EP1675989B1 - Procede et dispositif de conditionnement d'un processus - Google Patents

Procede et dispositif de conditionnement d'un processus Download PDF

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Publication number
EP1675989B1
EP1675989B1 EP04790717A EP04790717A EP1675989B1 EP 1675989 B1 EP1675989 B1 EP 1675989B1 EP 04790717 A EP04790717 A EP 04790717A EP 04790717 A EP04790717 A EP 04790717A EP 1675989 B1 EP1675989 B1 EP 1675989B1
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EP
European Patent Office
Prior art keywords
gas stream
primary
flow
conditioning
stream
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
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EP04790717A
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German (de)
English (en)
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EP1675989A1 (fr
Inventor
Hubert Wassenhoven
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Voith Patent GmbH
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Voith Patent GmbH
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    • D—TEXTILES; PAPER
    • D03—WEAVING
    • D03J—AUXILIARY WEAVING APPARATUS; WEAVERS' TOOLS; SHUTTLES
    • D03J1/00—Auxiliary apparatus combined with or associated with looms
    • D03J1/008—Cooling systems
    • D—TEXTILES; PAPER
    • D03—WEAVING
    • D03J—AUXILIARY WEAVING APPARATUS; WEAVERS' TOOLS; SHUTTLES
    • D03J1/00—Auxiliary apparatus combined with or associated with looms
    • D03J1/002—Climatic conditioning or removing lint or dust

Definitions

  • the invention relates to a method and a device for conditioning at least one process area.
  • conditioning systems In weaving machines for cleaning or dedusting of machine zones, in particular the supplied warps, conditioning systems are known which direct a directed air jet with relatively high flow rate to the process area to be conditioned via a slot-shaped outlet opening and dedust the machine zones, in particular the warps, by blowing off.
  • the slot-shaped outlet extends transversely to the warp over its full width and emits a directed against the warp beam conditioned air.
  • the conditioning size in these conditioning systems is the absence of dust or purity and possibly also the air humidity of the process area, in particular the warp threads.
  • a certain disadvantage is the relatively high induction by entrainment and mixing with ambient air, which is generally not or less conditioned, which reduces the conditioning performance, in particular increases the dust input to the conditioned air by induction-induced intake of dust from the ambient air.
  • Such systems are for example in EP 0 558 718 B1 described as prior art.
  • a method and a device for conditioning of looms are known in which the climate is locally influenced directly on the loom, so a space area is conditioned on the weaving machine.
  • a flow referred to as a "piston-like displacement flow” is understood to mean approximately uniform distribution over its full cross section and an approximately equal speed. Outlet speeds between 0.3 and 1.2 m / s are set for the air flow.
  • the climate air is at this known system used for wetting the warp of the loom.
  • Conditioner size is therefore the moisture content of the air.
  • the room and process air can be controlled with a climate system.
  • the invention is based on the object of specifying a method and a device for conditioning a process in at least one process area, in which the disadvantages mentioned in the prior art are at least partially reduced or completely avoided.
  • the apparatus according to claim 12 is suitable for conditioning at least one process area or process in at least one process area and / or performing a method according to the invention and comprises means for generating at least one conditioning gas stream to be fed to the or each process area; wherein at least one conditioning gas stream comprises at least one primary gas stream and at least one secondary gas stream, the secondary gas stream substantially completely enclosing the primary gas stream and the primary gas stream having at least a higher average flow rate than the secondary gas stream.
  • the invention is based on the idea of embedding or enclosing a stream of primary gas at a comparatively high flow rate in a secondary flow of gas at a lower flow rate.
  • the secondary gas flow thus surrounds the primary gas flow at a peripheral surface or outer surface enclosing the flow lines or flow direction of the primary gas flow, so that ambient air can not enter the primary gas flow directly from there.
  • the induction of ambient air in the rapidly flowing primary gas flow and thus a distortion of the conditioning of the primary gas flow through the ambient air is thus reduced or even completely prevented.
  • the primary gas stream with the high flow velocity also carries with it the secondary gas flow and aligns with it in accordance with the flow guidance of the primary gas stream.
  • a conditioning gas flow is generated, which has quite a comparable directional characteristic as a known air jet according to the aforementioned prior art, but on the other hand, less sensitive to a negative effect on the conditioning by induction of ambient air than an air jet in the prior art.
  • the primary gas stream (s) are generally at least partially turbulent, while the secondary gas stream (s) is at least partially diffused and / or at least partially laminar.
  • the average flow rate of the or each primary gas stream is preferably at least twice, in particular at least five times and preferably at least ten times higher than the mean flow velocity of the or each associated secondary gas stream.
  • the average flow rate of the or each primary gas stream at least initially, is between about 6 m / s and about 20 m / s and / or the mean flow velocity of the or each secondary gas stream, at least initially, between about 0.1 m / s and about 2 m / s.
  • At least one and preferably each primary gas flow is adjusted along a predetermined or predefinable main flow direction or in the manner of a jet. It is particularly advantageous if the primary gas stream aligns and / or stabilizes the secondary gas flow at least approximately parallel to the primary gas flow and / or along the set main flow direction.
