US3186694A - Temperature control system for jet convection strip heating furnace - Google Patents

Temperature control system for jet convection strip heating furnace Download PDF

Info

Publication number
US3186694A
US3186694A US205901A US20590162A US3186694A US 3186694 A US3186694 A US 3186694A US 205901 A US205901 A US 205901A US 20590162 A US20590162 A US 20590162A US 3186694 A US3186694 A US 3186694A
Authority
US
United States
Prior art keywords
temperature
strip
compressible
heating
heated
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.)
Expired - Lifetime
Application number
US205901A
Inventor
Beggs Donald
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Midland Ross Corp
Original Assignee
Midland Ross 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
Application filed by Midland Ross Corp filed Critical Midland Ross Corp
Priority to US205901A priority Critical patent/US3186694A/en
Priority to GB19062/63A priority patent/GB983345A/en
Application granted granted Critical
Publication of US3186694A publication Critical patent/US3186694A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Classifications

    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21DMODIFYING THE PHYSICAL STRUCTURE OF FERROUS METALS; GENERAL DEVICES FOR HEAT TREATMENT OF FERROUS OR NON-FERROUS METALS OR ALLOYS; MAKING METAL MALLEABLE, e.g. BY DECARBURISATION OR TEMPERING
    • C21D1/00General methods or devices for heat treatment, e.g. annealing, hardening, quenching or tempering
    • C21D1/74Methods of treatment in inert gas, controlled atmosphere, vacuum or pulverulent material
    • C21D1/767Methods of treatment in inert gas, controlled atmosphere, vacuum or pulverulent material with forced gas circulation; Reheating thereof

