• 专利附录
  • 专利说明
  • 权利要求
  • 类似技术
  • 同族专利
  • 引用文献
  • 法律状态
  • 优先权
    • 专利摘要:
    The invention relates to an industrial furnace comprising a thermally insulated enclosure and a plurality of burners distributed over a plurality of heating zones, the furnace further comprising recovery means (6) intended to recover thermal energy from recovery fumes (F2 ) resulting from a first combustion carried out by the burners. According to the invention, the recovery means (6) comprise a rotating regenerator (7) associated with each heating zone (Z1, Z2, Z3), each of the rotating regenerators (7) being adapted to receive a predetermined flow of smoke from recoveries, a predetermined flow rate of a supply air, and preheating this supply air to supply the burners (3) of the associated heating zone with a predetermined flow rate of preheated combustion air (9).
    公开号:BE1023618B1
    申请号:E2015/5066
    申请日:2015-02-10
    公开日:2017-05-17
    发明作者:Ludovic Ferrand；Patrick Dubois；De Sousa Eduardo Pinto
    申请人:Cockerill Maintenance & Ingenierie S.A.；
    IPC主号:
    专利说明:

    The invention relates to an industrial furnace for heating products such as iron and steel products.
    BACKGROUND OF THE INVENTION
    Many industrial furnaces for heating steel products, such as preheating furnaces for processing steel coils, comprise a thermally insulated enclosure and a plurality of burners arranged in the enclosure to heat the steel products circulating in 1 '. pregnant.
    The burners, conventionally distributed according to several temperature-controlled heating zones, are supplied with combustion air and with a natural gas type fuel, produce, by a first combustion, flames that heat the iron and steel products, and generate fumes circulating counter-cyclically. current of said steel products. These fumes are usually themselves treated by a second combustion called "post-combustion", whose role is to ensure complete combustion to remove fumes at least a portion of polluting gases such as carbon monoxide. The resulting smoke and less polluting are then removed from the oven and released into the atmosphere by a chimney.
    The energy consumption of preheating furnaces for processing steel coils is particularly high, of the order of 220 kWh of natural gas per tonne of heated steel. It is therefore particularly important, both from an environmental and an economic point of view, to try to improve the energy efficiency of these ovens.
    For this, a first method usually used is to equip the furnaces with energy recovery means to recover the heat lost in the fumes. These recovery means are typically constituted by a tubular bundle heat exchanger comprising metal tubes in which circulates the combustion air used by the burners. The fumes, circulating around the tubes, preheat the combustion air, which improves the efficiency of the first combustion mentioned earlier. This heat recovery is, however, limited by the maximum permissible temperature that can withstand the tubes, which makes it necessary to dilute the fumes with cold air.
    A second method, which has now largely supplanted the first method, is to use regenerative burners. This solution, however, has a number of disadvantages. First of all, the regenerative burners are not suitable for sucking fumes that are unburned in the burner, because it then becomes impossible to carry out an afterburner. This solution is moreover difficult to apply to compact furnaces because of the one hand, of the space of regenerative tanks which are equipped with the burners and, on the other hand, the need to install the double of regenerative burners compared to to the number of burners of a standard solution. Regenerative burners operate in pairs, according to a cyclic operation: the burners are half of the time in one mode of combustion and the other half of the time in a mode of accumulation of heat.
    OBJECT OF THE INVENTION The invention aims to improve the energy efficiency of an industrial furnace while having an acceptable size.
    SUMMARY OF THE INVENTION
    In order to achieve this goal, an industrial furnace is proposed for heating products such as steel products, the furnace comprising a thermally insulated enclosure and a plurality of burners arranged in the enclosure for heating the products flowing from one end to the other. the other of the enclosure, the burners being distributed according to a plurality of temperature-controlled heating zones. The oven further comprises recovery means for recovering thermal energy recovery fumes from a first combustion performed by the burners so as to improve energy efficiency of the furnace. According to the invention, the recovery means comprise a rotating regenerator associated with each heating zone, each of the rotating regenerators being adapted to receive a predetermined flow rate of the recovery fumes via a first pipe, to receive a predetermined flow rate of air from a supply via a second pipe, to preheat this supply air to provide the burners of the associated heating zone a predetermined flow of preheated combustion air via a third pipe, and to exhaust exhaust gases via a fourth pipe .
