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Publication numberUS2413567 A
Publication typeGrant
Publication dateDec 31, 1946
Filing dateApr 10, 1944
Priority dateMar 22, 1943
Publication numberUS 2413567 A, US 2413567A, US-A-2413567, US2413567 A, US2413567A
InventorsHornbostel Lloyd
Original AssigneeBeloit Iron Works
Export CitationBiBTeX, EndNote, RefMan
External Links: USPTO, USPTO Assignment, Espacenet
Drier drum having keat-exchangefluid supply and removal means
US 2413567 A
Abstract  available in
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Claims  available in
Description  (OCR text may contain errors)

2 Sheets-Sheet vl Dec. 3l, 1946. L. HoRNBosTEL l DRIER DRUM HAVING HEAT-EXCHANGE-F'LUID SUPPLY AND REMOVAL MEANS Filed April 1o, 1944 Dea 31, 1946- l l.. HoRNBosTEL 2,413,567

DRIER DRUM HAVING HEAT-EXCHANGE-FLUID SUPPLY AND REMOVAL MEANS FiledApril 10, 19.44 2 Sheets-Sheet 2 Patented Dec. 31, 1.946

DRIER DRUM 2,413,567 HAVING HEAT-EXCHANGE- FLUID SUPPLY AND REMOVAL MEANS moya nombostel. Beloit, wis., assignmto Beloit Iron Works, Beloit, Wis., a corporation of Wisconsin Application April 10, 1944, Serial No. 530,373

6 Claims.

1 This invention relates to a rotatable drum structure that is heated with a vaporized material thatl boils at high temperatures, More particularly this invention relates to a drier drum fora paper making machine and to means for heating the drying surface of the drum with a high temperature boiling material that has been transformed into a vapor by subjecting the material to high pressure or superheated steam in a chamber*v that is located outside the drum.

'This application is a continuation-in-part of my copending application Serial No. 480,054, filed' March 22, 1943. entitled Drier drum, now Patent No. 2,365.2'71.

While this invention has been disclosed herein as embodied in the drier drum of a paper making machine, itis not intended to in any way limit the structure to this type of drum since the improvements are equally applicable to many types of drums in the other arts.

Heretofore, in order to attain a rapid drying capacity for a drier drum in certain types of paper making and other machines wherein a singie drum of large size is employed, it has been the practice to use high pressure steam in the drum as the heat transfer medium therefor. but this has required a thickening of the drum wall in order to withstand such internal high pressure to which the drum is subjected. This thick wall structure results in a decrease in the heat transfer through the wall to the paper sheet or other web thereon. and the heavier wall also places a higher load upon the drum actuating devices thereby requiring an increased power to rotate the drum. i

The present improvements aim to overcome the conditions above mentioned by providing a high pressure steam boiler exterior to the drum for heating and vaporizlng a high boiling point material. and then transferring this vaporized material which is at a relatively low pressure, to the interior of the drum to transfer heat to the surface thereof. The products of condensation of this vaporized material that accumulate on the walls of the drum are removed and are returned to the high pressure steam boilerfor reheating,

,revaporizing and recircuiating it, By using a high boiling point heat transfer liquid material the steam boiler may be charged with high pressure steam at a temperature up to around 850 pounds per square inch pressure to heat and transform the liquid high boiling heat transfer material into a vapor that is characterized by its high temperature as well as its low pressure which will be only slightly above atmospheric pressure. As a result thereof, the drum structure 2 may be made comparatively light since it is not subjected to high internal pressure.

In carrying out this invention it is contemplated to use a high boiling point material such as that commercially known as Dowtherm" which is-a eutectic mixture of diphenyl and diphenyl oxide. This material is a relatively inert,

colorless and non-corrosive liquid that is stable pressure boiler unit for revaporization and recir.

up to 725 C. and has a boiling point of 258 C. with a heat vaporization of 123 B. t. u. per pound at its boiling point.

