stopped.That is blind off a line 10 open and close valve 9.Steady running zone lower limit when so-called necessary minimum flow means the design fan.
In addition, the flow control that imports the waste gas of above-mentioned suction device 8 also can be carried out as flow control valve by the open and close valve 9 with pipeline 10.But the operation of flow control valve is miscellaneous, and its structure is also complicated, and setup fee is also high.In the present invention, adopt the short-cut method of the pipeline 10 that opens and closes the regulation caliber simply.
At this, the caliber of pipeline 10 for example can be according to following formula (A) and (B) is designed.
(waste gas dew point)≤Ta≤Tb... (A)
ΔP1＝ΔP2...(B)
In the formula,
Ta: be the temperature of the mix waste gas of V2=V1+V3
Tb: the durable temperature upper limit of suction device (is representative with the bearing)
At this,
V1: the waste gas traffic attraction during the minimum burning of burner (utmost point underload)
V2: be the necessary minimum flow of the waste gas that makes the suction device steady running
V3: be the exhausted air quantity of the difference of replenishing V2-V1
Δ P1: the pressure-losses between burner on the path 45 and the pipeline junction of two streams
Δ P2: the pressure-losses on the pipeline 10
In addition, as shown in Figure 4, be provided with interchanger 7a at the upstream side of the pipeline 10 of flue 7.By waste gas in the stove is fed interchanger 7a, like this, will become cryogenic waste gas supply line 10, this is more satisfactory to the durable life-span that prolongs suction device 8.
Above-mentioned form of implementation is not that the waste gas in the process furnace directly is mixed into from the waste gas that burner is discharged, but waste gas in the flue is mixed into from the waste gas that burner is discharged, so can not be subjected to external interference for the furnace pressure of process furnace.
Sneaking into the gas from the waste gas that burner is discharged, need not be confined to waste gas in the flue, can be that pyritous gas is hot blast.For example, can be to be heated to the pyritous air, perhaps also can establish combustion unit in addition, the combustion exhaust that produces with this combustion unit mixes.
Shown in Fig. 2 A and 2B, on heat-accumulating burner, the waste gas that is attracted by burner 40a or 40b passes through outside dual-purpose path 41a or the 41b guiding stove.The attraction of this waste gas is to carry out with path shown in Figure 17.Promptly, will be on the dual-purpose path 41a and the intensive exhaust pipeline 8a and 8b on each burner group of a side of being located at the furnace wall respectively and opposite side of 41b of the extension of array heat-accumulating burner, and exhaust pipeline 8a and 8b is intensive on 1 conduit 9, make this conduit 9 by attracting fan 10, being communicated with the flue 7 of process furnace.Utilize to attract the magnetism of fan 10,,, be discharged to outside the stove the waste gas flue 7 that leads by dual- purpose path 41a and 41b, exhaust pipeline 8a and 8b and conduit 9.
On above waste gas drain passageway, in example shown in Figure 17, in the way of conduit 9, insert gauge head 11.Be captured in mobile part waste gas in the conduit 9 by this gauge head 11, measure the concentration of various compositions with the waste gas of 12 pairs of these collections of analyzer.Resulting so various mensuration concentration value has been represented the distribution of the particularly stove cross direction of furnace atmosphere well.Can be with its typical value as the constituent concentration of position, for example soaking zone 3 in the stove that heat-accumulating burner is set.
At this, measure the occasion of oxygen concn and, investigated error with respect to average oxygen concentration in the stove by measure the occasion of oxygen concn from the gauge head of furnace wall insertion for gathering from the waste gas of above-mentioned heat-accumulating burner attraction.It the results are shown in Figure 18.As known in the figure, gather the occasion that the waste gas that attracts from heat-accumulating burner is measured oxygen concn, minimum with the difference of average oxygen concentration in the stove of reality.That is,, can measure the constituent concentration of actual furnace atmosphere by inquiry from the waste gas of heat-accumulating burner attraction.In addition, in the stove average oxygen concentration be close extract fire door and the fire door of packing into out, be 0Nm invading furnace air
3The furnace pressure of/h imposes a condition down, according to the gas flow, gaseous constituent and the air ratio that drop into burner, the calculated value of obtaining theoretically.Other condition is expression in detail in embodiment described later.
