US20040079354A1 - Direct gas burner type furnace - Google Patents

Direct gas burner type furnace Download PDF

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Publication number
US20040079354A1
US20040079354A1 US10/688,658 US68865803A US2004079354A1 US 20040079354 A1 US20040079354 A1 US 20040079354A1 US 68865803 A US68865803 A US 68865803A US 2004079354 A1 US2004079354 A1 US 2004079354A1
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US
United States
Prior art keywords
furnace
combustion
rate
gas burner
gas
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Abandoned
Application number
US10/688,658
Inventor
Takanori Takeda
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Denso Corp
Original Assignee
Denso Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
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Assigned to DENSO CORPORATION reassignment DENSO CORPORATION ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: TAKEDA, TAKANORI
Publication of US20040079354A1 publication Critical patent/US20040079354A1/en
Abandoned legal-status Critical Current

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Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26DRYING
    • F26BDRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B15/00Machines or apparatus for drying objects with progressive movement; Machines or apparatus with progressive movement for drying batches of material in compact form
    • F26B15/10Machines or apparatus for drying objects with progressive movement; Machines or apparatus with progressive movement for drying batches of material in compact form with movement in a path composed of one or more straight lines, e.g. compound, the movement being in alternate horizontal and vertical directions
    • F26B15/12Machines or apparatus for drying objects with progressive movement; Machines or apparatus with progressive movement for drying batches of material in compact form with movement in a path composed of one or more straight lines, e.g. compound, the movement being in alternate horizontal and vertical directions the lines being all horizontal or slightly inclined
    • F26B15/18Machines or apparatus for drying objects with progressive movement; Machines or apparatus with progressive movement for drying batches of material in compact form with movement in a path composed of one or more straight lines, e.g. compound, the movement being in alternate horizontal and vertical directions the lines being all horizontal or slightly inclined the objects or batches of materials being carried by endless belts
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26DRYING
    • F26BDRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B21/00Arrangements or duct systems, e.g. in combination with pallet boxes, for supplying and controlling air or gases for drying solid materials or objects
    • F26B21/06Controlling, e.g. regulating, parameters of gas supply
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26DRYING
    • F26BDRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B23/00Heating arrangements
    • F26B23/02Heating arrangements using combustion heating

Definitions

  • Circulation fans 11 are provided within the furnace, for making the furnace temperature uniform by circulating the combustion gas in the furnace, and are driven by circulation fan motors 14 provided outside the furnace, respectively.
  • the number of the circulation fans 11 is preferably equal to that of the burners.
  • a temperature sensor 3 is provided in the furnace for monitoring the furnace temperature variable in accordance with the load variation due to the articles existing within the furnace, and transmitting information related to the furnace temperature to a temperature/output controller 4 .
  • Exhaustion rate control means includes the temperature/output controller 4 , a motor rotation controller 10 and an exhaust fan motor 9 for driving the exhaust fan 8 . That is, information (a signal) representing the combustion rate of the gas burner 2 is transmitted from the temperature/output controller 4 to the motor rotation controller 10 which, in turn, controls the exhaust fan motor 9 to regulate the rotational speed of the exhaust fan 8 based on this information. Accordingly, the exhaustion rate of the combustion gas is controllable in accordance with the combustion rates of the gas burner 2 .

Abstract

A direct gas burner type furnaces for directly heating articles 13 by combustion gas and then exhausting the combustion gas outside the furnace, controls the combustion rate of a gas burner 2 based on the furnace temperature detected by a temperature sensor 3 in the furnace, and controls the rotational speed of an exhaust fan 8 based on the combustion rate to control the exhaust rate of the combustion gas in the furnace. Accordingly, it is possible to exhaust the combustion gas from the furnace in correspondence with the introduction rate of the combustion gas into the furnace and to prevent air at a normal temperature from being sucked into the furnace.

