CA2008155C - Method and apparatus for reducing a transporting strain on elongated material passing through a treatment chamber - Google Patents
Method and apparatus for reducing a transporting strain on elongated material passing through a treatment chamberInfo
- Publication number
- CA2008155C CA2008155C CA002008155A CA2008155A CA2008155C CA 2008155 C CA2008155 C CA 2008155C CA 002008155 A CA002008155 A CA 002008155A CA 2008155 A CA2008155 A CA 2008155A CA 2008155 C CA2008155 C CA 2008155C
- Authority
- CA
- Canada
- Prior art keywords
- guide
- elongated material
- fluid
- elongated
- nozzle
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
- 239000000463 material Substances 0.000 title claims abstract description 196
- 238000011282 treatment Methods 0.000 title claims abstract description 67
- 238000000034 method Methods 0.000 title claims abstract description 21
- 239000012530 fluid Substances 0.000 claims abstract description 112
- 230000008859 change Effects 0.000 claims description 35
- 238000011144 upstream manufacturing Methods 0.000 claims description 12
- 238000007664 blowing Methods 0.000 claims description 6
- 238000012545 processing Methods 0.000 claims description 6
- 239000007788 liquid Substances 0.000 claims description 3
- 239000002184 metal Substances 0.000 claims description 3
- 230000004044 response Effects 0.000 claims description 3
- 229920002994 synthetic fiber Polymers 0.000 claims description 2
- 230000009969 flowable effect Effects 0.000 claims 2
- 239000011248 coating agent Substances 0.000 claims 1
- 238000000576 coating method Methods 0.000 claims 1
- 230000032258 transport Effects 0.000 description 78
- 239000004020 conductor Substances 0.000 description 5
- 241000592503 Speea Species 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- 239000004744 fabric Substances 0.000 description 3
- 230000006978 adaptation Effects 0.000 description 2
- 230000009467 reduction Effects 0.000 description 2
- AYFVYJQAPQTCCC-GBXIJSLDSA-N L-threonine Chemical compound C[C@@H](O)[C@H](N)C(O)=O AYFVYJQAPQTCCC-GBXIJSLDSA-N 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000004753 textile Substances 0.000 description 1
- 210000005239 tubule Anatomy 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B65—CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
- B65H—HANDLING THIN OR FILAMENTARY MATERIAL, e.g. SHEETS, WEBS, CABLES
- B65H23/00—Registering, tensioning, smoothing or guiding webs
- B65H23/04—Registering, tensioning, smoothing or guiding webs longitudinally
- B65H23/24—Registering, tensioning, smoothing or guiding webs longitudinally by fluid action, e.g. to retard the running web
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B65—CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
- B65H—HANDLING THIN OR FILAMENTARY MATERIAL, e.g. SHEETS, WEBS, CABLES
- B65H2406/00—Means using fluid
- B65H2406/10—Means using fluid made only for exhausting gaseous medium
- B65H2406/11—Means using fluid made only for exhausting gaseous medium producing fluidised bed
- B65H2406/111—Means using fluid made only for exhausting gaseous medium producing fluidised bed for handling material along a curved path, e.g. fluidised turning bar
Landscapes
- Treatment Of Fiber Materials (AREA)
- Advancing Webs (AREA)
- Registering, Tensioning, Guiding Webs, And Rollers Therefor (AREA)
- Drying Of Solid Materials (AREA)
- Supplying Of Containers To The Packaging Station (AREA)
- Package Closures (AREA)
- Transition And Organic Metals Composition Catalysts For Addition Polymerization (AREA)
- Manufacturing And Processing Devices For Dough (AREA)
Abstract
ABSTRACT OF THE DISCLOSURE
The method and apparatus are for reducing a trans-porting strain on elongated material passing through a treatment chamber. The transport is accomplished by a flowing transport fluid which is applied to the elongated material through at least one, preferably several jet nozzles in the direction reversing stations. The fluid is applied in a direction substantially corresponding to the transport direction and passes around a guide surface where it forms a travelling cushion between the guide surface and the elongated material. The flow speed of the fluid corresponds at least to the transport speed or the inlet speed into the chamber. Each direction changing station includes a guide body having a surface around which the elongated material is guided from an inlet side of the guide body to its outlet side. Each station includes the above mentioned nozzles through which the transport fluid is flowing under pressure to form the required jet speeds between the guide surface and a surface of the elongated material.
The method and apparatus are for reducing a trans-porting strain on elongated material passing through a treatment chamber. The transport is accomplished by a flowing transport fluid which is applied to the elongated material through at least one, preferably several jet nozzles in the direction reversing stations. The fluid is applied in a direction substantially corresponding to the transport direction and passes around a guide surface where it forms a travelling cushion between the guide surface and the elongated material. The flow speed of the fluid corresponds at least to the transport speed or the inlet speed into the chamber. Each direction changing station includes a guide body having a surface around which the elongated material is guided from an inlet side of the guide body to its outlet side. Each station includes the above mentioned nozzles through which the transport fluid is flowing under pressure to form the required jet speeds between the guide surface and a surface of the elongated material.
Description
2~81~a l FIELD OF THE INVENTION
The invention relates to a method and apparatus for reducing a transporting strain on elongated material passing through a treat-ment chamber.
BACKG~OUND INFORMATION
,, , Elongated material in the present context may include ribbons, tapes, band-~haped material, for example, made of textiles, '-:. synthetic materials, or paper. The term also includes threads, '~'ya''rns, ro'pe's,''strings~,''an'd the~ e. Such ~aterlals frequently require a treatment in a treatment chamber. For this purpose, :~ the elongated materials must be transported through the treatment ~ chamber pa~sing through an inlet lnto the chamber and through .' an outlet out of the chamber. Inside the chamber or treatment '. zone the surface of the elongated material pas~es along the sur-face of at least one guide body whlch changes the travel direc-tion of the elongated material through the treatment zone or ~ chamber. The material to be treated usually travel~ through ;.~;; the treatment zone along a meandering path, for example, for the .. purpose of drylng or dyelng or lmpregnating or the like. The ~ 20 conventional dlrection changing guide body 18 usually a rotatably . . .
.' mounted roller which 1~ either positively driven or it rotates as a result of the contact of its surface with the material being treated.
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~; In order to transport the material through the treatment chamber or zone, it was nece~sary heretofore, to provide a posltive drive.
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2 ~ 3 -~ 2 l Such positive drive may involve the driving of the guide rollers and/or a further drive which pu119 the elongated material through the treatment chamber or zone. In all conventional transport drives of this type it is unavoidable that the elongated material is subjected to a substantial transporting strain caused by a longitudinally effected stress applied by the pulling force of a take-up reel or the like. The direction reversing guide rollers inside the treatment chamber are mounted in a fixed position, except one such roller is mounted in a floating manner to provide for some yielding, whereby the elongated material is protected to some extent against too large tension stress.
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Thus, when the take-up roller rotates too fast, the floating roller travels out of lts orlglnal position into a posltion in which the total length of elongated material within the treat-ment zone or chamber i8 reduced. This movement direction of . ~
~i the floating roller is maintained, for example, until a pre-,A
determined threshold tensile stress is reached ln response to `~ which, for example, an end switch or sen60r swltch provides a signal for the control of the feed advance. Such a signal .~ 20 may slow down the take-up speed or may increase the feed-in :. . . speed. As a result, the floatlng roller again moves ln the opposite dlrection untll a re~pective thre~hold value is sensed.
The feed advance 18 thus controlled to provlde for a back and forth shuttling of the floating guide roller between presettable limit values for the tensile stress applied to the material.
, In spite of such a floating guide roller it is unavoidable, that the type of material hereinvolved may be exposed to rela-~i tively large tension stress during its transport through a .~ .
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This problem has not been solvea heretofore.
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i OBJECTS OF TIIE INVENTION
~, In view of the foregoing it is the aim of the invention to achieve the following objects 6ingly or in combination:
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to reduce the above de~crlbed ten~ion ~tress to which materials of the mentioned type are expo~ed in their treatment ; while still transporting the material uniformly and at the desired speed through the treatment ~one or chambert ~ to transport the material by means of a blowing medium ;:.
which substantially reduces the appli~ation of tension stres6, pos6ibly to the extent that at the take-up end of the elongated J~ material a pulling mechani6m can be avoided:
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- to support the elongated medium on a transporting -- cushion of flowing fluid; and to provided a transport for the elongated material with a minimum of stress independently of the fact that the treatment may somewhat lengthen the material or that the treatment may shorten the material, e.g. by , stretching or shrinking.
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~ SUM~ARY OF THE INVENTION
:' 10 According to the present invention, there is provided a method for reducing a transporting strain on elongated flat material passing through a treatment chamber, ~ comprising the following steps:
J$ 1 5 ~ a) transporting said elongated material with a transporting speed through said treatment chamber having . an inlet and an outlet for said elongated material, whereby a transport direction is from said inlet to said outlet, (b) guiding said elongated material at least around one travel direction changing guide means defining a zone . where a direction change begins between said inlet and said outlet, (c) forming a space of substantially triangular cross-section bounded by a straight portion of said guide means upstream, as viewed in said transport direction, of said direction change zone, by a nozzle wall, and by said elongated flat material, whereby said straight portion merges, away from said nozzle wall, into a curved portion of said guide means where said direction change zone begins, I
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~s 4a 2~081 ', (d) introducing at least one flowing fluid jet through said nozzle wall into said space of substantially -triangular cross-section at least approximately in said transport direction and substantially in parallel to said straight guide means portion upstream of said direction change zone of said travel direction changing guide means as viewed in said travel direction, whereby a force component extending radially to said travel direction around said guide means is substantially reduced to thereby reduce said strain, and (e) imparting to said flowing fluid jet a flow speed corresponding at least to said transporting speed for transporting said elongated material through said chamber.
The flowing medium generates a cushion at each location where the travel direction of the elongated material is changed. The cushion is produced between the surface of a direction changing or direction reversing guide body and the surface of the material facing the guide body surface. Thus, the elongated material can float on such a cushion and is transported by the flowing cushion substantially free of friction. This type of transport completely avoids the need for direction changing guide rollers regardless whether they are of the driven or undriven type. The direction reversing guide body may be stationary and rigid but it must have a smooth surface of the suitable curvature to .~ ~
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1 achieve the direction change or reversal, whereby the radius of curvature can be selected in a very wide range. Provided s the direction reversal is performed several times in the treat-ment zone or chamber, it i8 now also possible to avoid the above mentioned floating roller.
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The above mentioned floating of the elongated material on the cushion of flowing fluid which simultaneously transports the elongated material, can be enhanced by additionally intxoducing flowing fluid between the elongated material and an exit guide plane, for example, in the form of a baffle plate, whereby again the flowing fluid must have a suitable flowing speed. Due to the low friction between the material and the flowing fluid it i6 possible to even shrink the elongated material in the ;~ treatment chamber or zone without generating any tension stresg in the elongated material ln the transport dlrection. Thus, even where a shrinking takes place as part of the treatment of the elongated materlal, a take-up roller downstream of the f treatment zone or chamber is no longer necessary since the flowing ~ fluid performs the transport regardless whether the elongated .,! 20 material is shrinking or even expanding. It 18 also no longer necessary to correlate the lnput speed to the output speed.
Nevertheless, the transport is uniform and tenslon stress 18 avoided because the infeed and wlthdrawal of materlal no longer depends on friction contact wlthln the treatment zone. ~8 much material as necessary can be fed into the treatment zone or chamber and a~ much material can be taken out as is necesgary.
