Combustion systems are employed in a vast number of applications, including, for example, domestic and commercial HVAC, smelters, foundries, and refineries, chemical manufacturing, research operations, power generation, etc. In many applications, electrical energy is applied to a combustion reaction.
According to an embodiment, a combustion system is provided, including a burner assembly configured to support a flame within a combustion volume, an electrode positioned within the combustion volume and configured to apply electrical energy to a flame supported by the burner assembly, and a dielectric electrode support having a tubular form, extending into the combustion volume and configured to support the electrode and further configured to be cooled by a coolant fluid circulated therethrough.
According to an embodiment, the electrode support extends through a furnace wall into the combustion volume, and has first and second coolant ports in fluid communication with a coolant channel extending within the tubular form of the electrode support.
According to an embodiment, the first coolant port is in fluid communication with a fluid coolant source. During operation, a fluid coolant flows through the electrode support, holding a temperature of the electrode to within a selected range.
According to an embodiment, the fluid coolant source includes a gas compressor configured to deliver a gas coolant to the electrode support.
According to an embodiment, the gas compressor includes a blower configured to draw and deliver ambient air as the fluid coolant to the electrode support.
According to an embodiment, the electrode support is one of a plurality of electrode supports, each configured to support a respective electrode within the combustion volume.
According to another embodiment, the electrode support is configured to support the weight of the electrode, while a second electrode support is positioned and configured to hold the electrode at a selected orientation.
According to an embodiment, a method includes supporting a flame with a burner assembly positioned within a combustion volume and supporting an electrode in the combustion volume with a substantially dielectric electrode support having a tubular form and extending into the combustion volume. The method includes applying electrical energy to the flame with the electrode and cooling the electrode by circulating a coolant fluid through the electrode support.
In the following detailed description, reference is made to the accompanying drawings, which form a part hereof. In the drawings, similar symbols typically identify similar components, unless context dictates otherwise. The illustrative embodiments described in the detailed description, drawings, and claims are not meant to be limiting. Other embodiments may be utilized, and other changes may be made, without departing from the spirit or scope of the subject matter presented here.
Some combustion systems are configured to operate at very high temperatures, and in some of these systems, it is desirable to position one or more electrodes very close to a flame within the systems. One concern in such systems is the selection of a suitable material for supports intended to hold the electrodes within the combustion volume. The electrode supports should preferably be made of a material capable of retaining its strength and stiffness at or near the maximum operating temperature of the particular system, to resist deformation during operation. The material should also be a good insulator, inasmuch as the electrodes can be charged to extremely high voltage potentials, sometimes on the order of tens of thousands of volts. Under these conditions, the material should have a high breakdown voltage, in order to resist breakdown failure, and should also preferably be highly electrically resistive, to minimize parasitic currents via the electrode support to other system components, such as, e.g., a furnace wall.
Few dielectric materials are suitable for supporting electrodes within the combustion volume of a furnace, particularly in furnaces that operate at high temperatures. Most simply cannot tolerate high temperatures. Ceramic is a preferred support material because many ceramic formulations retain their rigidity at temperatures above 1500 degrees F. Additionally, ceramics can be formed using a number of different processes, including, e.g., various molding processes, extrusion, machining, and 3-D printing. However, the inventor has found that many ceramics increase in electrical conductivity at high temperatures, to a degree that varies according to the temperature and the formulation of the ceramic. Very often, as a ceramic electrode support is heated, its electrical resistance decreases, and it begins to act as a parasitic current path to ground, via furnace walls and other structures. In many systems, the electrodes do not discharge a current through the flame, so the current requirements of the power supply can be very low. However, when a parasitic current path exists, the power supply must be capable of meeting the additional current draw while still applying the nominal voltage potential to the electrodes. Thus, operational costs are increased, because of the additional power required, and equipment costs are higher, because of the more powerful voltage supply required. Safety is another concern, because components of a system can become electrically charged if they are not adequately grounded.
The inventor has conceived and tested cooled electrode supports, which can support electrodes in extremely high temperature environments without losing their dielectric characteristics.
