WO2018108746A1 - Dispositif d'humidification d'un flux d'air - Google Patents

Dispositif d'humidification d'un flux d'air Download PDF

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Publication number
WO2018108746A1
WO2018108746A1 PCT/EP2017/082065 EP2017082065W WO2018108746A1 WO 2018108746 A1 WO2018108746 A1 WO 2018108746A1 EP 2017082065 W EP2017082065 W EP 2017082065W WO 2018108746 A1 WO2018108746 A1 WO 2018108746A1
Authority
WO
WIPO (PCT)
Prior art keywords
nozzle
nozzles
pump
air
liquid
Prior art date
Application number
PCT/EP2017/082065
Other languages
German (de)
English (en)
Inventor
Stephan Herrmann
Norbert PAKATCHI
Michael GÜNKEL
Peter Averhage
Karl Maier
Original Assignee
Eisenmann Se
Lavair Ag Klimatechnik
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Eisenmann Se, Lavair Ag Klimatechnik filed Critical Eisenmann Se
Priority to CN201780077242.2A priority Critical patent/CN110073150A/zh
Priority to EP17811949.1A priority patent/EP3704418A1/fr
Priority to US16/469,755 priority patent/US20200080736A1/en
Publication of WO2018108746A1 publication Critical patent/WO2018108746A1/fr

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Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24FAIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
    • F24F11/00Control or safety arrangements
    • F24F11/0008Control or safety arrangements for air-humidification
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24FAIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
    • F24F6/00Air-humidification, e.g. cooling by humidification
    • F24F6/12Air-humidification, e.g. cooling by humidification by forming water dispersions in the air
    • F24F6/14Air-humidification, e.g. cooling by humidification by forming water dispersions in the air using nozzles
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24FAIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
    • F24F6/00Air-humidification, e.g. cooling by humidification
    • F24F6/12Air-humidification, e.g. cooling by humidification by forming water dispersions in the air
    • F24F6/14Air-humidification, e.g. cooling by humidification by forming water dispersions in the air using nozzles
    • F24F2006/146Air-humidification, e.g. cooling by humidification by forming water dispersions in the air using nozzles using pressurised water for spraying
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02BCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
    • Y02B30/00Energy efficient heating, ventilation or air conditioning [HVAC]
    • Y02B30/54Free-cooling systems

Definitions

  • the invention relates to a device for humidifying an air flow, with a nozzle system having a plurality of nozzles for atomizing liquid, and with at least one pump, by means of which the liquid to be atomized is pressurized, and a plant for treating workpieces.
  • DE 41 10 550 C2 a device for humidification with pressurized water is described, which consists of a reservoir for the water, an overlying, flowed through by the air housing, a nozzle arranged therein and the water to this nozzle promotional, continuously variable pump consists.
  • DE 42 291 72 C1 discloses a device for humidifying an air flow of an air conditioning device, in particular a process air technology or air conditioning system, with a spray nozzle arrangement for a liquid atomization, in particular water atomization, which has a plurality of with respect to the air flow direction juxtaposed, lying in the air flow spray nozzles.
  • the object of the present invention is to provide a device for humidification, which is improved in terms of their functionality over the prior art and is particularly suitable for industrial use.
  • a device of the aforementioned type wherein the nozzles are formed as swirl nozzles and arranged in one or more nozzle strands, and / or wherein the pump is designed such that the pressure of the liquid to be atomized is between 3 and 50 bar , Such a fine atomization through the nozzles and / or a good degree of evaporation can be achieved. At the same time, the amount of lost water can be reduced.
  • the inventive device is also characterized by a low susceptibility, a long service life of the pump and low maintenance.
  • the operating and investment costs in the device according to the invention in particular compared to known air washers, Hochlichbefeuchtern or hybrid humidifiers are relatively low.
  • the nozzles may be formed as simplex nozzles.
  • the robustness of the device against light water impurities and suitability for industrial use can be further improved.