If the feed-in speed should be reduced at the inlet end of the i~ chamber, such reduction does not have any noticeable effect on A
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1 the quality of the elongated material because it does not affect ~,~ any tension stress within the material travelling through the treatment zone or chamber.
By varying the density of the flowing fluid with due regard to the density of the medium forming the environment in the treatment chamber, it i8 posslble to influence the treatment.
The flowlng transport fluid and the treatment medium may both be gaseous or both may be liquid or one may be gaseous and the other liquid. The flowing fluid may contain additives for the treatment of the elongated material. The flowing fluid could be heated or it could be cooled, whereby again the desired influence on the elongated material may be achieved.
,., Frequently, it is suitable that the flowing 1uid~ and the treat-ment or environmental medium in the treatment zone, have substan-, .
tially the same composition, whereby intermixing i~ of little ; concern and any need for any separation of components subsequent , to the treatment is avoided.
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~ Depending on the type of transport intended, it is po~ible ; according to the invention to apply dlfferent flowing speed~
`~` to the flowing tran~port fluld at the lndlvldual dlrection ,~ changing guide bodies. For example, the flowing speed may increase `; from guide body to guide body. Different flowing fluids may be used at different guide bodies and the density of the flowing ,~ Eluid may be different at different gulde bodies. These features make it possible to take into account the characterietics of ,~:
~,~ the elongated material a~ they may change along the pass of .,.~. .
~ the material through the treatment chamber or zone. For example, ..
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7 2 ~ 5 1 if the elongated material should lenqthen as a re~ult of the treatment, it is necessary to increase the transport speed from the inlet of the treatment chamber toward the outlet of the treatment chamber to properly transport the increasing length of the elongated material. Similarly, lf the material should shrink as a result of the treatment, it is possible `' to reduce the transport speed from the inlet to the outlet.
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In all instances it i8 advantageous to avoid directlng the flowing transport fluid in a direction radially to the length of the materlal to thereby avoid any distortions in the material.
In the light of the foregoing it will be appreciated that the , flow speed of the flowing transport fluid can influence the ~ transport speed of the elongated material. However, the trans-,, port speed also depends on the surface characteristics of the :i material and on the den~ity of the flowing transport fluld.
Normally, the transport speed of the elongated material will be smaller than the flow speed of the flowing transport flula~
and the transport speed can be controlled without any problems.
Another advantage of the lnvention is seen ln that in addltion ~''$!' 20 to the transportlng by means of the flcwlng fluld,a conventlonal tran~port may be comblned by means of a take-up roller outside the treatment zone. Due to the reduced frictlon assured by the cushionlng formed by the flowlng transport fluld, the stress on the elongated material will be very small because the pullinq forces generated by a take-up roller can be very .~ small.
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1 Depending on the characteristic~ of the elongated material it may be advantageousto apply the flowlng transport fluid over the entire width of the material. However, a denser elongated material, such as paper web~, can be transported when the flowing transport fluid i9 applied only to certain zones or even only along a center strip or only along the outer eages. ~urther, it may be aavantageous to distribute the flow speea over the width of the elongated material 80 that, for example, a larger flowing speed is applied along the edgefi while a smaller flowing speed 10 iS effective along the center of the elongated material or vice versa. By applyingan increasea flowing speea along the edges it ~ is, for example, possible to reduce an escape of flowing tran~-i port fluid away from the central zone of the elongated material, whereby unaesirable force components that may be exerted by the flowing transport fluid on the elongated material, are either prevented or minimized. On the other hand, for certain materials it may be desirable to have a higher flowing speed for the flowlng transport fluid along a central zone than the transport fluid speed along the edges. Such a speed distribu-tion of the flowing transport fluid may be aesirable, for example, for double ribbons having a central transport zone of a different composition than the edges 80 that the transporting iB aacomplished primarily by applying the flowing transport fluld to the central strip while the lateral eages of the elongated material are .~ merely æupported by the slower speed of the flowing transport ~ fluid, thereby preventing a slowihg down of the lateral edges '~ of the elongated material relative to the central zone. The ~` flowing transport fluid may be applied in the form of a plurality of individual jets having, for example, circular cro~s-sections ~ .
2~81~
. g or any other suitable cross sections. Instead of a plurality of individual jets, a broad flat jet may be employed which has a width corresponding to the entire width of the elongated material or which has several zones distributed across the width of the elongated material. Thus, it is possible to support the elongated material along its entire width or along certain zones.
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According to the present invention, there is provided an apparatus for reducing a transporting strain on elongated flat material passing through a treatment operation in a travel direction, comprising a treatment chamber for treating said elongated material, said chamber having an inlet and an outlet defining a transport direction from said inlet to said outlet, means for transporting said elongated material from said inlet to said outlet, said transporting means including at least one material guide means having a curved material guide surface for changing the travel direction of said elongated material between said inlet and said outlet, whereby said material guide means define a direction change zone where a direction change begins, æaid material guide means further having a straight portion merging into said curved material guide surface, and fluid flow means including a nozzle wall upstream of said straight portion, as viewed in said travel direction, said nozzle wall, said straight portion and said flat material bounding a space of substantially triangular cross-section tapering toward a point where said guide means begin changing said travel direction in said direction change zone for introducing substantially in said travel direction at least one flowing fluid jet ~,, ... . ~, .. ,,. :
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`<s 2~81 ~
9a into said space of substantially triangular cross-section between said straight portion of said material guide means and said elongated flat material, whereby a force component extending radially of said curved material guide surface is substantially reduced for reducing said strain, said fluid flow means imparting to said flowing fluid a flow speed corresponding at least to a transporting speed of said elongated material.
The elongated material travels around the guide body for the direction reversal. Each guide body is equipped with at least one jet means for introducing a flowing i transport fluid into a space between a surface of the guide body and the elongated material. The flowing ; 15 transport fluid is introduced substantially in the travel direction. The jet means impart to the flowing transport fluid a flow speed which corresponds at least to the transporting speed of the elongated material. The flowing transport fluid may, for example, be compressed air. The compressed air forms a moving support cushion for the elongated material, thereby keeping the elongated material substantially in a floating condition so that ~3 the latter may travel substantially free of friction ~ around the guide body while the flowing fluid transports ; 25 the elongated material. Thus, a substantial pulling force does not have to be applied to the elongated material, nor is it necessary that the elongated material x entrains any guide rollers for rotating the guide , rollers. By substantially reducing the friction and hence the pulling forces on the elongated material, it is possible to transport the elongated :
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1 material through its treatment zone or chamber substantially without any distorting influences.
The jet means for introducing the flowing transport fluld compri~e advantageously at least one nozzle which is arranged at a spacing from the point where the change in the transport direction begins to take place, whereby such spacing extends substantially in - the transport direction upstream of said point. The nozzle is 80 directed that the flowing transport fluid i8 aimed tangentiallytoward said point. The nozzle may, for example, be of the type capable of producing a so-called flat section jet. Such jet has a flat ribbon-type cross-section. However, other nozzle types may be :~
used, for example, groups of nozzles may be arranged in a row across the entire width of the elongated material to be transported.
One or 6everal nozzle groups may be arranged in this manner.
Preferably, each group is arranged along a straight line across the width of the material. All nozzles in a row may produce .,~ .
fluid jets all having the same cross-section or a different cross-section, thereby generating transport jets having the same cross-sectional flow area or different cross-sectional flow areas. In ~ 20 the embodiment where several nozzles produce several different jets, these jets may be produced by transport flulds under dif-. . .
ferent pressures or by transport fluids having dlfferent densities ~i~ or other different characteristlcs. Nowever, depending on the ~;, type of material being transported and treated, it is quite pos-~; sible to supply the ~ame transport fluid by a common source under pressure to all nozzles. Where a common source of fluid under pressure is used, the nozzles may be arranged in a ~ide wall ; of a tubular member having a rectangular or square cross-section, ....
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1 whereby the nozzles are simply bores located in said side wall close to a neighboring or adjacent wall forming part of the guide body for changing the travel direction.
By using different types of nozzles and nozzle shapes and by different nozzle arrangements it is possible according to the invention to vary the influence of the flowing transport fluid on the elongated material. The variation is accomplished by properly selecting a desired nozzle configuration or nozzle shape - and the respective fluid flow is then effective on the elongated material during its transport through the treatment zone or chamber.
Thus, it is, for example, possible to tran6port a 6en8itive thin elongated material, such a6 a fabric that is homogeneous in its ~ cros~-sectional structure, by a flat transport ~et without any ^~ problems, and without sub~tantially any distorting influences of the flat jet stream on the seh~itive thin fabrlc. A quite similar result is achieved by arranglng a plurality of nozzles in the form of a row of bores, whereby the flat jet ~tream is replaced by a plurality of small diameter individual ~et streams.
^~ The plurality of nozzles can simply be provided by the above mentioned bore~ arranged in a side wall of a rectangular cross-~ section or square cros~-~ection plpe resulting in a very 8imple '~''t'.'~' structure.
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`~ By applying the pressurlzed transport fluid in a controlled manner to individual nozzles or to group~ of such nozzle~, it is also possible to influence the effect of the flowing tran~port fluid ;~ on the elongated material. In this context it is po~sible to ;, vary individually or in combination the fluid pressure, the fluid .:
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1 den~ity, the fluid composition, and/or the fluid temperature.
Thus, the influence on the transporting can be modlfied in a multitude of ways to assure that the elongated material is sub-stantially free of di~tortions while simultaneously using the transporting fluid as a treatment medium, for example, for im-pregnating or drying the elongated material. The present trans-port and it~ multitude of control possibilities is equally appli-cable to elongated material not having a homogeneous cross-sec-tional structure. For example, fabric ribbons may be aenser along their edges and less den~e in a central area between the edges. Similarly, the density may change along the length of ~uch fabric ribbons. The present transport fluid can be con-trolled to take into account these characterl~tics of elongated material. For example, a rlbbon with denser or thicker marginal zones will require a higher flowing speed along these denser or thicker zones a~ compared to the flowing speea of the trans-port fluid contacting a central zone of the ribbon. Thus, the proper adjustment of the several flowing speeds wlth due regard to the ribbon characteristics will assure that the marginal zones will not be di~placed relative to a central zone 80 that again ~, the transport take~ place substantially without any distortion of the ribbon being transported.
The guide body for changing or reversing the travel direction of the elongated material is, for example, made o sheet metal : which provides a simple and relatively inexpensive way of produc-ing these guide boaies. The wall portion of the guide body where ; a direction change or reversal begins, must have a 6uitable spacing ''! from the outlet openings of the nozzle or nozzle~. Thus, the i~.; ~, ' .
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2 ~ ~ 8 1 ~ 3 guide wall extends perpendicularly or at a3~all angle to a nozzle wall of the guide body. The nozzle wall portlon reaches beyvnd the guide wall portion so that the nozzles face in a direction approxi-mately in parallel to the guide wall portion. Thu33, the flowing transport fluid travels toward the point of direction change substantially in a tangential direction. The arrangement is such, that the guide-wall portion and the flowing fluid facing surface of the elongated material form a wedge 6hape which in itself also forms a type of nozzle into which the tran3sport fluid is blown since the wedge shape nanxws toward the point of the directionchange.
