Device and method for heating furnaces by means of radiant tubes
10830432 · 2020-11-10
Assignee
Inventors
Cpc classification
F23N2237/10
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F23C3/002
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F23C2900/99001
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F23K2900/05003
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F23N5/02
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
Y02E20/34
GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
International classification
F23C3/00
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
Abstract
To heat a furnace chamber (16) indirectly using radiant tubes (11) to (14), heating energy is transferred through the radiant tube wall into the furnace chamber (16). During steady-state operation, the temperature in the radiant tube (11) to (14) and on its surface is higher than the furnace, depending on the specific heat output of the radiant tube (11) to (14). At a furnace temperature of 770 C. and a heat output of 50 kW/m2, the radiant tube has a temperature of 900 C. The radiant tube (11) to (14) can thus operate continuously with flameless oxidation at this output, even though the temperature in the furnace is only 100 C. However, if the radiant tube (11) to (14) has cooled to the furnace temperature of 770 C. during a break in burning, deflagration is avoided when the associated burner is ignited by initially operating said burner with a flame for a few seconds.
Claims
1. A furnace heating device, for the heat treatment of goods in a furnace chamber (16), comprising: at least one radiant tube (11), configured to heat the furnace chamber (16) and which can be heated using a burner (17), which can be operated in a first operating mode (F) with a flame and in a second operating mode (NF) with flameless oxidation, at least one control device (21), configured to control on and off states and an operating mode setting for the burner (17) of the radiant tube (11), wherein the at least one control device (21) is configured to fix the temperature (T) of the furnace chamber (16) to a setpoint temperature (T.sub.s), which lies below a critical temperature (T.sub.k), which must at least be present in a combustion chamber for flameless oxidation of the used fuel, but lies above a lower temperature (T.sub.u), at which the burner (17) of the radiant tube (11) can be operated in a flameless manner, wherein the at least one control device (21) is designed to operate the burner (17) in the second operating mode (NF) at a temperature (T) of the furnace chamber (16) lying above the lower temperature (T.sub.u) and below the critical temperature (T.sub.k); wherein the control device (21) is designed to identify a warm start only if the temperature (T) of the furnace chamber (16) lies below the critical temperature limit (T.sub.k), but above the lower temperature (T.sub.u); wherein the control device (21) is designed to operate the burner (17) in the first operating mode (F) for a period of time (t) only in case of a warm start; wherein the period of time (t) is fixed.
2. The furnace heating device according to claim 1, wherein the control device (21) is designed, at start-up and with a temperature (T) of the furnace chamber (16) below the critical temperature (T.sub.k), but above the temperature (T.sub.u), to ignite the burner (17) initially in the first operating mode (F) and to operate the burner (17) in said mode for the period of time (t) and to then operate the burner (17) in the second operating mode (NF).
3. The furnace heating device according to claim 1, wherein the control device (21) is designed to switch the burner (17) between the on and off states in order to adjust the temperature of the furnace chamber (16).
4. The furnace heating device according to claim 1, further comprising a device (26) configured to detect the furnace temperature at least locally and that is connected to the control device (21).
5. The furnace heating device according to claim 4, wherein the device (26) comprises at least one switching temperature sensor (27).
6. The furnace heating device according to claim 4, wherein the device (26) is arranged outside the radiant tube (11), at a distance therefrom.
7. The furnace heating device according to claim 1, wherein the period of time (t) is fixed depending on the temperature (T) of the furnace chamber (16).
8. A method for igniting burners (17) for heating intermittently operated radiant tubes (11) in a warm start mode following a break in burning when the furnace is hot, in which the operating temperature (T) of the furnace lies below a critical temperature (T.sub.k), which at least must be present in a furnace chamber for flameless oxidation of the used fuel, but above a lower temperature (T.sub.u) at which the burner (17) of the radiant tube (11) can be operated in a flameless manner, wherein the method comprises: igniting the burner (17) in a first operating mode (F), in which it functions with flame, and switching the burner (17) over to a second operating mode (NF) with flameless oxidation, regardless of the furnace temperature (T) still lying below the temperature limit (T.sub.k); identifying a warm start only if the temperature (T) of the furnace chamber (16) lies below the critical temperature limit (T.sub.k), but above the lower temperature (T.sub.u); operating the burner (17) in the first operating mode (F) for a period of time (t) only in case of a warm start; wherein the period of time (t) is fixed.