  • the nozzles may each have at least one filter device integrated in the nozzle.
  • the pump may be designed as a centrifugal pump. In this way, the maintenance can be further reduced and the pump life increased.
  • the pump is designed as a reciprocating pump.
  • the pressure provided by the pump can be between 20 and 50 bar. In this pressure range, a comparatively fine atomization of the liquid can be achieved with advantageous operating costs.
  • the device can be operated particularly favorably if the pressure provided by the pump is between 3 and 30 bar, preferably between 8 and 25. In this way, a favorable droplet spectrum of the atomization can be achieved are, especially when using centrifugal pumps, the maintenance and operating costs are relatively low and the pump life is relatively high.
  • the effectiveness of the humidification of the air flow can be further improved if the nozzles are arranged on a turbulizer nozzle.
  • the device for humidifying the air flow may comprise at least one adjusting device for adjusting the alignment of one or more nozzles of the nozzle system.
  • a particularly favorable solution with regard to different moisture requirements is given if the nozzles of a first nozzle line have a degree of atomization which differs from the atomization level of the nozzles of a second nozzle line.
  • successive nozzles each have a different orientation along a nozzle train.
  • a control device may be provided, by means of which the liquid supply to the nozzles is controllable, for example via the control of the pump speed. Depending on the pump speed, the atomization pressure and / or the volume flow can be adjusted.
  • a plurality of nozzle strands may each be coupled to a valve device with the aid of which the liquid supply to the corresponding nozzle senstrang is controllable.
  • the nozzle strands can be individually clocked and / or activated or deactivated, thereby enabling a variable and particularly efficient operation of the device.
  • a control technology particularly favorable solution is given if at least one coupled to the control device sensor for measuring moisture in the air flow, preferably in the humidified air flow is provided.
  • FIG. 1 shows the structure of an air conditioning system in a schematic diagram
  • FIG. 2 shows a part of a nozzle block in a perspective view.
  • FIG. 3 shows a turbulator device in perspective view
  • FIG. 4 shows a part of a nozzle block with a nozzle and with a turbulator device in a sectional view
  • FIG. 5 shows a side view of a nozzle with a spray cone
  • FIG. 6 shows a side view of an air-flow nozzle with a spray cone
  • FIG. 7 shows a side view of an air-flow nozzle with a spray cone and with a turbulator device
  • FIG. 8 shows a nozzle with a plurality of nozzle strands in a perspective view
  • 9 shows a nozzle with several nozzle strands in a perspective view
  • Fig. 1 1 is a longitudinal section of a treatment device for treating
  • FIG. 1 shows the basic structure of an air-conditioning installation 2 for conditioning room and / or process air with a device for humidifying an air flow.
  • the device for humidifying an air flow is designed in accordance with the example shown as an air humidifier 4 with a reaction space 6 and with a control device 48.
  • the reaction space 6 has an inlet 92 and an outlet 94 for the air flow.
  • the air flow to be conditioned is supplied to the air humidifying device 4, as indicated by the arrow 10, on the side of the inlet 92 and flows through the reaction space 6 of the air humidifying device 4 in the direction of the arrows 10, 12.
  • the air passes through a nozzle system 8 with a plurality of nozzles 14, wherein the nozzles 14 are arranged in a so-called nozzle 30.
  • a liquid preferably water
  • the nozzles 14 are arranged in a so-called nozzle 30.
  • a liquid preferably water
  • the atomized liquid can be absorbed by the air as moisture.
  • the conditioned air flow leaves the humidifying device 4, as indicated by the arrow 12.
  • the arranged in the reaction chamber 6 nozzles 14 water is supplied via leads 32, wherein the water is pressurized by means of a pump 34 and is pumped by a water inlet 38 to the nozzles 14 of the nozzle system 8.
  • a fine filter eg for particles with a
  • the nozzle system 8 has a plurality of nozzle strands 28, wherein a nozzle train 28 in each case has a plurality of nozzles 14.
