This application relates to an sensor system that is integrated into a furnace for improving operation of the combustion processes in the furnace, including but not limited to process efficiency, yield, and throughput.
Many industries use oxy-fuel combustion in a furnace for heating of bulk materials or feedstock but often have inadequate means to measure and control furnace parameters in order to optimize the heating processes. It is typical in a variety of industries (e.g., aluminum recycling, steel production, glass manufacturing) to place basic temperature sensors in locations around a furnace dictated by “common sense” or convenience, which often results in measurement errors and lost production capability.
Most typically, the rate of energy input in a heating or melting furnace is controlled based on comparing the temperature measurement of a thermocouple (TC) with a pre-determined setpoint (Tsp). This thermocouple, denoted herein as TOPEN, usually has three characteristics—(1) it is open or exposed to the furnace atmosphere, (2) it is located on a roof or an opposing wall from a burner and (3) it is installed flush with refractory hot face—the combination of which renders the TC susceptible to picking up “direct radiation” from a flame in the furnace just like other surfaces in the furnace (e.g., refractory walls and product surfaces). The charge or product being heated and/or melted is the largest heat sink in the furnace and is able to absorb (at its surface) and conduct (into the body of the charge due to its higher thermal conductivity) the incident energy. However, the refractory wall surface (which has a lower thermal conductivity) and open TC, TOPEN, continue to be radiated upon and increase in temperature. This results in a deviation between the actual product temperature, TPROD, (measured either at the product surface or as an average temperature of the bulk product), and in particular, TOPEN can exceed TPROD by a few or even several hundred degrees. As a consequence, the energy input into the furnace from the burners maybe prematurely decreased because the temperature of the control thermocouple TOPEN reaches the temperature setpoint TSP well before the actual product temperature TPROD, thereby leading to longer heating and/or melting times than desired.
Methods and systems are described herein which strategically position various combinations of sensors and/or sensor types in a furnace, such that the strategic placement (which may include physical co-locality of some or all of the sensors), creates an integrated sensor system that enables improved furnace control and operation. This results in enhanced process yields, efficiencies, and/or throughputs. Field and lab generated data demonstrate several surprising operational advantages that can be obtained using the methods and systems described herein.
Aspect 1. An integrated sensor system for use in a furnace system including a furnace and a flue, the integrated sensor system comprising: a sensor block configured to be mounted in a wall of the furnace system, the sensor block including at least two ports, each port being configured to receive a sensor; two or more sensors each positioned in a corresponding one of the ports in the sensor block; and a controller programmed to receive signals from the two or more sensors and to adjust operation of the furnace system in response to the received signals; wherein the two sensors are each selected from the group consisting of: temperature sensors, pressure sensors, composition sensors, concentration sensors, radiation sensors, density sensors, thermal conductivity sensors, optical sensors, acoustic sensors, level sensors, angle sensors, distance sensors, position sensors, image acquisition sensors, and video acquisition sensors.
Aspect 2. The integrated sensor system of Aspect 1, wherein the controller is programmed to monitor at least one of the sensor signals continuously.
Aspect 3. The integrated sensor system of Aspect 1, wherein the controller is programmed to monitor at least one of the sensor signals intermittently.
Aspect 4. The integrated sensor system of Aspect 1, further comprising an actuator mechanism corresponding to one of the sensors for advancing said sensor into a position for taking a measurement and retracting said sensor to a protected position; wherein the controller is programmed to monitor the signal from said sensor only when the sensor is advanced into the position for taking a measurement.
Aspect 5. A method of controlling energy input and energy distribution in a furnace using an integrated sensor system as in Aspect 1, wherein the two or more sensors include a first temperature sensor open to the furnace and second temperature sensor embedded in a wall of the furnace, comprising: controlling energy input into the furnace based on a signal from the second temperature sensor while controlling energy distribution based on a signal from the first temperature sensor, wherein the first temperature sensor responds more rapidly to local conditions that the second temperature sensor.
Aspect 6. A method of controlling energy input and energy distribution in a furnace using an integrated sensor system as in Aspect 1, wherein the two or more sensors include a first optical pyrometer or sensor directed at one location in the furnace and second optical pyrometer or sensor directed at another location in the furnace, comprising: controlling energy input into the furnace based on a signal from the second temperature sensor while controlling energy distribution based on a signal from the first temperature sensor, wherein the first temperature sensor responds more rapidly to local conditions that the second temperature sensor.