For example, when elastic elongated materials for forming bandages are to be transported, lt is deslrable to direct the transport flow substantially in parallel to the guide wall portion of the guide body at least at the point where a change in the travel direction begins. This may be accomplished by changing the angle between the guide wall portion and the nozzle portion of the guide body from 90 to an angle smaller than 90 to provide for , ., ~ a more rapid reductlon in the cross-sectional flow area in the ;~ nozzle channel formed by the wedge-shape, 80 that the channel narrows quickly toward the point of dlrection change. In this manner, the direction of the transport fluid and the direction :.,.
o~ travel may sub~tantially correspond to each other. The radius of curvature for a guide body wall portion intended for transporting ~ such flexible bandage material, may have a radius of curvature '~j of about 10 mm. As a result, the entire apparatus can be rather ; compact, even though the guide body is requlred to provide a complete direction reversal of 180. In such an lnstance the guide ~urface portion will have a semi-circular cross-section.
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1 ~ccording to the invention the nozzle or nozzles at each guide body can be controlIed in accordance with the conditions pre-vailing at the particular guide body. Thus, it i9, for example, possible to provide a sensitive adaptation of the transport speed to any shrinking or ~tretching of the elongated material at the - particular gulde body within the treatment zone. For this pur-'' pose, a speed sensor may be arranged just up~tream of the respec-" tive guide body, as viewed in the transport direction, the respec--,. tive signal from the speed ~en~or ig then used by a central proce~sing unit for controlling the flow speed of the transport , fluid. On the other hand, all nozzles can be centrally controlled ", in uni~ff,~ rathër tha~'lndivid~ally.
,'~ BRIEF DESCRIPTION OF THE DRAWINGS
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In order that the invention may be, clearly under~tood, it will now be described, by way of example, with reference to the ac-companying drawings, wherein:
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~ Fig. 1 is a schematic sectional view through a treatment ,',, chamber equipped with a plurality of guide bodies, ,,' each of which i~ provided wlth lt~ transport :.
' 20 nozzle~ for moving the elongated material through ...~
,,~ the treatment chamber,by a flùid flow~
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',f~ Fig. 2 is a sectional view, on an enlarged scale compared ~` to the illustration of Fig. 1, through a guide i body with its nozzle ~tructure, whereby the sec-tion extenas approximately along ~ection line II - II in Fig. 4, or section llne ~-~ in F~g. 5s .
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1 F~g. 2A ~hows a ~ectionAl ~lew ~imilAr to that of F~g. 2, but lllu~trating a modlfied ~uide body wlth tran~-port nozzle~ up~tr~am and downstream of the dlrec-tlon changing zono ~f the gulde body~
Fi~, 3 i9 a ~eatLon~l vle~ similar to thAt of ~ig. 2, however, ~howlng an ~nal~ned gulde leg of the qulde bodyl Fig. 4 is n sectlonal ~iew ~long seot~on line IV - IV
ln Fig. 2, or in Fig. 3J
. 10 F1g~J f8 d ~l~oti~ v~ 41m$1ar~~o~Chat of Fig. 4, but ~howlng ~ comblnation of clrcular cro~s-~ea-¦ tional nozsl~s with ~lot cro~-soctional nozzle and ~ig. 6 lllu~trato~ w hQmAtlcally ~ ~low control ~ystem for the supply of pre~urlzcd tranBpOrt fluid to lndlvidual no~zles with the ~ld o~ a a~ntral proce~-~ng ~nit.
~ DE~AI~ED DESCRIPSION OF P~E~ERRED EXAMPLE EMBODIM~NT~ AND OF
:, THE ~E6T MODE 0~ ~HE ~NVENTION
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Flg. 1 lllu~trAt~ ~chematlaAlly A longltudl~l sectlon through o. I,~ea~.u~e~ L 3~ ~I~c~ I L~ lelll- ;6V1101 2 W~ e .; chamber. ~he chamb~r 33 has an lnlet 33a ~nd an o~tlet 33b for the elong~ted materi~ uch 8~ a r~bbon or the llke. In~d~
the chamber 33 oppo~lte the inlet 33a there 1~ mounted A firBt ... .
,. 2~asl~
1 direction changlng 6tation 34 which imparts to the ribbon 1 a directional change of about 90. The ribbon 1 travels through the chamber 33 in the direction indicated by the arrows 8. Down-stream of the guide station 34, as viewed in the travel direction of the ribbon 1, there i~ a further guide station 35 imparting to the ribbon 1 substantially a direction reversal of about 180.
The ribbon 1 then meanders back and forth horizontally in the chamber 33 as guided by further guide stations 36, 37, and 38.
Although the inlet 33a and the outlet 33b are shown in Fig. 1 on the same side of the chamber 33, this construction is not ~, necessary for embodying the present teaching. Such an arrange-ment may be convenient, but not absolutely necessary.
. . , The guiding of the ribbon 1 along a meandering path as shown in Fig. 1, permits introducing into the treatment zone 2 a suf-ficient quantity of ribbon for a uniform treatment while still keeping the volume of the chamber 33 relatively compact. The meandering also exposes the material to a relatively long path within the treatment chamber 2, whereby the residence time within the treatment zone 2 can be malntalned sufflclently long for the desired treatment, even if the travel speed through the cham-ber 33 is relatlvely high.
Guide plates 49, 50, 51, and 52 are mounted withln the chamber 33 for separating the treatment zone 2 into several sections. Con-ventional speed ~ensors 39, 40, 41, and 42 are mounted wlthin the chamber 33 in such positions that the speed of the rlbbon 1 can be measured. For this purpose, the ribbon 1 may, for example, ' .
- . . :~ . . -,. . . - :
2 ~ a 1 be provided with markers equally spaced along the length of the ribbon and the sensors count the number of markers pa~sing per unit of time, thereby providing a speed signal. In another speed sensor, the ribbon may drive a wheel for generatlng a speed signal.
In any event, conductors 53, 54, 55, and 56 connect the respective speed sensor to a central processing unit 48 shown in Fig. 6.
The CPU 48 processes the speed signals in accordance with a pro-; gram stored in a memory 48a of the CPU 48 for producing control impul~es to be supplied to control valves 43, 44, 45, 46, and 47 also shown in Fig. 6. These control valves are, for example,electromagnetically operated valvee connected through control - conductors 57 to 61 to re6pective outputs of the CPU 48.
i j Referring further to Fig. 6, the valves 43 to 47 are volume con-trol valves connected through plpes 28 to 32 to the respective ~' guide station 34 to 38 shown in Fig. 1, or rather, to the tubular mem-ber 20 ofthe nozzle structure of the corresponding guide station.
The volume control valves 43 to 47 are further connected to a manifold 62 which in turn is supplied with transport fluid under pressure from a compressor 19 including a drive motor not shown.
The intake of the compressor 19 is connected to a noise muffler 63 if the transport fluid is a gas such as air.
., ~
~eferring to Figs. 2, 2A, and 3, each of the direction changing stations 34 to 38 comprises a tubular member 20, for example, having a rectangular cross-section and extending, for example, across the chamber 33 from one side wall to the other opposite side wall. The tubular member 20 has a first side wall 21 facing in the travel direction prior to direction reversal and a rear : . . ;. ~ , .
. , . :
2~1a81~
1 side wall 21a facing in the travel direction after direction reversal. A pipe 30 is connected through the side wall 21a to supply fluid under pressure into the chamber formed by the pipe 20.
llowever, fluid under pres~ure may be alternatively supplied through an end wall a~ 6hown at 30'. The side wall 21 has an extension 21b provided with a plurality of nozzle bores 15 and/or 16, please ee Figs. 4 and S. These nozzles 15, 16 are distributed along the entire width 9 of the elongated material 1 as seen in Fig. 5.
~; In Fig. 4 the nozzle~ 15 do not extend entirely to the very edges of the material width 9. The arrangement in Fig. 4 i9 such that no flowing tran6port fluid i8 ejected in zones 13. On the other hand, in Fig. 5, the nozzle arrangement i8 such that elongated flat nozzles 16 eject the transport fluid in zones 10 while the circular cross-6ection nozzles 15 eject fluid in zones 12. In the zones 12 no fluid i~ ejected along the spacings between neigh-boring nozzle~ 15. The nozzles may be arranged in a row, preferably a linear row, as shown in Fig. 4 or in two rows as shown in Fig. 5.
By changing the cross-sectional flow area and the configuration of the cross-~ectional flow opening, it 18 possible to desirably influence the flow pattern. The nozzle~ 15, 16 are located in the extension 21b of the ~ide wall 21 of the tubularm ~ er 20 ~uqtnext to a further side wall 22 of the tubular member 20.
A contact surface 21c for the elongated material 1 i~ formed where the exten6ion 21b and the lower wall 22 of the tubular member 20 meet. Thi~ contact surface 21c i~ al~o spaced from the zone 18 where the direction change begins around the surface 3 of a curved portion 5 of the guide b~dy 4 having a ~horter leg 25 and a longer leg 25'. The tubular member 20 has a wall extension 27 , 2 ~ 5 1 extending away, preferably at a right angle, from the ~ide wall 21 of the tubular member 20. The exten~ion 27 prov~de~ a ~top and a means for mounting the end of the shorter leg 25 to the tubular member 20. The longer leg 25' rests on an upper wall 22a of the tubular member 20, whereby the outwardly facing surface of the leg 25' forms a guide surface7 for the material 1 and may extend beyond the location of the tubular member 20 as shown in Fig. 1.
The leg 25' may, for example, be welded to the wall 22a of the member 20. The legs 25, 25' and the curved portion 5 form a U-shape.
As described above, in the example embodiment the nozzles 15 and 16-receive-the pressurlzed-fluid-from-the interior of the tubular member 20 which is connected to the respective supply pipe 28 to 32 shown in Fig. 6. Where the ~upply pipe~ 28 to 32 are connected through the end walls as shown at 30', the outer chamber walls must be sealed to the ends of the tubular member~ 20 or vice-versa.
Referring further to Fig~. 2, 2a, and 3, the individual guide bodies 4 are preferably formed of sheet metal as the curved end section of the gulde members 49 to 52. Preferably, the radius of curvature of the curved portion 5 i~ a semi-circle having a radius of, for example, 10 mm for a curvature of at lea~t 180. ~he so formed guide body 4 is then connected, as mentloned above with its leg 25 to the wall exten~ion 27 of the tubular member 20. Thus, the outwardly facing surface 23 of the ~hort leg 25 and the elon-gated material, form, or rather enclose, a wedge-shape into which the fluid under pressure is blown through the nozzles 15, 16, as indicated by the arrows 64. Due to the suction effect through the nozzles 15, 16 there is a tendency of the elongated material 1 ., ,. . . .
2~8~
1 to be drawn against the contact surface 21c formed at the corner between the wall extension 21b and the wall 22 of the tubular member 20.
Fig. 2A show~ an embodiment similar to those shown in Figs. 2 and 3, however, in Fig. 2A additional nozzles 65 are arranged in the upper right-hand corner of the tubular member 20, whereby fluid under pressure as indicated by the arrows 65' ls blown along the surface 66 of a gulde member 67 to further aid in the transporting of the elongated material 1. The guide mem-ber 67 is mounted with it~ left-hand end to a wall extension 27a in the same manner as was described above with reference to the end o the leg 25 that is mounted to the wall extension 27.
Here again, due to the suction effect by the flowing fluid indi-cated by the arrow 65' there i~ a tendency of the elongated material 1 to contact a contact surface 21d of the tubular member 20.