  • the nozzle strands 28 extend perpendicular to the plane of the drawing.
  • one or more valve devices 36 are provided, wherein preferably one valve device 36 per nozzle strand 28 is provided.
  • each nozzle train 28 has a feed line 32 equipped with a valve device 36.
  • a valve device 36 may be designed, for example, as a two / two-way valve.
  • the pump 34 and the valve devices 36 are coupled to the controller 48. By means of the control device 48, in particular the liquid supply to the nozzles 14 can be regulated.
  • the atomized liquid can form a very fine droplet spectrum even at a relatively low pressure.
  • a comparatively fine atomization can already be achieved from a pressure of approximately 3 bar.
  • the liquid to be atomized is pressurized in a range of about 3 bar to about 50 bar.
  • the operation in a pressure range of about 20 bar to about 50 bar may be beneficial.
  • the fineness of the atomized liquid spray and the evaporation, especially of water, increases with increasing pressure.
  • multistage centrifugal pumps can provide a pressure of up to approximately 45 bar. Accordingly, it may be advantageous if the liquid to be atomized is subjected to a pressure in a range from about 3 bar to about 30 bar, preferably between 8 bar and 25 bar. In a further embodiment, it is possible to provide a reciprocating pump as a pump 34 for the nozzle system 8 of the air humidifier 4.
  • a rectifier 16 is provided for the air flow in the entrance area of the humidifier 4, ie upstream of the nozzle system 8 in the direction of the air flow.
  • a rectifier 16 can be dispensed with such a rectifier 16.
  • a separation system 18 is preferably provided, with the aid of which water not taken up by the air can be separated off.
  • the separation system 18 can be constructed, for example, in one or two stages. In the example shown, the separation system 18 has a two-stage design and has an agglomerator 20 and a droplet separator 22 arranged downstream of the agglomerator 20.
  • the agglomerator 20 is used in particular for the deposition and subsequent evaporation of fine droplets from an aerosol.
  • the agglomerator 20 for example, have at least one stainless steel braid and / or a plastic braid, which is flowed through by the air or the aerosol. If the agglomerator 20 is wetted with water, it can also serve as a post-evaporator and reduce fluctuations in the humidification of the air.
  • the humidifying device 4 be equipped with a trough 24, which has a level sensor 26 and a water outlet 40 in the example shown.
  • a valve not provided with a reference numeral valve is provided in the water outlet 40, so that the level rises in the tub 24 with the valve closed, which is opened at a sensor signal of the sensor 26, so that the residual water can flow.
  • the water drain 40 may be formed as always open overflow, so that can be dispensed with the valve in the water drain 40 and the level sensor 26.
  • the level sensor 26 can also be used in an overflow to possibly detect a blockage of the water outlet 40 when then the water level in the tub 24 increases.
  • At least one first sensor device 42 is arranged on the output side of the air humidifier 4, i. preferably downstream of the separation system 18.
  • This output-side sensor device 42 may have a humidity sensor and / or a temperature sensor.
  • at least one second sensor device 44 which preferably has a humidity sensor, can be arranged on the input side of the air humidification device 4. With the aid of these sensor devices 42, 44, the moisture content and / or the temperature in the air stream can be detected.
  • the sensor devices 42, 44 are coupled to the control device 48.
  • a pressure sensor 46 for detecting the water pressure is provided. This at least one pressure sensor 46 is coupled to the control device 48.
  • the one or more sensor devices coupled to the control device 48 tions 42, 44 and / or the pressure sensor 46 provide signals to the control device 48, wherein the signals can be processed by the control device 48 and used to control the humidifier 4.
  • the control device 48 outputs control signals to actuators of the humidifying device 4, for example to the pump 34, an adjusting device 80 (see FIGS. 9 and 10) for the nozzles 14 and / or one or more valve devices 36.