9. The method according to claim 8, further comprising: igniting the burner (17), in the cold-start mode, with a temperature of the furnace chamber (16) below the lower temperature (T.sub.u), with a flame in the first operating mode (F), and switching the burner (17) over to the second operating mode (NF) without flame in response to the temperature (T) of the furnace chamber (16) exceeding the lower temperature (T.sub.u).
10. The method according to claim 8, further comprising operating the burner (17) in pulsed burning operation in order to adjust the temperature (T) of the furnace chamber to a desired temperature (T.sub.s).
11. The method according to claim 10, wherein the desired temperature (T.sub.s) of the furnace chamber (16) lies above the lower temperature (T.sub.u), but below the critical temperature (T.sub.k).
12. The method according to claim 8, wherein the period of time (t) is fixed depending on the temperature (T) of the furnace chamber (16).
Description
BRIEF DESCRIPTION OF THE DRAWINGS
(1) Details of advantageous developments of the invention are the subject of the drawing of the description or claims. In the drawings:
(2)
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DETAILED DESCRIPTION
(7) A furnace heating device 10 is shown in
(8) The radiant tubes 11 to 14 are heated by burners 17, 18, 19, 20 depicted merely symbolically in
(9) Each burner 17 to 20 comprises heat recovery devices, for example in the form of recuperators and/or generators, in order to use waste gas heat in order to preheat combustion air (and fuel). The burners 17 to 20 preferably work with high air preheating, such that the air fed for combustion has a temperature of more than 500 C. The air, gas and waste gas lines and control members arranged therein, for example valves, are not shown separately in
(10) The burners 17 to 20 can be operated in a first operating mode F, in which they form a flame. This operating mode is used for a cold start, i.e. for heating operation of the radiant tubes 11 to 14 and of the furnace chamber. Once the furnace chamber has been heated to at least a temperature T.sub.u, the burners 17 to 20 operated up to this point in the first operating mode F are switched over to a second operating mode NF without flame (operation with flameless oxidation FLOX). The second operating mode NF is characterised by a particularly low level of NOx production.
(11) The lowest temperature T.sub.u of the furnace chamber at which the burners can be operated in the second operating mode NF is dependent on the burner output and thus on the temperature reached with operating burners in the radiant tube interior. The lowest temperature T.sub.u of the furnace chamber at which FLOX operation, i.e. operation in the second operating mode NF, is possible can be 750 C., for example (
(12) In order to switch the burners 17 to 20 on and off and in order to switch the burners 17 to 20 over from the first operating mode F into the second operating mode NF (or vice versa), a control device 21 is provided. The control device controls the operation of the group formed by the burners 17 to 20, as indicated by arrows 22, 23, 24, 25, so as to switch said burners on and off jointly (i.e. simultaneously) in order to hold the temperature of the furnace chamber 16 at the setpoint temperature T.sub.s of for example 770 C., for example during the course of two-step control. The temperature T.sub.s is slightly above the temperature T.sub.u.
(13) In order to detect the furnace temperature T, a temperature detection device 26 is provided, which has at least one, possibly also a plurality of temperature sensors 27, 28. The temperature sensors 27, 28 are preferably formed as temperature switches. For example, the temperature sensor 27 can be set to the desired furnace temperature T.sub.s and to this end can have a switching temperature of 770 C., for example. The temperature sensor 27 can be used to implement pulsed burning of the burners 17 to 20 in order to adjust the furnace temperature to the desired value.
(14) The second temperature sensor 28 can be set to the lowest temperature T.sub.u at which an active burner can be switched over from the first operating mode F into the second operating mode NF. For example, it can have a switching temperature of 750 C.
(15) The furnace heating device 10 described in this respect functions as follows:
(16) In the case of a cold start shown on the left in
(17) If the furnace chamber 16 is heated to the setpoint temperature T.sub.s, for example 770 C., this temperature T.sub.s is maintained by pulsed burning operation of the burners 17 to 20. For example, the temperature sensor 27 switches on and off with a certain hysteresis as the operating temperature is exceeded and undershot, i.e. it outputs a switching signal to the control device 21. This control device adjusts the temperature in the furnace chamber 16 by switching the burners 17 to 20 on and off accordingly.