Aspect 7. A method of controlling one or more of excess oxygen, NOx, CO, and flammable emissions in a furnace using an integrated sensor system as in Aspect 1, wherein the two or more sensors include a pressure sensor and a composition sensor, comprising: controlling one or both of a flue gas damper and an oxygen-enrichment level in the furnace based on a signal from the pressure sensor, and controlling the oxy-fuel ratio of burners in the furnace based on a signal from the composition sensor.
Aspect 8. The method of Aspect 7, wherein the two or more sensors further include a temperature sensor, the method further comprising: restricting control of the flue gas damper, an oxygen-enrichment level in the furnace, and the oxy-fuel ratio of the burners based on a signal from the temperature sensor to maintain desired heat transfer.
Aspect 9. The method of Aspect 7, wherein the sensor block is located in the furnace.
Aspect 10. The method of Aspect 7, wherein the sensor block is located in the flue.
Aspect 11. A method of controlling furnace operation using an integrated sensor system as in Aspect 1, comprising: detecting opacity indicative of particles in one or both of the furnace and the flue; and adjusting furnace input parameters based on the detected opacity.
Aspect 12. The method of Aspect 11, wherein the two or more sensors include a sender and a receiver, and opacity is measured by attenuation of a signal from the sender to the receiver.
Aspect 13. The method of Aspect 11, wherein the two or more sensors include a radiation receiver, and opacity is measured by attenuation of furnace radiation that would otherwise be detected in the absence of particles.
Aspect 14. The method of Aspect 11, further comprising: detecting one or more predetermined particle sizes as indicative of non-optimized combustion; and adjusting furnace input parameters based on the detected particle sizes.
Aspect 15. A method of controlling heat distribution in a furnace using one or more integrated sensor systems as in Aspect 1, comprising: detecting heat load in one part or zone of the furnace; detecting heat load in another part or zone of the furnace; adjusting the input of combustion energy to the respective parts or zones of the furnace based on the detected heat loads.
Aspect 16. An integrated sensor system for use in a furnace system including a furnace having a flue and at least one burner introducing fuel and oxidant into the furnace, the furnace containing a charge and having walls bounding a furnace environment, the walls including at least one of a side wall, an end wall, and a roof, the furnace having two or more zones each differently affected by at least one furnace parameter regulating energy input into the furnace, the integrated sensor system comprising: a first temperature sensor positioned to measure a first temperature in the furnace system; a second temperature sensor positioned to measure a second temperature in the furnace system; and a controller programmed to receive signals from the first and second temperatures sensors indicative of the first and second measured temperatures, respectively, and to adjust operation of a furnace system parameter based on a relationship between the first and second temperatures, thereby differentially regulating energy input into at least two of the zones of the furnace; wherein the relationship between the first and second temperatures is a function of one or more of a difference between the two temperatures, a ratio of the two temperatures, and a weighted average of the two temperatures.
Aspect 17. The system of Aspect 16, wherein the first temperature sensor is mounted in a wall in a first zone of the furnace and exposed directly to the furnace environment; and wherein the second temperature sensor is embedded in a wall in the first zone of the furnace and isolated from direct exposure to the furnace environment.
Aspect 18. The system of Aspect 16, wherein the first temperature sensor is an optical sensor oriented to detect the temperature of the charge in a first zone in the furnace; and wherein the second temperature sensor is an optical sensor oriented to detect the temperature of the charge in a second zone in the furnace.
Aspect 19. The system of Aspect 16, wherein the first temperature sensor is an optical sensor oriented to detect the temperature of the charge in a first zone in the furnace; and wherein the second temperature sensor is embedded in a wall in the first zone of the furnace and isolated from direct exposure to the furnace environment.
Aspect 20. The system of any of Aspects 16 to 19, wherein the furnace system parameter to be adjusted includes at least one of a burner firing rate, a burner stoichiometry, a burner staging, a firing rate distribution among two or more burners, a staging distribution among two or more burners, and a furnace pressure.