    Thus, the energy efficiency of the furnace is improved through a recovery of thermal energy achieved by means of rotating regenerators which have congestion acceptable for most industrial furnaces. The invention will be better understood in the light of the following description of a particular non-limiting embodiment of the invention. BRIEF DESCRIPTION OF THE DRAWINGS Reference will be made to the single figure schematically showing an industrial furnace of the invention. DETAILED DESCRIPTION OF THE INVENTION The invention relates to an industrial furnace for heating products such as steel products, and is here implemented in a non-oxidizing preheating furnace of steel strips for continuous lines of treatment of coils of steel. 'steel.
    The furnace of the invention 1 comprises a thermally insulated enclosure 2, a plurality of burners 3 arranged in the enclosure 2 to achieve a first combustion and heat a steel strip 4 flowing from one end to the other of the enclosure 2, so-called "post-combustion" means 5 adapted to achieve a second combustion, and recovery means 6.
    The plurality of burners 3 is constituted by ten burners 3 distributed in a plurality of temperature-controlled heating zones, in this case according to three heating zones Z1, Z2, Z3. This distribution makes it possible to regulate the temperature of the oven 1 by virtue of only three thermocouples 7 positioned in the heating zones Z1, Z2, Z3, so as to conform the temperature of the oven to predetermined heating curves which depend in particular on a temperature of The heating zones Z1, Z2, Z3 are thus controlled according to temperature setpoints typically between 1200 and 1350 degrees Celsius for a desired band temperature at the level of a desired band at the furnace 1. SI strip output of oven 1 between 550 and 750 degrees Celsius.
    The first combustion performed by the burners 3 requires a fuel, here natural gas, and an oxidant, here combustion air Ac.
    The burners 3 operate here in so-called "substoichiometric" mode, also called combustion in air defect or combustion in rich gas. In the sub-stoichiometric regime, a combustion air flow rate is always less than an air flow rate necessary to completely burn a flow rate of natural gas Gn introduced into the same burner. Fumes of first combustion F1 are then generated by the burners 3, said fumes of first combustion Fl having a so-called "incomplete" combustion, an oxygen content of which is almost zero, the oxygen of the combustion air having combined entirely or almost with natural gas. The sub-stoichiometric regime is particularly advantageous since it makes it possible to confer on the fumes of first combustion Fl a reducing power on the steel strip 4, which makes it possible to avoid the formation of oxides on the steel strip, type of iron oxide for example, and even to reduce some oxides possibly present on the steel strip before this first combustion. This improves the quality of the steel strip preheated by the furnace of the invention.
    The fumes of the first combustion Fl are charged with intermediate compounds after the first incomplete combustion, for example dihydrogen or carbon monoxide. Carbon monoxide can not be released into the atmosphere because it is a pollutant whose emissions are regulated.
    The post-combustion means 5 are thus used to carry out the second combustion, which consists in injecting air called "post-combustion air" Apc, whose role is to complete the first combustion, performed by the burners 3, in order to suppress the first combustion fumes Fl the intermediate compounds. Like the fumes of first combustion
    Fl flow generally against the current of the steel strip 4, the post-combustion means 5 are located in the furnace 1 upstream of the burners 3, that is to say they are located between an inlet E 3. The post-combustion air Apc is injected by the post-combustion means 5 according to a post-combustion air flow Apc dosed to ensure complete combustion without adding unnecessary air. Advantageously, the post-combustion air Apc is injected into an area of the enclosure in which the steel strip has a temperature that is too low to undergo the effects of oxidation caused by oxygen in the air. postcombustion Apc in excess. Alternatively, the afterburning air Apc can be injected from flue gas flues.
    Recovery fumes F2, at least partially depolluted, are generated by the second combustion.
    The recovery means 6 are intended to recover thermal energy from these recovery fumes F2, which are therefore derived from the first combustion and the second combustion. This improves the energy efficiency of the furnace 1.
    The recovery means 6 comprise a rotating regenerator 7 associated with each heating zone Z1, Z2, Z3, and hence here three rotating regenerators 7. The role of these rotating regenerators 7 is to heat a predetermined flow of supply air 8 so as to provide a predetermined flow rate of preheated combustion air 9. The fact of using a preheated combustion air Ac makes it possible to significantly increase the efficiency of the first combustion by decreasing the amount of natural gas Gn required for that and, therefore, to increase the energy efficiency of the furnace of the invention 1.
