US3694926A - Sonic drying of webs - Google Patents

Sonic drying of webs Download PDF

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US3694926A
US3694926A US46979A US3694926DA US3694926A US 3694926 A US3694926 A US 3694926A US 46979 A US46979 A US 46979A US 3694926D A US3694926D A US 3694926DA US 3694926 A US3694926 A US 3694926A
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web
sound
air
drying
wiping
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Stephen Anthony Rodwin
Eustace Cosmo Shuffler
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General Electric Canada Co
Valmet Montreal Inc
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Dominion Engineering Works Ltd
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Assigned to CANADIAN GENERAL ELECTRIC COMPANY LIMITED- COMPAGNIE GENERALE ELECTRIQUE DU CANADA LIMITEE reassignment CANADIAN GENERAL ELECTRIC COMPANY LIMITED- COMPAGNIE GENERALE ELECTRIQUE DU CANADA LIMITEE CHANGE OF NAME (SEE DOCUMENT FOR DETAILS). Assignors: DOMINION ENGINEERING WORKS LIMITED
Assigned to VALMET-DOMINION INC. reassignment VALMET-DOMINION INC. MERGER (SEE DOCUMENT FOR DETAILS). Assignors: CANADIAN GENERAL ELECTRIC COMPANY LIMITED- COMPANIE GENERAL ELECTRIQUE DU CANADA LIMITEE
Assigned to VALMET-DOMINION INC. reassignment VALMET-DOMINION INC. ASSIGNMENT OF ASSIGNORS INTEREST. Assignors: CANADIAN GENERAL ELECTRIC COMPANY LIMITED,, DOMINION ENGINEERING WORKS LIMITED
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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26DRYING
    • F26BDRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B7/00Drying solid materials or objects by processes using a combination of processes not covered by a single one of groups F26B3/00 and F26B5/00
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21FPAPER-MAKING MACHINES; METHODS OF PRODUCING PAPER THEREON
    • D21F5/00Dryer section of machines for making continuous webs of paper
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21FPAPER-MAKING MACHINES; METHODS OF PRODUCING PAPER THEREON
    • D21F5/00Dryer section of machines for making continuous webs of paper
    • D21F5/006Drying webs by using sonic vibrations
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26DRYING
    • F26BDRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B5/00Drying solid materials or objects by processes not involving the application of heat
    • F26B5/02Drying solid materials or objects by processes not involving the application of heat by using ultrasonic vibrations

Definitions

  • the present invention provides an apparatus for obtaining the mechanical dislocation of liquid within a web by the application of sonicly vibrating gaseous fluid thereto either alone or in combination with an impingement gas flow for the removal of the dislocated liquid. While such liquid is usually water, such is not necessarily the case, as other liquids in furnish are also known.
  • the raising of the temperature of the energizing fluid enhances sound energization.
  • dislocated moisture from the web partially moist air such as air issuing from the sound sources, after having picked up web moisture either as finely distributed mist or in vapor form, is effective as a moisture transporting agent, while also enhancing the sound field due to its characteristic of reducing sound attenuation, relative to a dry air sound field.
  • Web moisture may be carried in mist droplet fonn by the air stream, being dispersed by the sound field into micro droplets as opposed to passage only in the vapor form for conventional heat drying processes, thus enhancing the economics of extraction in liquid form.
  • the present invention may be utilized with stationary webs.
  • the present invention in order to meet production requirements of rapid dewatering for moving webs such as in a paper machine, the present invention is utilized in relation to a moving web, in which high web passage speeds may be achieved. It will be understood that the effect of increased speed may enhance drying rates due to improved action of the sonic field in the web boundary. Hence this process is particularly suited for high speed machines.
  • a particular advantage afforded by the present invention relates to the adaptability thereof with existing paper drying machinery whereby the drying rates of the combined plant may be increased, thereby permitting the speed of the paper making machine to be correspondingly increased.
  • the efi'ects of other subsequent surface drying processes are generally enhanced.
  • the fact, that sonic drying does not result in such a large temperature drop as is normally experienced in conventional evaporative drying due to evaporative cooling makes the achievement and maintenance of suitable web temperatures more economical.
  • Wiping or impingement air may be supplied in a variety of ways to afford control of drying rates.
  • air When air is used for actuating the sonic generator, it is generally possible and desirable to utilize resonated exhaust process air, with or without secondary air of low moisture content, by passing the air as a wiping fluid across the web surface. Low velocity air wiping may be achieved utilizing pressure build up in the sound field.
  • the control of air escape from the sonic zone by suitable throttle means is then readily provided, to effect the desired control over moisture removal by variation of the wiping air flow rate.
  • air pressurizing means such as a fan or blower, for the direct supply of secondary air in bypass relation to the whistle.
  • Such by-pass secondary air may be passed through the resonating field produced by the whistles. Local control by adjustment of wiping air flow permits the eradication of wet streaks in the web.
  • Such bypass secondary air may be fresh air or recirculation air, or a mixture of fresh and recirculation air to provide desired psychometric conditions.
  • the operation of the sound generation means is enhanced by the provision of sound reflector means to direct the sound energy against the web and by reflection to return a considerable portion of energy to the source in re-energizing relation therewith.
  • the provision of auxiliary sound reflectors to minimize the passage of sound energy from the zone enhances the sound intensity within the zone while reducing the provision of sound proofing necessary to reduce outside noise to practical working levels.
  • the provision of perforated reflectors adjacent the web entry and exit locations permits the passage of air therepast in web wiping relation, while enhancing the performance of the sound chamber. The sonic energy absorption losses in reflectors is effectively returned to the process in the form of heat energy.