In Fig. 3 the short leg 25 of the gulde body 4 extends at a small angle 26 relative to the wall extension 27 to modify the wedge shape of the wedge space between the ~urface 23 and the elongated material 1. The wedge shape is such, that the widest opening into the wedge space is located ln a plane 14 defined by the outer surface of the wall 21 in the extension 21b of which the nozzles 15, 16 are located. The narrowest section of the wedge space is located at the zone 18 where a direction change begins. The spacing 17 between the plane 14 and the zone 18 should be such that the fluid flow 64 can extend substantially tangentially to the surface of the guide body 4 2~81.~
; 1 at the point 18 where directlon change begins. If the spacing 17 - is too short, the fluid flow 64 will not coincide with the travel direction or transport direction 8 in the inlet to the zone 18.
If the space 17 is too large, the ~peed of the fluid flow may have become too ~mall for a proper feed advance of the elongated material 1. Further, the spacing 17 should also not be 80 long that an undesirable whirling of the fluld flow begins, causing a lateral expansion of the flow fluid.
,~ i In operation, the elongated material is first inserted into the ~ 10 chamber 33. For this purpose a side wall, functioning as a cover, i8 removed. Once the 1nsertion is completed 80 that the elongated material 1 passes around each of the direction changing stations 34 to 38, and the chamber i8 closed again, transport fluid under pressure is introduced into the tubular members 24 passing through the nozzles 15 and 16 to travel in the direction Z~ of the arrows 64. The fluid under pressure pushes itself between the material 1 and the surface 3 of the curvea section 5 of the guide body 4 at the point 8 where the direction change begins.
The fluid under pressure keeps lifting off the material 1 from the surface 3 to form a travelling cushion between the surface 3 and the material 1. As a result, the material 1 18 entrained by the fluid flow which thus transports the materlal 1 ln the direc-tion 8 from the inlet side 6 to the outlet side formed by the surface 7 of the guide body4. Such transport is substan-tially free of friction.The number of direction changing stations will depend on the dwell time needed for the particular treatment.
By varying the flow speed of the flowing transport fluid and/or by varying the mass throughput of the flowing fluid through the nozzles, it is possible to apply a transport spéed to the elongated 2 ~ S
1 material 1 with due regard to the characteristics of the material.
The influencing of the transport speed may be performed individually at each direction changlng station. For this purpose the speed sensors 39 to 42 are located in proper positions to sense the speed of the material 1 at these positions and to produce respec-tive control signals. Thu~, it is possible to take into account any flexible stretching or any shrinking of the material at dif-ferent points along the travelling path through the treatment zone. If the material shrinks due to the treatment, more ma-terial must be fed into the apparatus than will be carried outof the apparatus. The present control can be adju6td to such an operating condition. Simllarly, if the, material stretches due to the treatment, more material must be taken out of the chamber than is being passed into the chamber. Here again, a very individual adaptation of the feed advance i8 achieved according to the invention so that undesirable tension 6tre6s is not applied to the material 1.
In connection with the shrinking, it is, for example, known, based on experience and experiments, how much shrinking will 2n take place. Thus, the required speed reduction in response to the shrinking is a scalar amount that i~ known and the speed can be controlled accordingly. The inlet speed can first be adjusted at the guide station 34 by controlllng the valve 43.
The so established initial speed is then sensed by the sensor 39 to provide a signal on the conductor 53 to the central proces-sing unit 48 which now knows the speed upstream of the station 34.
The further speed sensor 40 just downstream of the station 34 provides a further speed signal on the conductor 54 to the - . ..: . - - ~ . . -.. . :;, ~ ., , : . :, - . .., :,. ...
23 2 0 ~
1 central processing unlt 48. Thus, it can be ascertained first whether the station 34 indeed transports the material 1 in the direction 8 and if the speed at 39 differs from the speed at 40, a shrinking or stretching 1B recognized. AB a result, the valve 43 can be controlled for providing the required adjust-ment of the flow speeds in the statlon 34.
If no shrinking or lengthening or stretching is noted at the inlet guide station 34, the speed measuring stations 41 and 42 still may provide further speed signals through the conductors 55 and 56 to the central processing unit to make ~ure that the same transport speed prevalls at the respective direction chang-ing stations to make sure that the quantity of material fed into the chamber 33 is also removed from the chamber 33, thereby providing an indication that no jamming takes place inside the chamber. However, if a shrinking does take place, the sensors 41 and 42 provide respective slower speea signals and the speed of the jet~ may be adjusted accordingly through the control valves 44 to 47 as controlled by the central proces~ing unit 48 through the conauctors 58 to 61. Some or all of the guide sta-`. 20 tions may be provided with their respective speed sensors up-. stream and/or aownstream of these stations 34 to 38.
,. . .
The central processing unit 48 shown in Fig. 6 has been des-cribed so far as controlling the flow control valves for the indiviaual stations 34 to 38. Nowever, the same control system :~ can be applied to controlling individual nozzles at one guide station. Thus, if the material 1 aoes not have a homogeneous :. structure across its width, the individual nozzle holes lS, 16 .,, ~
2 0 ~
1 may be aonnected to indlvidual ~luld flow ~upply pip~ or hoee~
r~ther th~n to A aommon c,h~mber in ~ tubul~r memb~r 20 a~ d~cribed above. ~hus, the ~u~d 10w can be lndlvldually And ~ensitively eontrolled in ~ccordance wlth the rQqulrQment~ of Any particul~r type o~ materi~l to b~ tran~ported. ~n ~ddltion to cont~olllng the flow speed, it i8 po~lble ~o modlf~ the compo~itlon ~nd denslty of the flowing tr~nsport ~luid in order to mlnlmlze any di~tortlon of the mhteri~l to be treAted.
The preeent method ~nd apparatuq tran~port the type of mater~als m~ntloned sub~ntlally fre~ of d~to~t~on~ bsaAu~e th~ tcn~on I ~t.r~ e~ harQt~f~rQ h~ h~n mlnlm~ by the ~e-crlbed ~eature~ And bec~u~e the direction re~er~lng frl¢tlonal forces ~nd/~r dr~gglng forca~ ha~e been reduced to such ~m~ lu~
¦ that the~e force~ can now be di~regarded.
Although the ln~entlon ha- been de4crlbe~ with refer-nce to speclftc ex~mple embodimente lt wlll be appr-ci~ted th~t it ~
~ Intended to aover all modifiaatlon~ and equl~ nt~ withln the : ecope of the appended alalm~.
;~ - .
The invention relates to a method and apparatus for reducing a transporting strain on elongated material passing through a treat-ment chamber.
BACKG~OUND INFORMATION
,, , Elongated material in the present context may include ribbons, tapes, band-~haped material, for example, made of textiles, '-:. synthetic materials, or paper. The term also includes threads, '~'ya''rns, ro'pe's,''strings~,''an'd the~ e. Such ~aterlals frequently require a treatment in a treatment chamber. For this purpose, :~ the elongated materials must be transported through the treatment ~ chamber pa~sing through an inlet lnto the chamber and through .' an outlet out of the chamber. Inside the chamber or treatment '. zone the surface of the elongated material pas~es along the sur-face of at least one guide body whlch changes the travel direc-tion of the elongated material through the treatment zone or ~ chamber. The material to be treated usually travel~ through ;.~;; the treatment zone along a meandering path, for example, for the .. purpose of drylng or dyelng or lmpregnating or the like. The ~ 20 conventional dlrection changing guide body 18 usually a rotatably . . .
.' mounted roller which 1~ either positively driven or it rotates as a result of the contact of its surface with the material being treated.
. .
~; In order to transport the material through the treatment chamber or zone, it was nece~sary heretofore, to provide a posltive drive.
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2 ~ 3 -~ 2 l Such positive drive may involve the driving of the guide rollers and/or a further drive which pu119 the elongated material through the treatment chamber or zone. In all conventional transport drives of this type it is unavoidable that the elongated material is subjected to a substantial transporting strain caused by a longitudinally effected stress applied by the pulling force of a take-up reel or the like. The direction reversing guide rollers inside the treatment chamber are mounted in a fixed position, except one such roller is mounted in a floating manner to provide for some yielding, whereby the elongated material is protected to some extent against too large tension stress.
: ..
Thus, when the take-up roller rotates too fast, the floating roller travels out of lts orlglnal position into a posltion in which the total length of elongated material within the treat-ment zone or chamber i8 reduced. This movement direction of . ~
~i the floating roller is maintained, for example, until a pre-,A
determined threshold tensile stress is reached ln response to `~ which, for example, an end switch or sen60r swltch provides a signal for the control of the feed advance. Such a signal .~ 20 may slow down the take-up speed or may increase the feed-in :. . . speed. As a result, the floatlng roller again moves ln the opposite dlrection untll a re~pective thre~hold value is sensed.
The feed advance 18 thus controlled to provlde for a back and forth shuttling of the floating guide roller between presettable limit values for the tensile stress applied to the material.
, In spite of such a floating guide roller it is unavoidable, that the type of material hereinvolved may be exposed to rela-~i tively large tension stress during its transport through a .~ .
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~.. ' ' .. ~ :' - : "' ~ - :': ' . . , 2~81~a ; 3 1 treatment zone or chamber. Thl6 i6 due to the fact that the material being transported must take up at least that stress that is necessary for moving the floating guide roller. To this stress is added a stress component neces~ary for rotating any guide rollers mounted in a ~tationary, but rotatable position. Even if the stationarily mounted guide rollers are positively driven, there may be synchronization errors that also re6ult in undesir-able tensions on the elongated material. Even the friction in the bearings of guide rollers that are rotating due to the contact with the elongated material results in undesirable tension stress which may differ from roller to roller and which aaas up with the number of rollers. Exposing the elongated material to such tension stress i6 undesirable because it ad-versely influences the quality of the fini6hed elongated material.
This problem has not been solvea heretofore.
:, .
i OBJECTS OF TIIE INVENTION
~, In view of the foregoing it is the aim of the invention to achieve the following objects 6ingly or in combination:
~:.
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to reduce the above de~crlbed ten~ion ~tress to which materials of the mentioned type are expo~ed in their treatment ; while still transporting the material uniformly and at the desired speed through the treatment ~one or chambert ~ to transport the material by means of a blowing medium ;:.
which substantially reduces the appli~ation of tension stres6, pos6ibly to the extent that at the take-up end of the elongated J~ material a pulling mechani6m can be avoided:
~e 2a~sl~s :
:
- to support the elongated medium on a transporting -- cushion of flowing fluid; and to provided a transport for the elongated material with a minimum of stress independently of the fact that the treatment may somewhat lengthen the material or that the treatment may shorten the material, e.g. by , stretching or shrinking.
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~ SUM~ARY OF THE INVENTION
:' 10 According to the present invention, there is provided a method for reducing a transporting strain on elongated flat material passing through a treatment chamber, ~ comprising the following steps:
J$ 1 5 ~ a) transporting said elongated material with a transporting speed through said treatment chamber having . an inlet and an outlet for said elongated material, whereby a transport direction is from said inlet to said outlet, (b) guiding said elongated material at least around one travel direction changing guide means defining a zone . where a direction change begins between said inlet and said outlet, (c) forming a space of substantially triangular cross-section bounded by a straight portion of said guide means upstream, as viewed in said transport direction, of said direction change zone, by a nozzle wall, and by said elongated flat material, whereby said straight portion merges, away from said nozzle wall, into a curved portion of said guide means where said direction change zone begins, I
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~s 4a 2~081 ', (d) introducing at least one flowing fluid jet through said nozzle wall into said space of substantially -triangular cross-section at least approximately in said transport direction and substantially in parallel to said straight guide means portion upstream of said direction change zone of said travel direction changing guide means as viewed in said travel direction, whereby a force component extending radially to said travel direction around said guide means is substantially reduced to thereby reduce said strain, and (e) imparting to said flowing fluid jet a flow speed corresponding at least to said transporting speed for transporting said elongated material through said chamber.