Aspect 21. The system of any of Aspects 16 to 20, wherein the controller is programmed to monitor at least one of the temperature sensor signals intermittently.
Aspect 22. The system of any of Aspects 16 to 21, further comprising at least a third sensor selected from the group consisting of: temperature sensors, pressure sensors, concentration sensors, radiation sensors, density sensors, optical sensors, acoustic sensors, level sensors, angle sensors, distance sensors, position sensors, image acquisition sensors, and video acquisition sensors.
Aspect 23. The system of Aspect 22, further comprising an actuator mechanism corresponding to the third sensor for advancing the third sensor into a position for taking a measurement and retracting the third sensor to a protected position; wherein the controller is programmed to monitor the signal from third sensor only when the third sensor is advanced into the position for taking a measurement.
Aspect 24. The system of any of Aspects 16 to 23, further comprising: a sensor block mounted in a wall in a first zone of the furnace and having at least two ports in which the first and second temperature sensors are respectively positioned.
Aspect 25. A method of controlling one or both of energy input and energy distribution in a furnace using an integrated sensor system as in Aspect 16, comprising: receiving a first temperature signal from the first temperature sensor to determine the first temperature; receiving a second temperature signal from the second temperature sensor to determine the second temperature; adjusting a furnace system parameter based on a relationship between the first and second temperatures, wherein the furnace system parameter includes at least one of a burner firing rate, a burner stoichiometry, a burner staging, a firing rate distribution among two or more burners, a staging distribution among two or more burners, and a furnace pressure, thereby differentially regulating energy input into at least two of the zones of the furnace.
Aspect 26. The method of Aspect 25, further comprising: controlling energy input into the furnace based on a signal from the second temperature sensor; and controlling energy distribution into the furnace based on a signal from the first temperature sensor; wherein the first temperature sensor responds more rapidly to changes in the furnace environment than the second temperature sensor.
Aspect 27. The method Aspect 25, further comprising: calculating a ratio of the first and second temperatures; and controlling one or both of the energy input and energy distribution based on the calculated ratio.
Aspect 28. The method of Aspect 25, wherein the first temperature sensor is mounted in a wall of the furnace and exposed directly to the furnace environment and the second temperature sensor is embedded in a wall of the furnace and isolated from direct exposure to the furnace environment; and wherein the controlling step includes adjusting energy input into the furnace based on a function of one or more of the difference between the first and second temperature sensor, the ratio of the first and second temperature, and a weighted average of the first and second temperatures.
Aspect 29. The method of Aspect 25, wherein the first and second temperature sensors are optical pyrometers each directed at a different one location in the furnace, wherein the controlling step includes adjusting energy distribution into the furnace based on a function of one or more of the difference between the first and second temperature sensor, the ratio of the first and second temperature, and a weighted average of the first and second temperatures.
Aspect 30. A method of controlling heat distribution in a furnace using one or more integrated sensor systems as in Aspect 16, comprising: detecting a heat requirement in one zone of the furnace; detecting a heat requirement in another zone of the furnace; and adjusting the input of combustion energy to the respective parts or zones of the furnace based on the detected heat loads.
Aspect 31. The system as in Aspect 16, wherein the temperature sensors may be contact or non-contact.
Aspect 32. The system as in Aspect 1, further comprising: two or more sensors each positioned in a corresponding one of the ports in the sensor block; and a controller programmed to receive signals from the two or more sensors and to adjust operation of a furnace system parameter in response to the received signals; wherein the two sensors include at least two temperatures sensors configured to measure two different temperatures in the furnace system; and wherein the wall of the furnace is one or more of a sidewall and a roof of the furnace.
An integrated sensor system has been developed to work synergistically with one or more burners in a furnace, by using feedback from two or more sensors installed in the furnace at one or more locations, to optimize process efficiency, yield and/or throughput.
A non-limiting list of the types of sensors that can be used, separately or in combination, in an integrated sensor system, is as follows:
The integrated sensor system maybe wired or wirelessly connected, so the furnace can be stationary or rotational in operation. The integrated sensor system may be powered using a battery, wired-in power, or via energy harvesting from the furnace (e.g., using vibration, heat, mechanical movement, optical methods for energy harvesting).
Features of an Integrated Sensor System.