  • the subject process includes the supply of compressed air to the sound generators.
  • the raising of the temperature of the supply air enhances both drying and whistle efficiency.
  • To produce higher temperature supply air the choice exists between heating of the already hot compressor output air by independent heating means or more effectively utilizing the compressor to produce the required exhaust temperature, by raising compressor inlet temperature slightly above ambient, providing intake air in the range of F to F at the compressor inlet.
  • the latter course is more economical in heat energy requirement, while capita cost is minimized.
  • FIG. 1 shows two perspective sectional arrangements of embodiments of the subject invention showing the use of transverse trough-like sound generators, and individual sound reflectors, respectively;
  • FIG. 2 is a side sectional view showing a first embodiment having an unsupported web and using only primary or whistle air as the moisture transport medium;
  • FIG. 3 is a side sectional view showing a further embodiment having a resonant chamber receiving secondary air;
  • FIG. 4 is a further embodiment similar to that of FIG. 1, with secondary air circulation provision;
  • FIG. 5 is a view similar to FIG. 3 of a further embodiment
  • FIG 6 is a sectional detail of an edge seal suitable for use with the sound chambers illustrated in FIGS. 2 5', and
  • FIG. 7 shows characteristic drying rate curves, and appears with FIG. 1.
  • this illustrates the form of two alternative sound generator arrangements, the first showing trough-shaped reflectors 18 in series arrangement within a sound hood, each trough reflector having a plurality of stem jet whistles herein, while in the second arrangement is shown a plurality of whistles, each with an individual reflector 18' and mounted in staggered relation.
  • this shows a vertical unsupported web run wherein the drier section 10 has a first sonic chamber 12, and an opposing sonic chamber 14, each chamber having a cap or cover 16 comprising reverberation plates.
  • Each chamber 12, 14 is provided with a plurality of sound generators 18 to propagate longitudinal sound waves against the web 20.
  • the chamber may be in horizontal or vertical arrangement, depending generally on the provision of web support netting and the symetry of incident energy, in relation to the grade of paper.
  • Each sound generator 18 comprises a trough-like reflector having a plurality of spaced whistles, such as a stern jet whistle 26 provided with air from a compressor by supply conduit means 24, and mounted within sound reflecting means 28, 30 to concentrate both the longitudinal sound emission and sound reflection at the surface of the web 20, the distance A" representing very nearly a multiple of the whistle half wave length at desired operating conditions.
  • the individual whistles 26 are spaced laterally in the reflecting means 28, 30 at substantially uniform distances having multiples of half wave length apart to minimize mutual interference. Intervening baffles may be used.
  • the reverberating cap or cover 16 defining a sonic chest also is located at a selected distance B from the web surface, equal to approximately a multiple of the whistle half wave length.
  • the reflector plates 23 adjacent the web path also serve to retain sound energy within the section 10.
  • the alternative provision of individual whistles having circular individual reflectors of similar diametral section to that of the trough reflectors is also contemplated.
  • the sound generators 18 including supporting side walls 25 having apertures 32 extending therethrough and connecting with vents 22 in the cover 16 to permit the passage of air from the whistles in fluid wiping relation over the surface of web 20, for exhaust to the hooded zone above the section 10, by way of the apertures 22, shown as having sound relfecting bafl'le means 11 therein to maintain a low sound level in the vicinity of the drier section.
  • the sound reflectors 31, 41 and 51 also are illustrated as extending for the width of the respective drier section 10.
  • the alternative use of individual circular reflectors shown in FIG. 1 shows a mutual staggered arrangement to provide distribution of sound field across the web.
  • FIG. 4 shows air circulator 45, having an enclosure mounted on the cover 16 of the sonic chest with an air circulating fan 41 mounted therein.
  • the apertures 37, 44 and 39 provide access for wiping air recirculating within the sonic chest of the drier section 10, while the dampers 43 and 47 operating in conjunction with apertures 51 and 53 provide blending elation with hood air from outside the sonic chest for a desired combination of hood air and recirculation air in accordance with desired psychometric conditions.
  • the setting of the dampers 43 and 47 is controlled by the levers 49 and 50.
  • FIG. 5 shows a horizontal arrangement wherein a support wire mesh 521 carries the web 520 in supported relation between the opposed sound chests 510.
  • Each chest 510 contains one or more troughlike reflectors 518, each reflector containing a plurality of stem whistles 526 in mutually spaced relation.
  • the cross-sectional profile of the rough reflectors 518 differs from the parabolic form of FIGS. 1 and 4.
  • Primary air from the whistles 526, together with secondary air passing downward through apertures 539, serves to scour the boundary layer from ofl the web 520.
  • the secondary air is heated by heaters 550, illustrated as being of the electrical resistance type.
  • Fan means 541 provides circulation of the secondary air, while the adjustable dampers 545 control the inlet access of hood air and the adjustable dampers 547 control the portion of air passing from the fans 541 in recirculating relation over the surface of web 520 by regulating the portion of mixed primary and secondary air escaping to the hood.
  • the maintenance of adequate ventilation is important in prevention of web rewetting by maintaining suitable psychometric conditions.
  • the sound reflectors or baffles 560 reduce the escape of noise upwards into the hood space.
  • the wiping of the moist boundary layer containing dislocated moisture in mistlike or droplet form is facilitated by the provision of mechanical wiping members 610 serving both to assist in removal of moist air, to maintain the sound level within the hood by reflection of incident sound waves back into the space beneath the whistles, and to stabilize the running of the web.