Description

    BACKGROUND OF THE INVENTION
  • 1. Field of the Invention [0001]
  • The present invention relates to a direct gas burner type furnace, for heating, capable of controlling an exhaust gas in accordance with the variation of heat load in the furnace. [0002]
  • 2. Description of the Related Art [0003]
  • In the prior art furnace adopting a direct gas burner, for heating, which necessitates ventilation within the furnace, such as a dryer furnace for handling dangerous articles, the combustion rate of the gas burner is solely controlled in accordance with the variation of heat load of articles to be heated in the furnace. That is, if it is found that there is no article to be heated in the furnace as a result of the monitoring of the furnace temperature, an amount of gas to be supplied to the burner is automatically throttled to reduce the combustion rate. [0004]
  • A reason why the direct gas burner is employed is that the article can be effectively heated by using hot combustion gas for the purpose of directly heating the atmosphere within the furnace. However, the combustion gas directly introduced into the furnace must be exhausted from the furnace. It is also necessary to exhaust the furnace atmosphere containing dangerous material such as oil or others evaporated from the heated article after the concentration thereof becomes lower than a threshold value above which there is a risk of explosion. [0005]
  • In the prior art, even if a rate of the combustion gas introduced into the furnace varies in accordance with the increase/decrease of heat load, i.e., the increase/decrease of the combustion rate, an exhaust rate of a fan for exhausting furnace gas is constant. Thereby, there is a problem in that, when the combustion rate decreases, the interior of the furnace becomes a negative pressure to suck outer air of a normal temperature from an opening of the furnace. Thus, the furnace temperature falls to increase the combustion rate even though the heat supply is unnecessary. In such a manner, in the prior art, there is no exhaust control of the furnace atmosphere due to the load variation, particularly for the purpose of energy-saving when the load decreases. [0006]
  • SUMMARY OF THE INVENTION
  • The present invention has been made to solve the above mentioned problems, and an object thereof is to provide a direct gas burner type furnace capable of maintaining the furnace temperature at a set temperature while decreasing a heat loss caused by the exhaustion, even if articles to be heated are not continuously introduced into the furnace, and also capable of saving energy as well as reducing an exhaustion amount of CO[0007] 2.
  • The inventive direct gas burner type furnace is adapted to control the combustion rate of combustion means based on a furnace temperature detected by a temperature sensor as well as to control an exhaustion rate of the combustion gas based on the combustion rate. As an amount of the combustion gas corresponding to that of the combustion gas introduced into the furnace is exhausted outside the furnace thereby, air of a normal temperature is not sucked from an opening of a furnace body into the furnace, whereby the furnace temperature does not fall. Accordingly, it is possible to reduce a heat loss due to the exhaust as well as to maintain the furnace at a set temperature, whereby energy saving and a reduction of the exhausted CO[0008] 2 are achievable.
  • The inventive direct gas burner type furnace may be provided with fans for circulating the combustion gas. Thereby, it is possible to make the furnace temperature uniform so that the articles to be heated are evenly heated. Also, it is possible to accurately detect the furnace temperature to optimize the combustion rate and the exhaustion rate. [0009]
  • The inventive direct gas burner type furnace may comprise a plurality of combustion means. Thereby, it is possible to enlarge and elongate the size of the furnace. Also, it is possible to make it correspond to various situations by separate control of the off-operating combustion means and the on-operating combustion means. [0010]
  • The present invention may be more fully understood from the description of the preferred embodiments of the invention, as set forth below, together with the accompanying drawings.[0011]
  • BRIEF DESCRIPTION OF THE DRAWINGS
  • In the drawings: [0012]
  • FIG. 1 is a schematic front view of an overall construction according to one embodiment of the inventive direct gas burner type furnace; and [0013]
  • FIG. 2 is a side view of a furnace body of the embodiment of the inventive direct gas burner type furnace.[0014]
  • DESCRIPTION OF THE PREFERRED EMBODIMENTS