Itis one of the principal objects of this invention to simplify the construction of a drier drum such as, contemplated herein and to improve the efiiciency, operation and dependability of such drier drum.

Another principal object of this invention resides in the provision of a high pressure boiler heating unit wherein the heat transfer medium is heated and vaporized at a location outside the drum to be heated, and then discharging such vaporized medium into the drum through a trunnion thereof to bring this hot vaporized material into heat exchange relation with the drum wall. The invention also contemplates the condensing of the vaporizedheating medium upon the walls oi the drum to be removed therefrom into a stationary tray or basket that is disposed axially of the drum, and then conveying the condensate out of the drum for returning it again to the high culation.

Another object of the invention aims to utilize super-heated or high-pressure steam to heat and vaporize a high boiling point heat transfer liquid for charging a drier drum of a paper making machine whereby the drum is maintained at a desirable high degree of temperature without subjecting the drum to a high internal pressure.

It is a further object of the invention to provide i means for removing or exhausting air that may accumulate within the upper segment of the drum thereby preventing the formation of an air pocket that might interfere with or prevent uniform heating of the drum surface upon which the paper is carried.

Another object of the invention is to provide a dipper device coacting with but spaced from the inner surface of the drum, said 'clipper being adapted toscoop up the condensate material from the drum surface and deposit it into a tray or basket within the drum. Scraper means are mounted on the tray or basket to terminate closely adjacent the drum wall to sweep the interior surface of the drum at a position between the lines of travel 0f a pair of spaced dippers. Spacing of the dippers and scrapervfrom the drum surface permits the heating material to contact al1 of the cylindrical part of the drum-thereby preventing formation of zones on the cylinder which are at different temperatures than the rest of the cylinder.

Additional objects, aims and advantages of the invention such as contemplated herein will be apparent to persons skilled in the art after the construction and operation of the drier drum is understood from the within description.

It is preferred to accomplish the numerous objects of this invention and to practice the same in substantially'the manner hereinafter fully described and as more particularly pointed out in the claims. Reference is now made to the accompanying drawings that form a part thereof.

Figure 1 is a vertical longitudinal section through the axis of a drier drum structure showing the instrumentalities of this invention incorporated therein;

Figure 2 is a vertical transverse section of the drier drum taken along the plane of line II--II on Figure l; and

Figure 3 is a diagrammatic view illustrating the manner of vaporizing and circulating the heat transfer material, the evacuation of'condensate liquid from the drum, and the other instrumentalities of the present invention.

The drawings are to be understood as being more or less of a schematic character for the purpose of disclosing a typical or preferred form of the improvements contemplated'herein.

The drier drum according to the invention is designated as a whole by reference numeral I0, and is shown to comprise a cylindrical wall II having end walls or heads I2 and I3 that preferably bulge inward as shown in Figure 1. The web or sheet of paper to be dried is received upon and usually travels with the outer surface of the cylindrical Wall II. The end walls or heads are provided with axially disposed hollow hubs I4 and I5, respectively.

The trunnions of the drum comprise tubular members I6 and I1, respectively, that have flanged end portions IBa and I1a, respectively, and are bolted to the end walls or heads I2 and I3 in surrounding relation with respect to the hubs I4 and I but spaced therefrom. The trunnions I6 and I1 are rotatably mounted in anti-friction bear- `ings I8 carried in journal housings I9 that are supported upon the upper portionsv of pedestals 20. The drum is rotated by means of a large gear 2I that is secured to the trunnion I1 and actuated by any suitable prime mover.