Sensors can be used for continuous or discontinuous measurement of process variables in a furnace. As a non-limiting example, continuous measurement can be performed by one or more thermocouples installed, each either embedded or open to the furnace atmosphere, and continuously measuring the temperature(s) in the furnace.
Alternatively, sensors may be mounted on an actuated mechanism that introduces the sensor into the measurement space and takes a discontinuous point measurement (in space and/or time) that is used, either in real-time or in a time-integrated manner, in the decision making process for control of the furnace. The use of an actuation mechanism that houses sensors also potentially eliminates or reduces the need for cooling, by water or air or other means, of a sensor that may not be suitable for continuous exposure to a furnace environment.
When using certain optical sensors, e.g., an infrared pyrometer, an image acquisition device, and the like, it is possible to have interference in measurement signals due to intense radiation from a flame. To address this, the actuation mechanism may be synchronized with the operation of a flame or flames, so that the sensor is actuated into position only when a flame or flames are least likely to interfere with measurements. This synchronization with a flame or flames would be beneficial to obtain more accurate data from the furnace, but is not necessary. The optical pyrometers may be configured to detect emissions in one or more wavelength ranges, for example, from 0.9 to 1.1 micrometers, from 1.5 to 1.7 micrometers, from 2.0 to 2.4 micrometers, from 3.8 to 4.0 micrometers, or combinations thereof, noting that a pyrometer need not be able to detect all of the wavelengths in any particular range.
In one example, an image acquisition device is used to take multiple photographic images in the furnace, and then a post-processing algorithm fuses or stitches those images together to provide a furnace overview. In addition, temperature and topographic information (obtained by nearly simultaneously operating sensors) may be overlaid on the furnace overview. This information can be used, for example, to determine the energy distribution required in a furnace having two or more zones each differently responsive to certain energy inputs (e.g., burners or burner configurations or operating parameters) into the furnace, as discussed in further detail below.
The integrated sensor system includes a sensor block that may have any number of channels, holes, passages, wells, or ports for sensors of various shapes and sizes, and any number of sensors may be used at any given time. Further, depending on the needs of the operation, the sensors within the integrated sensor system may be installed flush or extended into the furnace, or recessed into the refractory block, as shown in
Role of Components.
One or more process sensors may be located in the integrated sensor system, dictated by the needs of the control strategy being employed. Depending on the control needs of the application, a combination of sensors maybe ranked and weighted per their importance in the control strategy. In one non-limiting example, when managing the energy input and distribution needs of the furnace, a combination of temperature sensors may be used and weighted in the decision making. In another non-limiting example, when managing the excess oxygen concentration in the flue duct, a combination of pressure and composition sensors maybe used and weighted in the decision making. Note that any one type of process sensor, by itself, may be inadequate to define the control needs. Therefore, knowledge and understanding as to how a combination of variables respond, for example at a particular strategically-selected location or locations, can be instrumental in effectively determining how to control the combustion process in the furnace.
A package of information obtained from synergistically operating sensors in the integrated sensor system can be effectively used to control aspects of the furnace operation such as energy distribution, energy input (firing rates), stoichiometry, and/or to identify events such as substantial completion of process melting, and/or to determine suitable times for the next incremental charge, addition of salts/fluxes, stirring the metal bath, dealing with contaminated scrap, need for post combustion, control of emissions, adjustment of the burner staging either fuel or oxygen, material refining (e.g., oxidation or reduction), and other process steps or events.
Sensors may operate individually or in combination with other sensors in the integrated sensor system or a combination of integrated sensor systems.
Locating the sensors for the integrated sensor system.
The performance of integrated sensor system is significantly affected by the location of its sensors. In one embodiment, one or more sensor blocks may be strategically located in the roof and/or side-walls and/or flue gas duct, in order to get a complete picture of the control needs of a furnace, because every furnace is different. Many factors, including but not limited to the number, location and type (air-fuel, air-oxy-fuel, or oxy-fuel) of burners, energy input, size and shape of furnace, and location of the flue duct relative the burners, determine the fluid dynamic patterns of flue gases and heat release that develop in the furnace. These in turn help determine the appropriate location of sensors in the furnace.
One or more sensor blocks may be installed standalone or independently in the furnace or may be integrated within the burner system. Depending on the needs of the operation, the sensor blocks may be installed flush (preferably) or extended into the furnace or recessed into the furnace refractory.