  • the secondary gas flow in turn reduces the induction of non-conditioned ambient air through the primary gas flow, in particular practically completely.
  • At least one primary outlet opening is provided and for the or each secondary gas flow at least one secondary outlet opening surrounding the primary opening (s).
  • At least one primary gas stream is divided into an inner partial stream and at least one outer partial stream, wherein the secondary gas stream is passed together with the outer partial stream of the primary gas stream and the outer partial stream substantially completely surrounds and the inner partial stream of the primary gas stream initially within at least one Flow channel (primary flow channel) is guided separately from the outer partial flow and downstream is reunited with the outer partial flow.
  • Flow channel primary flow channel
  • At least one outer partial flow of the primary gas flow preferably flows at least partially along the outer side of the flow channel for the inner partial flow.
  • the flow direction of the inner partial flow of the primary gas flow in the flow passage generally corresponds at least at the exit from the flow passage substantially the main flow direction of the primary gas flow after union of the inner partial flow and outer partial flow.
  • the primary gas flow or the inner partial flow of the primary gas flow or the flow channel can be adjusted or moved within a predetermined solid angle range, in particular continuously or periodically and / or pivotally, oscillatingly or circling.
  • the process area to be conditioned or conditioned is then generally within the solid angle range detected by the primary gas flow or its inner partial flow.
  • the conditioning gas stream initially decreases in its flow cross-section to a constriction area in which the conditioning gas flow has the smallest flow cross-section, and then widens again.
  • This narrowing zone of the conditioning gas stream is placed in the process area to be conditioned or conditioned.
  • the transverse dimensions of the secondary gas flow measured from the primary gas flow to the outside or the flow cross section of the secondary gas flow are greater than the corresponding dimensions or the corresponding flow cross section of the primary gas flow, in particular by at least a factor of 2, preferably by at least a factor of 4 and in particular to one Factor 10.
  • the longitudinal dimension of the secondary gas stream and / or the primary gas stream downstream, as far as the process area, is preferably selected between 0.1 m and 1.5 m.
  • At least one primary gas stream or at least one primary outlet opening has a substantially rectangular and / or elongate and / or long slot-shaped flow cross-section.
  • the flow cross-section of at least one primary gas stream or at least one primary outlet opening closed in itself, extending around an interior, in particular annular, is formed.
  • At least one primary outlet opening is preferably designed as a nozzle.
  • a secondary gas stream can be generated in the interior space within a primary gas stream and a further secondary gas stream can be generated at the outside of the primary gas stream facing away from the interior, in particular in a concentric arrangement.
  • at least two primary gas streams may be embedded in or surrounded by at least one common secondary gas stream.
  • means are provided for generating the at least one conditioning gas stream, which in addition to at least one primary outlet opening as outlet for the primary gas stream and at least one secondary outlet opening as outlet for the secondary gas supply Zuleitsch, in particular at least one Zuleitkanal for supplying conditioning gas, wherein the Zuleitstoff with the at least one Primary outlet opening and the at least one secondary outlet opening are in flow communication or can be brought.
  • At least one group of a plurality of secondary outlet openings is provided, which are arranged around the at least one or a group of primary outlet opening (s).
  • At least one group of secondary outlet openings may extend over an area essentially bounded by a rectangle and / or lie substantially in a common group plane, which is preferably substantially parallel to an exit plane of at least one primary exit opening or coincides or inclined, in particular, with this exit plane perpendicular to an exit plane of at least one primary outlet opening.
  • the primary outlet opening (s) and the associated secondary outlet opening (s) of at least one conditioning gas flow are in fluid communication with a common supply channel, so that the conditioning gas from this supply channel forms both the at least one primary gas stream and the at least one secondary gas stream of the conditioning gas stream.
  • a common supply channel so that the conditioning gas from this supply channel forms both the at least one primary gas stream and the at least one secondary gas stream of the conditioning gas stream.
  • Zuleitkanälen for supplying each of a conditioning gas possible.
  • the means for generating the conditioning gas stream expediently comprise at least one housing, in the housing wall of which the primary outlet opening (s) and the secondary outlet opening (s) are formed at least in one outlet region.
  • the outlet region connected to the Zuleitschn or adjacent to the Zuleitkanal inlet region of the housing wall are in one embodiment, at least one primary inlet opening in fluid communication with the or the primary outlet opening (s) or can be brought, and at least one secondary inlet opening, with the or the secondary outlet opening (s) is in flow connection or can be brought formed.
  • At least one primary flow channel can be formed, which connects the primary inlet opening (s) to the primary outlet opening (s) and in which preferably flow rectifiers are arranged or can be arranged for rectification and / or equalization of the flow.
  • the housing preferably has on two opposite sides of the primary flow channel two housing parts, in particular substantially symmetrical to the primary flow channel, on whose outer walls both the secondary inlet opening (s) and the secondary outlet opening (s) are arranged and in each of which a secondary flow channel is formed, which connects the secondary inlet opening (s) with the or the secondary outlet opening (s).