In addition, the position of gathering the waste gas that attracts from heat-accumulating burner is preferably in the downstream side of the hot body of heat-accumulating burner as shown in figure 17.By the spent air temperture behind the heat storage recovery heat, lower than temperature in the stove certainly.Gauge head is inserted in downstream side at heat storage, and gauge head can not be exposed in the high-temperature atmosphere, can prolong its work-ing life.
Above example has illustrated the situation of using continuous furnace, and batch-type process furnace and rotary heating furnace etc. also can adopt this invention.
With continuous furnace shown in Figure 5 (landline height: from furnace bottom 0.5m), the thickness of packing into is that 220mm, width are that 1200mm and length are the plate slab of 9800mm, carries out being heated to from room temperature 1230 ℃ heating operation.The specification of 4 groups of heat-accumulating burners that is configured in the process furnace soaking zone is as follows.
Burning capacity: 20000000 (Kcal/H burners)
Burning switching time between a pair of burner: 60s/ time
Waste gas attraction rate: 0.4～0.8 (one)
The operation of above-mentioned process furnace is as shown in table 1, according to the burning load amount of whole process furnace, the waste gas attraction rate of burner is carried out various adjustings control furnace pressure.In addition, for making comparisons, also carried out waste gas attraction rate is made as certain existing operation.Its result under the various burning load conditions when the process furnace actually operating, can stablize the control furnace pressure, and is as shown in table 2, compares with existing method, and oxygen concn significantly reduces in the stove, can reduce unit consumption of fuel and slab fraction defective.
In addition, bottom, the soaking zone furnace pressure that will be when aforesaid operations and the relation of invading air amount are shown in Fig. 7 fifty-fifty through arrangement.
With continuous furnace shown in Figure 8 (landline height: from furnace bottom 0.5m), the thickness of packing into is that 220mm, width are that 1200mm and length are the plate slab of 9800mm, carries out being heated to from room temperature 1230 ℃ operation.Operational condition is as follows.
Process furnace (burner) burning load: 10～100%
Diluent air flow: 0～50000 (Nm
3/ H)
Heat exchanger entrance side spent air temperture: below 750 ℃
The flashboard aperture of flue: 5～100%
In above-mentioned furnace operation, heat exchanger entrance side spent air temperture is more than 750 ℃ the time or the furnace pressure of the lower region of soaking zone is 0mmAq when following, supplies with diluent air with the condition of heat exchanger entrance side spent air temperture≤750 ℃ and bottom, soaking zone furnace pressure＞0mmAq.In addition, in order to make comparisons, also carried out carrying out the operation of furnace pressure control without diluent air.
In these operations, when the burning load of process furnace is made many variations, to extract fire door out be that furnace pressure and this regional oxygen concn of the soaking zone lower region of closing condition measured.Its measurement result is carried out furnace pressure control with diluent air as shown in figure 10, can make furnace pressure keep malleation, and can make oxygen concn also keep low-level.In contrast to this, only with existing flashboard control furnace pressure, furnace pressure and oxygen concn all produce very big variation.
In addition, in same operation, furnace pressure and oxygen concn when extracting fire door out to opening and closing are similarly measured, its measurement result is respectively as Figure 11 and shown in Figure 12, even opening and closing under the situation of extracting fire door out, owing to carry out furnace pressure control with diluent air, also can make furnace pressure keep malleation, and make oxygen concn also keep low-level.
In continuous furnace shown in Figure 1, carried out plate slab is heated to from room temperature 1150 ℃ operation.When the plate slab after the heating was extracted out from extracting fire door 3a out, the heating of extracting end out was with burner 40a and the 40b running of burning under the conditions shown in Table 3.In addition, on continuous furnace shown in Figure 1, be provided with spaced walls shown in Figure 15 8, in operation, under the condition of showing of table 3, extract plate slab out with such continuous furnace by following specification.And in order to make comparisons, original furnace operation of also having carried out making the heating of extracting end out under same condition, to burn and turn round with burner 4 with burner 40a and 40b and other heating.
The air capacity in the intrusion process furnace in the above various operations and the oxygen concn of soaking zone atmosphere are measured, and the result lists table 3 in.
Spaced walls height: the above 1.2m of furnace bottom
Width: wide identical with stove
(the landline height: the above 0.5m of furnace bottom), the thickness of packing into is that 220mm, width are that 1200mm and length are the plate slab of 9800mm, carries out being heated to from room temperature 1230 ℃ operation with continuous furnace shown in Figure 1.The specification of 4 groups of heat-accumulating burners that is configured in the process furnace soaking zone is as follows.