  • the members 610 are adjustably mounted to provide adjustable spacing from the web surface, with the off-coming gap on the downstream side of a sound generator being greater than the on-coming or upstream gap.
  • sawtoothed or levelled surface wipers is contemplated.
  • a reverberating chamber 303 is provided.
  • secondary air is recirculated by fans 341 while heating means 350 impart additional heat to the secondary air.
  • the sound and heat insulated cap structures 310 are provided with sound external hood 311 therebetween to minimize noise loss to the external hood space.
  • Dampers 308 adjustably mounted at the respective cap edges permit control of secondary air recirculation though the fan means 341. Non-resonating incoming hood air or fresh air is admitted by way of inlets 339, while outward passage of moist air to the hood space takes place through the outlets 312.
  • the edge sound losses are minimized by provision of sound reflector plates 323.
  • the staggered opposed whistles 301 are mounted in a reverberating chamber 303 through which flows the incoming secondary air as circulated by the fans 341. Control of psychometric conditions at the web surface by use of controlled secondary recirculation and makeup air and the recirculation by the fans 341 permits optimized drying.
  • the provision of additional stem jet whistles in the reverberating chamber of at least one of the hoods 310 in excess of the usual requirement permits selective additional reverberating energization for wet streak control.
  • FIG. 7 which shows the variation of drying rate with web dampness, having tree characteristic Curves representing three different web speeds, it will be seen that, with the exception of the range 25 percent to 35 percent wetness (wet base), the characteristic drying rate curve has a positive gradient, so that in the majority of the wetness range there is a tendency to eliminate wet streaking.
  • a further and unobvious advantage afforded by the use of sonic drying is that, for a side range of web wetness the effective drying rate increases with the wetness of the web. Thus, for the range so affected, there is inherent tendency to control wet streaks.
  • Web drying apparatus having a passage for an endless web therethrough for controlled diminution of liquid within the surface of an elongated permeable web, having web positioning means to laterally locate a said web relative to the longitudinal edges thereof on passage through said apparatus, a plurality of sound generating whistle means on one side of a path of travel of said web in mutual spaced relation arranged to provide a sound field having a plurality of sequential high intensity zones, spaced along the web path of travel, and to propagate longitudinal sound waves in a direction substantially normal to the web, first gaseous fluid supply means connected to said sound generating means in energizing relation therewith to generate in operation said longitudinal sound waves, second gaseous fluid supply means having outlets intermediately of at least some of said zones to provide a wiping gaseous flow in a direction substantially normal to the plane of the web, plural housing means extending transversely of said web path respectively located adjacent at least some of said high intensity sound zones to provide a plurality of gaseous fluid return flow paths extending away from said web path, to receive said wiping gas
  • Apparatus as set forth in claim 1 including sound hood means to intensify said sound field at the surface of a said web.
  • Apparatus as claimed in claim 2 including air heating means to provide temperature control of gaseous fluid within said apparatus.

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  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Health & Medical Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Molecular Biology (AREA)
  • Drying Of Solid Materials (AREA)
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Abstract

A paper dryer is provided with a sonic drying section through which the web is passed and subjected to high intensity noise from grouped noise generators, usually air operated, to dislocate moisture from the web for enhanced drying rates.

Description

United States Patent [is] 3,694,926
Rodwin 8t 81. 1 0d. 3, 1972 [54] SONIC DRYING OF WEBS 3,346,932 10/1967 Cheape ..34/i55 X Inventors: Montreal Quebec; Eustace Cosmo Shuffler, 3,169,507 2/1965 Rich 16/137 A Lachine, Quebec, both of Canada Dominion Engineering Works, Limited, Lachine, Quebec, Canada Filed: June 17, 1970 Appi. No.: 46,979
Assignee:
Int. Cl ..F26b 19/00 Field of Search ..34/23, 69, 155, 158, 18
References Cited UNITED STATES PATENTS 4/1956 Fowie .34/155 X Primary Examiner-Carroll B. Dority, Jr.
Attorney-Raymond A. Eckersley, Frank L. Neuhauser, Oscar B. Waddeil and Joseph B. F orman [57] ABSTRACT 4Clairm,7DrnwingFigures PAT ENTEB 3 SHEET 2 0F 3 FIG. 2
INVENTOR. STEPHEN A. RODWIN EUSTACE C. SHUFFLER PAIENTEDncI 3 m2 3.694.926
sum 3 or 3 INVENTOR. STEPHEN A. RODWIN EUSTACE C. SHUFFLER BY Z L) SONIC DRYING OF WEBS This invention is directed to apparatus for dislocating moisture from a wet web using sonic generators.
In the pulp and paper industry a large portion of the cost of making paper arises from the need to dewater the pulp stock by the removal of the approximately 98 percent by weight water content of the stock. Conventionally, the removal by mechanical means of moisture from the web terminates at the end of the press section. From there on, further drying is usually achieved by more costly thermal drying, in the drier section. The present invention extends the use of mechanical removal of water throughout the drier section, with conseq uent economic benefit.
The present invention provides an apparatus for obtaining the mechanical dislocation of liquid within a web by the application of sonicly vibrating gaseous fluid thereto either alone or in combination with an impingement gas flow for the removal of the dislocated liquid. While such liquid is usually water, such is not necessarily the case, as other liquids in furnish are also known.
it has been found that the application of longitudinal sound waves to a web such as a felt or a paper web at appropriate levels of sound energy will promote transverse dislocation of liquid relative to the web.
