WO2014185886A1 - Système de génération de vapeur à plaques chauffantes - Google Patents

Système de génération de vapeur à plaques chauffantes Download PDF

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Publication number
WO2014185886A1
WO2014185886A1 PCT/US2013/040716 US2013040716W WO2014185886A1 WO 2014185886 A1 WO2014185886 A1 WO 2014185886A1 US 2013040716 W US2013040716 W US 2013040716W WO 2014185886 A1 WO2014185886 A1 WO 2014185886A1
Authority
WO
WIPO (PCT)
Prior art keywords
steam
heating device
condensate
thermocompressor
hot plate
Prior art date
Application number
PCT/US2013/040716
Other languages
English (en)
Inventor
Gregory L. Wedel
Gerald L. Timm
Kenneth C. HILL
Original Assignee
Kadant Johnson Inc.
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 Kadant Johnson Inc. filed Critical Kadant Johnson Inc.
Priority to PCT/US2013/040716 priority Critical patent/WO2014185886A1/fr
Publication of WO2014185886A1 publication Critical patent/WO2014185886A1/fr

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Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B31—MAKING ARTICLES OF PAPER, CARDBOARD OR MATERIAL WORKED IN A MANNER ANALOGOUS TO PAPER; WORKING PAPER, CARDBOARD OR MATERIAL WORKED IN A MANNER ANALOGOUS TO PAPER
    • B31F—MECHANICAL WORKING OR DEFORMATION OF PAPER, CARDBOARD OR MATERIAL WORKED IN A MANNER ANALOGOUS TO PAPER
    • B31F1/00—Mechanical deformation without removing material, e.g. in combination with laminating
    • B31F1/20—Corrugating; Corrugating combined with laminating to other layers
    • B31F1/24—Making webs in which the channel of each corrugation is transverse to the web feed
    • B31F1/26—Making webs in which the channel of each corrugation is transverse to the web feed by interengaging toothed cylinders cylinder constructions
    • B31F1/28—Making webs in which the channel of each corrugation is transverse to the web feed by interengaging toothed cylinders cylinder constructions combined with uniting the corrugated webs to flat webs ; Making double-faced corrugated cardboard
    • B31F1/2845—Details, e.g. provisions for drying, moistening, pressing
    • B31F1/2877—Pressing means for bringing facer sheet and corrugated webs into contact or keeping them in contact, e.g. rolls, belts
    • B31F1/2881—Pressing means for bringing facer sheet and corrugated webs into contact or keeping them in contact, e.g. rolls, belts for bringing a second facer sheet into contact with an already single faced corrugated web
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F22—STEAM GENERATION
    • F22B—METHODS OF STEAM GENERATION; STEAM BOILERS
    • F22B1/00—Methods of steam generation characterised by form of heating method
    • F22B1/28—Methods of steam generation characterised by form of heating method in boilers heated electrically
    • F22B1/282—Methods of steam generation characterised by form of heating method in boilers heated electrically with water or steam circulating in tubes or ducts
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F22—STEAM GENERATION
    • F22B—METHODS OF STEAM GENERATION; STEAM BOILERS
    • F22B37/00—Component parts or details of steam boilers
    • F22B37/02—Component parts or details of steam boilers applicable to more than one kind or type of steam boiler
    • F22B37/26—Steam-separating arrangements