  • the humidification device 4 it is possible to use measured values of the humidity sensor of the output-side sensor device 42. Since an adiabatic cooling takes place in the reaction space 6, it may be expedient to additionally use measured values of a temperature sensor of the output-side sensor device 42. The control accuracy can be further improved if additionally measured values of the humidity sensor of the input-side sensor device 44 are used.
  • the control device 48 may be equipped with a user interface and preferably has display and operating elements.
  • the liquid stream flowing into the nozzle system 8, in particular a water stream, can be adjusted by means of the control device 48.
  • liquid atomization is accomplished by clocking the individual nozzle strands 28 to the moisture requirements, i. the requirements for the conditioned air, adjusted.
  • the three nozzle strands 28 of the humidifier 4 are controlled separately.
  • a first nozzle train 28, eg the highest nozzle train 28, is activated as the moisture requirement increases and pulse-width modulated taking into account a minimum pulse width in the ratio of 0 to 100%. If the moistening performance for a permanent valve opening for the first nozzle train 28 is insufficient, a second nozzle train 28, for example the nozzle train 28 below the first, is activated and pulse-width modulated in the same or a similar manner. According to this principle, further nozzle strands 28 are activated until all the nozzle strands 28 are completely opened and thus the maximum humidifying capacity of the humidifying device 4 is set. As the moisture requirement decreases, the individual nozzle strands 28 are successively deactivated or simultaneously deactivated in an analogous procedure.
  • the pressure of the liquid provided by the pump 34 can be detected by means of the pressure sensor 46 and set to a default value, for example, via the rotational speed of the pump 34.
  • a bypass channel not shown in detail can be provided with a controllable proportional valve, with the aid of which the pressure can be controlled to the default value. Even if all the valve device 36 are closed, a pressure relief can take place via the bypass channel.
  • a further bypass channel with an overflow valve can be provided.
  • the overflow valve can also be used for pressure control, the pump 34 can be operated speed controlled or at a constant speed.
  • FIG. 2 shows a perspective view of part of a nozzle block 30 with a nozzle 14, which is arranged on a section of a distribution line 50 of the nozzle block 30.
  • a distribution line 50 may be equipped with a plurality of other nozzles 14, not shown here.
  • the nozzle 14 is arranged in a pipe section 52.
  • the head 58 of the nozzle 14 protrudes from the pipe section 52 and has an outlet opening 56.
  • the pipe section 52 for example, a sleeve, is connected to the distribution line 50, wherein the pipe section 52 may be suitably welded to the distribution line 50.
  • the pipe section 52 on an external thread 54, by means of which an attachment to the pipe section 52 can be attached.
  • the nozzle 14 is expediently designed as a swirl nozzle and may have a non-illustrated, arranged in the interior of the nozzle 14 vertebral body.
  • the pipe section 52 may have a not-shown internal thread into which the nozzle 14 can be screwed.
  • the liquid to be atomized preferably passes through the outlet opening 56 of the nozzle 14 as a rotating liquid film ring and then forms a liquid film cone, which disintegrates into small liquid droplets due to its instability.
  • FIG. 3 shows a perspective view of a turbulator device 60 for influencing the air flow at a nozzle 14, to whose head 58 an outlet opening 56 for water is provided.
  • the turbulator device 60 has at least one fixed wing 62 and can be designed, for example, as a sheet metal part. be guided.
  • turbulator device 60 has a plurality of wings 62. These wings 62 serve as turbulators for the air flow and are the nozzle 14, in particular the outlet opening 56 of the nozzle 14, upstream in the air flow.
  • the turbulator device 60 may expediently be screwed onto an external thread 54 of the tube piece 52 receiving the nozzle 14 (see FIG. 2).
  • the turbulator device 60 is designed and arranged such that the vanes 62 have a swirl direction, which counteracts unscrewing the turbulator device 60 from the external thread 54.
  • FIG. 4 shows in a simplified sectional view a distribution line 50 of a nozzle block 30 with a tube piece 52 which carries a nozzle 14.
  • the nozzle 30 is provided with turbulators.