Definitions

  • This invention relates to a temperature control system for a furnace adapted to heat strip by convection heat transfer from free jets of compressible uid directed to impinge on alternate sides of the strip.
  • the invention is particularly well suited for a thermal head strip heating furnace wherein the heating means for heating compressible fluid operates to heat compressible uid to a .temperature that is substantially higher than the temperature to which the strip is being heated.
  • the temperature of the compressible fluid which actually impinges on the strip bears no iixed relationship to the temperature to which the heated compressible uid is heated by the heater.
  • the reason for this phenomenon is that the jets of compressihle fluid which impinge on the strip do not consist solely of the heated compressible uid emitted toward the strip by the compressible fluid distributors, but rather, comprise a mixture of heated compressible iiuid and spent compressible fluid entrained by the heatedV compressible duid as it traverses the distance from the distributor toward the strip. ln a .typical installation the fluid which actually strikes the strip might comprise 70% of entrained spent fluid and only 30% heated fluid.
  • the spent compressible fluid component of the heating jets comprises duid which has already transferred heat to strip it is at some lower temperature than the temperature of compressible iiuid from the heater. Furthermore, the difference between the temperature of the spent compressible r'luid portion of the heating 'et and the temperature of the heated compressible duid portion does not remain at a constant value since it is affected by the overall heating load of the furnace. The heating load of the furnace, in turn, is affected by the width of the strip being processed. Thus, in the operation of prior art jet convection thermal head strip heating furnaces, it is necessary to reset the control temperature to which the heater heats the com- Y pressible fluid to an empirically determined value every time the width of strip being processed is changed.
  • the object of this invention to provide improved strip heating apparatus. It is a further object of the invention to provide an improved temperature control system for a thermal head jet convection strip heating furnace. It is a further object of the invention to provide such a temperature control system as to render the operation of the furnace insensitive to the width of the strip being processed.
  • FiG. l is an etevational sectional view of strip treating apparatus having a heating section constructed in accordance with the present invention.
  • FIG. 2 is a sectional view taken on line 2-2 of FIG. 1.
  • FIG. l simplified apparatus for heat treating substantially endless moving strip 11 on a continuous basis comprises a heating duid collecting chamber 12, defined by insulated wall means 13, and a cooling chamber 14,illustrated schematically ybecause its details of construction do not constitute a part of this invention.
  • Suitable strip conveying means comprising rollers 15 and 16 are provided to convey the strip through heating chamber 12 and cooling chamber 14 in that sequence.
  • Strip 11 is heated within chamber 12 by means of jets ofpcompressible uid which are directed against opposite sides thereof.
  • circulating means comprising a blower 17 and a heater 13, illustrated schematically, are provided to circulate compressible fluid at a suitable temperature, usually at a temperature in excess of the desired final strip temperature, into the heating chamber.
  • Heater 1S may be electrically heated, but is shown as being fuel fired and is provided with a fuel inlet line 19.v
  • the heated compressible uid from the circulating means is delivered to a manifold 21 from whence it passes, in parallel, into a first distributor 22 and a second distributor 23 spaced apart from the rst distributor.
  • Each of the distributors is adapted to distribute the heated compressible fluid within the chamber in a plurality of jets having a component of motion directed toward the other of the distributors, and each comprises a generally vertically extending header 24 and a plurality of ported pipes 26-35 each of which is disposed in iiuid communication with the header and generally transversely thereof.
  • the distributors are so arrangedV with respect to each other and with respect to the strip conveying means, which conveys the strip through the heating chamber intermediate the distributors, that the alternate sides of the strip are impinged upon by jets of compressible tiuid. After impingingon the strip and expending some of its heat thereby, the spent iiuid is collected in chamber 12 and may be evacuated therefrom and returned to blower 17 by means of conduit 41 to be recirculated back to the distributing means.
  • temperature control means is provided to control the heatingeffect of heater 1S on the compressible fluid circulated therethrough.
  • Appropriate control apparatus comprises a temperature sensing element 36, such as a thermocouple, located in a manner to be later discussed; an amplifier 37 adapted to receive a signalV from element 36 indicative of the temperature thereof and to transmit such signal at an amplified value; a controller 3S adapted to transmit a signal indicative of difference between the temperature sensed by element 36 and a predetermined set-point temperature; ⁇ and a ow control valve 39 subject to operation in response to the signal from controller 3S in such a manner as to increase the ow of fuel to heater 18 when the temperature sensed by element 36 is below the set point temperature and to decrease the flow of fuel when the temperature Vsensed Vby j element 36 is above the set point temperature.
  • thermal sensing element 35 differs from the prior art mainly in the location of thermalV sensing element 35.
  • thermal sensing element 36 is located within heating chamber 12 intermediate distributors.
  • at least g i ported pipe from distributor 23 are provided with Vextended portions and thermal sensing elementis disposed in the region of convergence therefrom.
  • sensing element is disposed intermediate opposed ported extensions 23e of opposed ported pipes 28.
  • thermal sensing element 36 is exposed heater t8 but also include lower temperature spent compressible iiuid entrained from the surroundings in chamber 12 by the jets of heated fluid from the ported pipes as they traverse the distance between the ports of the distributor and the strip.
  • the temperature control system of thepresent invention automatically compensates for the eliect ofchange in the temperature of spent cooling fluid within chamber 12 as might be caused by a change in the width of strip being processed.
  • L'Heating apparatus comprising,kin combination: wall Vmeans defining a chamber; circulating means comprising a heater located externally of the chamber for circulating heated compressible iluid into the chamber; distributing means within thechamber ycomprising a first distributor and a second distributor spaced apart from the first distributor with each of the distributors being adapted'to receive Vheated compressible iiuid from the circulating means and to distribute heated compressible iuid vwithin the chamber in at least one free jet having a component of motion directed toward .the other of the distributors; means for disposing work in a normal location in the chamber intermediate the distributors and in such a manner as to be impinged upon on opposite sides by jets'comprising a mixture of heated compressible uid and spent compressible fluid from within the chamber; a temperature sensing element disposed within the chamber between the distribtuors and generally laterally aligned with the normal alemana location of the workin a manner to ybe
  • each of said first and second distributors comprises, in combination: a header; a plurality of ported pipes disposed transversely of the header and in uid communication therewith with f at least one .ported pipe from the first distributor and a a predetermined value.
  • a heating method comprising heating compressible liuid and directing the heated compressible tiuid in opposed jets containing spent compressible fluid against opposite sides of the work being heated, the steps of sensing the temperature of the mixture of heated compressible iiuid and spent compressible iiuid in the region of coniverrgence of the opposed jets; and controlling the heating of compressible fluid to maintain the sensed temperature at a predetermined value.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Crystallography & Structural Chemistry (AREA)
  • Mechanical Engineering (AREA)
  • Materials Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Heat Treatment Of Strip Materials And Filament Materials (AREA)
  • Furnace Details (AREA)