In order to transport moisture from the surface or surface of the web, it is necessary to provide a gaseous or vapor flow against a surface or surfaces of the web. it has been found that by utilizing pressurized fluid medium such as air initially as the energizing source for a sound generator such as a stem jet whistle, and then passing the air from the whistle against the web, that the fluid can serve the dual function of whistle energization and the at least partial wiping and transportation of the released moisture mist away from the surface.
The raising of the temperature of the energizing fluid enhances sound energization. However, in the matter of transporting dislocated moisture from the web partially moist air, such as air issuing from the sound sources, after having picked up web moisture either as finely distributed mist or in vapor form, is effective as a moisture transporting agent, while also enhancing the sound field due to its characteristic of reducing sound attenuation, relative to a dry air sound field. Web moisture may be carried in mist droplet fonn by the air stream, being dispersed by the sound field into micro droplets as opposed to passage only in the vapor form for conventional heat drying processes, thus enhancing the economics of extraction in liquid form.
It has been further found that the effectiveness of the sound generators, such as stem jet whistles may be enhanced by the provision of suitable sound reflectors, thus improving considerably the efficiency of sound utilization.
The present invention may be utilized with stationary webs. However, in order to meet production requirements of rapid dewatering for moving webs such as in a paper machine, the present invention is utilized in relation to a moving web, in which high web passage speeds may be achieved. It will be understood that the effect of increased speed may enhance drying rates due to improved action of the sonic field in the web boundary. Hence this process is particularly suited for high speed machines.
A particular advantage afforded by the present invention relates to the adaptability thereof with existing paper drying machinery whereby the drying rates of the combined plant may be increased, thereby permitting the speed of the paper making machine to be correspondingly increased. In addition, owing to the general tendency of sonic drying to concentrate moisture at the web boundaries the efi'ects of other subsequent surface drying processes are generally enhanced. in addition, the fact, that sonic drying does not result in such a large temperature drop as is normally experienced in conventional evaporative drying due to evaporative cooling, makes the achievement and maintenance of suitable web temperatures more economical.
In utilizing a sonic field having sound generators such as stern jet whistles, it is necessary that the sonic energy input to the paper web shall not exceed the approximate value of 10 watts per square centimeter as chemical decomposition or donolysis may start to occur at this energy level. Thus the use of a maximum of up to 169 decibels (db) may be regarded as quite safe, in providing a maximum of 8 watts/cm, as compared with the 10 watts/cm which 170 decibels represents.
[t has been found that the apparent inefiiciency of a free open sound field is greatly improved when in web drying it is applied as a reflective field. Applied sound energy initially provides mechanical moisture dislocation, and subsequently a considerable portion of the generated sound energy is transformed into heat, hence supplying a staged energy transformation which benefits the overall drying process. Similarly, in providing uncooled compressed air as whistle energizing medium, the mechanical losses of the air compressor appear as a temperature rise in the whistle air to promote effective compressor and web drying efficiency while also enhancing whistle operation, if effectively utilized.
From psychometric charts, it is known that the requirement of energy for moisture removal from a web is diminished if the mean temperature of the air dyring the web is maintained as high as possible owing to favorable changes in it tension and viscosity which result. lr has been found that the action of a sonic field in an air streal also favorably changes boundary surface tension and heat transfer coefficients to enhance drying, while also suitably conditioning the inside of the porous web structure. Thus higher temperature air has been found highly beneficial in promoting heat and mass transfer to improve drying rates.
The effective use of sound generators such as stern jet whistles in drying a moving paper web require the capability of exercising control over the web drying rate, both generally and locally. One characteristic of a sonic field is the advisability to locate the plane of the paper web substantially perpendicular to the sound wave generally at distances representing multiples of half the wave length from the sound source. In general, a change in air flow conditions at the whistle inlet leads to a change in frequency with a consequent change in wave length. For permanently set whistles this would probably reduce resonation, so that resonation air flow ranges have to be established and maintained. For this reason, it is not practical to permit substantial changes to the air flow rates for a particular whistle arrangement, as the deviation of sonic conditions from the design point would not permit consistency in drying. In order to provide control of the rate of moisture removal with other than acoustic means, it is necessary to effect control over the additional moisture removal media, namely by controlling the wiping or impingement air flow within a predetermined range of mass flow, velocity and psychometric conditions.
Wiping or impingement air may be supplied in a variety of ways to afford control of drying rates. When air is used for actuating the sonic generator, it is generally possible and desirable to utilize resonated exhaust process air, with or without secondary air of low moisture content, by passing the air as a wiping fluid across the web surface. Low velocity air wiping may be achieved utilizing pressure build up in the sound field. The control of air escape from the sonic zone by suitable throttle means is then readily provided, to effect the desired control over moisture removal by variation of the wiping air flow rate. Alternative to the foregoing provision or additionally thereto, there may be provided air pressurizing means such as a fan or blower, for the direct supply of secondary air in bypass relation to the whistle. Such by-pass secondary air may be passed through the resonating field produced by the whistles. Local control by adjustment of wiping air flow permits the eradication of wet streaks in the web. Such bypass secondary air may be fresh air or recirculation air, or a mixture of fresh and recirculation air to provide desired psychometric conditions.
The operation of the sound generation means is enhanced by the provision of sound reflector means to direct the sound energy against the web and by reflection to return a considerable portion of energy to the source in re-energizing relation therewith. In addition, at the boundaries of the sonic drying zone, the provision of auxiliary sound reflectors to minimize the passage of sound energy from the zone enhances the sound intensity within the zone while reducing the provision of sound proofing necessary to reduce outside noise to practical working levels. The provision of perforated reflectors adjacent the web entry and exit locations permits the passage of air therepast in web wiping relation, while enhancing the performance of the sound chamber. The sonic energy absorption losses in reflectors is effectively returned to the process in the form of heat energy.