The flowing medium generates a cushion at each location where the travel direction of the elongated material is changed. The cushion is produced between the surface of a direction changing or direction reversing guide body and the surface of the material facing the guide body surface. Thus, the elongated material can float on such a cushion and is transported by the flowing cushion substantially free of friction. This type of transport completely avoids the need for direction changing guide rollers regardless whether they are of the driven or undriven type. The direction reversing guide body may be stationary and rigid but it must have a smooth surface of the suitable curvature to .~ ~
~ A
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1 achieve the direction change or reversal, whereby the radius of curvature can be selected in a very wide range. Provided s the direction reversal is performed several times in the treat-ment zone or chamber, it i8 now also possible to avoid the above mentioned floating roller.
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The above mentioned floating of the elongated material on the cushion of flowing fluid which simultaneously transports the elongated material, can be enhanced by additionally intxoducing flowing fluid between the elongated material and an exit guide plane, for example, in the form of a baffle plate, whereby again the flowing fluid must have a suitable flowing speed. Due to the low friction between the material and the flowing fluid it i6 possible to even shrink the elongated material in the ;~ treatment chamber or zone without generating any tension stresg in the elongated material ln the transport dlrection. Thus, even where a shrinking takes place as part of the treatment of the elongated materlal, a take-up roller downstream of the f treatment zone or chamber is no longer necessary since the flowing ~ fluid performs the transport regardless whether the elongated .,! 20 material is shrinking or even expanding. It 18 also no longer necessary to correlate the lnput speed to the output speed.
Nevertheless, the transport is uniform and tenslon stress 18 avoided because the infeed and wlthdrawal of materlal no longer depends on friction contact wlthln the treatment zone. ~8 much material as necessary can be fed into the treatment zone or chamber and a~ much material can be taken out as is necesgary.
If the feed-in speed should be reduced at the inlet end of the i~ chamber, such reduction does not have any noticeable effect on A
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1 the quality of the elongated material because it does not affect ~,~ any tension stress within the material travelling through the treatment zone or chamber.
By varying the density of the flowing fluid with due regard to the density of the medium forming the environment in the treatment chamber, it i8 posslble to influence the treatment.
The flowlng transport fluid and the treatment medium may both be gaseous or both may be liquid or one may be gaseous and the other liquid. The flowing fluid may contain additives for the treatment of the elongated material. The flowing fluid could be heated or it could be cooled, whereby again the desired influence on the elongated material may be achieved.
,., Frequently, it is suitable that the flowing 1uid~ and the treat-ment or environmental medium in the treatment zone, have substan-, .
tially the same composition, whereby intermixing i~ of little ; concern and any need for any separation of components subsequent , to the treatment is avoided.
~.' .:~
~ Depending on the type of transport intended, it is po~ible ; according to the invention to apply dlfferent flowing speed~
`~` to the flowing tran~port fluld at the lndlvldual dlrection ,~ changing guide bodies. For example, the flowing speed may increase `; from guide body to guide body. Different flowing fluids may be used at different guide bodies and the density of the flowing ,~ Eluid may be different at different gulde bodies. These features make it possible to take into account the characterietics of ,~:
~,~ the elongated material a~ they may change along the pass of .,.~. .
~ the material through the treatment chamber or zone. For example, ..
..
7 2 ~ 5 1 if the elongated material should lenqthen as a re~ult of the treatment, it is necessary to increase the transport speed from the inlet of the treatment chamber toward the outlet of the treatment chamber to properly transport the increasing length of the elongated material. Similarly, lf the material should shrink as a result of the treatment, it is possible `' to reduce the transport speed from the inlet to the outlet.
!.'.
In all instances it i8 advantageous to avoid directlng the flowing transport fluid in a direction radially to the length of the materlal to thereby avoid any distortions in the material.
In the light of the foregoing it will be appreciated that the , flow speed of the flowing transport fluid can influence the ~ transport speed of the elongated material. However, the trans-,, port speed also depends on the surface characteristics of the :i material and on the den~ity of the flowing transport fluld.
Normally, the transport speed of the elongated material will be smaller than the flow speed of the flowing transport flula~
and the transport speed can be controlled without any problems.
Another advantage of the lnvention is seen ln that in addltion ~''$!' 20 to the transportlng by means of the flcwlng fluld,a conventlonal tran~port may be comblned by means of a take-up roller outside the treatment zone. Due to the reduced frictlon assured by the cushionlng formed by the flowlng transport fluld, the stress on the elongated material will be very small because the pullinq forces generated by a take-up roller can be very .~ small.
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1 Depending on the characteristic~ of the elongated material it may be advantageousto apply the flowlng transport fluid over the entire width of the material. However, a denser elongated material, such as paper web~, can be transported when the flowing transport fluid i9 applied only to certain zones or even only along a center strip or only along the outer eages. ~urther, it may be aavantageous to distribute the flow speea over the width of the elongated material 80 that, for example, a larger flowing speed is applied along the edgefi while a smaller flowing speed 10 iS effective along the center of the elongated material or vice versa. By applyingan increasea flowing speea along the edges it ~ is, for example, possible to reduce an escape of flowing tran~-i port fluid away from the central zone of the elongated material, whereby unaesirable force components that may be exerted by the flowing transport fluid on the elongated material, are either prevented or minimized. On the other hand, for certain materials it may be desirable to have a higher flowing speed for the flowlng transport fluid along a central zone than the transport fluid speed along the edges. Such a speed distribu-tion of the flowing transport fluid may be aesirable, for example, for double ribbons having a central transport zone of a different composition than the edges 80 that the transporting iB aacomplished primarily by applying the flowing transport fluld to the central strip while the lateral eages of the elongated material are .~ merely æupported by the slower speed of the flowing transport ~ fluid, thereby preventing a slowihg down of the lateral edges '~ of the elongated material relative to the central zone. The ~` flowing transport fluid may be applied in the form of a plurality of individual jets having, for example, circular cro~s-sections ~ .
2~81~
. g or any other suitable cross sections. Instead of a plurality of individual jets, a broad flat jet may be employed which has a width corresponding to the entire width of the elongated material or which has several zones distributed across the width of the elongated material. Thus, it is possible to support the elongated material along its entire width or along certain zones.
,.
According to the present invention, there is provided an apparatus for reducing a transporting strain on elongated flat material passing through a treatment operation in a travel direction, comprising a treatment chamber for treating said elongated material, said chamber having an inlet and an outlet defining a transport direction from said inlet to said outlet, means for transporting said elongated material from said inlet to said outlet, said transporting means including at least one material guide means having a curved material guide surface for changing the travel direction of said elongated material between said inlet and said outlet, whereby said material guide means define a direction change zone where a direction change begins, æaid material guide means further having a straight portion merging into said curved material guide surface, and fluid flow means including a nozzle wall upstream of said straight portion, as viewed in said travel direction, said nozzle wall, said straight portion and said flat material bounding a space of substantially triangular cross-section tapering toward a point where said guide means begin changing said travel direction in said direction change zone for introducing substantially in said travel direction at least one flowing fluid jet ~,, ... . ~, .. ,,. :
. i ..
`<s 2~81 ~
9a into said space of substantially triangular cross-section between said straight portion of said material guide means and said elongated flat material, whereby a force component extending radially of said curved material guide surface is substantially reduced for reducing said strain, said fluid flow means imparting to said flowing fluid a flow speed corresponding at least to a transporting speed of said elongated material.
The elongated material travels around the guide body for the direction reversal. Each guide body is equipped with at least one jet means for introducing a flowing i transport fluid into a space between a surface of the guide body and the elongated material. The flowing ; 15 transport fluid is introduced substantially in the travel direction. The jet means impart to the flowing transport fluid a flow speed which corresponds at least to the transporting speed of the elongated material. The flowing transport fluid may, for example, be compressed air. The compressed air forms a moving support cushion for the elongated material, thereby keeping the elongated material substantially in a floating condition so that ~3 the latter may travel substantially free of friction ~ around the guide body while the flowing fluid transports ; 25 the elongated material. Thus, a substantial pulling force does not have to be applied to the elongated material, nor is it necessary that the elongated material x entrains any guide rollers for rotating the guide , rollers. By substantially reducing the friction and hence the pulling forces on the elongated material, it is possible to transport the elongated :
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1 material through its treatment zone or chamber substantially without any distorting influences.
The jet means for introducing the flowing transport fluld compri~e advantageously at least one nozzle which is arranged at a spacing from the point where the change in the transport direction begins to take place, whereby such spacing extends substantially in - the transport direction upstream of said point. The nozzle is 80 directed that the flowing transport fluid i8 aimed tangentiallytoward said point. The nozzle may, for example, be of the type capable of producing a so-called flat section jet. Such jet has a flat ribbon-type cross-section. However, other nozzle types may be :~
used, for example, groups of nozzles may be arranged in a row across the entire width of the elongated material to be transported.
One or 6everal nozzle groups may be arranged in this manner.
Preferably, each group is arranged along a straight line across the width of the material. All nozzles in a row may produce .,~ .
fluid jets all having the same cross-section or a different cross-section, thereby generating transport jets having the same cross-sectional flow area or different cross-sectional flow areas. In ~ 20 the embodiment where several nozzles produce several different jets, these jets may be produced by transport flulds under dif-. . .
ferent pressures or by transport fluids having dlfferent densities ~i~ or other different characteristlcs. Nowever, depending on the ~;, type of material being transported and treated, it is quite pos-~; sible to supply the ~ame transport fluid by a common source under pressure to all nozzles. Where a common source of fluid under pressure is used, the nozzles may be arranged in a ~ide wall ; of a tubular member having a rectangular or square cross-section, ....
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` 23~81~
1 whereby the nozzles are simply bores located in said side wall close to a neighboring or adjacent wall forming part of the guide body for changing the travel direction.
By using different types of nozzles and nozzle shapes and by different nozzle arrangements it is possible according to the invention to vary the influence of the flowing transport fluid on the elongated material. The variation is accomplished by properly selecting a desired nozzle configuration or nozzle shape - and the respective fluid flow is then effective on the elongated material during its transport through the treatment zone or chamber.
Thus, it is, for example, possible to tran6port a 6en8itive thin elongated material, such a6 a fabric that is homogeneous in its ~ cros~-sectional structure, by a flat transport ~et without any ^~ problems, and without sub~tantially any distorting influences of the flat jet stream on the seh~itive thin fabrlc. A quite similar result is achieved by arranglng a plurality of nozzles in the form of a row of bores, whereby the flat jet ~tream is replaced by a plurality of small diameter individual ~et streams.
^~ The plurality of nozzles can simply be provided by the above mentioned bore~ arranged in a side wall of a rectangular cross-~ section or square cros~-~ection plpe resulting in a very 8imple '~''t'.'~' structure.
, ., ,,:
`~ By applying the pressurlzed transport fluid in a controlled manner to individual nozzles or to group~ of such nozzle~, it is also possible to influence the effect of the flowing tran~port fluid ;~ on the elongated material. In this context it is po~sible to ;, vary individually or in combination the fluid pressure, the fluid .:
~ .: :. . . ................................ .
. , . , :
- - . : . . -2 ~
1 den~ity, the fluid composition, and/or the fluid temperature.