Description

D. BEGGs 3,186,694 TEMPERATURE CONTROL SYSTEM FOR JET CONVECTION June l, 1955 STRIP HEATING FURNACE Filed June 28, 1962 /lrm ATTY.
United States Patent 3,186,694 TEMERATURE CNTRL SYS'Elv FOR JET CNVESTUN STKE? EEA'HNG FURNACE Donald Boggs, Toledo, Ghia, assigner to Midland-Ross Corporation, Toledo, Unio, a corporation of hio Filed June 28, 1962, Ser. No. 205,901
4 Claims. (Cl. 263-3) Y This invention relates to a temperature control system for a furnace adapted to heat strip by convection heat transfer from free jets of compressible uid directed to impinge on alternate sides of the strip. The invention is particularly well suited for a thermal head strip heating furnace wherein the heating means for heating compressible fluid operates to heat compressible uid to a .temperature that is substantially higher than the temperature to which the strip is being heated.
ln the operation of a thermal head jet convection strip heating furnace it has been customary to control the heating effect of the compressible fluid heater in such a manner as to maintain the temperature of the compressible duid from the heater at a predetermined value. This was normally accomplished by means of a temperature control device responsive to a signal from a temperature sensing element, such as a thermocouple, disposed in the ductwork downstream of the heater, a location normally external to the furnace chamber.
It has now been discovered, however, that the temperature of the compressible fluid which actually impinges on the strip bears no iixed relationship to the temperature to which the heated compressible uid is heated by the heater. The reason for this phenomenon is that the jets of compressihle fluid which impinge on the strip do not consist solely of the heated compressible uid emitted toward the strip by the compressible fluid distributors, but rather, comprise a mixture of heated compressible iiuid and spent compressible fluid entrained by the heatedV compressible duid as it traverses the distance from the distributor toward the strip. ln a .typical installation the fluid which actually strikes the strip might comprise 70% of entrained spent fluid and only 30% heated fluid. Since the spent compressible fluid component of the heating jets comprises duid which has already transferred heat to strip it is at some lower temperature than the temperature of compressible iiuid from the heater. Furthermore, the difference between the temperature of the spent compressible r'luid portion of the heating 'et and the temperature of the heated compressible duid portion does not remain at a constant value since it is affected by the overall heating load of the furnace. The heating load of the furnace, in turn, is affected by the width of the strip being processed. Thus, in the operation of prior art jet convection thermal head strip heating furnaces, it is necessary to reset the control temperature to which the heater heats the com- Y pressible fluid to an empirically determined value every time the width of strip being processed is changed.
it is, therefore, the object of this invention to provide improved strip heating apparatus. It is a further object of the invention to provide an improved temperature control system for a thermal head jet convection strip heating furnace. it is a further object of the invention to provide such a temperature control system as to render the operation of the furnace insensitive to the width of the strip being processed.
F or a further consideration of what is considered to be novel and inventive, attention is directed to the following portionl of the specification, the drawing, and the appended claims.
in the drawing:
FiG. l is an etevational sectional view of strip treating apparatus having a heating section constructed in accordance with the present invention; and
ICC
FIG. 2 is a sectional view taken on line 2-2 of FIG. 1.
As shown in FIG. l simplified apparatus for heat treating substantially endless moving strip 11 on a continuous basis comprises a heating duid collecting chamber 12, defined by insulated wall means 13, and a cooling chamber 14,illustrated schematically ybecause its details of construction do not constitute a part of this invention. Suitable strip conveying means comprising rollers 15 and 16 are provided to convey the strip through heating chamber 12 and cooling chamber 14 in that sequence.
Strip 11 is heated within chamber 12 by means of jets ofpcompressible uid which are directed against opposite sides thereof. Pursuant to this method of heating, circulating means comprising a blower 17 and a heater 13, illustrated schematically, are provided to circulate compressible fluid at a suitable temperature, usually at a temperature in excess of the desired final strip temperature, into the heating chamber. Heater 1S may be electrically heated, but is shown as being fuel fired and is provided with a fuel inlet line 19.v
The heated compressible uid from the circulating means is delivered to a manifold 21 from whence it passes, in parallel, into a first distributor 22 and a second distributor 23 spaced apart from the rst distributor. Each of the distributors is adapted to distribute the heated compressible fluid within the chamber in a plurality of jets having a component of motion directed toward the other of the distributors, and each comprises a generally vertically extending header 24 and a plurality of ported pipes 26-35 each of which is disposed in iiuid communication with the header and generally transversely thereof. The distributors are so arrangedV with respect to each other and with respect to the strip conveying means, which conveys the strip through the heating chamber intermediate the distributors, that the alternate sides of the strip are impinged upon by jets of compressible tiuid. After impingingon the strip and expending some of its heat thereby, the spent iiuid is collected in chamber 12 and may be evacuated therefrom and returned to blower 17 by means of conduit 41 to be recirculated back to the distributing means.