While theoretical considerations of the application of compressed air against a moving web, applied initially as sound energy in energizing a whistle might lead to the conclusion that efficient utilization will produce rather low air temperature, it has been found that the appearance of sonic losses as heat energy, from the effects previously discussed, maintain the air temperature at a preset level, of for instance 200 F. Thus high recovery of sound energy as useful heat enhances the overall process efficiency. While the described embodiments are directed to single and double sided impingement against a planar web, the utilization of the present invention with a dryer cylinder is also contemplated.
In obtaining the full benefits of sonic web drying, removal of moisture displaced to air adjacent the web surface is particularly important, so as to avoid rewetting of the web. One very effective means for boundary moisture removal is the use of impingement air jets, as a form of air wiper.
The particular advantages obtained in utilizing sonic drying against both sides of a web is the improvement in drying rates and the balancing or manipulation of transverse forces acting upon the web. In the case of a symmetrical, balanced arrangement, the use of a support web or wire may on occasion be dispensed with.
In addition to the effectiveness of the foregoing disclosed drying process, it will be understood that particular advantages accrue in combining a short sonic dryer section with an existing conventional dryer, generally locating the sonic section at the inlet or wetter end in order to fully utilize the characteristic higher dislocation rates achieved with the wetter web. The improved overall performance of a so-modified dryer section permits up-rating of the speed of the complete paper machine in cases where the primary limitation to such up-rating has been dryer performance.
The subject process includes the supply of compressed air to the sound generators. The raising of the temperature of the supply air enhances both drying and whistle efficiency. To produce higher temperature supply air, the choice exists between heating of the already hot compressor output air by independent heating means or more effectively utilizing the compressor to produce the required exhaust temperature, by raising compressor inlet temperature slightly above ambient, providing intake air in the range of F to F at the compressor inlet. For most of the considered embodiments, the latter course is more economical in heat energy requirement, while capita cost is minimized.
Certain embodiments of the present invention are described, reference being had to the accompanying drawings wherein:
FIG. 1 shows two perspective sectional arrangements of embodiments of the subject invention showing the use of transverse trough-like sound generators, and individual sound reflectors, respectively;
FIG. 2 is a side sectional view showing a first embodiment having an unsupported web and using only primary or whistle air as the moisture transport medium;
FIG. 3 is a side sectional view showing a further embodiment having a resonant chamber receiving secondary air;
FIG. 4 is a further embodiment similar to that of FIG. 1, with secondary air circulation provision;
FIG. 5 is a view similar to FIG. 3 of a further embodiment;
FIG 6 is a sectional detail of an edge seal suitable for use with the sound chambers illustrated in FIGS. 2 5', and
FIG. 7 shows characteristic drying rate curves, and appears with FIG. 1.
Referring to FIG. I, this illustrates the form of two alternative sound generator arrangements, the first showing trough-shaped reflectors 18 in series arrangement within a sound hood, each trough reflector having a plurality of stem jet whistles herein, while in the second arrangement is shown a plurality of whistles, each with an individual reflector 18' and mounted in staggered relation.
Referring to FIG. 2, this shows a vertical unsupported web run wherein the drier section 10 has a first sonic chamber 12, and an opposing sonic chamber 14, each chamber having a cap or cover 16 comprising reverberation plates. Each chamber 12, 14 is provided with a plurality of sound generators 18 to propagate longitudinal sound waves against the web 20. The chamber may be in horizontal or vertical arrangement, depending generally on the provision of web support netting and the symetry of incident energy, in relation to the grade of paper.
Each sound generator 18 comprises a trough-like reflector having a plurality of spaced whistles, such as a stern jet whistle 26 provided with air from a compressor by supply conduit means 24, and mounted within sound reflecting means 28, 30 to concentrate both the longitudinal sound emission and sound reflection at the surface of the web 20, the distance A" representing very nearly a multiple of the whistle half wave length at desired operating conditions. The individual whistles 26 are spaced laterally in the reflecting means 28, 30 at substantially uniform distances having multiples of half wave length apart to minimize mutual interference. Intervening baffles may be used.
The reverberating cap or cover 16 defining a sonic chest also is located at a selected distance B from the web surface, equal to approximately a multiple of the whistle half wave length. In supplement to the reflecting surfaces 28, 30 and 16 the reflector plates 23 adjacent the web path also serve to retain sound energy within the section 10. The alternative provision of individual whistles having circular individual reflectors of similar diametral section to that of the trough reflectors is also contemplated.
The sound generators 18 including supporting side walls 25 having apertures 32 extending therethrough and connecting with vents 22 in the cover 16 to permit the passage of air from the whistles in fluid wiping relation over the surface of web 20, for exhaust to the hooded zone above the section 10, by way of the apertures 22, shown as having sound relfecting bafl'le means 11 therein to maintain a low sound level in the vicinity of the drier section.
In addition to the provision of trough end walls, the provision of intermediate separating walls between at least some of the adjacent whistles is contemplated.
In the embodiments of FIGS. 3, 4 and 5 the sound reflectors 31, 41 and 51 also are illustrated as extending for the width of the respective drier section 10. The alternative use of individual circular reflectors shown in FIG. 1 shows a mutual staggered arrangement to provide distribution of sound field across the web.