    Each rotating regenerator 7 is adapted to receive a predetermined flow of recovery fumes 10 via a first pipe 11, to receive the predetermined flow of supply air 8 via a second pipe 12, to preheat this supply air Aa to provide to the burners 3 of the heating zone associated with the regenerator rotating 7 the predetermined flow of preheated combustion air 9 via a third pipe 14, and to exhaust exhaust fumes F3 via a fourth pipe 15.
    Each rotating regenerator 7 is fed continuously by the predetermined flow of feed air 8 and by the predetermined flow rate of recovery fumes 10. Each rotating regenerator 7 comprises, in a manner known per se, rotating compartments which are placed in communication a first half of the time with the first pipe 11, which allows a warming of the interior of the regenerator 7, then a second half of the time with the second pipe 12, which allows to supply air supply Aa the rotating regenerator 7. The supply air Aa, which is never in contact with the recovery fumes, is thus preheated, which allows to provide the associated burner 7 the predetermined flow of preheated combustion air 9 .
    The recovery fumes F2 are distributed in each rotating regenerator 7 so as to always maintain a certain distribution ratio between the predetermined flow rate of supply air 8 and the predetermined flow rate of recovery fumes 10.
    Advantageously, a distribution ratio is set between the predetermined flow rate of supply air 8 and the predetermined flow rate of recovery fumes 10 of between approximately 1 and 1.2, such a distribution ratio making it possible to optimize the energy efficiency of the oven of the invention.
    To obtain the desired distribution ratio, the predetermined flow rate of recovery fumes received by each rotating regenerator 7 is first regulated by first regulating means comprising a first valve 17 mounted on the fourth line 15 of said rotary regenerator 7. Thus, for each rotating regenerator 7, the predetermined flow rate of recovery fumes 10 is regulated indirectly, thanks to a regulation of the flow rate of the exhaust fumes F3. This regulation is effected by means in particular of the first valve 17 which is mounted downstream of said rotary regenerator 7, that is to say which is located between the rotating regenerator 7 and a furnace exhaust outlet S2 which is here implemented. communication with a chimney 25 through which the exhaust fumes are removed from the furnace 1.
    The predetermined flow rate of supply air 8 received by each rotating regenerator 7 is further regulated by second regulating means comprising a second valve 20 mounted on the second pipe 12 of the said rotary regenerator 7. Thus, for each rotating regenerator 7, the predetermined flow rate of supply air 8 is regulated directly by means in particular of the second valve 20, which makes it possible to eliminate any regulatory inaccuracies due to possible leaks between feed air and recovery fumes. inside the rotating regenerators 7.
    It is necessary, in order to regulate the predetermined flow rate of the recovery fumes 10 and the predetermined feed air flow 8, to measure the predetermined flow rate of combustion air 9. To do this, a flowmeter 21 is mounted on the third conduit 14 each rotary regenerator 7, each flowmeter 21 being adapted to measure the combustion air flow rate 9 supplied to the burners 3 of the heating zone Z1, Z2, Z3 associated with said rotating regenerator 7. Advantageously, a flow measurement generating little loss of pressure in the pipe, which keeps the combustion air at a relatively low pressure. Preferably, a flowmeter 21 of the Venturi tube or Pitot tube or Vortex effect type will be chosen. The preheated combustion air is brought to temperatures typically between 800 degrees Celsius and 1000 degrees Celsius, while the exhaust fumes are brought to temperatures typically between 150 degrees Celsius and 250 degrees Celsius.
    It should be noted here that the first and second regulating means, comprising respectively the first 17 and second valves 20, are situated on the fourth and second conduits 8, which have relatively low temperatures relative to the first 11 and third lines 14. Control means are therefore a less expensive and more reliable solution than a similar solution located on the hotter pipes.
    It is furthermore intended to be able to ensure, if necessary, a complete seal between the third pipe 14 and the inside of the thermally insulated enclosure 2. In fact, when one or more heating zones Z1, Z2, Z3 are when stopped, for example due to a decrease in a speed of movement of the steel strip 4 in the chamber 2, a combustion air penetration into the chamber must absolutely be avoided. Such air penetration would tend to diminish the benefits of the sub-stoichiometric regime discussed earlier.
    As a simple valve can not be perfectly sealed, the third pipe 14 of each regenerator rotating two shutoff valves 22 is mounted on the third pipe 14, and inert gas injection means 23 is mounted on the third pipe 14. the nitrogen, to fill a gap between the two shutoff valves with gas 23. This maintains a positive pressure between the two shutoff valves 23, so that in case of leakage at one of the shutoff valves , only an inert gas leakage flow can enter the chamber 2.