The burner assembly 106 is not shown in significant detail because the details can vary widely, according to the type of combustion system, the nominal capacity of the system and burner assembly, the fuel used, etc. Burner assemblies configured according to the many variations of systems are very well known in the art. For example, according to various embodiments, the flame support element 110 can include a nozzle optimized to output liquid fuel, gaseous fuel, or solid fuel particles entrained in a flow of liquid or gas, or can be configured to include a grate configured to receive other types of solid fuels. Similarly, according to some embodiments, the fuel delivery control element 108 can be configured according to any of a number of designs, and can include, for example, a valve configured to regulate a flow of fluid, or can be configured for use with solid fuels, and can comprise a screw conveyor or a rotating chain grate, etc.
Returning to
A plurality of sensors 134 are positioned in and/or around the combustion volume 102 and configured to monitor various ones of a large number of parameters associated with the combustion system 100. For example, a first sensor 134a is positioned and configured to monitor combustion characteristics of the flame 116, which can include emissions of CO, CO2, and NOX, flame temperature, energy emission spectra, etc. Second sensors 134b are positioned at the coolant ports 126 of the electrode supports 124, and configured to detect the temperature of coolant entering and exiting the supports 124.
A controller 136 is provided, configured to receive input and control various aspects of the operation of the combustion system 100, via control connectors 138. In the present example, the controller 136 is operatively coupled to the fuel delivery control element 108, the voltage source 120, the coolant delivery control element 130, and the sensors 134, and is configured to regulate fuel delivered to the flame support element 110, voltage signals applied to the electrodes 118, and the flow of coolant through the electrode supports 124, in part on the basis of data received from the sensors 134.
In the embodiment of
With regard to the flame support elements 110, their shape and configuration can vary according to the details of a particular embodiment, as shown, for example, in the embodiment described below with reference to the embodiment of
According to an embodiment, the controller 136 is configured to monitor the temperature of the coolant as it exits each electrode support 124, and to control the output of the coolant delivery control element 130 to maintain a temperature of the electrode supports 124 below a selected value. According to another embodiment, the volume of coolant is preselected to be sufficient to maintain temperature of the electrode supports 124 below the selected value, even while the combustion system 100 is operating at a maximum operating temperature. This obviates the need for the second temperature sensors 134b at the coolant ports 126 of the electrode supports 124, and also reduces the workload on the controller 136, which is not required to monitor the coolant temperature.
Many common and well understood elements shown and described with reference to
The combustion system 200 includes a burner assembly 106 configured to burn solid fuel, and in which the flame support element 110 comprises a grate 202 to which the solid fuel is delivered via any of a number of mechanisms known in the art. Electrodes 118 are shaped as plate electrodes, with a control connector 138 coupled to each electrode 118 via a contact point 204 embedded in the side of the respective electrode 118 opposite the flame 116, as shown in
The coolant delivery control element 130 includes a blower 206 operatively coupled to a coolant port 126 of each electrode support 124. Second sensors 134b are positioned at the coolant ports 126 of the electrode supports 124 and configured to detect the temperature of coolant entering and exiting the supports 124. A first sensor 134a is positioned to monitor flue gases exiting the combustion volume 102 via a stack 208, and is configured to produce one or more signals representative of respective combustion characteristics of the flame 116.
In operating a test furnace in which electrodes were supported on refractory ceramic supports (performing tests that were not related to the subject of the present disclosure), the inventor determined that, in high-temperature conditions, a significant current flowed through the supports, which could skew the test results. The inventor conceived of aspects of the present invention as a solution to this problem, but recognized that the potential benefits would extend beyond the improved accuracy of a test furnace.
Using a test furnace configured substantially as the combustion system 200 of
Alumina is one example of a ceramic that is often used in high-temperature applications. At room temperature, alumina has a resistivity of more than 1014 Ωcm. At 600 degrees F., the resistivity is around 1010 Ωcm, while at 1500 degrees F., the resistivity drops to around 105 Ωcm.
In conducting the tests, the inventor did not employ the number of second sensors 134b shown in
One significant advantage of the use of cooled electrode supports is that the choice of materials is significantly increased, because the temperature of the supports can be held below the transition temperature of many different materials.
Turning now to
According to an embodiment, the combustion volume is defined in part by a furnace wall. The electrode support extends through the furnace wall into the combustion volume. The electrode support includes coolant ports in fluid communication with an interior of the electrode support, the coolant ports being positioned outside the combustion volume.
According to an embodiment, the method includes delivering the coolant fluid to an interior of the electrode support from a coolant source positioned outside the combustion volume.