The arrangement of FIG. 4 shows air circulator 45, having an enclosure mounted on the cover 16 of the sonic chest with an air circulating fan 41 mounted therein. The apertures 37, 44 and 39 provide access for wiping air recirculating within the sonic chest of the drier section 10, while the dampers 43 and 47 operating in conjunction with apertures 51 and 53 provide blending elation with hood air from outside the sonic chest for a desired combination of hood air and recirculation air in accordance with desired psychometric conditions. The setting of the dampers 43 and 47 is controlled by the levers 49 and 50.
FIG. 5 shows a horizontal arrangement wherein a support wire mesh 521 carries the web 520 in supported relation between the opposed sound chests 510. Each chest 510 contains one or more troughlike reflectors 518, each reflector containing a plurality of stem whistles 526 in mutually spaced relation. The cross-sectional profile of the rough reflectors 518 differs from the parabolic form of FIGS. 1 and 4. Primary air from the whistles 526, together with secondary air passing downward through apertures 539, serves to scour the boundary layer from ofl the web 520. The secondary air is heated by heaters 550, illustrated as being of the electrical resistance type. Fan means 541 provides circulation of the secondary air, while the adjustable dampers 545 control the inlet access of hood air and the adjustable dampers 547 control the portion of air passing from the fans 541 in recirculating relation over the surface of web 520 by regulating the portion of mixed primary and secondary air escaping to the hood. The maintenance of adequate ventilation is important in prevention of web rewetting by maintaining suitable psychometric conditions. The sound reflectors or baffles 560 reduce the escape of noise upwards into the hood space.
In the embodiment of FIG. 6 the wiping of the moist boundary layer containing dislocated moisture in mistlike or droplet form is facilitated by the provision of mechanical wiping members 610 serving both to assist in removal of moist air, to maintain the sound level within the hood by reflection of incident sound waves back into the space beneath the whistles, and to stabilize the running of the web. The members 610 are adjustably mounted to provide adjustable spacing from the web surface, with the off-coming gap on the downstream side of a sound generator being greater than the on-coming or upstream gap. The use of sawtoothed or levelled surface wipers is contemplated.
In the FIG. 3 embodiment a reverberating chamber 303 is provided. In addition to incoming whistle air from high pressure ducts 302 serving the whistles 301 shown mounted in mutual opposed staggered relation considered in the cross machine direction, secondary air is recirculated by fans 341 while heating means 350 impart additional heat to the secondary air. The sound and heat insulated cap structures 310 are provided with sound external hood 311 therebetween to minimize noise loss to the external hood space. Dampers 308 adjustably mounted at the respective cap edges permit control of secondary air recirculation though the fan means 341. Non-resonating incoming hood air or fresh air is admitted by way of inlets 339, while outward passage of moist air to the hood space takes place through the outlets 312. The edge sound losses are minimized by provision of sound reflector plates 323. The staggered opposed whistles 301 are mounted in a reverberating chamber 303 through which flows the incoming secondary air as circulated by the fans 341. Control of psychometric conditions at the web surface by use of controlled secondary recirculation and makeup air and the recirculation by the fans 341 permits optimized drying. The provision of additional stem jet whistles in the reverberating chamber of at least one of the hoods 310 in excess of the usual requirement permits selective additional reverberating energization for wet streak control.
Referring to FIG. 7, which shows the variation of drying rate with web dampness, having tree characteristic Curves representing three different web speeds, it will be seen that, with the exception of the range 25 percent to 35 percent wetness (wet base), the characteristic drying rate curve has a positive gradient, so that in the majority of the wetness range there is a tendency to eliminate wet streaking.
A further and unobvious advantage afforded by the use of sonic drying is that, for a side range of web wetness the effective drying rate increases with the wetness of the web. Thus, for the range so affected, there is inherent tendency to control wet streaks.
What I claim as new and desire to secure by Patent patent of the United States is:
1. Web drying apparatus having a passage for an endless web therethrough for controlled diminution of liquid within the surface of an elongated permeable web, having web positioning means to laterally locate a said web relative to the longitudinal edges thereof on passage through said apparatus, a plurality of sound generating whistle means on one side of a path of travel of said web in mutual spaced relation arranged to provide a sound field having a plurality of sequential high intensity zones, spaced along the web path of travel, and to propagate longitudinal sound waves in a direction substantially normal to the web, first gaseous fluid supply means connected to said sound generating means in energizing relation therewith to generate in operation said longitudinal sound waves, second gaseous fluid supply means having outlets intermediately of at least some of said zones to provide a wiping gaseous flow in a direction substantially normal to the plane of the web, plural housing means extending transversely of said web path respectively located adjacent at least some of said high intensity sound zones to provide a plurality of gaseous fluid return flow paths extending away from said web path, to receive said wiping gaseous flow having liquid and vapor entrained therewith, and recirculation means to recirculate a selected portion of return gaseous flow to the web, to provide control of web drying conditions.
2. Apparatus as set forth in claim 1 including sound hood means to intensify said sound field at the surface of a said web.
3. Apparatus as claimed in claim 2 wherein said recirculation means includes fan means for returning said selected portion in downflowing bypass relation with said whistle means; and controllable air admission means to admit additional air for mixing with said recirculation air, in controlling the psychrometric condition of said wiping fluid.
4. Apparatus as claimed in claim 2 including air heating means to provide temperature control of gaseous fluid within said apparatus.