To control theheating effect of the heating jets of Compressible fluid on strip 11, temperature control means is provided to control the heatingeffect of heater 1S on the compressible fluid circulated therethrough. Appropriate control apparatus comprises a temperature sensing element 36, such as a thermocouple, located in a manner to be later discussed; an amplifier 37 adapted to receive a signalV from element 36 indicative of the temperature thereof and to transmit such signal at an amplified value; a controller 3S adapted to transmit a signal indicative of difference between the temperature sensed by element 36 and a predetermined set-point temperature; `and a ow control valve 39 subject to operation in response to the signal from controller 3S in such a manner as to increase the ow of fuel to heater 18 when the temperature sensed by element 36 is below the set point temperature and to decrease the flow of fuel when the temperature Vsensed Vby j element 36 is above the set point temperature.
The apparatus according to this invention differs from the prior art mainly in the location of thermalV sensing element 35. in the prior art it is customary to control the heating effect of the heater of a thermal head jet convection strip heating furnace in response to the temperature of a sensing element sensitive only to the temperature of compressible fluid from the heater, Yas by means of a thermocouple in the heated compressible fluid ductwork external to the'heating chamber. In .this invention, however, thermal sensing element 36 is located within heating chamber 12 intermediate distributors. Specifically, at least g i ported pipe from distributor 23 are provided with Vextended portions and thermal sensing elementis disposed in the region of convergence therefrom. In the illustrated arrangement, sensing element is disposed intermediate opposed ported extensions 23e of opposed ported pipes 28. y
The advantages of the present invention are grounded in the fact that thermal sensing element 36 is exposed heater t8 but also include lower temperature spent compressible iiuid entrained from the surroundings in chamber 12 by the jets of heated fluid from the ported pipes as they traverse the distance between the ports of the distributor and the strip. Thus, the temperature control system of thepresent invention automatically compensates for the eliect ofchange in the temperature of spent cooling fluid within chamber 12 as might be caused by a change in the width of strip being processed.
The best mode known to me to carry out this invention has been described in terms of sufciently full, clear,'con oise, and exact as to enable any person skilled in the art to practice the invention. However, it is understood that various modiications will be readily apparent to a skilled artisan without departing from the scope of the invention which is delined only by appended Claims.
I claim: Y
L'Heating apparatus comprising,kin combination: wall Vmeans defining a chamber; circulating means comprising a heater located externally of the chamber for circulating heated compressible iluid into the chamber; distributing means within thechamber ycomprising a first distributor and a second distributor spaced apart from the first distributor with each of the distributors being adapted'to receive Vheated compressible iiuid from the circulating means and to distribute heated compressible iuid vwithin the chamber in at least one free jet having a component of motion directed toward .the other of the distributors; means for disposing work in a normal location in the chamber intermediate the distributors and in such a manner as to be impinged upon on opposite sides by jets'comprising a mixture of heated compressible uid and spent compressible fluid from within the chamber; a temperature sensing element disposed within the chamber between the distribtuors and generally laterally aligned with the normal alemana location of the workin a manner to ybe impinged on by a mixture of compressible uid similar to the mixture impinging on thel work; and temperaturer control means sensitive to a condition indicative of the temperature of the temperature sensing element for controlling .the heating eiiect of the heater in a manner to maintain the temperature of the temperature sensing element atV a predetermined value.
2. Apparatus according to claim l wherein each of said first and second distributors comprises, in combination: a header; a plurality of ported pipes disposed transversely of the header and in uid communication therewith with f at least one .ported pipe from the first distributor and a a predetermined value.
d. In a heating method comprising heating compressible liuid and directing the heated compressible tiuid in opposed jets containing spent compressible fluid against opposite sides of the work being heated, the steps of sensing the temperature of the mixture of heated compressible iiuid and spent compressible iiuid in the region of coniverrgence of the opposed jets; and controlling the heating of compressible fluid to maintain the sensed temperature at a predetermined value.
References Cited by the Examiner "UNITED STATES PATENTS 2,406,822 9/46 Fox 263-8 2,897,096 9/57 Kullgren et al 34-45 2,862,305 12/58 Dungler 34-155 X 2,991,989 7/61 Martin 263-3 3,021,236 Y 2/62 Beggs et al 26S-3X 3,091,441 5/ 63 Kullgren et al 263-3 CHARLES SUKALO, Primary Examiner. toi-1N J. CAMBY, Examiner.