(18) Although the furnace temperature in the case of pulsed burning operation lies at or above the lowest temperature T.sub.u (for example 750 C.) at which flameless operation FL is possible and at which a switchover is made during heating from flame operation (first operating mode F) to flameless operation (second operating mode NF), the burners 17 to 20 are operated in the first operating mode F with a flame when switched on again, in each case for a short time t. The burners 17 to 20 can thus be ignited without deflagration, even if the radiant tubes 11 to 14 have a temperature lower than the critical temperature T.sub.k (typically 850 C.). Once the period of time t has elapsed, the control device 21 switches over the burners 17 to 20 to flameless operation NF.
(19) This process is illustrated again in
(20) The furnace heating device 10 described in this regard has at least two operating modes, specifically heating of the radiant tubes 11 to 14 with the burners 17 to 20 in the first operating mode F, and control operation, by means of pulsed burning, in which the burners 17 to 20 are switched on and off in a pulsed manner in order to maintain a desired furnace temperature T.sub.s. The furnace temperature T.sub.s in the case of control operation lies below a critical temperature T.sub.k suitable for flameless oxidation. This temperature T.sub.k is dependent on the used fuel, and in the case of natural gas is approximately 850 C. In the case of control operation (pulsed burning operation), the burners 17 to 20 are therefore always ignited in a starting sequence, in which the burners 17 to 20 are ignited at the start in the first operating mode F for a short period of time t, wherein a transition is made to the second operating mode NF with flameless oxidation once the period of time t has elapsed. In this way, the furnace chamber 16 can be operated at moderate operating temperatures T.sub.s of less than T.sub.k with high air preheating and therefore improved energy utilisation alongside low nitrogen oxide emissions.
(21) It is possible to specify the period of time t as a fixed value, as is shown in
(22) Although the burner when switched on again is thus ignited at a furnace temperature T, which is above the temperature T.sub.u at which a transition was made after the cold start from the first operating mode F to the second operating mode NF, the burner when switched back on is now ignited firstly in the first operating mode F and is then switched over to the second operating mode NF only after a few seconds.
(23) Alternatively or additionally, further temperature sensors can be provided. For example, a temperature sensor for temperatures in the furnace chamber 16 above 850 C. can send a signal to the control device 21, so that said control device starts the burners immediately in the second operating mode NF without switching them first into a first operating mode F.
(24) A further possible modification or development of the principle according to the invention is possible in that the period of time t for which the burners 17 to 20 are operated in the first operating mode F with flame in the case of each start, in accordance with
(25) To heat a furnace chamber 16 indirectly using radiant tubes 11 to 14, heating energy is transferred through the radiant tube wall into the furnace chamber 16. During steady-state operation, the temperature in the radiant tube 11 to 14 and on the surface thereof is higher than the furnace, said higher temperature depending on the specific heat output of the radiant tube 11 to 14. At a furnace temperature of for example 770 C. (<T.sub.k) and a heat output of 50 kW/m.sup.2, the radiant tube has an inner temperature of 900 C. (>T.sub.k). The fuel-dependent critical temperature T.sub.k from which flameless oxidation is possible can be 850 C., for example. The radiant tube 11 to 14 can thus operate continuously with flameless oxidation at this output, even though the temperature in the furnace is only 770 C. (<T.sub.k). However, if the radiant tube 11 to 14 has cooled to a temperature below T.sub.k during a break in burning, deflagration is avoided when the associated burner is ignited by initially operating said burner with a flame (operating mode F) for a few seconds, before a transition is made to operating mode NF.
REFERENCE SIGNS
(26) TABLE-US-00001 10 furnace heating device 11-14 radiant heating tubes/radiant tubes 15 furnace wall 16 furnace chamber 17-20 burner 21 control device 22-25 arrows 26 temperature detection device 27, 28 temperature sensors F first operating mode, burner with flame NF second operating mode, flameless oxidation T temperature t time