Thus, the influence on the transporting can be modlfied in a multitude of ways to assure that the elongated material is sub-stantially free of di~tortions while simultaneously using the transporting fluid as a treatment medium, for example, for im-pregnating or drying the elongated material. The present trans-port and it~ multitude of control possibilities is equally appli-cable to elongated material not having a homogeneous cross-sec-tional structure. For example, fabric ribbons may be aenser along their edges and less den~e in a central area between the edges. Similarly, the density may change along the length of ~uch fabric ribbons. The present transport fluid can be con-trolled to take into account these characterl~tics of elongated material. For example, a rlbbon with denser or thicker marginal zones will require a higher flowing speed along these denser or thicker zones a~ compared to the flowing speea of the trans-port fluid contacting a central zone of the ribbon. Thus, the proper adjustment of the several flowing speeds wlth due regard to the ribbon characteristics will assure that the marginal zones will not be di~placed relative to a central zone 80 that again ~, the transport take~ place substantially without any distortion of the ribbon being transported.
The guide body for changing or reversing the travel direction of the elongated material is, for example, made o sheet metal : which provides a simple and relatively inexpensive way of produc-ing these guide boaies. The wall portion of the guide body where ; a direction change or reversal begins, must have a 6uitable spacing ''! from the outlet openings of the nozzle or nozzle~. Thus, the i~.; ~, ' .
`:
.. ^ - . . .
- .
-: . ~ ;: - ..
- ' ~
2 ~ ~ 8 1 ~ 3 guide wall extends perpendicularly or at a3~all angle to a nozzle wall of the guide body. The nozzle wall portlon reaches beyvnd the guide wall portion so that the nozzles face in a direction approxi-mately in parallel to the guide wall portion. Thu33, the flowing transport fluid travels toward the point of direction change substantially in a tangential direction. The arrangement is such, that the guide-wall portion and the flowing fluid facing surface of the elongated material form a wedge 6hape which in itself also forms a type of nozzle into which the tran3sport fluid is blown since the wedge shape nanxws toward the point of the directionchange.
For example, when elastic elongated materials for forming bandages are to be transported, lt is deslrable to direct the transport flow substantially in parallel to the guide wall portion of the guide body at least at the point where a change in the travel direction begins. This may be accomplished by changing the angle between the guide wall portion and the nozzle portion of the guide body from 90 to an angle smaller than 90 to provide for , ., ~ a more rapid reductlon in the cross-sectional flow area in the ;~ nozzle channel formed by the wedge-shape, 80 that the channel narrows quickly toward the point of dlrection change. In this manner, the direction of the transport fluid and the direction :.,.
o~ travel may sub~tantially correspond to each other. The radius of curvature for a guide body wall portion intended for transporting ~ such flexible bandage material, may have a radius of curvature '~j of about 10 mm. As a result, the entire apparatus can be rather ; compact, even though the guide body is requlred to provide a complete direction reversal of 180. In such an lnstance the guide ~urface portion will have a semi-circular cross-section.
... ~ ' ., i :, .
., ~ ,. . . - :
2 ~
1 ~ccording to the invention the nozzle or nozzles at each guide body can be controlIed in accordance with the conditions pre-vailing at the particular guide body. Thus, it i9, for example, possible to provide a sensitive adaptation of the transport speed to any shrinking or ~tretching of the elongated material at the - particular gulde body within the treatment zone. For this pur-'' pose, a speed sensor may be arranged just up~tream of the respec-" tive guide body, as viewed in the transport direction, the respec--,. tive signal from the speed ~en~or ig then used by a central proce~sing unit for controlling the flow speed of the transport , fluid. On the other hand, all nozzles can be centrally controlled ", in uni~ff,~ rathër tha~'lndivid~ally.
,'~ BRIEF DESCRIPTION OF THE DRAWINGS
.~ .
In order that the invention may be, clearly under~tood, it will now be described, by way of example, with reference to the ac-companying drawings, wherein:
, : .
~ Fig. 1 is a schematic sectional view through a treatment ,',, chamber equipped with a plurality of guide bodies, ,,' each of which i~ provided wlth lt~ transport :.
' 20 nozzle~ for moving the elongated material through ...~
,,~ the treatment chamber,by a flùid flow~
.:, ... .
',f~ Fig. 2 is a sectional view, on an enlarged scale compared ~` to the illustration of Fig. 1, through a guide i body with its nozzle ~tructure, whereby the sec-tion extenas approximately along ~ection line II - II in Fig. 4, or section llne ~-~ in F~g. 5s .
- . -' ' ~' '` ~ ' ' , 2~81'j~
1 F~g. 2A ~hows a ~ectionAl ~lew ~imilAr to that of F~g. 2, but lllu~trating a modlfied ~uide body wlth tran~-port nozzle~ up~tr~am and downstream of the dlrec-tlon changing zono ~f the gulde body~
Fi~, 3 i9 a ~eatLon~l vle~ similar to thAt of ~ig. 2, however, ~howlng an ~nal~ned gulde leg of the qulde bodyl Fig. 4 is n sectlonal ~iew ~long seot~on line IV - IV
ln Fig. 2, or in Fig. 3J
. 10 F1g~J f8 d ~l~oti~ v~ 41m$1ar~~o~Chat of Fig. 4, but ~howlng ~ comblnation of clrcular cro~s-~ea-¦ tional nozsl~s with ~lot cro~-soctional nozzle and ~ig. 6 lllu~trato~ w hQmAtlcally ~ ~low control ~ystem for the supply of pre~urlzcd tranBpOrt fluid to lndlvidual no~zles with the ~ld o~ a a~ntral proce~-~ng ~nit.
~ DE~AI~ED DESCRIPSION OF P~E~ERRED EXAMPLE EMBODIM~NT~ AND OF
:, THE ~E6T MODE 0~ ~HE ~NVENTION
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Flg. 1 lllu~trAt~ ~chematlaAlly A longltudl~l sectlon through o. I,~ea~.u~e~ L 3~ ~I~c~ I L~ lelll- ;6V1101 2 W~ e .; chamber. ~he chamb~r 33 has an lnlet 33a ~nd an o~tlet 33b for the elong~ted materi~ uch 8~ a r~bbon or the llke. In~d~
the chamber 33 oppo~lte the inlet 33a there 1~ mounted A firBt ... .
,. 2~asl~
1 direction changlng 6tation 34 which imparts to the ribbon 1 a directional change of about 90. The ribbon 1 travels through the chamber 33 in the direction indicated by the arrows 8. Down-stream of the guide station 34, as viewed in the travel direction of the ribbon 1, there i~ a further guide station 35 imparting to the ribbon 1 substantially a direction reversal of about 180.
The ribbon 1 then meanders back and forth horizontally in the chamber 33 as guided by further guide stations 36, 37, and 38.
Although the inlet 33a and the outlet 33b are shown in Fig. 1 on the same side of the chamber 33, this construction is not ~, necessary for embodying the present teaching. Such an arrange-ment may be convenient, but not absolutely necessary.
. . , The guiding of the ribbon 1 along a meandering path as shown in Fig. 1, permits introducing into the treatment zone 2 a suf-ficient quantity of ribbon for a uniform treatment while still keeping the volume of the chamber 33 relatively compact. The meandering also exposes the material to a relatively long path within the treatment chamber 2, whereby the residence time within the treatment zone 2 can be malntalned sufflclently long for the desired treatment, even if the travel speed through the cham-ber 33 is relatlvely high.
Guide plates 49, 50, 51, and 52 are mounted withln the chamber 33 for separating the treatment zone 2 into several sections. Con-ventional speed ~ensors 39, 40, 41, and 42 are mounted wlthin the chamber 33 in such positions that the speed of the rlbbon 1 can be measured. For this purpose, the ribbon 1 may, for example, ' .
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2 ~ a 1 be provided with markers equally spaced along the length of the ribbon and the sensors count the number of markers pa~sing per unit of time, thereby providing a speed signal. In another speed sensor, the ribbon may drive a wheel for generatlng a speed signal.
In any event, conductors 53, 54, 55, and 56 connect the respective speed sensor to a central processing unit 48 shown in Fig. 6.
The CPU 48 processes the speed signals in accordance with a pro-; gram stored in a memory 48a of the CPU 48 for producing control impul~es to be supplied to control valves 43, 44, 45, 46, and 47 also shown in Fig. 6. These control valves are, for example,electromagnetically operated valvee connected through control - conductors 57 to 61 to re6pective outputs of the CPU 48.
i j Referring further to Fig. 6, the valves 43 to 47 are volume con-trol valves connected through plpes 28 to 32 to the respective ~' guide station 34 to 38 shown in Fig. 1, or rather, to the tubular mem-ber 20 ofthe nozzle structure of the corresponding guide station.
The volume control valves 43 to 47 are further connected to a manifold 62 which in turn is supplied with transport fluid under pressure from a compressor 19 including a drive motor not shown.
The intake of the compressor 19 is connected to a noise muffler 63 if the transport fluid is a gas such as air.
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~eferring to Figs. 2, 2A, and 3, each of the direction changing stations 34 to 38 comprises a tubular member 20, for example, having a rectangular cross-section and extending, for example, across the chamber 33 from one side wall to the other opposite side wall. The tubular member 20 has a first side wall 21 facing in the travel direction prior to direction reversal and a rear : . . ;. ~ , .
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1 side wall 21a facing in the travel direction after direction reversal. A pipe 30 is connected through the side wall 21a to supply fluid under pressure into the chamber formed by the pipe 20.
llowever, fluid under pres~ure may be alternatively supplied through an end wall a~ 6hown at 30'. The side wall 21 has an extension 21b provided with a plurality of nozzle bores 15 and/or 16, please ee Figs. 4 and S. These nozzles 15, 16 are distributed along the entire width 9 of the elongated material 1 as seen in Fig. 5.
~; In Fig. 4 the nozzle~ 15 do not extend entirely to the very edges of the material width 9. The arrangement in Fig. 4 i9 such that no flowing tran6port fluid i8 ejected in zones 13. On the other hand, in Fig. 5, the nozzle arrangement i8 such that elongated flat nozzles 16 eject the transport fluid in zones 10 while the circular cross-6ection nozzles 15 eject fluid in zones 12. In the zones 12 no fluid i~ ejected along the spacings between neigh-boring nozzle~ 15. The nozzles may be arranged in a row, preferably a linear row, as shown in Fig. 4 or in two rows as shown in Fig. 5.
By changing the cross-sectional flow area and the configuration of the cross-~ectional flow opening, it 18 possible to desirably influence the flow pattern. The nozzle~ 15, 16 are located in the extension 21b of the ~ide wall 21 of the tubularm ~ er 20 ~uqtnext to a further side wall 22 of the tubular member 20.
A contact surface 21c for the elongated material 1 i~ formed where the exten6ion 21b and the lower wall 22 of the tubular member 20 meet. Thi~ contact surface 21c i~ al~o spaced from the zone 18 where the direction change begins around the surface 3 of a curved portion 5 of the guide b~dy 4 having a ~horter leg 25 and a longer leg 25'. The tubular member 20 has a wall extension 27 , 2 ~ 5 1 extending away, preferably at a right angle, from the ~ide wall 21 of the tubular member 20. The exten~ion 27 prov~de~ a ~top and a means for mounting the end of the shorter leg 25 to the tubular member 20. The longer leg 25' rests on an upper wall 22a of the tubular member 20, whereby the outwardly facing surface of the leg 25' forms a guide surface7 for the material 1 and may extend beyond the location of the tubular member 20 as shown in Fig. 1.