Claims (1)

1. IN A HEATING METHOD COMPRISING HEATING COMPRESSIBLE FLUID AND DIRECTING THE HEATED COMPRESSIBLE FLUID IN AT LEAST ONE FREE JET CONTAINING SPENT COMPRESSIBLE FLUID AGAINST THE WORK TO BE HEATED, THE STEPS OF SENSING THE TEMPERATURE OF THE MIXTURE OF HEATED COMPRESSIBLE FLUID AND ENTRAINED SPENT COMPRESSIBLE FLUID WHICH ACTUALLY IMPINGES ON THE WORK; AND CONTROLLING THE HEATING OF COMPRESSIBLE FLUID TO MAINTAIN THE SENSED TEMPERATURE AT A PREDETEMINED VALUE.
US205901A 1962-06-28 1962-06-28 Temperature control system for jet convection strip heating furnace Expired - Lifetime US3186694A (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
US205901A US3186694A (en) 1962-06-28 1962-06-28 Temperature control system for jet convection strip heating furnace
GB19062/63A GB983345A (en) 1962-06-28 1963-05-14 Temperature control system for jet convection strip heating furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US205901A US3186694A (en) 1962-06-28 1962-06-28 Temperature control system for jet convection strip heating furnace

Publications (1)

Publication Number Publication Date
US3186694A true US3186694A (en) 1965-06-01

Family

ID=22764132

Family Applications (1)

Application Number Title Priority Date Filing Date
US205901A Expired - Lifetime US3186694A (en) 1962-06-28 1962-06-28 Temperature control system for jet convection strip heating furnace