According to an embodiment, the method includes delivering the coolant fluid to the interior of the electrode support from the coolant source via a coolant port of the electrode support positioned outside the combustion volume.
According to an embodiment, delivering the coolant fluid to the interior of the electrode support includes delivering a pressurized gas from the coolant source with a gas compressor.
According to an embodiment, the gas compressor is a blower.
According to an embodiment, the method includes drawing and delivering ambient air as the fluid coolant to the electrode support with the blower.
According to an embodiment, the method includes controlling an operation of the fluid coolant source with a controller.
According to an embodiment, the method includes controlling operation of the fluid coolant source with the controller based at least in part on a temperature of fluid coolant exiting the electrode support.
According to an embodiment, the method includes sensing the temperature of the coolant fluid exiting the electrode support and providing a signal to the controller indicative of the temperature of coolant fluid exiting the electrode support.
According to an embodiment, the method includes controlling a voltage signal applied to the electrode with the controller.
According to an embodiment, the method includes controlling the voltage signal applied to the electrode at least in part based on combustion parameters of the flame.
According to an embodiment, the method includes providing a signal to the controller from a sensor indicative of a combustion parameter of the flame.
According to an embodiment, the method includes supporting the electrode with a plurality of electrode supports.
According to an embodiment, supporting the electrode includes supporting the weight of the electrode by a first one of the plurality of electrode supports while holding the electrode in position by a second one of the electrode supports.
According to an embodiment, the method includes supporting the weight of the electrode by the first one and a third one of the plurality of electrode supports.
According to an embodiment, the method includes supporting a plurality of electrodes in the combustion volume with a plurality of electrode supports. The electrode can be one of a plurality of electrodes. According to an embodiment, the method includes applying electrical energy to the flame with the plurality of electrodes and cooling the plurality of electrode supports by passing the coolant fluid through respective interiors of the plurality of electrode supports.
Where employed by the specification or claims to refer to a quantity that is applied to a combustion reaction via a charge element, such as an electrode, the term electrical energy is to be construed as including within its scope any form of energy or potential energy that might reasonably be applied to the combustion reaction, given the structure and configuration of the charge element upon which the language in question can be read, and may include, for example, electromagnetic energy, a charge, a voltage, an electrical field, etc.
The abstract of the present disclosure is provided as a brief outline of some of the principles of the invention according to one embodiment, and is not intended as a complete or definitive description of any embodiment thereof, nor should it be relied upon to define terms used in the specification or claims. The abstract does not limit the scope of the claims.
While various aspects and embodiments have been disclosed herein, other aspects and embodiments are contemplated. The various aspects and embodiments disclosed herein are for purposes of illustration and are not intended to be limiting, with the true scope and spirit being indicated by the following claims.
The present application claims priority benefit from U.S. Provisional Patent Application No. 62/376,662, entitled “COOLED CERAMIC ELECTRODE SUPPORTS,” filed Aug. 18, 2016; which, to the extent not inconsistent with the disclosure herein, is incorporated by reference.