    Advantageously, the post-combustion air (Apc) comes in part from the preheated combustion air generated by at least one rotating regenerator, possibly oversized for this purpose. This further improves the energy efficiency of the furnace of the invention. The invention is not limited to the particular embodiment which has just been described, but, on the contrary, covers any variant within the scope of the invention as defined by the claims.
    It is in particular possible to provide an oven having a different number of burners distributed according to a different number of heating zones.
    The temperature ranges provided are indicative, and may of course differ in different applications using the oven of the invention.
    权利要求:
    Claims (10)
    [1]
    1. Industrial furnace for heating products (4) such as steel products, the furnace comprising a thermally insulated enclosure (2) and a plurality of burners (3) arranged in the enclosure (2) for heating the products flowing from a end to another of the chamber, the burners (3) being distributed in a plurality of temperature-controlled heating zones (Z1, Z2, Z3), the oven further comprising recovery means (6) for recovering a thermal energy recovery fumes (F2) from a first combustion performed by the burners so as to improve an energy efficiency of the furnace, characterized in that the recovery means (6) comprise a rotary regenerator (7) associated with each heating zone (ZI, Z2, Z3), each of the rotating regenerators (7) being adapted to receive a predetermined flow rate of recovery fumes (10) via a first pipe (11), to be received a predetermined flow of a feed air (8) via a second pipe (12), to preheat this supply air to provide the burners (3) of the associated heating zone a predetermined flow of preheated combustion air (9) via a third pipe (14), and to evacuate exhaust fumes (F3) via a fourth pipe (15).
    [2]
    2. Industrial furnace according to claim 1, wherein the predetermined flow rate of the recovery fumes (10) received by each rotating regenerator (7) is regulated by first regulating means comprising a first valve (17) mounted on the fourth pipe ( 15) of said rotating regenerator (7).
    [3]
    3. Industrial furnace according to claim 1, wherein the predetermined flow rate of supply air (8) received by each rotating regenerator (7) is regulated by second regulating means comprising a second valve (20) mounted on the second conduit (12) of said rotating regenerator (7).
    [4]
    4. Industrial furnace according to claim 1, wherein, for each rotating regenerator, a flowmeter (21) is mounted on the third pipe (14) of said revolving regenerator (7).
    [5]
    5. Industrial furnace according to claim 4, wherein at least one of the flowmeters is Venturi tube type or Pitot tube or Vortex effect.
    [6]
    6. Industrial furnace according to claim 1, wherein, for each rotating regenerator, two shutoff valves (22) are mounted on the third pipe (11), and gas injection means (23) are mounted on the third conduit (14) for filling an inert gas space between the two shutoff valves (22).
    [7]
    7. Industrial furnace according to claim 6, wherein the injected gas is nitrogen.
    [8]
    8. Industrial furnace according to one of the preceding claims, wherein the recovery fumes are generated by a second combustion to complete the first combustion performed by the burners (3).
    [9]
    9. Industrial furnace according to claim 9, wherein a post-combustion air (Apc) used for the second combustion comes in part from the preheated combustion air (Ac) generated by at least one rotating regenerator (7).
    [10]
    10. Industrial furnace according to one of the preceding claims, a ratio between the predetermined flow rate of supply air (8) and the predetermined flow rate of recovery fumes (10) is between 1 and 1.2.
    类似技术:
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    BE460236A|
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    同族专利:
    公开号 | 公开日
    BE1023618A1|2017-05-17|
    FR3018344A1|2015-09-11|
    RU2016138842A|2018-04-04|
    EP3114243B1|2018-10-24|
    WO2015132082A1|2015-09-11|
    EP3114243A1|2017-01-11|
    US20170082364A1|2017-03-23|
    RU2016138842A3|2018-10-22|
    FR3018344B1|2016-04-29|
    CN106164302A|2016-11-23|
    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
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    法律状态:
    2020-10-28| MM| Lapsed because of non-payment of the annual fee|Effective date: 20200229 |
    优先权:
    申请号 | 申请日 | 专利标题
    FR1451767A|FR3018344B1|2014-03-04|2014-03-04|INDUSTRIAL OVEN FOR HEATING PRODUCTS SUCH AS STEEL PRODUCTS|
    FR1451767|2014-03-04|
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