Country Status (2)

Country Link
US (1) US3186694A (en)
GB (1) GB983345A (en)

Cited By (17)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3633256A (en) * 1969-08-15 1972-01-11 Monsanto Co Orientation drawing chamber for fibers
US3920382A (en) * 1974-08-14 1975-11-18 Bloom Eng Co Inc Method and apparatus for heat treating articles in a recirculating type furnace
US3994678A (en) * 1975-05-12 1976-11-30 Oliver Machinery Company Heater for billets
US4043292A (en) * 1975-07-21 1977-08-23 Corning Glass Works Microscope slide staining apparatus having temperature control
US4069008A (en) * 1976-03-19 1978-01-17 Allegheny Ludlum Industries, Inc. Method and apparatus for heating a workpiece
US4135312A (en) * 1977-04-21 1979-01-23 Hope Henry F Film dryer
US4235591A (en) * 1977-05-24 1980-11-25 Gautschi Electro-Fours SA. Continuous flow oven
US4373702A (en) * 1981-05-14 1983-02-15 Holcroft & Company Jet impingement/radiant heating apparatus
US4568274A (en) * 1983-06-21 1986-02-04 Chugai Ro Co., Ltd. Heat treating furnace for metallic strip
US4696642A (en) * 1985-05-15 1987-09-29 Yoshida Kogyo K. K. Apparatus for continuously heating an elongated textile article
US4797172A (en) * 1988-02-12 1989-01-10 The Boeing Company Filament preheat apparatus
US4836774A (en) * 1984-11-08 1989-06-06 Mitsubishi Jukogyo Kabushiki Kaisha Method and apparatus for heating a strip of metallic material in a continuous annealing furnace
US4957432A (en) * 1987-09-01 1990-09-18 Phillips Petroleum Company Forced jet convection oven for vacuum bagging
US5186885A (en) * 1990-10-22 1993-02-16 Perneczky George C Apparatus for cooling a traveling strip
US4828483B1 (en) * 1988-05-25 1994-03-22 Bloom Eng Co Inc Method and apparatus for suppressing nox formation in regenerative burners
US5827056A (en) * 1997-01-09 1998-10-27 Drever Company Device and method for improving strip tracking in a continuous heating furnace
CN112763294A (en) * 2020-12-29 2021-05-07 广东金泉医疗科技有限公司 Heat treatment module and automatic drop dyeing mounting equipment with same

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2406822A (en) * 1942-02-20 1946-09-03 Vernie A Fox Control system and mechanism for heat processing machines
US2807096A (en) * 1954-08-16 1957-09-24 Aetna Standard Eng Co Apparatus for heating and stretching fabrics
US2862305A (en) * 1953-07-29 1958-12-02 Dungler Julien Apparatus for drying strip material
US2991989A (en) * 1958-03-10 1961-07-11 Midland Ross Corp Convection strip heater and control therefor
US3021236A (en) * 1958-05-28 1962-02-13 Midland Ross Corp Convective heat transfer furnace and method
US3091441A (en) * 1961-02-02 1963-05-28 Blaw Knox Co Apparatus for heating and stretching of fabrics

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2406822A (en) * 1942-02-20 1946-09-03 Vernie A Fox Control system and mechanism for heat processing machines
US2862305A (en) * 1953-07-29 1958-12-02 Dungler Julien Apparatus for drying strip material
US2807096A (en) * 1954-08-16 1957-09-24 Aetna Standard Eng Co Apparatus for heating and stretching fabrics
US2991989A (en) * 1958-03-10 1961-07-11 Midland Ross Corp Convection strip heater and control therefor
US3021236A (en) * 1958-05-28 1962-02-13 Midland Ross Corp Convective heat transfer furnace and method
US3091441A (en) * 1961-02-02 1963-05-28 Blaw Knox Co Apparatus for heating and stretching of fabrics