  • the pipe section 52 may be provided with a turbulator device 60 which has a plurality of turbulators formed as vanes 62.
  • a nozzle 14 is screwed, in the head 58, an outlet opening 56 is provided for water.
  • a sealing device 64 is provided, which may preferably be formed as an O-ring.
  • the nozzle 14 shown in FIG. 4 is designed as a simplex nozzle.
  • This simplex nozzle is equipped with at least one filter device, wherein the nozzle 14 in the example shown has a primary filter 68 and a secondary filter, not shown.
  • the primary filter 68 comprises a so-called drop stop, as it is known per se.
  • the at least one filter device is in the nozzle 14 integrated. Downstream of the at least one filter device may be provided in the interior of the simplex nozzle, a non-illustrated vertebral body, which is equipped at its the outlet opening 56 of the nozzle 14 side facing one or more channels 66 for the liquid. Through the at least one channel 66, the water can reach the outlet opening 56 of the nozzle 14.
  • the tube piece 52 may have a diameter of about 2 to 3 cm, wherein the distribution line 50 of the nozzle block 30 may have a diameter of about 5 cm, and the turbulator device 60 is typically an outer diameter of up to 30 cm.
  • FIGS. 5 to 7 show side views of a nozzle 14 for atomizing water in a greatly simplified schematic representation, wherein the nozzle 14 is arranged on a nozzle 30.
  • the water emerging from the nozzle 14 forms a spray cone 70, 74 or 78, the spray cones 70, 74 and 78 shown in FIGS. 5 to 7 each differing from one another.
  • a measure of the size of such a spray cone 70, 74 and 78 is, for example, its opening angle.
  • FIG. 5 exemplarily illustrates the spray cone 70 of the nozzle 14 when it is not surrounded by air.
  • FIG. 6 shows the nozzle 14 in an air flow 72, wherein the spraying direction of the nozzle 14 is aligned in the direction of the main flow direction of the air flow 72. Due to the air flow 72, the opening angle of the spray cone 74 of the nozzle 14 shown in FIG. 6 is smaller than the opening angle of the spray cone 70 of the nozzle 14 without air flow according to FIG. 5.
  • FIG. 7 shows the nozzle 14 in an air flow 76, wherein a turbulator device Device 60 is provided for influencing the air flow 76.
  • the turbulators forming wings of the turbulator device 60 are not provided with reference numerals for the sake of clarity.
  • the opening angle of the spray cone 78 according to FIG. 7 is greater than the opening angle of the spray cone 74 according to FIG. 6.
  • the air flow 76 can be influenced such that the opening angle of the 7 is greater than the opening angle of the spray cone 70 at a nozzle 14 without air flow according to FIG 5.
  • the turbulator 60 of the nozzle 14 in the air flow 76 is directly upstream.
  • Figures 8 and 9 show a simplified schematic representation of the nozzle 30 of a Beerbefeuchtungs noisy 4.
  • the nozzle 30 has a plurality of nozzle strands 28 which extend horizontally in each case in the reaction chamber 6 of the humidifying 4 in the examples shown and are arranged parallel to each other. It is possible to provide the nozzle strands 28 in a different arrangement in the reaction space 6.
  • the nozzle strands 28 may extend vertically or diagonally in the reaction space 6.
  • the nozzles are arranged distributed at least almost over the entire cross section of the reaction space 6.
  • a distribution line 50a, 50b or 50c is provided for each nozzle line 28.
  • Each distribution line 50a, 50b, 50c carries a plurality of nozzles 14, which are provided for better clarity only partially with reference numerals.
  • the nozzles 14 may be configured and / or operated such that the Zerstäubungsgrad of nozzles 14, which are arranged on different distribution lines 50a, 50b, 50c, different from each other.
  • the nozzles 14 disposed on the lower manifold 50c may atomize the liquid more finely than the nozzles 14 of the middle manifold 50b, the nozzles 14 of the upper manifold 50c atomizing the liquid more coarsely than the nozzles 14 located on the middle manifold 50b
  • the angle of attack of the nozzles 14 can be adjusted during assembly of the nozzle block 30.