Claims (4)

1. Web drying apparatus having a passage for an endless web therethrough for controlled diminution of liquid within the surface of an elongated permeable web, having web positioning means to laterally locate a said web relative to the longitudinal edges thereof on passage through said apparatus, a plurality of sound generating whistle means on one side of a path of travel of said web in mutual spaced relation arranged to provide a sound field having a plurality of sequential high intensity zones, spaced along the web path of travel, and to propagate longitudinal sound waves in a direction substantially normal to the web, first gaseous fluid supply means connected to said sound generating means in energizing relation therewith to generate in operation said longitudinal sound waves, second gaseous fluid supply means having outlets intermediately of at least some of said zones to provide a wiping gaseous flow in a direction substantially normal to the plane of the web, plural housing means extending transversely of said web path respectively located adjacent at least some of said high intensity sound zones to provide a plurality of gaseous fluid return flow paths extending away from said web path, to receive said wiping gaseous flow having liquid and vapor entrained therewith, and recirculation means to recirculate a selected portion of return gaseous flow to the web, to provide control of web drying conditions.
2. Apparatus as set forth in claim 1 including sound hood means to intensify said sound field at the surface of a said web.
3. Apparatus as claimed in claim 2 wherein said recirculation means includes fan means for returning said selected portion in downflowing bypass relation with said whistle means; and controllable air admission means to admit additional air for mixing with said recirculation air, in controlling the psychrometric condition of said wiping fluid.
4. Apparatus as claimed in claim 2 including air heating means to provide temperature control of gaseous fluid within said apparatus.
US46979A 1969-07-07 1970-06-17 Sonic drying of webs Expired - Lifetime US3694926A (en)

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US3965581A (en) * 1972-06-16 1976-06-29 Candor James T Liquid removing method and apparatus
WO2000001883A1 (en) * 1998-07-01 2000-01-13 The Procter & Gamble Company Process for removing water from fibrous web using oscillatory flow-reversing impingement gas
US6085437A (en) * 1998-07-01 2000-07-11 The Procter & Gamble Company Water-removing apparatus for papermaking process
US6308436B1 (en) 1998-07-01 2001-10-30 The Procter & Gamble Company Process for removing water from fibrous web using oscillatory flow-reversing air or gas
DE10022110A1 (en) * 2000-05-08 2001-11-22 Dieter Ronnenberg A characteristic profile of a paper/cardboard web or a pulp suspension is set by a sectional and aligned acoustic field during production/finishing or at a coating station or glue press
WO2002033337A1 (en) * 2000-10-17 2002-04-25 Starlinger & Co. Gesellschaft M.B.H. Device and method for the drying of plastic webs
US6662812B1 (en) * 1999-07-24 2003-12-16 Allen David Hertz Method for acoustic and vibrational energy for assisted drying of solder stencils and electronic modules
US20090000142A1 (en) * 2006-01-12 2009-01-01 Dyson Technology Limited Drying Apparatus
AU2005270587B2 (en) * 2004-08-13 2009-11-19 Sanovo Biosecurity A/S Method and device for enhancing a process involving a solid object and a gas
US20100199510A1 (en) * 2009-02-09 2010-08-12 Zinovy Plavnik Ultrasonic drying system and method
WO2014048431A3 (en) * 2012-09-28 2014-05-30 Papierfabrik August Koehler Se Dryer section and method for drying a web of fibrous material, and machine having such a dryer section
US20140150284A1 (en) * 2012-12-04 2014-06-05 Andrew Ciaschi Acoustic drying system with interspersed exhaust channels
WO2014088805A1 (en) * 2012-12-04 2014-06-12 Eastman Kodak Company Acoustic drying system with matched exhaust flow
US8943706B2 (en) 2013-01-18 2015-02-03 Eastman Kodak Company Acoustic wave drying method
US9140494B2 (en) 2013-01-18 2015-09-22 Eastman Kodak Company Acoustic wave drying system
US9163875B2 (en) 2013-01-18 2015-10-20 Eastman Kodak Company Acoustic drying system with sound outlet channel
US20160003541A1 (en) * 2014-07-01 2016-01-07 Heat Technologies, Inc. Indirect acoustic drying system and method
WO2016182832A1 (en) * 2015-05-08 2016-11-17 Ut-Battelle, Llc Dryer using high frequency vibration
US9671166B2 (en) 2014-07-24 2017-06-06 Heat Technologies, Inc. Acoustic-assisted heat and mass transfer device
RU2705504C2 (en) * 2018-05-04 2019-11-07 Анатолий Кузьмич Соломаха HOUSEHOLD PURPOSE PAPER DRYING DEVICE WITH WEIGHT FROM 10 TO 40 g/m2, AS WELL AS NEWSPRINT WEIGHT 51 g/m2, ON A PAPER MAKING MACHINE AT A SPEED OF 2,000 m/min AND HIGHER BY A CONTACTLESS METHOD USING INFRARED ENERGY

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US3169507A (en) * 1961-06-14 1965-02-16 Northern Ind Inc Elastic wave generator
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US3965581A (en) * 1972-06-16 1976-06-29 Candor James T Liquid removing method and apparatus
US6393719B1 (en) 1998-07-01 2002-05-28 The Procter & Gamble Company Process and apparatus for removing water from fibrous web using oscillatory flow-reversing air or gas