  • One embodiment of the inventive direct gas burner type furnace will be described below with reference to the attached drawings. FIG. 1 is a schematic front view of an overall construction according to one embodiment of the inventive direct gas burner type furnace, and FIG. 2 is a side view thereof. [0015] Articles 13 are continuously supplied by a conveyor device 12, to a furnace body 1 of the direct gas burner type furnace according to the present invention, through an opening 1a provided in the furnace body. Gas burners 2 are attached to the furnace body 1 as combustion means for heating the articles 13 and internal structures of the furnace. While three gas burners 2 are provided in FIG. 1, the number of gas burners may be suitably selectable in accordance with the size of the furnace body 1.
  • [0016] Circulation fans 11 are provided within the furnace, for making the furnace temperature uniform by circulating the combustion gas in the furnace, and are driven by circulation fan motors 14 provided outside the furnace, respectively. The number of the circulation fans 11 is preferably equal to that of the burners. A temperature sensor 3 is provided in the furnace for monitoring the furnace temperature variable in accordance with the load variation due to the articles existing within the furnace, and transmitting information related to the furnace temperature to a temperature/output controller 4.
  • Combustion rate control means includes the temperature/output controller [0017] 4 and a damper control motor 5 connected to a gas feeding rate control damper 6 for adjusting a feeding rate of gas supplied to the gas burner 2 and to a combustion air feeding rate control damper 7 for adjusting a feeding rate of combustion air supplied to the gas burner 2. Accordingly, a signal representing the furnace temperature detected by the temperature sensor 3 is input to the temperature/output controller 4 which, in turn, creates a control signal based on the information input thereto and output the same to the damper control motor 5. The damper control motor 5 controls the gas rate control damper 6 and the combustion air control damper 7 based on the control signal. In such a manner, the combustion rate of the gas burner 2 is controlled.
  • Further, to exhaust the combustion gas introduced into the furnace, an [0018] exhaust duct 15 inserted into the interior of the furnace and connected to an exhaust fan 8 is provided. Exhaustion rate control means includes the temperature/output controller 4, a motor rotation controller 10 and an exhaust fan motor 9 for driving the exhaust fan 8. That is, information (a signal) representing the combustion rate of the gas burner 2 is transmitted from the temperature/output controller 4 to the motor rotation controller 10 which, in turn, controls the exhaust fan motor 9 to regulate the rotational speed of the exhaust fan 8 based on this information. Accordingly, the exhaustion rate of the combustion gas is controllable in accordance with the combustion rates of the gas burner 2.
  • In this regard, in FIG. 1, front and [0019] rear chambers 16 and 17 provided adjacent to the furnace body 1 are suitably used in accordance with uses of the direct gas burner type furnace. For example, when the direct gas burner type furnace is used as a drier for drying coated articles, the front chamber 16 may be used as a coating chamber and the rear chamber 17 may be used as a cooling chamber. Or, both the front and rear chambers may be used as a preheating chamber and a cooling chambers, respectively, or as atmosphere-shutter chambers.
  • As described above, in the present invention, only the [0020] motor rotation controller 10 is newly provided for controlling the exhaust fan motor 9 and, by using the signal from the originally provided temperature/output controller 4, the exhaustion rate of the exhaust fan 8 is controlled to regulate the exhaustion rate of the gas burner 2 in correspondence to the combustion rate of the gas burner, that is, the rate of the combustion gas introduced into the furnace.
  • Accordingly, in the present invention, it is possible to automatically control the exhaust rate of the combustion gas in conformity with the combustion rate of the gas burner; i.e., the rate of the combustion gas introduced into the furnace; and in accordance with the variation of heat load due to the article to be heated in the furnace. Thereby, it is possible to suppress the unnecessary introduction of air due to an excessive exhaust in the prior art when the combustion rate is reduced, and to save energy as well as reduce the CO[0021] 2 exhaust rate.
  • While the invention has been described by reference to specific embodiments chosen for the purpose of illustration, it should be apparent that numerous modification could be made thereto by those skilled in the art without departing from the basic concept and scope of the invention. [0022]