The end walls or heads I2 vand I3 of the drum are exteriorly covered with insulating material 22 that is held in place and protected by means of retainer plates 23. The hollow hubs I4 and I5 of the end walls or heads are sheathed with insulating material 24 that is held in place by cylindrical retainers 25. Suitable access openings 26 are provided in convenient portions of the heads I2 and I3, and these openings are closed by caps or covers 21 that are lined with insulating material 28. Cooling fins 29 project from the flanges I6a and I1a of the trunnions and between these ns the trunnions are provided with apertures 30 that permit coolant air to enter the trunnions to circulate between them and the insulated hubs I4 and I5 of the heads of the drum. The cylindrical wall II of the drum is an effective heat transfer metal that is adapted to retain its shape during the repeated heating and cooling thereof that takes place between the Operating 3|,l and the shut-down periods of the machine. By reason of the above mentional insulating arrangement ,and the cooling of the hub, the cylinder II will be the only heat radiating surface of the drum and it therefore may be made of a relatively thin metal because it is not subjected to internal high pressure due to the use of a heat transfer material that vaporizes at a high boiling point.

A comparatively shallow tray or basket 3I is disposed within the drum and it is of a Width to extend across the diameter of the drum in the manner shown in Figure 2 to space its ends from the inner surface ofthe drum. l

The tray has a trough-shaped bottom portion 32 the outer portions of which are down-turned as at 33, and its edges are connected to suitable end walls 34. A depending rib 35 extends along the lower portion of the tray bottom wall to reinforce and strengthen the tray structure. 'I'he end walls 34 of the tray are suitably secured to annular fianges 35 upon the inner ends of tubular members 31 and 38 that freely pass through the hubs I4 and I5 of the respective heads I2 and I3 of the drum so that their other ends project beyond the ends of said hubs as shown '1n Figure l.

The outer end portion of the tubular member 31 is iixedly mounted in a support 39 on a pedestal 40, and the'outer end of the other tubular member 3B is iixedly mounted in a support 4I upon a pedestal 42 that is located beyond the 4driving gear 2|. The supports 39 and 4| grip the tubes 31 and 38 to support them in spaced relation to the hubs I 4 and I5 that rotate free thereof. This arrangement provides a fixed exterior support for the tray or basket 3l that is Within the drum and it also provides annular passageways 43 and 44 in the clearances between the trunnions and the tubes.

'I'he tray end wall 34 that is secured to the tube 38 has an aperture 45 at least the major portion of which is disposed abcvethe axis of said tube, and the other end wall 34 of the tray that is secured to the tube 31 has an opening 46 ytherein that is preferably co-extensive with the interior bore of the tube 31. A scraper or doctor 41 projects from the mid-portion of a margin of the tray into close proximity to the inner surface of the drum for the purpose of directing condensate swept by it from the drum into the tray. The liquid is drawn ofi' the tray through the large aperture 48 and flows through the tubular member 31. At its outer end the tubular member 31 communicates with a drain-pipe 43 that conveys the condensate to an accumulator or tank 49.

The outer end o'f the tubular member 38 communicates with a nozzle 50 on theA support 42 that receives the heat transfer material in a vaporized form 'at relatively low pressure from a. .conduit 5I that leads thereto from a vapor chest or boiler 52. This vaporized material is discharged into the drum through the aperture 45 in the tray end wall. The lower portion of the end w'all below the aperture 45 provides a dam 53 that prevents the flow of liquid from the tray into the tubular member 33 through which the vapor passes.

*For the purpose of evacuating air from the upper portion of the drum to prevent formation of an air pocket therein, a, suitable air exhaust pipe 54 is disposed in the cylinder with its upper chest 52 comprises a closed shell vthat surroundsy a coil 59 in Ywhich super-heated or high-pressure steam is circulated from any suitable source. The heat transfer material in a liquid form is contained in the shell where it surrounds the coiil 4 59. The temperature of the heat transfer material is thus raised above its high boiling point to vaporize it, and this vapor leaves the boiler shell through a feed pipe 5I that conveys the vaporized -material to the nozzle 50 for discharging it into' the drum through the tube 38 andthe opening 45 in the end wall of the tray.