US6085437A (en) * 1998-07-01 2000-07-11 The Procter & Gamble Company Water-removing apparatus for papermaking process
US6308436B1 (en) 1998-07-01 2001-10-30 The Procter & Gamble Company Process for removing water from fibrous web using oscillatory flow-reversing air or gas
WO2000001883A1 (en) * 1998-07-01 2000-01-13 The Procter & Gamble Company Process for removing water from fibrous web using oscillatory flow-reversing impingement gas
JP2002519539A (en) * 1998-07-01 2002-07-02 ザ、プロクター、エンド、ギャンブル、カンパニー A method for removing water from a fibrous web using an oscillating and reversing impinging gas
US6662812B1 (en) * 1999-07-24 2003-12-16 Allen David Hertz Method for acoustic and vibrational energy for assisted drying of solder stencils and electronic modules
DE10022110A1 (en) * 2000-05-08 2001-11-22 Dieter Ronnenberg A characteristic profile of a paper/cardboard web or a pulp suspension is set by a sectional and aligned acoustic field during production/finishing or at a coating station or glue press
US20030188842A1 (en) * 2000-05-08 2003-10-09 Dieter Ronnenberg Influencing the profile of the properties of a web by means of an acoustic field
US20060157213A1 (en) * 2000-05-08 2006-07-20 Dieter Ronnenberg Influencing the profile of the properties of a web by means of at least one acoustic field
DE10022110B4 (en) * 2000-05-08 2007-10-25 Dieter Ronnenberg Influencing a web property profile by means of at least one sound field
WO2002033337A1 (en) * 2000-10-17 2002-04-25 Starlinger & Co. Gesellschaft M.B.H. Device and method for the drying of plastic webs
AU2005270587B2 (en) * 2004-08-13 2009-11-19 Sanovo Biosecurity A/S Method and device for enhancing a process involving a solid object and a gas
US20090000142A1 (en) * 2006-01-12 2009-01-01 Dyson Technology Limited Drying Apparatus
US20100199510A1 (en) * 2009-02-09 2010-08-12 Zinovy Plavnik Ultrasonic drying system and method
US11353263B2 (en) 2009-02-09 2022-06-07 Heat Technologies, Inc. Ultrasonic drying system and method
EP2394121A4 (en) * 2009-02-09 2016-11-23 Heat Technologies Inc Ultrasonic drying system and method
US9068775B2 (en) * 2009-02-09 2015-06-30 Heat Technologies, Inc. Ultrasonic drying system and method
US10006704B2 (en) 2009-02-09 2018-06-26 Heat Technologies, Inc. Ultrasonic drying system and method
US10775104B2 (en) 2009-02-09 2020-09-15 Heat Technologies, Inc. Ultrasonic drying system and method
US9851146B2 (en) 2012-09-28 2017-12-26 Papierfabrik August Koehler Se Dryer section and method for drying a web of fibrous material, and machine having such a dryer section
CN104797755B (en) * 2012-09-28 2018-02-02 奥古斯特科勒纸厂欧洲公司 Drying portion and the drying method of width material and the machine with drying portion made of fibrous material
WO2014048431A3 (en) * 2012-09-28 2014-05-30 Papierfabrik August Koehler Se Dryer section and method for drying a web of fibrous material, and machine having such a dryer section
RU2639108C2 (en) * 2012-09-28 2017-12-19 Папирфабрик Аугуст Кёлер Се Drying section, way of drying web from fibre material and machine with drying section
CN104797755A (en) * 2012-09-28 2015-07-22 奥古斯特科勒纸厂欧洲公司 Dryer section and method for drying a web of fibrous material, and machine having such a dryer section
US8931891B2 (en) 2012-12-04 2015-01-13 Eastman Kodak Company Acoustic drying system with matched exhaust flow
US9127884B2 (en) * 2012-12-04 2015-09-08 Eastman Kodak Company Acoustic drying system with interspersed exhaust channels
CN104812585A (en) * 2012-12-04 2015-07-29 伊斯曼柯达公司 Acoustic drying system with matched exhaust flow
US8770738B2 (en) 2012-12-04 2014-07-08 Eastman Kodak Company Acoustic drying system with matched exhaust flow
WO2014088805A1 (en) * 2012-12-04 2014-06-12 Eastman Kodak Company Acoustic drying system with matched exhaust flow
US20140150284A1 (en) * 2012-12-04 2014-06-05 Andrew Ciaschi Acoustic drying system with interspersed exhaust channels
US8943706B2 (en) 2013-01-18 2015-02-03 Eastman Kodak Company Acoustic wave drying method
US9163875B2 (en) 2013-01-18 2015-10-20 Eastman Kodak Company Acoustic drying system with sound outlet channel
US9140494B2 (en) 2013-01-18 2015-09-22 Eastman Kodak Company Acoustic wave drying system
US20160003541A1 (en) * 2014-07-01 2016-01-07 Heat Technologies, Inc. Indirect acoustic drying system and method
US10488108B2 (en) 2014-07-01 2019-11-26 Heat Technologies, Inc. Indirect acoustic drying system and method
US9671166B2 (en) 2014-07-24 2017-06-06 Heat Technologies, Inc. Acoustic-assisted heat and mass transfer device
US10139162B2 (en) 2014-07-24 2018-11-27 Heat Technologies, Inc. Acoustic-assisted heat and mass transfer device
WO2016182832A1 (en) * 2015-05-08 2016-11-17 Ut-Battelle, Llc Dryer using high frequency vibration
US10520252B2 (en) 2015-05-08 2019-12-31 Ut-Battelle, Llc Dryer using high frequency vibration
RU2705504C2 (en) * 2018-05-04 2019-11-07 Анатолий Кузьмич Соломаха HOUSEHOLD PURPOSE PAPER DRYING DEVICE WITH WEIGHT FROM 10 TO 40 g/m2, AS WELL AS NEWSPRINT WEIGHT 51 g/m2, ON A PAPER MAKING MACHINE AT A SPEED OF 2,000 m/min AND HIGHER BY A CONTACTLESS METHOD USING INFRARED ENERGY

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FR2054305A5 (en) 1971-04-16
DE2033427A1 (en) 1971-01-14
GB1311363A (en) 1973-03-28
SE382108B (en) 1976-01-12

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