  • At least one pre-distributor with a plurality of passage openings can be arranged within the housing in the flow path between the secondary inlet opening (s) and the secondary outlet opening (s).
  • the or each primary gas stream and / or the or each secondary gas stream are generally substantially stationary, that is, constant in time, during conditioning.
  • the conditioning gas stream generally sets at least one conditioning quantity in the associated process area, in particular the moisture content and / or the temperature and / or the purity and / or the sterility and / or the composition of the gas atmosphere in the process area.
  • the conditioning variable (s) in the at least one primary gas stream and in the associated at least one secondary gas stream of the conditioning gas stream are set substantially the same, but may also be set differently from one another.
  • a preferred application or use of the method and the apparatus is in a textile production process and / or for conditioning a process area on or within a textile machine, in particular a loom, preferably in the field of warp.
  • Zuleitkanal 7 a conditioning device is shown, which extends horizontally and is fed through the direction of the arrow shown a conditioning gas 6, which is conditioned with a K conditioningier discourse.
  • a conditioning gas 6 which is conditioned with a K conditioningier discourse.
  • At the bottom of Zuleitkanals 7 are above two separate process areas 5 and 5 'of a process plant, not shown, in which processes or sub-processes are performed, each a housing 10 or 10' of the conditioning arranged.
  • a primary inlet opening with 23 and secondary inlet openings are designated by 26.
  • the inlet openings are not further specified.
  • On a downwardly directed bottom of the housing 10 and 10 'outlet openings are provided, from which the conditioning gas 6 down to the associated process area 5 and 5' emerges out.
  • These outlet openings comprise in FIG. 1 in each case a central primary outlet opening 13 or 13 'and this primary outlet opening 13 or 13' surrounding secondary outlet openings 14 and 14 'on the housing 10 or 10'.
  • the primary inlet opening 23 at the top of the housing 10 is for forwarding the passing of the Zuleitkanal 7 through them conditioning gas 6 to the primary outlet opening 13 with the primary outlet opening 13 on the underside of the housing 10 via a central slot-shaped primary flow channel 15 connected and points according FIG. 1 the same width as the primary outlet opening 13.
  • the secondary inlet openings 24 of the housing 10 are connected to the secondary outlet openings 14 via one or more secondary flow channels 16 for forwarding the conditioning gas 6.
  • the primary gas flow 3 is set by adjusting the flow velocity VP as a function of the conditioning gas 6 used as a turbulent flow.
  • the primary outlet opening 13 and the primary inlet opening 23 preferably together with the primary flow channel 15 connecting them form a nozzle, in particular a slot nozzle.
  • the secondary gas flow 4 surrounding the primary gas flow 3 is generated as a diffuse flow or at least partially laminar flow.
  • the average flow velocity VS or VS 'of the secondary gas flow 4 or 4' is kept low, in particular due to the high flow resistance of the secondary outlet openings 14 and 14 'and the turbulence in the secondary flow channel 16, and in particular smaller than VP or VP'.
  • the flow velocity VP of the primary gas stream 3 is usually set between 6 m / s and 20 m / s.
  • the flow velocity VS of the secondary gas flow 4 is significantly lower, usually at 0.1 m / s to 2 m / s.
  • the primary gas flow 3 or 3' Due to its high flow velocity VP or VP ', the primary gas flow 3 or 3' carries the slower secondary gas flow 4 or 4 'as a result of the suction effect or induction caused thereby, so that the Secondary gas stream 4 or 4 'still receives a directional characteristic despite its initially substantially underengered character and is carried substantially parallel to the primary gas stream 3 and 4'.
  • the primary gas flow 3 or 3 remains relatively concentrated due to the high flow velocity VP or VP' or diverges only slightly.
  • the secondary gas stream 4 or 4 'initially converges due to the fluid-dynamic conditions up to a constriction region 20 or 20' and then expands again (or: diverges).
  • the conditioning gas stream 2 or 2 'composed of primary gas flow 3 or 3' and secondary gas flow 4 or 4 ' is now adjusted so that the constriction point or narrowing region 20 or 20' comes to lie in the process region 5 or 5 ', respectively Length 1 or 1 'of the conditioning gas flow 2 or 2' from the outlet openings 13 or 13 'and 14 or 14' in the flow direction to the process area 5 or 5 'thus covers a convergent region of the secondary gas flow 4 or 4'.
  • Laying the process area 5 or 5 'in the focused area or narrowing area 20 or 20' of the conditioning gas stream 2 or 2 ' has the advantage of a more precise setting of the conditioning size K.
  • the narrowing area 20 sets the maximum distance 1 in most applications or 1 'between air outlet and process area 5, in which the different flow velocities VP and VS of primary gas stream 3 and secondary gas stream 4 are still effective.
  • the pressure difference between the feed duct 7 and the downstream area into which the conditioning gas flow 2 or 2 'flows, in particular in the process area 5 or 5', is typically between 100 Pa and 500 Pa. is set and depends on the concrete embodiment of the flow guide and the flow outlets in the housing 10 or 10 'and the desired flow velocities VP or VP' and VS or VS 'for the primary gas stream 3 or 3' and the secondary gas stream 4 and 4 respectively '.