Number | Name | Date | Kind |
---|---|---|---|
2374610 | MacLaren, Jr. | Apr 1945 | A |
2405807 | Arant | Aug 1946 | A |
2412373 | Wejnarth | Dec 1946 | A |
2412374 | Wejnarth | Dec 1946 | A |
2412375 | Wejnarth | Dec 1946 | A |
2412376 | Wejnarth | Dec 1946 | A |
2445296 | Wejnarth | Jul 1948 | A |
2975145 | Harris | Mar 1961 | A |
3037942 | Ingold | Jun 1962 | A |
3207953 | Smith | Sep 1965 | A |
3245457 | Smith | Apr 1966 | A |
3446902 | Akers | May 1969 | A |
3475352 | Yerouchalmi | Oct 1969 | A |
3707644 | Hirt | Dec 1972 | A |
4327282 | Nauerth | Apr 1982 | A |
4332295 | LaHaye | Jun 1982 | A |
4652318 | Masuda | Mar 1987 | A |
4831432 | Hori | May 1989 | A |
4867848 | Cordier | Sep 1989 | A |
5046144 | Jensen | Sep 1991 | A |
5183101 | Penaluna | Feb 1993 | A |
5529651 | Yoshida | Jun 1996 | A |
5620616 | Anderson et al. | Apr 1997 | A |
5702244 | Goodson et al. | Dec 1997 | A |
5784889 | Joos et al. | Jul 1998 | A |
6166903 | Ranchy | Dec 2000 | A |
6610964 | Radmacher | Aug 2003 | B2 |
6887069 | Thornton et al. | May 2005 | B1 |
7927095 | Chorpening et al. | Apr 2011 | B1 |
8385041 | Goudy, Jr. | Feb 2013 | B2 |
8411406 | Goudy, Jr. | Apr 2013 | B2 |
8851882 | Hartwick | Oct 2014 | B2 |
8881535 | Hartwick et al. | Nov 2014 | B2 |
8901467 | Radmacher | Dec 2014 | B2 |
8911699 | Colannino et al. | Dec 2014 | B2 |
9062882 | Hangauer et al. | Jun 2015 | B2 |
9151549 | Goodson et al. | Oct 2015 | B2 |
9209654 | Colannino et al. | Dec 2015 | B2 |
9243800 | Goodson et al. | Jan 2016 | B2 |
9267680 | Goodson et al. | Feb 2016 | B2 |
9284886 | Breidenthal et al. | Mar 2016 | B2 |
9289780 | Goodson | Mar 2016 | B2 |
9310077 | Breidenthal et al. | Apr 2016 | B2 |
9366427 | Sonnichsen et al. | Jun 2016 | B2 |
9371994 | Goodson et al. | Jun 2016 | B2 |
9377188 | Ruiz et al. | Jun 2016 | B2 |
9377189 | Ruiz et al. | Jun 2016 | B2 |
9377195 | Goodson et al. | Jun 2016 | B2 |
9441834 | Colannino et al. | Sep 2016 | B2 |
9453640 | Krichtafovitch et al. | Sep 2016 | B2 |
9469819 | Wiklof | Oct 2016 | B2 |
9494317 | Krichtafovitch et al. | Nov 2016 | B2 |
9496688 | Krichtafovitch | Nov 2016 | B2 |
9513006 | Krichtafovitch et al. | Dec 2016 | B2 |
9562681 | Colannino et al. | Feb 2017 | B2 |
9574767 | Anderson et al. | Feb 2017 | B2 |
9664386 | Krichtafovitch | May 2017 | B2 |
9696034 | Krichtafovitch et al. | Jul 2017 | B2 |
9702547 | Krichtafovitch et al. | Jul 2017 | B2 |
9702550 | Colannino et al. | Jul 2017 | B2 |
9732958 | Wiklof | Aug 2017 | B2 |
9739479 | Krichtafovitch et al. | Aug 2017 | B2 |
9746180 | Krichtafovitch et al. | Aug 2017 | B2 |
10006715 | Colannino | Jun 2018 | B2 |
20020056548 | Nakamura | May 2002 | A1 |
20020113151 | Forber Jones | Aug 2002 | A1 |
20040147986 | Baumgardner et al. | Jul 2004 | A1 |
20070020567 | Branston et al. | Jan 2007 | A1 |
20080179033 | Forbes Jones | Jul 2008 | A1 |
20080179034 | Forbes Jones | Jul 2008 | A1 |
20090038958 | Coyle | Feb 2009 | A1 |
20100067164 | Goudy, Jr. | Mar 2010 | A1 |
20100147676 | Goudy, Jr. | Jun 2010 | A1 |
20110027734 | Hartwick | Feb 2011 | A1 |
20120100497 | Joo | Apr 2012 | A1 |
20120317985 | Hartwick | Dec 2012 | A1 |
20130040067 | Kennedy | Feb 2013 | A1 |
20130071794 | Colannino et al. | Mar 2013 | A1 |
20130230810 | Goodson et al. | Sep 2013 | A1 |
20130260321 | Colannino | Oct 2013 | A1 |