Thecondensate that accumulates in la iilm upon the interior. surface oi.' the drum is removed therefrom by the scraper or doctor 41 and iiows into the tray or basket 3|. Suitable concave or pocket-shaped dippers 60 are carried by brackets 3| that project inward from the heads I2 and I3 of the drum and are disposed with their lip portions close to the inside surface of the drum to scoop up the condensate liquid that forms a puddle in the bottom or lower segment of the drum during its rotation. 'I'he scoops or dippers travel with the drum and they are arranged preferably in pairs at diametrically opposite portions of the drum, and being in non-contacting relation to the inner surface of the cylinder II they do not interfere with the heating of the drum surface. apart a distance that permits them to clear the end edges of the scraper 41 when the drum is The dippers of each pair are spaced.'

operating. These dippers 60 are adapted to spill the condensate liquidlnto the tray or basket 3I after they have traveled above the horizontal plane of said tray. The superficial area of the tray is sufiicient to receive any drip 0f the con..

densate that may gravitate from or -be thrown off during rotation of the drum. The liquid of condensation passes out of the tray through the large aperture 46 in its end Walland flows into tubular member 31 from which it is removed by the drain-pipe 48 that discharges into the accumulator 49. From .the accumulator the condensate liquid is returned to the steam chest or boiler by means of a fluid pump B2 and a return pipe E3. This arrangement is effective for the recirculation and the revaporization of the heat transfer material. r

An annular seal casing 64 is carriedby the end `iace of the hub I5 to rotate with lthe drum in surrounding rel-ation to the end portion of the stationary'tubular member 38. Within this casing the tubular member 38 has an annular collar 65 secured to it that has a radial bore B6 alined with a hole in this tubular member.v An elbow coupling 81 is threaded into the hole to establish communication between the radial bore and a suction pipe 68 that extendsout of the supported end of the tubular member 38 and through a gland 59 in the wall of the nozzle 50 and thence to the condenser 51. A pair of spaced diaphragm rings 10 are carried by the inner surface of seal casing 64 and extend inwardly toward and past the outer face of the collar 95 on tubular member 38 where they are provided with seal rings 1I vthat slidably engage or oppose the side face oi' said collar to bear against them in sealingr relation. The spacing of these diaphragm rings 1I! provides between them an annular sealed chamv may pass through `suctionpipe 38.

-ber 12 with which the radial bore 88 of collar 95 .is in communication, so that the said chamber may be evacuated by suction pipe 88 in response The outer end face of the other drum hub I3 carries a seal casing 13 the surface of which has diaphragm rings 14 secured to it that extend inwardly toward the adjacent end portion of tubular member 31 upon each side of a collar 15 secured to said tubular member 31. Seal rings 16 are secured to the diaphragm rings 14 in contacting relation to the side faces of the collar against which they are adapted to slide toveffect a seal therebetween. This arrangement provides a sealed annular chamber 11 between the diaphragm rings 14 andy surrounding the adjacent portion of the tubular member 31. A radial bore 1B is made in the collar 15 that opens into chamber 11 and is registered with a hole in the adiacent portion of the tubu1armember31. An elbow coupling 19 has an end threaded into the hole to establish communication between the annular chamber 11 and a suction pipe 80 that is screwed intothe other end of the coupling 19. The suction pipe 80 passes through a gland 8| in the closure plate or cap 55 at the end face of the tubular member 31 and leads to the condenser 51 that is located in advance of the vacuum pump 58 in the same manner as before described with respect to the suction pipe 68.

'Ihe action of the vacuum pump 5B is to establish a vacuum in the annular chamber 12 in the seal casing 64 carried at the end of trunnion I5,

.and also a vacuum in the annular chamber 11 in the seal casing 13 carried at the end of trunnion I4.

The interiors of the seal casings 64 and 13 next to the ends' of the respective trunnions, are in communication with the interior of the drum through the annular passageways 43 and 44 that are provided by the clearances 'between the trunnions and the telescoped adjacent tubular members that carry the tray 3i. By means of this arrangement, any vaporized heat transfer material that may seep past the seal rings 1I and 16, due to an increase of pressure in the drum above the desired pressure, will be sucked out of the respective chambers 'l2 and 11 through the suction pipes 68 and and delivered to the condenser 51.. Condensate liquid matter will flow from the condenser into `the accumulator 49 through a pipe 82 and the volatile, non-condensibles will be drawn off by the vacuum pump 58 and discharged into the atmosphere.. A similar condens-er 51? and pump 58 are provided in communication with the accumulator 49 through the pipe 82 so as to remove volatile non-condensibles from the iiuid circuit including the accumulator and boiler. This arrangement provides a blowoil' for the drum and is eilective to clear the drum of abnormal pressure and to discharge the noncondensible matter at a location remote to the paper making machine.