As shown in
An example of the importance of locating thermocouples (TC) in a reheating furnace to control the rate of energy input (instantaneous burner firing rate) in the process can be understood with reference to Gangoli, et. al., “Importance of Control Strategy for Oxy-Fuel Burners in a Steel Reheat Furnace,” PR-364-181—2013 AISTech Conference Proceedings, which is incorporated herein by reference in its entirety. A Control Location Optimizer Program (CLOP) uses a unique strategy to determine the effective location of the control TC.
By moving the control TC location to AFTER, the cycle times and fuel savings obtained in the process improved by 29% (faster) and 20% (lower), respectively.
Examples of Control Strategies using an integrated sensor system:
A) Controlling Energy Input and Energy Distribution in a furnace.
In a scenario when standard (e.g., type- K) thermocouples are used to control energy input and distribution of energy in the furnace, it is preferred to use them in pairs, or at least to use at least one thermocouple that is open to the furnace environment and radiation and at least another thermocouple that is embedded in a refractory block, typically 1 to 2 inches from the hot face. This arrangement may be implement using a sensor block as shown in in
The embedded TC reacts slower while the open or exposed TC reacts faster to the changes in the process. Similarly, the overall energy input needed by the furnace changes slower (usually linear for given rate of scrap input), while the heat distribution needs change faster (melting/movement of scrap, furnace events such as charging, stirring, etc.). Consequently, a control strategy incorporating the integrated sensor system can use the open TC to control heat distribution decisions and the embedded TC to manage the overall energy input into the furnace.
When an open or exposed thermocouple is used to control the rate of energy input into the furnace, it is prone to picking up heat much faster than surrounding refractory and product within the furnace. This causes a premature reduction of energy input into the furnace leading to extended cycle times (see
B) Controlling excess-O2 in the furnace.
Sensors may be located close to or in the flue gas duct. In this situation, pressure and composition (e.g., O2 concentration) process variables may be used as the primary inputs to the decision making, while temperature can play a secondary role as an input to the decision making. For example, pressure is used to control the flue gas damper or oxygen-enrichment level in the furnace and consequently air leakages (leakage of O2), while composition is used to control the oxygen-to-fuel ratio used in combustion and consequently furnace pressure. In this scenario, it is preferable to have the pressure and composition sensors at the same location (i.e., incorporated into the same sensor block) because oxygen concentration is interconnected to pressure and composition variables. The temperature information could then be used as a check to make sure that the changes made to the furnace do not adversely affect heat transfer.
C) Controlling NOx in the furnace.
Sensors may be located close to or in the flue gas duct. In this situation, pressure and composition process variables maybe used as primary inputs in the decision making, while temperature can play a secondary role, so that the stoichiometry of burners can be adjusted based on each burner's location relative to the flue and burners' relative to each other.
D) Detection of particulates in the flue gas duct.
i) Active detection, using a sender and a receiver, where attenuation in signal indicates presence of particulates. For example, a particulate detector such as sold commercially by Forbes Marshall (e.g., Opacity/Dust Monitor—FM CODEL DCEM2100) may be integrated with a sensor block and the furnace controls. Controlling the opacity of a flue by adjusting control parameters has also been shown in at least one test case (see http://lehigh.edu/energy/leu/leu_54.pdf).
ii) Passive detection, using furnace radiation and a receiver, where attenuation in signal indicates presence of particulates. This method uses a light sensitive detector (e.g. photodiode, CCD) that, in the absence of particulates, would measure light from a hot refractory, flame, or other surface emitting radiation. The presence of particulates reduces the light intensity. However a reduction in furnace temperature, firing rate, or other item could also reduce the intensity observed by the light sensitive detector. Therefore a synthesis of information is needed to determine the cause of the reduction in light. For instance by combining information about the burner(s) firing rate, furnace temperature, sensor block temperature, other light sensitive detectors, and/or other information, the controls for the furnace can determine if the reduction in light intensity is due to particulates blocking the light source or a reduction in background radiation. This would eliminate the problems associated with alignment of (active) catch and receive devices. Once there is a determination that there are additional particulates, the combustion/furnace controls could be adjusted/optimized to reduce particulates or other non-optimized combustion conditions. This could be from improved combustion using known techniques such as improved stoichiometry control, improved flame stability, and the like.
iii) Use a specific wavelength to distinguish between particulates.