Definitions

  • the invention pertains to a method and apparatus for improving the heating capacity of steam-heated hot plates, and in particular, to steam-heated hot plates used in the corrugating industry.
  • Corrugated containerboard is manufactured on machines that combine one or more "liners” in a stack with fluted webs ("medium”) in between, with the peaks of the medium flutes glued to the surfaces of the liners.
  • the adhesive between the fluted medium and the liners of the combined board (that is, the corrugated containerboard) is then dried by passing the board through a double face heating section.
  • the double face heating section (“double-backer") consists of a series of steam-heated "steam chests” or “hot plates.” Individual steam chests and hot plates are generally less than two feet in machine direction length and extend to the width of the corrugator, which is typically 100" to 120" in width.
  • the containerboard is held against these steam chests and hot plates by belts and ballast rollers that serve to keep the board in good thermal contact with the top surfaces of the hot plates/steam chests.
  • FIG. 1 shows a steam chest 10 according to the prior art.
  • FIG. 2 shows a hot plate according to the prior art.
  • Steam chests 10 and hot plates 40 are examples of steam heating devices designed to transfer heat from steam to a heating surface.
  • Steam chests 10 can be constructed as large metal boxes 12 that are designed to hold the steam at input "A" to the box interior 16 under pressure. The steam condenses on the top inside surface of the box 12 and the condensed steam (“condensate”) falls onto and collects on the bottom of the box 12.
  • the condensate is drained by gravity to a steam trap 22 from which the condensate is returned to the boiler at "B."
  • the box upper surface 14 is in contact with the containerboard 15 to be dried, which is held down to the upper surface 14 by a belt 20.
  • Steam chests 10 are conventionally heated by steam that is supplied under pressure to each of the steam chests.
  • the steam pressure to each group of steam chests 10 is typically controlled by a pressure control valve (not shown) working in conjunction with a pressure transmitter and a pressure indicating controller.
  • FIG. 2 shows a "hot plate” 40 (herein distinguished from “steam chest” 10) is similar in function to a steam chest 10, except the hot plate 40 has drilled internal passages 44 adjacent to the hot plate surface 46.
  • the corrugated containerboard 48 can be held down to the hot plate surface 46 by a belt 50.
  • the hot plate surface 46 and internal passages 44 are formed as part of the hot plate frame 42. These internal passages 44 generally extend from one side of the hot plate frame 42 to the opposite side, and then back again, forming several loops before the passage leaves the plate.
  • the steam flows into inlet 43 and through these internal passages 44 and condenses as it transfers its heat to the corrugated containerboard 48 on the outside of surface 46.
  • the condensate flows slowly by gravity toward a drain (45).
  • the drain line is conventionally connected to a steam trap. Steam traps open to drain the condensate from the hot plate and then close to prevent the passage of uncondensed steam. The condensate that leaves the steam trap is returned to the boiler. At high condensing rates, the condensate that forms inside the passages of the hot plates 40 tends to accumulate and result in a reduction in rate and uniformity of heat transfer.
  • a typical corrugated containerboard making machine 300 that includes a double backer section 314 is shown in FIG. 3.
  • the corrugated containerboard making machine 300 includes supply rollers 302 for the first liner, supply rollers 304 for the medium and supply rollers 306 for the second liner.
  • the corrugated containerboard making machine 300 also includes a corrugator 308, drive rollers 310 and adhesive applicator 312.
  • the corrugated containerboard making machine also includes a hot plate section 318 in the double backer section 314 for drying the adhesive applied at 312.
  • each double backer section 3114 In order to minimize the non-uniformity of heat transfer, a multitude of hot plates are used in each double backer section 314. The pressure is adjusted on the belt 316 that holds the board to the hot plates 318 in an attempt to correct for these reductions in rate and uniformity of heat transfer.
  • the hot plate performance is controlled by the belt pressure, adding backing rolls, loading the backing rolls, increasing the steam pressure, venting some steam to atmosphere, adding more hot plates, or running the corrugating machine at a slower speed.
  • FIG. 4 shows a steam line 402 inputting steam at "A.”
  • the steam line 402 delivers steam either directly to a hot plate 408 via delivery lines 414 or to pressure control valves 404, 406, which regulate the steam pressure and deliver steam to hot plates 410, 412 via delivery lines 416, 418.
  • the steam heats the hot plates 408, 410, 412 and condenses, forming a condensate that is collected by condensate trap lines 420, 422, 424 and carried to separators 426, 428 which separate condensate from steam and returns separated steam to the delivery lines 416, 418, or returned directly to a pump 432.
  • Condensate is routed to pumps 430, 432 to be returned to the steam boiler (not shown) via return line 434 at "B.”
  • the prior art hot plates and their steam systems are not suitable for high-speed corrugated boxboard production where uniformity, high heat transfer rates, and energy efficiency are important.
  • aspects of disclosed embodiments include an improved method for transferring heat from a steam heating device including introducing steam into the steam heating device with a steam supply system; circulating the steam through the steam heating device creating steam condensate and collecting the steam and steam condensate with a separator tank which separates the steam from the steam condensate; returning the steam condensate to the boiler to be reheated; returning the steam to a thermocompressor which heats and pressurizes the steam and introduces it back into the steam supply system; and wherein the steam heating device includes a ratio of steam to steam condensate of at least 20: 1 by volume.
  • aspects of disclosed embodiments also include an apparatus for transferring heat from a steam heating device including a steam supply system for supplying steam; a steam heating device; a separator tank which separates the steam from the steam condensate; a thermocompressor which heats and pressurizes the steam and introduces it back into the steam supply system; and wherein the steam heating device includes a ratio of steam to steam condensate of at least 20: 1 by volume.
  • FIG. 1 is a diagram of a prior art steam box
  • FIG. 2 is a diagram of a prior art hot plate
  • FIG. 3 is a diagram of a prior art corrugating system
  • FIG. 4 is a diagram of a prior art steam control system
  • FIG. 5 is a diagram of a steam control system according ; to disclosed embodiments.
  • FIG. 6 is a diagram of a steam control system according ; to disclosed embodiments.
  • the method and apparatus of the subject disclosure includes a steam-heated hot plate of the type typically used in the double-face heating section of machines that manufacture corrugated board, a steam pressure transmitter, a steam pressure indicator controller, a steam and condensate separator tank, a blow-down valve, a steam jet thermocompressor, and a pressure powered condensate pump.