  • a double gas flow with different flow velocities is generated with an internal slot nozzle and outer diffuser outlet surrounding the slot nozzle.
  • the primary gas flow 3 or 3 ' serves as a support jet for the secondary gas flow 4 or 4'. Due to the high flow velocity VP or VP 'of the primary gas flow 3 or 3', it cleans the blown process area 5 or 5 'and any process plant parts or machine parts or products of dust deposits to be processed therein. Furthermore, the primary gas stream 3 or 3 'stabilizes the set direction of the entire conditioning gas stream 2 or 2' and increases the penetration depth of the surrounding, diffuse secondary gas stream 4 or 4 '. By contrast, the diffused secondary gas flow 4 exiting at a low flow velocity VS prevents the induction of unconditioned ambient air 28 and, in particular, reduces the entry of dust particles from the ambient air 28 into the conditioning gas flow 2 or 2 '.
  • any number of process areas 5, 5 'or machine zones can be supplied with conditioned gas by means of distribution devices integrated in the device, such as housings 10 and 10'.
  • FIG. 2 now shows a concrete embodiment of a device for conditioning a process area 5 with an elongated housing 10 for generating an elongated conditioning gas flow 2.
  • the housing 10 comprises two symmetrical with respect to a median plane M (which in FIG. 2 only as a central axis M in the front cross-section is shown) and formed housing parts 17 and 18, which are separated in the region of the median plane M by a primary flow channel 15 which is formed as a longitudinal slot.
  • a Zuleitkanal 7 for conditioning 6 arranged above the housing 10.
  • a primary flow channel 15 overlapping, plate-shaped Mengeneinstell 180 is arranged on the Zuleitkanal 7 facing upper flat sides of the housing parts 17 and 18.
  • the two housing parts 17 and 18 are connected or integrated with the side parts of the housing.
  • the encourageneinstell shark 33 comprises a central, above the primary flow channel 15 between the two housing parts 17 and 18 extending row of slots with linearly one behind the other and spaced apart slot-shaped primary inlet openings 23 and arranged on both sides of the row of primary inlet openings 23 each have a parallel row of spaced apart one behind the other Secondary inlet openings 24.
  • the secondary inlet openings 24 are in FIG. 2 around and provided with a respective baffle 34.
  • a quantity (volume flow or mass flow) of conditioning gas 6, which is defined by the flow cross section of these open secondary inlet openings 24, passes from the supply channel 7 into a respective secondary flow channel 16 within the associated housing part 17 and 18, as partially indicated by the arrows.
  • conditioning gas 6 is passed through a, designed in particular as a perforated plate, pre-manifold 19 with individual openings in a further secondary flow space 36 within the housing part 17 and 18 and then passes through on the lateral and lower outer wall of the housing 10 and the housing parts 17 and 18 of the housing 11 arranged secondary outlet openings 14 as a secondary gas stream 4 to the outside, as indicated by the flow arrows.
  • the flowing through the primary inlet openings 23 from the Zuleitkanal 7 flow of Konditioniergases 6 is aligned in the primary flow channel 15 and flows in a fixed predetermined by the primary flow channel 15 direction, which in the example of FIG. 2 down, that is parallel to gravity, is directed, from the primary outlet opening 13 as the primary gas stream 3 from.
  • rectifiers are preferably arranged which rectify the flow along the main flow direction, for example an arrangement of juxtaposed, for example rectangular, tubes which are separated from one another by walls.
  • the amount adjustment is preferably carried out by moving the encourageneinstell issued 33, namely the secondary gas stream 4 in the longitudinal direction and the primary gas flow 3 in the transverse direction and the change in the flow cross-section of the secondary inlet openings 24 or primary inlet openings 23 caused thereby.
  • FIG. 5 shows the exit of the primary gas stream 3 from the primary outlet opening 13 according to FIG. 2 in an enlarged and more detailed view.
  • the primary gas stream 3 is according to FIG. 2 and 5 immediately after exiting the primary outlet opening 13 into an inner primary part stream 31 and split into an outer primary part stream 32.
  • the inner partial flow 31 flows through a primary partial flow channel 27 adjoining the primary outlet opening 13, in the example of FIG. 2 down, along its main flow direction and then moves offset to the same at the same time on the outside of the Primärteilstromkanals 27 along outer partial flow 32 at the side facing away from the primary outlet opening 13 orifice portion primary exit 29 and then reunites with the outer partial flow 32 to a single Primary gas flow 3.
  • the diffused from the secondary outlet openings 14 flow of Konditioniergases 6 forms a (diffuse) secondary gas stream 4, which is also aligned by the directivity of the primary gas stream 3 down and envelops the primary gas stream 3.
  • the combination of primary gas stream 3 and 4 again forms a conditioning gas stream 2 which, in particular in the region of the constriction 20, is fed to the process region 5 to be conditioned.
  • 3 and 4 show in two different views an embodiment with concentrically arranged primary gas streams and secondary gas streams or primary outlet openings and secondary outlet openings.