Claims (4)

What is claimed is:
1. A direct gas burner type furnace for directly heating articles continuously fed into the furnace by combustion gas which gas is then exhausted outside the furnace thereafter, comprising
combustion means opening to the interior of the furnace,
a temperature sensor for detecting the furnace temperature,
exhaust fans for discharging the combustion gas from the interior of the furnace to outside the furnace,
combustion rate control means for controlling a combustion rate of the combustion means based on the furnace temperature detected by the temperature sensor, and
exhaust rate control means for controlling an exhaust rate of the combustion gas in the furnace by controlling the exhaust fans based on the combustion rate.
2. A direct gas burner type furnace as defined by claim 1, wherein a circulation fan is provided in the furnace for circulating the combustion gas in the furnace.
3. A direct gas burner type furnace as defined by claim 1, wherein a plurality of said combustion means are provided.
4. A direct gas burner type furnace as defined by claim 2, wherein a plurality of said combustion means are provided.
US10/688,658 2002-10-25 2003-10-17 Direct gas burner type furnace Abandoned US20040079354A1 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
JP2002311036A JP2004144421A (en) 2002-10-25 2002-10-25 Direct fire gas burner furnace
JP2002-311036 2002-10-25

Publications (1)

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US20040079354A1 true US20040079354A1 (en) 2004-04-29

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JP (1) JP2004144421A (en)

Cited By (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2007130257A2 (en) * 2006-05-04 2007-11-15 Abbott Cardiovascular Systems Inc. Methods and devices for coating stent
US20080104859A1 (en) * 2006-10-12 2008-05-08 Bryan Wolowiecki Method and apparatus for inhibiting pitch formation in the wet seal exhaust duct of a veneer dryer
US20080311280A1 (en) * 2007-06-15 2008-12-18 David Rego Methods and devices for coating stents
US20100215436A1 (en) * 2007-07-17 2010-08-26 William Nevil Heaton Johnson Flood barrier or the like
US8003157B2 (en) 2007-06-15 2011-08-23 Abbott Cardiovascular Systems Inc. System and method for coating a stent
US8304012B2 (en) 2006-05-04 2012-11-06 Advanced Cardiovascular Systems, Inc. Method for drying a stent
US8545214B2 (en) 2008-05-27 2013-10-01 Honeywell International Inc. Combustion blower control for modulating furnace
US8667703B2 (en) 2007-02-09 2014-03-11 Usnr/Kockums Cancar Company Method and apparatus for controlling cooling temperature and pressure in wood veneer jet dryers
US8764435B2 (en) 2008-07-10 2014-07-01 Honeywell International Inc. Burner firing rate determination for modulating furnace
US8876524B2 (en) 2012-03-02 2014-11-04 Honeywell International Inc. Furnace with modulating firing rate adaptation
CN104154767A (en) * 2014-08-11 2014-11-19 湖北大别山窑炉产业研究设计院有限公司 Temperature measurement and control system for plate-type SCR denitration catalyst calcining furnace
WO2017080067A1 (en) * 2015-11-13 2017-05-18 太仓权阡机械自动化有限公司 Paper tube drying device
CN106839719A (en) * 2017-02-23 2017-06-13 包头市海罗水泥制品机械有限公司 One kind automation tunnel drying system
CN108955105A (en) * 2017-05-17 2018-12-07 巨石集团有限公司 A kind of waste heat recovering energy conserving baking oven and exhaust heat recovering method
CN109708477A (en) * 2018-12-27 2019-05-03 西南铝业(集团)有限责任公司 A kind of method, apparatus, equipment and storage medium improving kiln temperature uniformity

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP4583256B2 (en) * 2005-06-23 2010-11-17 株式会社神戸製鋼所 Heat treatment furnace
CN106017035B (en) * 2016-07-11 2018-06-12 天津金戈科技发展有限责任公司 A kind of three-layer network belt drying machine for montmorillonite processing
CN110186269A (en) * 2019-06-10 2019-08-30 江苏明德玩具股份有限公司 Automatic drier is used in a kind of processing of educational toy

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4608961A (en) * 1984-04-30 1986-09-02 Lanham Machinery Company, Inc. Exhaust damper control
US4941819A (en) * 1986-12-01 1990-07-17 Stewart Systems, Inc. Air circulation and exhaust control system for commercial ovens

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4608961A (en) * 1984-04-30 1986-09-02 Lanham Machinery Company, Inc. Exhaust damper control
US4941819A (en) * 1986-12-01 1990-07-17 Stewart Systems, Inc. Air circulation and exhaust control system for commercial ovens
US4941819B1 (en) * 1986-12-01 1995-08-15 Stewart Systems Inc Air circulation and exhaust control system for commercial ovens