Knowing the distribution of particulate sizes could be useful for determining the source of the particulates. For instance, larger particle sizes may indicate that a pulverizer is not operating properly and smaller sizes may indicate non-optimized combustion in the burner, both in the case of solid fuel combustion. Similarly the particle size could indicate if the particle is a combustion product or if it was picked up from the heated material due to gas currents within the furnace. It may also be important to know the particle size for permitting reasons. The particle size could be inferred by using different wavelengths of light either through the use of catch and receive optics using lasers, filters, or gratings or through the use of background radiation and optical filters or gratings (or other means). With this information the combustion could be adjusted, a warning provided for combustion related equipment, the gas flows in the furnace could be adjusted to reduce particle pick-up, and/or other actions could be taken to rectify the issue. Note also that the detection of specific wavelengths can be done using either passive or active detection as discussed above.
E) Controlling CO/flammables emissions from the furnace.
Various means can be used to control the CO/flammable emissions. For example, the method described in US2013/0307202, incorporated herein by reference in its entirety, could be employed using a sensor block to incorporate both the optical detector and temperature measurement device. Beyond controlling for unexpected volatiles, the same sensors or different sensors could be used to control the furnace at minimum excess oxygen based on the emissions of flammables from the furnace. Such flammables would be the result of imperfect control by the control system, imperfect mixing of oxygen and fuel within the burner and/or furnace, and/or from the charge or other sources. However, as differentiated from the control methodology of the '202 patent application, the burner flow control stoichiometry can be controlled in a narrower range. One objective of the present application is to minimize excess O2, wherein the burner input flows can be slowly changed to new setpoints in response to the sensor system inputs. This slowly changing control system allows for minor modifications to the stoichiometry to account for the dynamics in the furnace while maintaining the ability to respond to more major changes in the system.
F) Controlling “heat distribution” using an integrated sensor system.
As shown in
When used in a melting application (e.g., secondary aluminum or copper melting), the product load can potentially move around the furnace due to lopsided charging practices, movement of solids in the furnace via melting, molten metal pumps, or other causes. In this case, the integrated sensor systems can detect the relative zonal changes in the load and make adjustments to the heat distribution accordingly.
Scope of use of integrated sensor system.
The integrated sensor system may be used in a wide variety of energy applications including melting, heating/reheating, secondary ferrous/non-ferrous metal refining, (high temperature applications) for all metals, glass, gasification, direct reduced iron, boilers, reformers (add others), as non-limiting examples.
Experimental Data.
In addition to control, temperature setpoints are often used to prevent over heating of a charge or product in a furnace more so than to protect the refractory, simply because most refractories in heating or melting furnaces are rated for working temperatures far higher than target process temperatures of the product. For example, some refractories can handle temperatures in excess of 3000° F., while a product in the furnace may melt or become oxidized (in situations where it is desired to avoid melting and/or oxidation) well below those temperatures. However, control based on an open thermocouple TOPEN that overestimates the product temperature (as discussed above with regard to
The lagging of product temperature TPROD as compared with TOPEN can be simulated with the help of an embedded thermocouple, TEMB that serves as a reasonable proxy for TPROD. For example, in a sensor block as illustrated schematically in
A third, preferable option is to control the furnace using a more optimal operation variable, deemed TCONTROL, which may be a calculated function of TOPEN and TEMB, and optionally TSP. In one non-limiting example equation for TCONTROL, which is graphically shown in
In the depicted graph, the Constant is set at 0.8. The control temperature variable TCONTROL reaches the setpoint temperature at point B after about 4 hours, without allowing the TOPEN to exceed 2500° F., thereby gaining about 0.8 hours or 48 minutes of continuing to operate at high firing rate as compared with controlling based on TOPEN alone, which will enable the furnace to decrease cycle times and improve productivity. As an example, for a furnace being fired at 10 MMBtu/hr with specific fuel consumption of 0.8 MMBtu/ton and processing about 60 tons/batch, this exemplary control scheme enables the input of an additional 5 to 8 MMBtu more energy into the furnace over the same period of time, resulting in about 8 to 13% improvement in the productivity.