  • the central primary outlet opening 13 and the central primary gas flow 3 have a substantially circular disk-shaped cross-section.
  • the primary outlet opening 13 is surrounded by a multiplicity of secondary outlet openings 21 which generate a first secondary gas flow 4 surrounding the central primary gas flow 3 and which has a substantially annular flow cross-section.
  • annular gap opening or self-contained primary outlet opening 12 is provided.
  • the primary outlet opening 12 is connected via an annular primary flow channel 25 to the supply channel 7 and generates an annular primary gas stream 8, which encloses the inner secondary gas stream 4.
  • This second primary gas stream 8 is now in turn enveloped by an outer secondary gas stream 9, which is generated by means of the second primary outlet opening 12 surrounding outer secondary outlet openings 22.
  • the outer secondary outlet openings 22 are similar to FIG FIG. 2 connected in each case via a secondary flow channel 26 in the housing 10 and not further designated inlet openings and secondary inlet openings with the supply channel 7.
  • the two primary gas streams 3 and 8 can cover different areas in the process area 5 and an improved cleaning effect or blow-off effect can be achieved.
  • the inner secondary gas flow 4 between the two primary gas streams 3 and 8 is very well managed and can thus effect a virtually lossless or virtually unattenuated conditioning in the process area 5.
  • the primary part flow channel 27 may be pivotable in a non-illustrated embodiment about a rotary joint or pivot bearing.
  • the pivot axis is located in the region of the primary outlet opening 13. This makes it possible to pivot the primary gas stream 3 in a solid angle range and thereby flow around this area with the primary gas stream 3.
  • the secondary gas stream 4 is carried along by the directional beam characteristic of the primary gas stream 3 during the pivoting movement.
  • the Primärteilstromkanal could also be pivoted in a ball joint or the like in two angular directions, that is spherical in a solid angle range.
  • the gas used for the conditioning gas 6 is in all embodiments usually air or a composition of air very similar gas, usually air from an outdoor space or the earth's atmosphere taken, cleaned and after exposure to the conditioning size (conditioning) in the supply channel. 7 is directed.
  • the conditioning of a process area 5 or a process-relevant zone made possible with the conditioning gas stream 2 according to the invention, in particular in the illustrated embodiments, is selected and can be dependent on the process taking place in this process area 5, in particular the products or process conditions (process conditions) to be passed there in principle, be any achievable with a gas flow conditioning a process or a process area.

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  • Engineering & Computer Science (AREA)
  • Textile Engineering (AREA)
  • Duct Arrangements (AREA)
  • Feeding, Discharge, Calcimining, Fusing, And Gas-Generation Devices (AREA)
  • Devices That Are Associated With Refrigeration Equipment (AREA)
  • Electrical Discharge Machining, Electrochemical Machining, And Combined Machining (AREA)

Claims (19)

  1. Procédé de conditionnement d'au moins une zone de traitement, dans lequel
    a) au moins un écoulement (2) de gaz de conditionnement est apporté dans la ou les zones de traitement,
    caractérisé en ce que
    b) ce ou ces écoulements de gaz de conditionnement comprennent
    b1) au moins un écoulement (3) de gaz primaire et
    b2) au moins un écoulement (4) de gaz secondaire,
    b3) l'écoulement de gaz secondaire entourant essentiellement complètement l'écoulement de gaz primaire et
    c) en ce que l'écoulement de gaz primaire présente une vitesse d'écoulement au moins en moyenne supérieure à celle de l'écoulement de gaz secondaire.
  2. Procédé selon la revendication 1, dans lequel le ou les écoulements de gaz primaire sont au moins partiellement turbulents et le ou les écoulements de gaz secondaire sont au moins partiellement diffus et/ou au moins partiellement laminaires, et/ou
    dans lequel la vitesse moyenne d'écoulement de l'écoulement de gaz primaire représente au moins deux fois, en particulier au moins cinq fois et de préférence au moins dix fois la vitesse moyenne d'écoulement de l'écoulement de gaz secondaire, et/ou
    dans lequel la vitesse moyenne d'écoulement du ou des écoulements de gaz primaire est réglée entre environ 6 m/s et environ 20 m/s au moins lors de leur sortie ou à leur extrémité située en amont et/ou
    dans lequel la vitesse moyenne d'écoulement du ou des écoulements de gaz secondaire est réglée entre environ 0,1 m/s et environ 2 m/s au moins à leur sortie ou à leur extrémité située en amont.
  3. Procédé selon la revendication 1 ou la revendication 2, dans lequel l'écoulement de gaz primaire est établi dans une direction principale d'écoulement prédéterminée ou prédéterminable et/ou dans lequel l'écoulement de gaz primaire oriente et/ou stabilise l'écoulement de gaz secondaire au moins sensiblement en parallèle à l'écoulement de gaz primaire et/ou le long de la direction principale d'écoulement qui a été établie.