Cited By (18)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3633256A (en) * 1969-08-15 1972-01-11 Monsanto Co Orientation drawing chamber for fibers
US3920382A (en) * 1974-08-14 1975-11-18 Bloom Eng Co Inc Method and apparatus for heat treating articles in a recirculating type furnace
US3994678A (en) * 1975-05-12 1976-11-30 Oliver Machinery Company Heater for billets
US4043292A (en) * 1975-07-21 1977-08-23 Corning Glass Works Microscope slide staining apparatus having temperature control
US4069008A (en) * 1976-03-19 1978-01-17 Allegheny Ludlum Industries, Inc. Method and apparatus for heating a workpiece
US4135312A (en) * 1977-04-21 1979-01-23 Hope Henry F Film dryer
US4235591A (en) * 1977-05-24 1980-11-25 Gautschi Electro-Fours SA. Continuous flow oven
US4373702A (en) * 1981-05-14 1983-02-15 Holcroft & Company Jet impingement/radiant heating apparatus
US4568274A (en) * 1983-06-21 1986-02-04 Chugai Ro Co., Ltd. Heat treating furnace for metallic strip
US4836774A (en) * 1984-11-08 1989-06-06 Mitsubishi Jukogyo Kabushiki Kaisha Method and apparatus for heating a strip of metallic material in a continuous annealing furnace
US4696642A (en) * 1985-05-15 1987-09-29 Yoshida Kogyo K. K. Apparatus for continuously heating an elongated textile article
US4957432A (en) * 1987-09-01 1990-09-18 Phillips Petroleum Company Forced jet convection oven for vacuum bagging
US4797172A (en) * 1988-02-12 1989-01-10 The Boeing Company Filament preheat apparatus
US4828483B1 (en) * 1988-05-25 1994-03-22 Bloom Eng Co Inc Method and apparatus for suppressing nox formation in regenerative burners
US5186885A (en) * 1990-10-22 1993-02-16 Perneczky George C Apparatus for cooling a traveling strip
US5827056A (en) * 1997-01-09 1998-10-27 Drever Company Device and method for improving strip tracking in a continuous heating furnace
CN112763294A (en) * 2020-12-29 2021-05-07 广东金泉医疗科技有限公司 Heat treatment module and automatic drop dyeing mounting equipment with same
CN112763294B (en) * 2020-12-29 2023-09-08 广东金泉医疗科技有限公司 Heat treatment module and automatic drop dyeing sealing piece equipment with same

Also Published As

Publication number Publication date
GB983345A (en) 1965-02-17

Similar Documents

Publication Publication Date Title
US3186694A (en) Temperature control system for jet convection strip heating furnace
US4333777A (en) Method and apparatus for compensating for local temperature difference of steel product
US3448969A (en) Fluid pressure sealing system for processing oven
US3517916A (en) Aluminum annealing furnace
US3671027A (en) Heat processing of minerals
US3033539A (en) Heat transfer apparatus for continuously moving strip
US2573019A (en) Strip metal heat-treating
US4444554A (en) Heating method and apparatus
US4422573A (en) Heating system
JP3082211B2 (en) Vacuum furnace and temperature uniforming method in vacuum furnace
US2991535A (en) Tunnel kiln firing section
US2638333A (en) Continuous furnace
KR101851252B1 (en) Heat blocking apparatus of outlet plug of vertical annealing furnace
US3222042A (en) Annealing furnace
US3035824A (en) Furnace with cooled and recirculated atmosphere
US4092143A (en) Tunnel furnace for the thermal treatment of glass products
JPS6115079A (en) Gas circulation type heating or cooling furnace
JPH049030Y2 (en)
US3138200A (en) Cooling of moving metal strip
US2668040A (en) Furnace system
JPH0117072B2 (en)
JPS6145691B2 (en)
JPH0437880Y2 (en)
SU905600A1 (en) Furnace for chemical thermic treatment of articles
US2049473A (en) Heating of fluids