  • the subject disclosure is applicable both to steam chests and to hot plates. Steam chests and hot plates can be referred to collectively as steam heating devices. If, when the steam chests or hot plates are first heated, the residual non-condensing gases (mostly air) are not purged, this can result in a further reduction in rate and uniformity of heat transfer.
  • Steam heating devices can be equipped with a trap or separator which separates the live steam from condensed steam (water).
  • a small line or passageway can be installed around the trap to by-pass the trap and allow "live” (uncondensed) steam to purge the air.
  • the discharge of the live steam gives rise to poor thermal efficiency and lack of process control. This escape of live steam with residual non-condensing gasses is called blow through.
  • a steam pressure indicating controller maintains the desired steam pressure in the header that feeds one or more of the hot plates in the double -backer section.
  • the drain line from the hot plate(s) discharges to the steam and condensate separator.
  • the condensate is returned to the boiler through the pressure powered condensate pump.
  • the blow through steam from the separator is piped to the suction port of the thermocompressor from where it is boosted in pressure by the thermocompressor and recirculated back to the supply header for the hot plate section. With this concept, the entire blow through steam is re-used.
  • FIG. 5 is a diagram showing a steam control system 500 for supplying steam to a number of steam heating devices, which in this example include one or more hot plates 508.
  • the steam pressure indicating controller 530 is used to maintain the hot plate header 506 pressure. This is accomplished by modulating the actuator on the thermocompressor 504 using the steam pressure indicating controller 530.
  • the steam pressure indicating controller 530 is connected to transducer 532 which can measure steam pressure and temperature. Steam enters the high pressure steam input 502 at "A" and is routed to the thermocompressor 504 and the blow down valve 528 via line 518. Steam from the high pressure steam input 502 is combined with pressurized circulated steam at the thermocompressor 504 and routed to the hot plate header 506, which distributes the steam to the hot plates 508, under the direction of the steam pressure indicating controller 530.
  • the steam circulates through the hot plates 508 and partially condenses.
  • the circulated steam and condensate is output from the hot plates 508 through the return lines 510.
  • the return lines 510 route the circulated steam and condensate to a separator tank 512 where circulated steam is separated from condensate.
  • the condensate is removed from the separator tank 512 via condensate line 514 to pump 516, which pumps the condensate back to the steam boiler (not shown) via line 520 in direction "B.”
  • thermocompressor 504 via the re-circulation line 522 to be pressurized and blended in with the new steam arriving from the high pressure steam input 502 to be returned to the hot plate header 506 and thereby to the hot plates 508.
  • the amount of blow through flow and the differential steam pressure across the hot plates 508 depend on the operation of the thermocompressor 504 and are not primary control parameters.
  • the thermocompressor 504 ensures the drainage of condensate from the hot plate(s) 508 and maintains high and uniform heat transfer from the hot plates 508 by a continuous and appropriate flow of blow through steam through the hot plate section.
  • FIG. 6 shows another disclosed embodiment of a steam supply system 600.
  • the amount of blow through flow and the differential steam pressure across the hot plates 608 are alternatively selected as control parameters for the thermocompressor 604.
  • the steam pressure in the hot plate steam supply header 606 is controlled directly by the steam pressure control valve 638.
  • the thermocompressor 604 set point ensures the drainage of condensate from the hot plate(s) 608 and maintains high and uniform heat transfer from the hot plates 608 by a continuous and appropriate flow of blow through steam through the hot plate section.
  • thermocompressor 604 is supplied with steam at a pressure that is equal to or suitably higher than the steam supply header 606 to the hot plates 608.
  • the high pressure (“motive") steam that is supplied to the thermocompressor 604 is mixed with the low pressure steam from the separator tank 612 and discharges the mixture to the steam supply header 606 at a pressure that is at least as high as the steam supply header 606.
  • the thermocompressor 604 mixes high pressure steam from the high pressure steam input 602 with pressurized circulated steam from the separator tank 612 under the control of a pressure indicating controller 630, which gets information from a digital pressure transducer 632.
  • thermocompressor 604 The output of the thermocompressor 604 is controlled by a control valve 638 that mixes high pressure steam from the high pressure steam input 602 with pressurized circulated steam under the control of a pressure indicating controller 636, which gets information from a pressure transducer 634.
  • Circulated steam and condensate exit the hot plates 608 via return lines 610 which route the circulated steam and condensate to the separator tank 612, which separates the circulated steam from the condensate.
  • the condensate is sent through condensate line 614 to a pump 616, which pumps the condensate back to the steam boiler (not shown) via boiler return line 620.
  • Circulated steam is routed from the separator tank 612 via steam return line 622.
  • the returning steam can be routed through valve 624 to blow down line 626 to blow down the system upon start up or be routed to thermocompressor 604.
  • This method and apparatus maintains a flow of blow-through steam that is by volume that can be 20-30 times higher than the condensate flow volume.
  • This high volume of steam quickly purges the hot plate section 608 of all non-condensable gases, flushes the condensate through the passages in the hot plate 608 to decrease the amount of sub-cooled water that is in the passages, and prevents passages from flooding with condensate, thermally bowing, and losing heat transfer.
  • This concept allows the simultaneous achievement of high and uniform heat transfer and high operating efficiency, because the high volume of blow through steam is reused in the hot plate section 608. Still further, this concept can quickly purge non-condensable gases from the heaters and reduce the amount of sub-cooled condensate in the heaters that would otherwise cause thermal bowing of the heaters and the corresponding loss of adhesive bond uniformly.
  • thermocompressor 604 can be directed to the hot plate steam header of a down-stream hot plate section (not shown). This would be termed a "cascade thermocompressor system.”
  • Embodiments of this disclosure include aspects in which the differential pressure transmitter 630 of FIG. 6 is configured to measure the pressure drop across an appropriate orifice plate (not shown) in the uncondensed steam (blow through) line 622 so that the position of the control spindle in thermocompressor 604 will be adjusted to maintain a fixed flow rate of uncondensed steam.
  • a further feature of the subject invention is the addition of a blow-down system to facilitate the start-up of the corrugator by purging air and other non-condensable gases from the corrugator system. This is accomplished by suitable control of a blow-down valve 524, 624 that discharges as shown in FIGS. 5 and 6 to the blow-down lines 526, 626.
  • a suitable thermostatic trap 540, 640 is used to clear non-condensable gases from the separator tank 512, 612 intermittently directing the discharge flow as needed to the blow-down line 526, 626.