The leg 25' may, for example, be welded to the wall 22a of the member 20. The legs 25, 25' and the curved portion 5 form a U-shape.
As described above, in the example embodiment the nozzles 15 and 16-receive-the pressurlzed-fluid-from-the interior of the tubular member 20 which is connected to the respective supply pipe 28 to 32 shown in Fig. 6. Where the ~upply pipe~ 28 to 32 are connected through the end walls as shown at 30', the outer chamber walls must be sealed to the ends of the tubular member~ 20 or vice-versa.
Referring further to Fig~. 2, 2a, and 3, the individual guide bodies 4 are preferably formed of sheet metal as the curved end section of the gulde members 49 to 52. Preferably, the radius of curvature of the curved portion 5 i~ a semi-circle having a radius of, for example, 10 mm for a curvature of at lea~t 180. ~he so formed guide body 4 is then connected, as mentloned above with its leg 25 to the wall exten~ion 27 of the tubular member 20. Thus, the outwardly facing surface 23 of the ~hort leg 25 and the elon-gated material, form, or rather enclose, a wedge-shape into which the fluid under pressure is blown through the nozzles 15, 16, as indicated by the arrows 64. Due to the suction effect through the nozzles 15, 16 there is a tendency of the elongated material 1 ., ,. . . .
2~8~
1 to be drawn against the contact surface 21c formed at the corner between the wall extension 21b and the wall 22 of the tubular member 20.
Fig. 2A show~ an embodiment similar to those shown in Figs. 2 and 3, however, in Fig. 2A additional nozzles 65 are arranged in the upper right-hand corner of the tubular member 20, whereby fluid under pressure as indicated by the arrows 65' ls blown along the surface 66 of a gulde member 67 to further aid in the transporting of the elongated material 1. The guide mem-ber 67 is mounted with it~ left-hand end to a wall extension 27a in the same manner as was described above with reference to the end o the leg 25 that is mounted to the wall extension 27.
Here again, due to the suction effect by the flowing fluid indi-cated by the arrow 65' there i~ a tendency of the elongated material 1 to contact a contact surface 21d of the tubular member 20.
In Fig. 3 the short leg 25 of the gulde body 4 extends at a small angle 26 relative to the wall extension 27 to modify the wedge shape of the wedge space between the ~urface 23 and the elongated material 1. The wedge shape is such, that the widest opening into the wedge space is located ln a plane 14 defined by the outer surface of the wall 21 in the extension 21b of which the nozzles 15, 16 are located. The narrowest section of the wedge space is located at the zone 18 where a direction change begins. The spacing 17 between the plane 14 and the zone 18 should be such that the fluid flow 64 can extend substantially tangentially to the surface of the guide body 4 2~81.~
; 1 at the point 18 where directlon change begins. If the spacing 17 - is too short, the fluid flow 64 will not coincide with the travel direction or transport direction 8 in the inlet to the zone 18.
If the space 17 is too large, the ~peed of the fluid flow may have become too ~mall for a proper feed advance of the elongated material 1. Further, the spacing 17 should also not be 80 long that an undesirable whirling of the fluld flow begins, causing a lateral expansion of the flow fluid.
,~ i In operation, the elongated material is first inserted into the ~ 10 chamber 33. For this purpose a side wall, functioning as a cover, i8 removed. Once the 1nsertion is completed 80 that the elongated material 1 passes around each of the direction changing stations 34 to 38, and the chamber i8 closed again, transport fluid under pressure is introduced into the tubular members 24 passing through the nozzles 15 and 16 to travel in the direction Z~ of the arrows 64. The fluid under pressure pushes itself between the material 1 and the surface 3 of the curvea section 5 of the guide body 4 at the point 8 where the direction change begins.
The fluid under pressure keeps lifting off the material 1 from the surface 3 to form a travelling cushion between the surface 3 and the material 1. As a result, the material 1 18 entrained by the fluid flow which thus transports the materlal 1 ln the direc-tion 8 from the inlet side 6 to the outlet side formed by the surface 7 of the guide body4. Such transport is substan-tially free of friction.The number of direction changing stations will depend on the dwell time needed for the particular treatment.
By varying the flow speed of the flowing transport fluid and/or by varying the mass throughput of the flowing fluid through the nozzles, it is possible to apply a transport spéed to the elongated 2 ~ S
1 material 1 with due regard to the characteristics of the material.
The influencing of the transport speed may be performed individually at each direction changlng station. For this purpose the speed sensors 39 to 42 are located in proper positions to sense the speed of the material 1 at these positions and to produce respec-tive control signals. Thu~, it is possible to take into account any flexible stretching or any shrinking of the material at dif-ferent points along the travelling path through the treatment zone. If the material shrinks due to the treatment, more ma-terial must be fed into the apparatus than will be carried outof the apparatus. The present control can be adju6td to such an operating condition. Simllarly, if the, material stretches due to the treatment, more material must be taken out of the chamber than is being passed into the chamber. Here again, a very individual adaptation of the feed advance i8 achieved according to the invention so that undesirable tension 6tre6s is not applied to the material 1.
In connection with the shrinking, it is, for example, known, based on experience and experiments, how much shrinking will 2n take place. Thus, the required speed reduction in response to the shrinking is a scalar amount that i~ known and the speed can be controlled accordingly. The inlet speed can first be adjusted at the guide station 34 by controlllng the valve 43.
The so established initial speed is then sensed by the sensor 39 to provide a signal on the conductor 53 to the central proces-sing unit 48 which now knows the speed upstream of the station 34.
The further speed sensor 40 just downstream of the station 34 provides a further speed signal on the conductor 54 to the - . ..: . - - ~ . . -.. . :;, ~ ., , : . :, - . .., :,. ...
23 2 0 ~
1 central processing unlt 48. Thus, it can be ascertained first whether the station 34 indeed transports the material 1 in the direction 8 and if the speed at 39 differs from the speed at 40, a shrinking or stretching 1B recognized. AB a result, the valve 43 can be controlled for providing the required adjust-ment of the flow speeds in the statlon 34.
If no shrinking or lengthening or stretching is noted at the inlet guide station 34, the speed measuring stations 41 and 42 still may provide further speed signals through the conductors 55 and 56 to the central processing unit to make ~ure that the same transport speed prevalls at the respective direction chang-ing stations to make sure that the quantity of material fed into the chamber 33 is also removed from the chamber 33, thereby providing an indication that no jamming takes place inside the chamber. However, if a shrinking does take place, the sensors 41 and 42 provide respective slower speea signals and the speed of the jet~ may be adjusted accordingly through the control valves 44 to 47 as controlled by the central proces~ing unit 48 through the conauctors 58 to 61. Some or all of the guide sta-`. 20 tions may be provided with their respective speed sensors up-. stream and/or aownstream of these stations 34 to 38.
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The central processing unit 48 shown in Fig. 6 has been des-cribed so far as controlling the flow control valves for the indiviaual stations 34 to 38. Nowever, the same control system :~ can be applied to controlling individual nozzles at one guide station. Thus, if the material 1 aoes not have a homogeneous :. structure across its width, the individual nozzle holes lS, 16 .,, ~
2 0 ~
1 may be aonnected to indlvidual ~luld flow ~upply pip~ or hoee~
r~ther th~n to A aommon c,h~mber in ~ tubul~r memb~r 20 a~ d~cribed above. ~hus, the ~u~d 10w can be lndlvldually And ~ensitively eontrolled in ~ccordance wlth the rQqulrQment~ of Any particul~r type o~ materi~l to b~ tran~ported. ~n ~ddltion to cont~olllng the flow speed, it i8 po~lble ~o modlf~ the compo~itlon ~nd denslty of the flowing tr~nsport ~luid in order to mlnlmlze any di~tortlon of the mhteri~l to be treAted.
The preeent method ~nd apparatuq tran~port the type of mater~als m~ntloned sub~ntlally fre~ of d~to~t~on~ bsaAu~e th~ tcn~on I ~t.r~ e~ harQt~f~rQ h~ h~n mlnlm~ by the ~e-crlbed ~eature~ And bec~u~e the direction re~er~lng frl¢tlonal forces ~nd/~r dr~gglng forca~ ha~e been reduced to such ~m~ lu~
¦ that the~e force~ can now be di~regarded.
Although the ln~entlon ha- been de4crlbe~ with refer-nce to speclftc ex~mple embodimente lt wlll be appr-ci~ted th~t it ~
~ Intended to aover all modifiaatlon~ and equl~ nt~ withln the : ecope of the appended alalm~.
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Claims (40)
1. A method for reducing a transporting strain on elongated flat material passing through a treatment chamber, comprising the following steps:
(a) transporting said elongated material with a transporting speed through said treatment chamber having an inlet and an outlet for said elongated material, whereby a transport direction is from said inlet to said outlet, (b) guiding said elongated material at least around one travel direction changing guide means defining a zone where a direction change begins between said inlet and said outlet, (c) forming a space of substantially triangular cross-section bounded by a straight portion of said guide means upstream, as viewed in said transport direction, of said direction change zone, by a nozzle wall, and by said elongated flat material, whereby said straight portion merges, away from said nozzle wall, into a curved portion of said guide means where said direction change zone begins, (d) introducing at least one flowing fluid jet through said nozzle wall into said space of substantially triangular cross-section at least approximately in said transport direction and substantially in parallel to said straight guide means portion upstream of said direction change zone of said travel direction changing guide means as viewed in said travel direction, whereby a force component extending radially to said travel direction around said guide means is substantially reduced to thereby reduce said strain, and (e) imparting to said flowing fluid jet a flow speed corresponding at least to said transporting speed for transporting said elongated material through said chamber.
(a) transporting said elongated material with a transporting speed through said treatment chamber having an inlet and an outlet for said elongated material, whereby a transport direction is from said inlet to said outlet, (b) guiding said elongated material at least around one travel direction changing guide means defining a zone where a direction change begins between said inlet and said outlet, (c) forming a space of substantially triangular cross-section bounded by a straight portion of said guide means upstream, as viewed in said transport direction, of said direction change zone, by a nozzle wall, and by said elongated flat material, whereby said straight portion merges, away from said nozzle wall, into a curved portion of said guide means where said direction change zone begins, (d) introducing at least one flowing fluid jet through said nozzle wall into said space of substantially triangular cross-section at least approximately in said transport direction and substantially in parallel to said straight guide means portion upstream of said direction change zone of said travel direction changing guide means as viewed in said travel direction, whereby a force component extending radially to said travel direction around said guide means is substantially reduced to thereby reduce said strain, and (e) imparting to said flowing fluid jet a flow speed corresponding at least to said transporting speed for transporting said elongated material through said chamber.
2. The method of claim 1, wherein said step of introducing comprises blowing a gas for forming said flowing fluid jet for transporting said elongated material.
3. The method of claim 1, wherein said step of introducing comprises blowing a liquid for forming said flowing fluid jet for transporting said elongated material.
4. The method of claim 1, further comprising filling a flowable treatment medium into said treatment chamber independently of said introducing step.
5. The method of claim 4, using as said flowable fluid for transporting said elongated material a first fluid and using as said treatment medium a second fluid, said first and second fluids having substantially the same composition.
6. The method of claim 1, wherein said guiding step comprises guiding said elongated material at least partially around a plurality of guide means, providing each guide means with at least one jet nozzle, and controlling said flow speed of said flowing fluid jets in such a way that at least one flowing fluid jet has a flow speed that differs from other flow speeds.