It is understood that many alternative functions of TOPEN and TEMB may be used to achieve improved process results compared with controlling based on either TOPEN or TEMB alone. In one example, TCONTROL may be formulated based on a difference between TOPEN and TEMB rather than a ratio, or some other relative weighting of TOPEN and TEMB than the linear example given above, In another example, TCONTROL may be varied taking into account a range about the setpoint temperature TSP, wherein when TOPEN is within a range near TSP, a formula is used to provide a relative weighting of TOPEN and TEMB, while below that range TOPEN alone is used and above that range TEMB alone is used. (Note that this could be accomplished, for example, by setting X in equation (1) to 0 below the range and 1 above the range.) The range may have a lower limit that is 10% or 15% or 20% or 25% below TSP, and the range may have an upper limit that is 10% or 15% or 20% or 25% above TSP, and theses ranges can be adjusted appropriately depending on the temperature scale being used.
With reference to
The furnace layout is shown in
As shown, the flue may be equipped with an infrared sensor (FIR) to detect combustion intensity. Positioned in the exemplary furnace of
The data in
As shown in
The open thermocouples shown in
With reference to
The data in
Point P1 marks the time when the furnace door was opened, the bed was stirred, and new scrap was added. The embedded thermocouple T13 detects the bulk heat change due to these operations, while the pyrometer T11 detects the resultant local change in energy distribution and the open thermocouple T12 similarly shows a more dramatic response to the influx of cold air and cold charge. The bed thermocouple T14 drops to or slightly below the melting temperature of copper at point P2, when the door has been closed and the new charge is being heated. The bed thermocouple T14 remains flat during the phase change until point P3, when melting is complete. The pyrometer T11 temperature curve shows a flattening during the phase change, before it resumes an upward trend. Note that the pyrometer temperature curve does not remain consistently flat during the phase change possibly due to some reflections from the burner flames and furnace walls.
As shown in
The data of
The data of
Note that pyrometers are sensitive to the flame radiation, but when the burner firing rate is reduced (e.g., when loading), the pyrometer and thermocouple temperatures align very closely. Thus, more accurate pyrometer measurements may be obtained by placing sensor blocks away from the flame, or by taking pyrometer measurements where or when a flame is temporarily not present, or by corresponding or synchronizing a temporarily reduction in burner firing rate with the taking of a pyrometer and/or other optical temperature measurement.
As described herein, a ratio, difference, or other relationship between the open pyrometer and embedded thermocouple measurements, or open thermocouple and embedded thermocouple measurements, can be used to determine that the furnace should be heated faster or more slowly depending on that relationship, or that heat should preferentially be delivered to one or more zones of the furnace as compared to one or more other zones of the furnace. For instance, if the open/embedded ratio is greater than or equal to 2 (or 1.75 or 1.5 or 1.25), then the system may decrease firing rate to avoid overheating the refractory walls and roof. Conversely, if the open/embedded ratio is less than or equal to 1 (or 1.05 or 1.1 or 1.15 or 1.2), then the system may increase firing rate to enable faster heating without risk of damage to the refractory walls and roof.
The data of
A heating or melting furnace may be operationally divided into two or more zones, where the energy input and thus the temperature of each zone can, to at least some degree, be separately or differentially controlled by varying one or more furnace parameters that regulate energy input into the furnace.
In one common example, as illustrated in
In another example, a burner such as is disclosed in US 20150247673 can be used to selectively and dynamically target or direct more heat preferentially into one or more zones of a furnace, and less heat preferentially into one or more other zones in the furnace, in order to achieve a desired zonal control.
The present invention is not to be limited in scope by the specific aspects or embodiments disclosed in the examples which are intended as illustrations of a few aspects of the invention and any embodiments that are functionally equivalent are within the scope of this invention. Various modifications of the invention in addition to those shown and described herein will become apparent to those skilled in the art and are intended to fall within the scope of the appended claims.
This application claims the priority of U.S. Provisional Application No. 62/062,578, filed on Oct. 10, 2014, which is incorporated by reference herein in its entirety.
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PCT/US2015/054880 | 10/9/2015 | WO | 00 |
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