20130291552 | Smith et al. | Nov 2013 | A1 |
20130323661 | Goodson et al. | Dec 2013 | A1 |
20130333279 | Osler et al. | Dec 2013 | A1 |
20130336352 | Colannino et al. | Dec 2013 | A1 |
20140051030 | Colannino et al. | Feb 2014 | A1 |
20140076212 | Goodson et al. | Mar 2014 | A1 |
20140080070 | Krichtafovitch et al. | Mar 2014 | A1 |
20140162195 | Lee et al. | Jun 2014 | A1 |
20140162198 | Krichtafovitch et al. | Jun 2014 | A1 |
20140170569 | Anderson et al. | Jun 2014 | A1 |
20140170571 | Casasanta, III et al. | Jun 2014 | A1 |
20140170575 | Krichtafovitch | Jun 2014 | A1 |
20140170576 | Colannino et al. | Jun 2014 | A1 |
20140196368 | Wiklof | Jul 2014 | A1 |
20140208758 | Breidenthal et al. | Jul 2014 | A1 |
20140212820 | Colannino et al. | Jul 2014 | A1 |
20140216401 | Colannino et al. | Aug 2014 | A1 |
20140227645 | Krichtafovitch et al. | Aug 2014 | A1 |
20140227646 | Krichtafovitch et al. | Aug 2014 | A1 |
20140227649 | Krichtafovitch | Aug 2014 | A1 |
20140255856 | Colannino et al. | Sep 2014 | A1 |
20140272731 | Breidenthal et al. | Sep 2014 | A1 |
20140287368 | Krichtafovitch et al. | Sep 2014 | A1 |
20140295094 | Casasanta, III | Oct 2014 | A1 |
20140335460 | Wiklof et al. | Nov 2014 | A1 |
20150079524 | Colannino et al. | Mar 2015 | A1 |
20150104748 | Dumas et al. | Apr 2015 | A1 |
20150107260 | Colannino et al. | Apr 2015 | A1 |
20150118629 | Colannino et al. | Apr 2015 | A1 |
20150121890 | Colannino et al. | May 2015 | A1 |
20150140498 | Colannino | May 2015 | A1 |
20150147704 | Krichtafovitch et al. | May 2015 | A1 |
20150147705 | Colannino et al. | May 2015 | A1 |
20150219333 | Colannino et al. | Aug 2015 | A1 |
20150226424 | Breidenthal et al. | Aug 2015 | A1 |
20150276211 | Colannino et al. | Oct 2015 | A1 |
20150338089 | Krichtafovitch | Nov 2015 | A1 |
20150345780 | Krichtafovitch | Dec 2015 | A1 |
20150345781 | Krichtafovitch et al. | Dec 2015 | A1 |
20150362177 | Krichtafovitch et al. | Dec 2015 | A1 |
20150362178 | Karkow et al. | Dec 2015 | A1 |
20150369476 | Wiklof | Dec 2015 | A1 |
20160018103 | Karkow et al. | Jan 2016 | A1 |
20160040872 | Colannino et al. | Feb 2016 | A1 |
20160047542 | Wiklof | Feb 2016 | A1 |
20160047547 | Barels | Feb 2016 | A1 |
20160091200 | Colannino et al. | Mar 2016 | A1 |
20160123577 | Dumas et al. | May 2016 | A1 |
20160138799 | Colannino | May 2016 | A1 |
20160161110 | Krichtafovitch et al. | Jun 2016 | A1 |
20160161115 | Krichtafovitch et al. | Jun 2016 | A1 |
20160215974 | Wiklof | Jul 2016 | A1 |
20160273763 | Colannino et al. | Sep 2016 | A1 |
20160273764 | Colannino et al. | Sep 2016 | A1 |
20160290633 | Cherpeske et al. | Oct 2016 | A1 |
20160290639 | Karkow et al. | Oct 2016 | A1 |
20160298836 | Colannino et al. | Oct 2016 | A1 |
20160363315 | Colannino et al. | Dec 2016 | A1 |
20170146233 | Krichtafovitch | May 2017 | A1 |
20170146234 | Krichtafovitch et al. | May 2017 | A1 |
Number | Date | Country |
---|---|---|
58-019609 | Feb 1983 | JP |
3678937 | Aug 2005 | JP |
WO 1995034784 | Dec 1995 | WO |
WO-2014005143 | Jan 2014 | WO |
WO 2015089306 | Jun 2015 | WO |
WO 2015123683 | Aug 2015 | WO |
WO 2016140681 | Sep 2016 | WO |
Entry |
---|
JP-3678937-B2—English translation (Year: 2005). |
Number | Date | Country | |
---|---|---|---|
20180051874 A1 | Feb 2018 | US |
Number | Date | Country | |
---|---|---|---|
62376662 | Aug 2016 | US |