  4. Procédé selon l'une ou plusieurs des revendications précédentes, dans lequel l'écoulement de gaz secondaire diminue et en particulier bloque pratiquement l'induction d'air ambiant non conditionné à travers l'écoulement de gaz primaire et/ou dans lequel l'écoulement de gaz primaire sort par au moins une ouverture de sortie primaire, en particulier une tuyère primaire, et l'écoulement de gaz secondaire sort d'au moins une ouverture de sortie secondaire qui entoure la ou les ouvertures primaires.
  5. Procédé selon l'une ou plusieurs des revendications précédentes, dans lequel l'écoulement de gaz primaire est divisé en un écoulement partiel intérieur et au moins un écoulement partiel extérieur, l'écoulement de gaz secondaire étant guidé en même temps que l'écoulement partiel extérieur de l'écoulement de gaz primaire et entourant essentiellement complètement l'écoulement partiel extérieur, l'écoulement partiel intérieur de l'écoulement de gaz primaire étant d'abord guidé à l'intérieur d'au moins un canal d'écoulement séparément de l'écoulement partiel extérieur et étant réuni de nouveau à l'écoulement partiel extérieur en aval, le ou les écoulements partiels extérieurs de l'écoulement de gaz primaire s'écoulant au moins en partie sur le côté extérieur du canal d'écoulement prévu pour l'écoulement partiel intérieur et/ou au moins lors de la sortie du canal d'écoulement, de préférence la direction d'écoulement de l'écoulement partiel intérieur de l'écoulement de gaz primaire dans le canal d'écoulement correspond essentiellement à la direction d'écoulement principale de l'écoulement de gaz primaire après rassemblement de l'écoulement partiel intérieur et de l'écoulement partiel extérieur.
  6. Procédé selon l'une ou plusieurs des revendications précédentes, dans lequel l'écoulement de gaz primaire, l'écoulement partiel intérieur de l'écoulement de gaz primaire ou le canal d'écoulement peuvent être établis, sont établis ou sont déplacés à l'intérieur d'une plage prédéterminée d'angles solides, l'écoulement de gaz primaire, son écoulement partiel intérieur ou le canal d'écoulement étant de préférence déplacés de manière permanente ou périodique à l'intérieur de la plage prédéterminée d'angles solides et étant en particulier déplacés par pivotement, de manière pendulaire ou en cercle, et/ou la zone de traitement à conditionner ou conditionnée est située à l'intérieur de la plage d'angles solides délimitée par l'écoulement de gaz primaire ou son écoulement partiel intérieur.
  7. Procédé selon l'une ou plusieurs des revendications précédentes, dans lequel, vue vers l'aval, la section transversale d'écoulement de l'écoulement de gaz de conditionnement diminue d'abord jusqu'à une zone rétrécie dans laquelle l'écoulement de gaz de conditionnement présente la plus petite section transversale d'écoulement et s'évase ensuite de nouveau, la zone rétrécie de l'écoulement de gaz de conditionnement étant située dans la zone de traitement à conditionner ou conditionnée.
  8. Procédé selon l'une ou plusieurs des revendications précédentes, dans lequel les dimensions de l'écoulement de gaz secondaire mesurées depuis l'écoulement de gaz primaire en direction de l'extérieur ou la section transversale d'écoulement de l'écoulement de gaz secondaire est supérieure en particulier d'au moins un facteur 2, de préférence d'au moins un facteur 4 et en particulier d'un facteur 10 aux dimensions correspondantes ou à la section transversale d'écoulement correspondante de l'écoulement de gaz primaire,
    dans lequel la longueur de l'écoulement de gaz secondaire et/ou de l'écoulement de gaz primaire vue dans la direction aval jusqu'à la zone de traitement est comprise entre 0,1 m et 1,5 m,
    dans lequel au moins un écoulement de gaz primaire présente une section transversale d'écoulement essentiellement rectangulaire et/ou allongée et/ou
    dans lequel au moins un écoulement de gaz primaire présente une section transversale d'écoulement qui s'étend de manière intrinsèquement fermée autour d'un espace intérieur, en particulier en forme d'anneau, un écoulement de gaz secondaire s'étendant en particulier dans l'espace intérieur à l'intérieur de l'écoulement de gaz primaire et un autre écoulement de gaz secondaire s'étendant sur le côté de l'écoulement de gaz primaire non tourné vers l'espace intérieur.
  9. Procédé selon l'une ou plusieurs des revendications précédentes, dans lequel au moins un écoulement de gaz primaire et au moins deux écoulements de gaz secondaire sont disposés de manière essentiellement concentrique les uns par rapport aux autres,
    dans lequel au moins deux écoulements de gaz primaire sont incorporés dans au moins un écoulement de gaz secondaire commun ou sont entourés par ce dernier et/ou
    dans lequel le ou les écoulements de gaz primaire et/ou le ou les écoulements de gaz secondaire sont essentiellement stationnaires.
  10. Procédé selon l'une ou plusieurs des revendications précédentes, dans lequel au moins une grandeur de conditionnement est ajustée avec l'écoulement de gaz de conditionnement dans la zone de traitement associée, tandis que comme grandeur ou grandeurs de conditionnement, on règle de préférence la teneur en humidité, la température, la pureté, l'absence de germes et/ou la composition de l'atmosphère gazeuse dans la zone de traitement et/ou
    dans lequel la ou les grandeurs de conditionnement ont été réglées ou sont réglées à des valeurs essentiellement identiques ou différentes l'une de l'autre dans au moins un écoulement de gaz primaire et dans le ou les écoulements de gaz secondaire associés de l'écoulement de gaz de conditionnement.