Burning capacity: 2000000 (Kcal/H burners)
Burning load: 10～100%
Burning switching time between a pair of burner: 60s/ time
Waste gas attraction rate: 60～90%
In the operation of above-mentioned process furnace, the waste gas that attracts from heat-accumulating burner is gathered a part of waste gas by the gauge head that inserts in conduit 9 ways, with the 12 pairs of waste gas of being gathered mensuration of analyzer oxygen concn by behind the heat storage.The oxygen concentration determination scope is 0～21Vol% in the stove, and atmosphere temperature is 200 ℃ in the pipe of conduit 9.In addition, in order to make comparisons,, measured oxygen concn by the gauge head that inserts from the furnace wall of soaking zone.
These are measured in concentration values and the stove average oxygen concentration make correlated result, as shown in figure 18,, use the occasion of measuring from the waste gas of heat-accumulating burner attraction according to the present invention, with the error of average oxygen concentration value in the stove less than 0.5%.And measure the occasion of oxygen concn by the gauge head that inserts from the furnace wall, with the error of average oxygen concentration value in the stove be 1～3%.
The possibility of utilizing on the industry
As mentioned above, can strictly carry out controling of the pressure of the oven according to the present invention. By this controling of the pressure of the oven, Can prevent positively that air from entering in the heating furnace from extracting fire door out. Can prevent material-to-be-heated quality Reduce. Can reduce the unit consumption of fuel of heating furnace. According to the present invention, even in the combustion of heat-accumulating burner Burn in the littler situation of load, the running of waste gas suction device also can be stablized. Owing to do not produce So condensed water is the stable operation of heating furnace. According to the present invention, can correctly measure gas in the heating furnace The constituent concentration of atmosphere. By the Atmosphere Control of carrying out according to this measured value, can produce height The product of quality. The assay method of the constituent concentration of mensuration heating furnace atmosphere of the present invention can Utilize existing equipment to carry out, thus do not need new equipment investment, can be real with lower cost Existing.
Table 1
| Operation | The burning load of whole heating furnace (%) | Example | Original example | ||
| Waste gas attraction rate (one) | Bottom, soaking zone furnace pressure (mmAq) | Waste gas attraction rate (one) | Bottom, soaking zone furnace pressure (mmAq) | ||
| 1 | 20 | 0.4 | 0 | 0.8 | -1.4 |
| 2 | 30 | 0.4 | 0 | 0.8 | -1.0 |
| 3 | 40 | 0.5 | 0 | 0.8 | -0.7 |
| 4 | 50 | 0.5 | 0.1 | 0.8 | -0.5 |
| 5 | 60 | 0.6 | 0.1 | 0.8 | -0.3 |
| 6 | 70 | 0.6 | 0.2 | 0.8 | -0.1 |
| 7 | 80 | 0.7 | 0.2 | 0.8 | 0 |
| 8 | 90 | 0.7 | 0.3 | 0.8 | 0.1 |
| 9 | 100 | 0.8 | 0.3 | 0.8 | 0.3 |
Table 2
| Invade furnace air amount (Nm3/ | Oxygen concentration (vol%) in the stove of soaking zone | Unit consumption of fuel (*) (index) | Fraction defective (*) (index) | |
| Example | Less than 500 | Less than 1 | 0.95 | Less than 0.1 |
| Original example | About 50000 | 5～10 | 1.0 | 1.0 |
(*): take the result of the original example exponential representation as 1 o'clock
(the more little achievement of numerical value is more good)
Table 3
| Operation | Burning load (%) | Air ratio | Spaced walls | Invading air amount (Nm3/H) | Oxygen concentration (vol%) | Remarks | ||
| Extract the end burner out | Other burner | Extract the end burner out | |
|||||
| 1 | 100 | 80 | 0.8 | 1.05 | Do not have | 500 | ≤1.0 | Example |
| 2 | 100 | 50 | 0.8 | 1.05 | Do not have | 600 | ≤1.5 | Example |
| 3 | 100 | 50 | 0.8 | 1.05 | Have | 300 | ≤1.0 | Example |
| 4 | 60 | 1.0 | Do not have | 5000 | 5～10 | Original example | ||
Claims (1)
1. the furnace pressure control method of a process furnace; it is characterized in that; in way, be provided with interchanger with the flue outside the guiding of the waste gas in the process furnace stove; when being the combustion air of burner with the heating source of the pre-heat supply process furnace of this interchanger; in order to protect interchanger not to be subjected to the infringement of high-temperature atmosphere; when the heat exchanger entrance side of flue is supplied with diluent air; regulate the flow of diluent air according to the burning load of the spent air temperture of heat exchanger entrance side and process furnace, control furnace pressure by the flow of diluent air.