  • the angle of attack of the nozzles 14 can be changed by means of one or more actuators.
  • an actuator 80 may be provided which may be used, for example, as a motor, e.g. as an electric motor, or as another drive unit, e.g. as adjusting cylinder, may be formed.
  • the adjusting device 80 for example, one or more distribution lines 50a, 50b, 50c can be rotated together or independently of one another, whereby the orientation of the nozzles 14 arranged on the distribution lines 50a, 50b or 50c changes.
  • a distribution line 50a, 50b, 50c is rotated about its axis, then the nozzles 14 arranged on the distribution line 50a, 50b, 50c are pivoted.
  • the adjusting device 80 can thus adjust the angle of attack of one or more groups of nozzles 14.
  • the adjusting device 80 is preferably coupled as an actuator to the control device 48 (see FIG. 1).
  • the nozzles 14 of all the distribution lines 50a, 50b, 50c have the same orientation.
  • the Nozzles 14 of all distribution lines 50a, 50b, 50c are arranged horizontally and parallel to one another. It is also possible for the angle of incidence of the nozzles 14 on different distribution lines 50a, 50b, 50c to differ from one another.
  • the nozzles 14 of the lowest distribution line 50c have an angle of attack of approximately 30 ° to the horizontal, while the nozzles 14 of the remaining distribution lines 50a, 50b are aligned horizontally.
  • FIG. 10 shows, in a perspective and simplified schematic representation, a nozzle 30 having nozzles 14 of a nozzle line 28 arranged along a section of a distribution line 50.
  • the nozzles 14 arranged along the distribution line 50 have different orientations, wherein in the example shown successive nozzles 14 follow each other along the distribution line 50 have a different orientation.
  • adjacently arranged nozzles 14 each alternately on a positive and a negative angle to the horizontal, wherein the difference in the angle of attack between adjacent nozzles 14 according to Figure 10 is approximately 60 °.
  • These nozzle strands 28 can in turn be designed and arranged in such a way that a type of two-dimensional nozzle matrix is formed with nozzles 14 which are alternately oriented differently in each case in the two dimensions of the matrix.
  • the reaction space 6 can have a cross-sectional area of up to 50 m 2 and more.
  • the cross-sectional area of the reaction raums 6 in a room air application up to about 4 m 2 and in industrial applications between about 4 m 2 and about 50 m 2 .
  • a nozzle 14 may be provided on the nozzle train 28 per meter of a nozzle train 28.
  • the present invention relates to a device for conditioning room and / or process air, with a nozzle system 8, which has a plurality of nozzles 14 arranged in one or more nozzle lines 28 for Spraying of liquid, and with at least one pump 34, by means of which the liquid to be atomized is pressurized, wherein the nozzles 14 are formed as swirl nozzles, and / or wherein the pump 34, the liquid to be atomized at a pressure between 3 and 50 bar applied.
  • the liquid in particular water
  • the inventive device is characterized by a low susceptibility, a long service life of the pump 34 and a low maintenance.
  • Figure 1 1 shows a treatment device 96 with a treatment booth 98 of a total of 100 designated plant for treating workpieces 102.
  • the air flow to be treated at least partially exhaust air 104, which results in the running in the treatment device 96 working process.
  • Such a treatment device 96 can be used, for example, in the automotive industry in systems for treating vehicle bodies and, in particular, in treatment booths in which coated vehicle bodies are used. Series be treated as part of a painting process. These include in particular paint booths, but also, for example, evaporative booths, cooling cabins and dryers, each with a treatment tunnel. As an example of workpieces 102 each vehicle bodies are therefore shown here. However, the workpieces 102 can also be other workpieces and, in particular, attachments or body parts of vehicle bodies such as bumpers, side mirrors or the like. Smaller workpieces 102 may optionally be placed on a workpiece carrier not specifically shown.