  11. Procédé selon l'une ou plusieurs des revendications précédentes, dans lequel le procédé est un procédé de fabrication de textile et/ou la zone de traitement est disposée sur ou à l'intérieur d'une machine textile, en particulier un métier à tisser, de préférence dans la zone occupée par la chaîne de tissage.
  12. Dispositif de conditionnement d'au moins une zone de traitement, en particulier en vue de l'exécution d'un procédé selon l'une des revendications 1 à 11, et comprenant :
    a) des moyens de formation d'au moins un écoulement de gaz de conditionnement qui peut être amené ou est amené dans la ou les zones de traitement, caractérisé en ce que
    b) ce ou ces écoulements de gaz de conditionnement comprennent
    b1) au moins un écoulement de gaz primaire et
    b2) au moins un écoulement de gaz secondaire,
    b3) l'écoulement de gaz secondaire entourant essentiellement complètement l'écoulement de gaz primaire et
    c) en ce que le ou les écoulements de gaz primaire présentent au moins en moyenne une vitesse d'écoulement plus élevée que le ou les écoulements de gaz secondaire associés.
  13. Dispositif selon la revendication 12, dans lequel les moyens de formation du ou des écoulements de gaz de conditionnement comprennent
    a) des moyens d'amenée qui amènent le gaz de conditionnement,
    b) au moins une ouverture de sortie primaire qui sert de sortie pour l'écoulement de gaz primaire et
    c) au moins une ouverture de sortie secondaire qui sert de sortie pour l'écoulement de gaz secondaire,
    d) les moyens d'amenée étant en communication d'écoulement ou pouvant être amenés en communication d'écoulement avec la ou les ouvertures de sortie primaires et/ou la ou les ouvertures de sortie secondaires.
  14. Dispositif selon la revendication 13, dans lequel la ou les ouvertures de sortie secondaires sont configurées en forme de fente, sont allongées ou rectangulaires, sont configurées au moins approximativement en forme d'anneau et/ou sont configurées comme tuyères.
  15. Dispositif selon l'une ou plusieurs des revendications 12 à 14, dans lequel au moins un groupe de plusieurs ouvertures de sortie secondaires qui sont disposées autour de la ou des ouvertures de sortie secondaires est prévu, au moins un groupe d'ouvertures de sortie secondaires s'étendant sur une zone délimitée essentiellement par un rectangle et/ou toutes les ouvertures de sortie secondaires d'au moins un groupe d'ouvertures de sortie secondaires sont situées essentiellement dans un plan de groupe, le plan de groupe d'au moins un groupe d'ouvertures de sortie secondaires étant situé essentiellement en parallèle à un plan de sortie d'au moins une ouverture de sortie primaire ou coïncide avec ce plan de sortie et/ou de préférence le plan de groupe d'au moins un groupe d'ouvertures de sortie secondaires est incliné, en particulier est perpendiculaire à un plan de sortie d'au moins une ouverture de sortie primaire.
  16. Dispositif selon la revendication 13 ou l'une des revendications qui renvoient à la revendication 13, dans lequel les moyens d'amenée comprennent au moins un canal d'amenée qui guide le gaz de conditionnement et dans lequel de préférence la ou les ouvertures de sortie secondaires et la ou les ouvertures de sortie secondaires associées à au moins un écoulement de gaz de conditionnement sont en communication d'écoulement ou peuvent être amenées en en communication d'écoulement avec un canal d'amenée commun, de sorte que le gaz de conditionnement provenant du canal d'amenée forme à la fois le ou les écoulements de gaz primaire et le ou les écoulements de gaz secondaire de l'écoulement de gaz de conditionnement, et/ou de préférence la ou les ouvertures de sortie primaires et la ou les ouvertures de sortie secondaires associées d'au moins un écoulement de gaz de conditionnement sont en communication d'écoulement ou peuvent être amenées en communication d'écoulement avec des canaux d'amenée associés, séparés les uns des autres, qui amènent chacun un gaz de conditionnement, de sorte que le gaz de conditionnement provenant d'un canal d'amenée forme le ou les écoulements de gaz primaire et que le gaz de conditionnement provenant de l'autre canal d'amenée forme le ou les écoulements de gaz secondaire de l'écoulement de gaz de conditionnement.