7. The method of claim 6, wherein said control is performed so that each of said fluid jets has a different flow speed.
8. The method of claim 1, wherein said flow speed is so controlled that a required transport speed for said elongated material is assured at the respective guide means.
9. The method of claim 1, wherein said step of introducing comprises blowing said flowing fluid jet with a jet width across said elongated material, said jet width corresponding to a width of said elongated material.
10. The method of claim 1, wherein said step of introducing comprises blowing said flowing fluid jet with a jet width, as viewed across a material width of said elongated material, which jet width is less than said material width.
11. The method of claim 1, wherein said flow speed is controlled so that different flow speeds are effective along the width of said elongated material.
12. The method of claim 1, wherein said step of introducing comprises forming said flowing fluid jet as a plurality of individual jets along a width of said elongated material, said individual jets having fluid densities which differ along said width of said elongated material.
13. The method of claim 1, wherein said step of introducing comprises producing a plurality of individual fluid jets and directing said individual jets substantially in said transport direction.
14. The method of claim 13, further comprising producing said individual fluid jets to have an approximately circular cross-section.
15. The method of claim 1, wherein said step of introducing comprises producing at least one fluid jet having a flow cross-sectional area that is substantially longer in one direction than in a direction perpendicularly to said one direction.
16. An apparatus for reducing a transporting strain on elongated flat material passing through a treatment operation in a travel direction, comprising a treatment chamber for treating said elongated material, said chamber having an inlet and an outlet defining a transport direction from said inlet to said outlet, means for transporting said elongated material from said inlet to said outlet, said transporting means including at least one material guide means having a curved material guide surface for changing the travel direction of said elongated material between said inlet and said outlet, whereby said material guide means define a direction change zone where a direction change begins, said material guide means further having a straight portion merging into said curved material guide surface, and fluid flow means including a nozzle wall upstream of said straight portion, as viewed in said travel direction, said nozzle wall, said straight portion and said flat material bounding a space of substantially triangular cross-section tapering toward a point where said guide means begin changing said travel direction in said direction change zone for introducing substantially in said travel direction at least one flowing fluid jet into said space of substantially triangular cross-section between said straight portion of said material guide means and said elongated flat material, whereby a force component extending radially of said curved material guide surface is substantially reduced for reducing said strain, said fluid flow means imparting to said flowing fluid a flow speed corresponding at least to a transporting speed of said elongated material.
17. The apparatus of claim 16, wherein said fluid flow means comprise at least one nozzle means directed for blowing a jet of said flowing fluid into a direction change zone where a change in the travel direction of said elongated material begins, said nozzle means being arranged at a spacing upstream of said direction change zone, said guide means having, in addition to said material guide surface, a material contact surface upstream of said material guide surface, said material contact surface spacing said elongated material from said material guide surface to lead said elongated material at a slant toward said direction change zone, thereby forming said wedge space into which said nozzle means blows.
18. The apparatus of claim 17, wherein said nozzle means comprise at least one group of a plurality of individual blow nozzles.
19. The apparatus of claim 18, wherein said individual blow nozzles are arranged substantially across the entire width of said elongated material.
20. The apparatus of claim 18, wherein said individual blow nozzles are arranged substantially in a row along a line, especially a straight line with a spacing between neighboring nozzles so that there is no fluid flow where said spacings are.
21. The apparatus of claim 18, wherein said nozzle means comprise two groups of individual blow nozzles forming two rows of nozzles.
22. The apparatus of claim 18, wherein said individual blow nozzles have different blow influencing characteristics.
23. The apparatus of claim 18, further comprising supply means for supplying pressurized fluid individually and/or in common to said blow nozzles or groups of blow nozzles.
24. The apparatus of claim 23, wherein said supply means for supplying pressurized fluid to said nozzle means comprise a tubular member having at least one flat wall, and wherein said blow nozzles comprise nozzle holes in said one flat wall, said nozzle holes being located close to said material contact surface.
25. The apparatus of claim 24, wherein said tubular member comprises a pipe section of rectangular cross-section, said nozzle holes including a first set of nozzle holes in said pipe section facing in said travel direction upstream of said direction change zone and a second set of nozzle holes in said pipe section facing in said travel direction downstream of said direction change zone.
26. The apparatus of claim 25, wherein said pipe section has a first wall extension in parallel to said first set of nozzle holes and a second wall extension in parallel to said second set of nozzle holes, said wall extension supporting guide wall elements of said guide means.
27. The apparatus of claim 24, wherein said guide means comprise an approximately U-shaped wall member having two guide legs and a curved guide section interconnecting said two guide legs, one guide leg contacting with its leg end said flat wall of said tubular member at a location next to said nozzle holes, the other guide leg contacting said tubular member remote from said nozzle holes, said one guide leg having a surface forming part of said wedge space with said elongated material upstream of said direction change zone, so that said nozzle holes can blow into said wedge space.
28. The apparatus of claim 27, wherein said tubular member has at least two flat walls extending substantially perpendicularly to each other, one of said flat walls having said nozzle holes therein and extending substantially perpendicularly to said travel direction, the other of said flat walls extending substantially in the travel direction, said two guide legs of said U-shaped wall member having a first shorter leg reaching to said one flat wall next to said nozzle holes, and a second longer leg extending in parallel to the other flat wall of said tubular member.
29. The apparatus of claim 27, wherein said surface of said one guide leg of said U-shaped wall member is inclined toward said direction change zone for influencing the shape of said wedge space.
30. The apparatus of claim 27, wherein said curved guide section (5) of said U-shaped wall member has a semicircular cross-sectional configuration.
31. The apparatus of claim 27, wherein said U-shaped wall member with its curved guide section its guide legs is an integral structure of bent sheet material.
32. The apparatus of claim 31, wherein said integral structure is bent of flat sheet metal.
33. The apparatus of claim 27, wherein said flat wall of said tubular member has a wall extension running in parallel to said nozzle holes and perpendicularly to said flat wall of said tubular member for providing a mounting support for said one guide leg of said U-shaped wall member.
34. The apparatus of claim 27, wherein at least said curved guide section of said U-shaped wall member has grooves in its surface facing said elongated material.
35. The apparatus of claim 27, wherein at least said curved guide section of said U-shaped wall member has a polished surface facing said elongated material.
36. The apparatus of claim 27, wherein at least said curved guide section of said U-shaped wall member has a roughened surface facing said elongated material, said roughened surface having a roughness measured in the micron range.
37. The apparatus of claim 27, wherein at least said curved guide section of said U-shaped wall member has a coated surface with a coating of synthetic material.
38. The apparatus of claim 24, wherein said tubular member comprises connector means for connection to pressurized fluid supply means.
39. The apparatus of claim 24, wherein siad tubular member has a substantially rectangular cross-sectional configuration mounted in said treatment chamber so that ends of said tubular member are sealed against inner surfaces of walls of said treatment chamber.
40. The apparatus of claim 16, further comprising means for measuring said transporting speed of said elongated material to produce transport speed signals, said fluid flow means comprising controllable fluid volume control means, said apparatus further comprising a central processing unit having inputs connected to receive said speed signals and control outputs connected to said fluid volume control means for controlling the supply of fluid in response to said transport speed signals.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DEP3901782.6 | 1989-01-21 | ||
| DE3901782A DE3901782A1 (en) | 1989-01-21 | 1989-01-21 | METHOD FOR THE LOW-DISTURBINE TRANSPORT OF TAPE-SHAPED PRODUCTS AND DEVICE THEREFOR |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CA2008155A1 CA2008155A1 (en) | 1990-07-21 |
| CA2008155C true CA2008155C (en) | 1994-05-03 |
Family
ID=6372549
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CA002008155A Expired - Lifetime CA2008155C (en) | 1989-01-21 | 1990-01-19 | Method and apparatus for reducing a transporting strain on elongated material passing through a treatment chamber |
Country Status (6)
| Country | Link |
|---|---|
| EP (1) | EP0379685B1 (en) |
| JP (1) | JPH02231352A (en) |
| AT (1) | ATE78451T1 (en) |
| CA (1) | CA2008155C (en) |
| DE (2) | DE3901782A1 (en) |
| ES (1) | ES2034569T3 (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2000039011A2 (en) * | 1998-12-23 | 2000-07-06 | Bachofen + Meier Ag Maschinenfabrik | Device for guiding or treating a continuous line of material in a contactless manner, especially a line of paper or cardboard or a metal or plastic film |
| JP2012056683A (en) * | 2010-09-08 | 2012-03-22 | Ihi Corp | Air float system |
Family Cites Families (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE1215465B (en) * | 1961-02-18 | 1966-04-28 | Svenska Flaektfabriken Ab | Device for deflecting running webs |
| ES274570A1 (en) * | 1961-02-18 | 1962-10-16 | Svenska Flaektfabriken Ab | Means for turning or reversing the direction of movement of web-shaped material at the end of a run |
| GB1016703A (en) * | 1962-04-16 | 1966-01-12 | British Iron Steel Research | Improvements relating to fluid pressure support bearings |
| CH473038A (en) * | 1967-05-16 | 1969-05-31 | Ciba Geigy | Deflection device for strip-shaped material |
| GB1307695A (en) * | 1970-08-19 | 1973-02-21 | Ilford Ltd | Air flotation turner bars |
| US4055003A (en) * | 1975-08-28 | 1977-10-25 | Johnson & Johnson | Method and apparatus for altering the rigidity of webs by oscillation |
| CH599893A5 (en) * | 1976-12-17 | 1978-06-15 | Bachofen & Meier Maschf | |
| US4182472A (en) * | 1978-07-13 | 1980-01-08 | W. R. Grace & Co. | Contactless turning guide for running webs |
| US4197972A (en) * | 1978-08-28 | 1980-04-15 | W. R. Grace & Co. | Contactless turning guide having air slots longitudinally along running web edges |
| US4342413A (en) * | 1981-02-05 | 1982-08-03 | Crown Zellerbach Corporation | Turning bar for moving web |
| JPS58188248A (en) * | 1982-04-28 | 1983-11-02 | Anritsu Corp | Tape feeder |
| GB8704721D0 (en) * | 1987-02-27 | 1987-04-01 | Molins Plc | Cigarette paper feed |
-
1989
- 1989-01-21 DE DE3901782A patent/DE3901782A1/en not_active Withdrawn
- 1989-12-06 EP EP89122505A patent/EP0379685B1/en not_active Expired - Lifetime
- 1989-12-06 ES ES198989122505T patent/ES2034569T3/en not_active Expired - Lifetime
- 1989-12-06 AT AT89122505T patent/ATE78451T1/en not_active IP Right Cessation
- 1989-12-06 DE DE8989122505T patent/DE58901891D1/en not_active Expired - Lifetime
-
1990
- 1990-01-09 JP JP2001150A patent/JPH02231352A/en active Pending
- 1990-01-19 CA CA002008155A patent/CA2008155C/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| ES2034569T3 (en) | 1993-04-01 |
| EP0379685B1 (en) | 1992-07-22 |
| EP0379685A2 (en) | 1990-08-01 |
| JPH02231352A (en) | 1990-09-13 |
| ATE78451T1 (en) | 1992-08-15 |
| CA2008155A1 (en) | 1990-07-21 |
| DE58901891D1 (en) | 1992-08-27 |
| DE3901782A1 (en) | 1990-08-02 |
| EP0379685A3 (en) | 1990-12-19 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| EEER | Examination request | ||
| MKEX | Expiry |