Applications Claiming Priority (6)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2001008524A JP3937729B2 (en) | 2001-01-17 | 2001-01-17 | Heating furnace atmosphere control method and heating furnace |
| JP8523/01 | 2001-01-17 | ||
| JP8524/01 | 2001-01-17 | ||
| JP14230/01 | 2001-01-23 | ||
| JP16974/01 | 2001-01-25 | ||
| JP17017/01 | 2001-01-25 |
Related Parent Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNB018092470A Division CN100338236C (en) | 2001-01-17 | 2001-12-27 | Heating furnace with regenerative burners and method of operating heating furnace |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1693755A CN1693755A (en) | 2005-11-09 |
| CN1333087C true CN1333087C (en) | 2007-08-22 |
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ID=18876136
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNB2005100789386A Expired - Fee Related CN1333087C (en) | 2001-01-17 | 2001-12-27 | Heating furnace with regenerative burners and method of operating heating furnace |
| CNA2005100789456A Pending CN1693757A (en) | 2001-01-17 | 2001-12-27 | Heating furnace with regenerative burners and method of operating the heating furnace |
| CNA2005100789441A Pending CN1693756A (en) | 2001-01-17 | 2001-12-27 | Heating furnace with regenerative burners and method of operating heating furnace |
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| Application Number | Title | Priority Date | Filing Date |
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| CNA2005100789456A Pending CN1693757A (en) | 2001-01-17 | 2001-12-27 | Heating furnace with regenerative burners and method of operating the heating furnace |
| CNA2005100789441A Pending CN1693756A (en) | 2001-01-17 | 2001-12-27 | Heating furnace with regenerative burners and method of operating heating furnace |
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| JP (1) | JP3937729B2 (en) |
| CN (3) | CN1333087C (en) |
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| JP5452955B2 (en) * | 2009-03-13 | 2014-03-26 | 本田技研工業株式会社 | Preform heating device |
| CN101900359B (en) * | 2010-09-05 | 2012-02-15 | 无锡市盛力达机械工程有限公司 | Automatic pressure control device for gas furnace pressure |
| DE102011053698C5 (en) * | 2011-09-16 | 2017-11-16 | Benteler Automobiltechnik Gmbh | Process for the manufacture of structural and chassis components by thermoforming and heating station |
| US20180044758A1 (en) * | 2015-03-26 | 2018-02-15 | Taiyo Nippon Sanso Corporation | Device for heating iron and steel products, and method for heating iron and steel products |
| CN104949517A (en) * | 2015-06-19 | 2015-09-30 | 邯钢集团邯宝钢铁有限公司 | Rapid cooling method for steel rolling heating furnace heat exchanger |
| CN106676252B (en) * | 2017-02-21 | 2018-02-23 | 东北大学 | A kind of direct flame impingement heater of sheet metal strip |
| CN109141051B (en) * | 2018-10-12 | 2020-03-17 | 厦门大学嘉庚学院 | Optimal design method for furnace pressure control of heat accumulating type industrial heating furnace |
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- 2001-12-27 CN CNB2005100789386A patent/CN1333087C/en not_active Expired - Fee Related
- 2001-12-27 CN CNA2005100789456A patent/CN1693757A/en active Pending
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|---|---|---|---|---|
| JPS5776198A (en) * | 1980-10-30 | 1982-05-13 | Nippon Steel Corp | Control of terperature of material in heating furnace |
| JPH0728956U (en) * | 1993-09-30 | 1995-05-30 | 石川島播磨重工業株式会社 | Steel heating furnace |
| JPH07316645A (en) * | 1994-05-30 | 1995-12-05 | Sumitomo Metal Ind Ltd | Method for controlling heating furnace |
| JPH09209032A (en) * | 1996-02-01 | 1997-08-12 | Nippon Steel Corp | Method for controlling optimum furnace pressure in heating furnace |
Also Published As
| Publication number | Publication date |
|---|---|
| CN1693756A (en) | 2005-11-09 |
| JP3937729B2 (en) | 2007-06-27 |
| CN1693755A (en) | 2005-11-09 |
| CN1693757A (en) | 2005-11-09 |
| JP2002213879A (en) | 2002-07-31 |
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