Cited By (33)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8927050B2 (en) 2006-05-04 2015-01-06 Abbott Cardiovascular Systems Inc. Method and apparatus for coating a stent
US8637110B2 (en) 2006-05-04 2014-01-28 Advanced Cardiovascular Systems, Inc. Rotatable support elements for stents
US8430057B2 (en) 2006-05-04 2013-04-30 Advanced Cardiovascular Systems, Inc. Stent support devices
US8596215B2 (en) 2006-05-04 2013-12-03 Advanced Cardiovascular Systems, Inc. Rotatable support elements for stents
WO2007130257A3 (en) * 2006-05-04 2008-04-03 Abbott Cardiovascular Systems Methods and devices for coating stent
WO2007130257A2 (en) * 2006-05-04 2007-11-15 Abbott Cardiovascular Systems Inc. Methods and devices for coating stent
US8003156B2 (en) 2006-05-04 2011-08-23 Advanced Cardiovascular Systems, Inc. Rotatable support elements for stents
US8465789B2 (en) 2006-05-04 2013-06-18 Advanced Cardiovascular Systems, Inc. Rotatable support elements for stents
US8741379B2 (en) 2006-05-04 2014-06-03 Advanced Cardiovascular Systems, Inc. Rotatable support elements for stents
US8304012B2 (en) 2006-05-04 2012-11-06 Advanced Cardiovascular Systems, Inc. Method for drying a stent
US8069814B2 (en) 2006-05-04 2011-12-06 Advanced Cardiovascular Systems, Inc. Stent support devices
US8046932B2 (en) * 2006-10-12 2011-11-01 Usnr/Kockums Cancar Company Method and apparatus for inhibiting pitch formation in the wet seal exhaust duct of a veneer dryer
US8381414B2 (en) 2006-10-12 2013-02-26 Usnr/Kockums Cancar Company Method and apparatus for inhibiting pitch formation in the wet seal exhaust duct of a veneer dryer
US20080104859A1 (en) * 2006-10-12 2008-05-08 Bryan Wolowiecki Method and apparatus for inhibiting pitch formation in the wet seal exhaust duct of a veneer dryer
US9228780B2 (en) 2007-02-09 2016-01-05 Usnr, Llc Method and apparatus for controlling cooling temperature and pressure in wood veneer jet dryers
US8667703B2 (en) 2007-02-09 2014-03-11 Usnr/Kockums Cancar Company Method and apparatus for controlling cooling temperature and pressure in wood veneer jet dryers
US9797655B2 (en) 2007-02-09 2017-10-24 Usnr, Llc Method and apparatus for controlling cooling temperature and pressure in wood veneer jet dryers
US7897195B2 (en) 2007-06-15 2011-03-01 Abbott Cardiovascular Systems Inc. Devices for coating stents
US8003157B2 (en) 2007-06-15 2011-08-23 Abbott Cardiovascular Systems Inc. System and method for coating a stent
US8691320B2 (en) 2007-06-15 2014-04-08 Abbott Cardiovascular Systems Inc. Method for coating stents
US20110217450A1 (en) * 2007-06-15 2011-09-08 Bryan Russell Hemphill Method for Coating Stents
US20080311280A1 (en) * 2007-06-15 2008-12-18 David Rego Methods and devices for coating stents
US20100215436A1 (en) * 2007-07-17 2010-08-26 William Nevil Heaton Johnson Flood barrier or the like
US8545214B2 (en) 2008-05-27 2013-10-01 Honeywell International Inc. Combustion blower control for modulating furnace
US10094593B2 (en) 2008-05-27 2018-10-09 Honeywell International Inc. Combustion blower control for modulating furnace
US8764435B2 (en) 2008-07-10 2014-07-01 Honeywell International Inc. Burner firing rate determination for modulating furnace
US8876524B2 (en) 2012-03-02 2014-11-04 Honeywell International Inc. Furnace with modulating firing rate adaptation
US9453648B2 (en) 2012-03-02 2016-09-27 Honeywell International Inc. Furnace with modulating firing rate adaptation
CN104154767A (en) * 2014-08-11 2014-11-19 湖北大别山窑炉产业研究设计院有限公司 Temperature measurement and control system for plate-type SCR denitration catalyst calcining furnace
WO2017080067A1 (en) * 2015-11-13 2017-05-18 太仓权阡机械自动化有限公司 Paper tube drying device
CN106839719A (en) * 2017-02-23 2017-06-13 包头市海罗水泥制品机械有限公司 One kind automation tunnel drying system
CN108955105A (en) * 2017-05-17 2018-12-07 巨石集团有限公司 A kind of waste heat recovering energy conserving baking oven and exhaust heat recovering method
CN109708477A (en) * 2018-12-27 2019-05-03 西南铝业(集团)有限责任公司 A kind of method, apparatus, equipment and storage medium improving kiln temperature uniformity

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Owner name: DENSO CORPORATION, JAPAN

Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNOR:TAKEDA, TAKANORI;REEL/FRAME:014628/0052

Effective date: 20031006

STCB Information on status: application discontinuation

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