This invention provides a drier drum construction that is heated with a low pressure hot vapor that is produced outside the drum by subjecting a high boiling material in a boiler to heat transfer from high pressure or superheated steam. There is a closed fluid circuit in which the drum and the boiler are interposed, with one side of the iluidcircuit constituting a drain leading from the drum to the boiler, and the other side of said fluid circuit providing the means whereby the vaporized high boiling material is delivered to the drum. This arrangement effects the continuous revaporization and recirculation of the high boiling heat exchange material. It also provides for the heating of the drum with a low pressure vapor slightly above atmospheric pres-sure but having the temperature of high pressure steam, without subjecting the walls of the drum to undesirably high internal pressures.

I claim as my invention:

1. In a drier drum assembly the combination of a rotatable cylinder; a closed fiuid circuit, in which said cylinder is interposed, for passing vaporized heat transfer material into the cylinder to heat the same, one side of said uid circuit constituting a drain for said cylinder; a stationarily supported tray within said cylinder -With scraper means attached thereto and extending into close proximity with the inner surface of said cylinder adapted to collect condensate from the inner surface of said cylinder and'deliver the condensate to the drain side of said fluid circuit; means including dipper means supported within said cylinder and rotatable therewith for collecting condensate from the surface of the cylinder for delivery to said tray; a heat exchanger exterior to said cylinder col rising a housing interposed in said fluid circuit to receive condensate from the drain side of said fluid circuit; high boiling low vapor pressure material in said housing; and means for passing high pressure steam through said housing in heat exchange relation to the high boiling material to vaporize the material for delivery to the other side of said fluid circuit; said heat exchanger and said fluid circuit constituting means whereby the high boiling material is continuously revaporized and recirculated through said cylinder 2. A drier drum comprising a cylinder; hollow trunnions for supporting and journaling said cylinder for rotation; a tray disposed diametrically across the interior of said cylinder for receiving condensate from the inner surface thereof; stationary hollow -supports extending through the trunnions into the cylinder for maintaining the tray in fixed relation within said cylinder, one of said supports adapted to drain condensate from said tray; means for discharging heating vapor through the other of said supports to charge said cylinder with said vapor; scraper means projecting from said tray into close relation with the interior surface of said cylinder for -removing condensate from said interior surface and for discharging the condensate into said tray; and dipper means mounted in said cylinder adjacent the ends thereof and rotatable therewith for collecting condensate of the vapor from the inner surface of the cylinder for discharge to said tray.

3. In a drier drum assembly the combination of a cylinder; hollow trunnions for supporting and journaling said cylinder for rotation; a tray disposed in said cylinder for receiving condensate from the inner surface thereof; hollow stationary supports extending through the trunnions into said cylinder for maintaining said tray in fixed relation within said cylinder, one of said supports adapted to drain the condensate from said tray; the other of said supports providing communication with the interior of said cylinder; means including dipper means supported Within said cylinder and rotatable therewith for collecting condensate of the vapor from the surface of said cylinder for delivery to said tray; a heat exchanger exterior to said cylinder comprising a casing containing high boiling material, and a hlghrpressure steam coil in said casing positioned to be submerged in the material to vaporize the same; and a conduit establishing communication between said casing and said other tray support for charging the cylinder with the vaporized material.