  17. Dispositif selon la revendication 13 ou l'une des revendications qui renvoient à la revendication 13, dans lequel les moyens de formation de l'écoulement de gaz de conditionnement comprennent au moins un boîtier dans la paroi duquel la ou les ouvertures de sortie primaires et la ou les ouvertures de sortie secondaires sont formées au moins dans une partie de sortie, au moins une ouverture d'entrée primaire qui est en communication d'écoulement ou peut être amenée en communication d'écoulement avec la ou les ouvertures de sortie primaires, au moins une ouverture d'entrée secondaire qui est en communication d'écoulement ou peut être amenée en communication d'écoulement avec la ou les ouvertures de sortie secondaires étant formées dans une zone d'entrée de la paroi du boîtier, différente de la zone de sortie, reliée aux moyens d'amenée ou adjacente au canal d'amenée, tandis que de préférence par modification de la section transversale d'écoulement de la ou des ouvertures d'entrée primaires et/ou des ouvertures d'entrée secondaires, l'écoulement volumique du gaz de conditionnement qui traverse peut être réglé au moyen d'un dispositif en particulier coulissant de réglage de mélange,
    dans lequel de préférence dans le boîtier, au moins un canal d'écoulement primaire qui relie la ou les ouvertures d'entrée primaires à la ou aux ouvertures de sortie secondaires est formé, des redresseurs d'écoulement qui redressent et/ou uniformisent l'écoulement étant disposés ou pouvant être disposés de préférence dans le canal d'écoulement primaire,
    dans lequel le boîtier présente de préférence sur des côtés opposés du canal d'écoulement primaire deux parties de boîtier en particulier essentiellement symétriques par rapport au canal d'écoulement primaire, tant la ou les ouvertures d'entrée secondaires que la ou les ouvertures de sortie secondaires étant disposées sur les parois extérieures de ces parties de boîtier, un canal d'écoulement secondaire étant formé dans ces parties de boîtier et reliant la ou les ouvertures d'entrée secondaires à la ou aux ouvertures de sortie secondaires, et/ou
    dans lequel de préférence à l'intérieur du boîtier, au moins un pré-répartiteur qui présente plusieurs ouvertures de passage est disposé dans le parcours d'écoulement entre la ou les ouvertures d'entrée secondaires et la ou les ouvertures de sortie secondaires.
  18. Dispositif selon la revendication 13 ou l'une des revendications qui renvoient à la revendication 13, dans lequel les moyens de formation de l'écoulement de gaz de conditionnement comprennent au moins un canal d'écoulement partiel primaire qui se raccorde en aval à au moins une ouverture intérieure de sortie primaire pour amener un écoulement partiel intérieur de l'écoulement de gaz primaire à l'intérieur du canal d'écoulement partiel primaire, de préférence au moins une autre ouverture de sortie primaire extérieure étant prévue et disposée à l'extérieur de la zone d'entrée du canal d'écoulement partiel primaire de telle sorte qu'un écoulement partiel de l'écoulement de gaz primaire qui sort de cette ou de ces ouvertures de sortie primaires extérieure s'écoule le long d'un côté extérieur du canal d'écoulement partiel primaire,
    dans lequel de préférence le canal d'écoulement partiel primaire s'étend au moins approximativement en ligne droite ou exactement dans une direction d'écoulement principal et/ou
    dans lequel la plage d'angles solides et/ou la longueur du canal d'écoulement partiel primaire dans la direction d'écoulement peuvent être ajustés.
  19. Dispositif selon la revendication 18, doté d'un entraînement qui permet de déplacer en particulier de manière périodique, pendulaire et/ou en cercle le canal d'écoulement partiel primaire à l'intérieur d'une plage d'angles solides.
EP04790717A 2003-10-21 2004-10-21 Procede et dispositif de conditionnement d'un processus Expired - Lifetime EP1675989B1 (fr)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE10349396A DE10349396A1 (de) 2003-10-21 2003-10-21 Verfahren und Vorrichtung zum Konditionieren eines Prozesses
PCT/EP2004/011912 WO2005040471A1 (fr) 2003-10-21 2004-10-21 Procede et dispositif de conditionnement d'un processus

Publications (2)

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EP1675989A1 EP1675989A1 (fr) 2006-07-05
EP1675989B1 true EP1675989B1 (fr) 2010-10-06

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AT (1) ATE483838T1 (fr)
DE (2) DE10349396A1 (fr)
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Family Cites Families (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CH684101A5 (de) 1991-09-23 1994-07-15 Luwa Ag Verfahren und Vorrichtung zur Webmaschinenklimatisierung.
DE4309416A1 (de) * 1993-03-15 1994-10-20 August Proett Gmbh & Co Kg K Verfahren und eine Vorrichtung zur Arbeitszonen- und Raumluft-Klimatisierung vorzugsweise für Textilmaschinen
DE59401040D1 (de) * 1993-04-16 1996-12-19 Luwa Ag Anlage zum beeinflussen der umgebungsbedingungen von textilen verarbeitungsprozessen
US5910598A (en) * 1994-11-02 1999-06-08 Shofner Engineering Associates, Inc. Modular process zone and personnel zone environmental control with dedicated air jet cleaning
US6128832A (en) * 1999-06-04 2000-10-10 Ltg Air Engineering, Inc. Method and system for providing conditioned air

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Publication number Publication date
DE502004011757D1 (de) 2010-11-18
ATE483838T1 (de) 2010-10-15
WO2005040471A1 (fr) 2005-05-06
DE10349396A1 (de) 2005-06-16
EP1675989A1 (fr) 2006-07-05

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