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  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • General Engineering & Computer Science (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Sustainable Development (AREA)
  • Sustainable Energy (AREA)
  • Machines For Manufacturing Corrugated Board In Mechanical Paper-Making Processes (AREA)

Abstract

Cette invention concerne un procédé et un appareil conçus pour améliorer la capacité de chauffage de plaques chauffantes chauffées par vapeur, comprenant un ou plusieurs séparateurs et un ou plusieurs thermocompresseurs ajoutés à la sortie des plaques chauffantes pour séparer la vapeur purgée du condensat et pressurer et injecter la vapeur purgée à l'intérieur des plaques chauffantes.
PCT/US2013/040716 2013-05-13 2013-05-13 Système de génération de vapeur à plaques chauffantes WO2014185886A1 (fr)

Priority Applications (1)

Application Number Priority Date Filing Date Title
PCT/US2013/040716 WO2014185886A1 (fr) 2013-05-13 2013-05-13 Système de génération de vapeur à plaques chauffantes

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
PCT/US2013/040716 WO2014185886A1 (fr) 2013-05-13 2013-05-13 Système de génération de vapeur à plaques chauffantes

Publications (1)

Publication Number Publication Date
WO2014185886A1 true WO2014185886A1 (fr) 2014-11-20

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PCT/US2013/040716 WO2014185886A1 (fr) 2013-05-13 2013-05-13 Système de génération de vapeur à plaques chauffantes

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Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS60292A (ja) * 1983-06-17 1985-01-05 Mitsubishi Plastics Ind Ltd ホツトプレスの加熱冷却装置
GB2155164A (en) * 1984-02-10 1985-09-18 Andritz Ag Maschf Heat conservation on the drier section of paper making machines

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS60292A (ja) * 1983-06-17 1985-01-05 Mitsubishi Plastics Ind Ltd ホツトプレスの加熱冷却装置
GB2155164A (en) * 1984-02-10 1985-09-18 Andritz Ag Maschf Heat conservation on the drier section of paper making machines

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