-maintaining the tray in fixed relation Within said cylinder, said supports communicatingwith the interior of said cylinder and one of said supports adapted to drain said tray; means including dipper means supported within said cylinder and rotatable therewith for collecting condensate of the vapor from the surface of said cylinder for delivery to said tray; means exterior to said cylinder for subjecting heat transfer material to high pressure steam to vaporize the material; means for delivering the vaporized material through the other of said supports for charging the cylinder. with said vaporized material; an exhaust pipe extending inside said cylinder and having an inlet adjacent the top thereof; a pump `for removing vapor from the inside of said cylinder through said exhaust pipe; a condenser for condensing the removed vapor; and means for returning the condensed vapor to said fluid circuit. 5. In adrier drum assembly the combination 0f a Cylinder having end heads; hollow trunnions projecting from said heads for supporting and journaling said cylinder for rotation; a tray disposed diametrically across the interior of said cylinder for receiving condensate from the inner surface thereof; stationary hollow supports yextending through the trunnions into the cylinder for maintaining the tray in fixed relation within f said cylinder, one of said supports adapted to drain condensate from said tray; means for dis.- charging heating vapor through the other of said supports to charge said cylinder with Vapor; and dippers carried by saidheads in non-contacting relation to the inner surface of the cylinder for removing condensate from said inner surface and depositing the condensate in said tray.

6. In a drier drum assembly the combination of a cylinder; hollow trunnions for supporting and journaling said cylinder forl rotation; a tray disposed diametrically across the interior of said cylinder for receiving condensate from the inner surface thereof; means including dipper means supported within said cylinder and rotatable therewith for collecting condensate of the vapor from the surface of said cylinder for delivery to said tray; apertured end walls for said tray, stationary hollow supports extending through said trunnions into the cylinder for maintaining the tray in fixed relation within said cylinder, one of said supports adapted to drain condensate from said tray through one of the apertured end walls, and means for discharging heating vapor through the other of said supports and the other apertured end wall to charge the cylinder with vapor, the said other end wall having its aperture so adapted that the solid portion of said wall provides a dam beneath its aperture to prevent flow of liquid from the tray into the adjacent hollow support.

. LLOYD HORNBOSTEL.

Referenced by
Citing PatentFiling datePublication dateApplicantTitle
US2598182 *Dec 6, 1948May 27, 1952Power Jets Res & Dev LtdHeat exchanger bearing arrangement
US2714538 *Sep 11, 1952Aug 2, 1955Beloit Iron WorksInsulating sleeve for dryer bearings
US3142866 *Jan 16, 1961Aug 4, 1964Eastman Kodak CoLiquid cooled casting drums
US3146078 *Feb 15, 1961Aug 25, 1964Heinrich GersterInstallation for heating drying drums of drying machines
US3363328 *Nov 26, 1965Jan 16, 1968Kimberly Clark CoRotary drying drum
US3807950 *Oct 13, 1971Apr 30, 1974R RogersMethod of dyeing and/or washing fabric
US4385453 *Apr 28, 1981May 31, 1983Leland A. Withers, Sr.End panel insulator assembly for temperature controlled rotary cylinder
US4385455 *Nov 3, 1981May 31, 1983Leland A. Withers, Sr.Rotary cylinder end wall insulator with seal
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US8826560 *Sep 1, 2006Sep 9, 2014Kadant Inc.Support apparatus for supporting a syphon
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US20100126033 *Nov 9, 2009May 27, 2010Osvaldo Ricardo HaurieCylindrical dryer having conduits provided within a plurality of holding plates
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DE19747555A1 *Oct 28, 1997Apr 29, 1999Voith Sulzer Papiertech PatentHeiz- und/oder kühlbarer Zylinder
DE19756152A1 *Dec 17, 1997Jul 1, 1999Voith Sulzer Papiertech PatentSteam heated roller for treating surface of paper webs
DE19756152C2 *Dec 17, 1997Jun 27, 2002Voith Paper Patent GmbhDampfbeheizte Walze
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Classifications
U.S. Classification34/124, 165/89, 34/119
International ClassificationD21F5/02
Cooperative ClassificationD21F5/02
European ClassificationD21F5/02