  • the above-described air humidification device 4 is part of a conditioning device 106, in which the air flow, which contains the exhaust air 104, is conditioned to conditioned process air 108.
  • the treatment cabin 98 of the treatment device 96 delimits a working space in the form of a treatment tunnel 110 having a tunnel entrance and a tunnel exit, through which the workpieces 102 to be treated are conveyed by means of a conveyor system 12, as it is known per se and not must be received further.
  • the treatment tunnel 1 10 has an air outlet 1 14 and an air inlet 1 16, between which the conditioning device 106 is arranged so that exhaust 104 sucked out of the treatment tunnel 1 10, promoted by the conditioning 106 and after conditioning the treatment tunnel 1 10 again as Process air 108 can be supplied in a circuit.
  • the returned process air 108 is guided in a manner known per se via non-specifically illustrated nozzles onto the workpieces 102 to be treated. In this way, it is possible to maintain in the treatment tunnel 10 the temperature and treatment conditions required for effective treatment.
  • the treatment tunnel 1 10 may also be divided into a plurality of tunnel sections, each having a separate air outlet and air inlet, which are connected to the conditioning device 106.
  • each existing tunnel section can be assigned its own conditioning device 106, so that different temperatures and treatment conditions can be set in each tunnel section, as is the most favorable for the treatment process.
  • the conditioning device 106 defines a flow path for the air flow with a plurality of conditioning stages 1 18 is formed.
  • six conditioning stages 1 18 are present, which are a preheater 1 18.1, a first filter device 1 18.2, a cooling device 1 18.3, an afterheating device 1 18.4, an air humidification stage 1 18.5 in the form of the air humidification device 4 and a second filter device 1 18.6 include.
  • the air flow with the exhaust air 104 is conveyed by means of a blower 120 through the conditioning stages 1 18.
  • a feed line 122 connects the air outlet 1 14 of the treatment tunnel 1 10 with the conditioning device 106.
  • a valve 124 is arranged in the feed line 122 so that the volume flow of the exhaust air 16 to the input connection unit 36 can be adjusted.
  • the conditioning device 106 is also connected to a fresh air line 126, via which fresh air, the air flow can be introduced.
  • the volume flow of the fresh air to the conditioning device 106 can by means of a Valve 128 can be adjusted.
  • a proportion of a mixed gas in the present case, a proportion of fresh air, is mixed. Consequently, as a rule, the conditioning device 106 is always flowed through by a mixture of the exhaust air 104 and fresh air 56.
  • a process air line 130 with a valve 132 leads to the air inlet 16 of the treatment device 96, so that the flow circuit is closed.

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  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Dispersion Chemistry (AREA)
  • Air Humidification (AREA)

Abstract

L'invention concerne un dispositif de conditionnement d'air ambiant et/ou de processus comprenant un système de buses (8), qui comporte une pluralité de buses (14) disposées dans au moins un conduit de buses (28) et destinées à pulvériser un liquide, et au moins une pompe au moyen de laquelle le liquide à pulvériser est mis sous pression. Les buses (14) sont conçues comme des buses de turbulence et/ou la pompe (34) soumet le liquide à pulvériser à une pression comprise entre 3 et 50 bar. Selon l'invention, le liquide, en particulier de l'eau, peut être nébulisé de manière particulièrement fine et un bon degré d'évaporation peut être obtenu, ce qui réduit également la quantité d'eau perdue. Le dispositif de l'invention se caractérise par une faible sensibilité aux interférences, une longue durée de vie de la pompe (34) et un faible entretien.
PCT/EP2017/082065 2016-12-15 2017-12-08 Dispositif d'humidification d'un flux d'air WO2018108746A1 (fr)

Priority Applications (3)

Application Number Priority Date Filing Date Title
CN201780077242.2A CN110073150A (zh) 2016-12-15 2017-12-08 用于加湿气体流的设备
EP17811949.1A EP3704418A1 (fr) 2016-12-15 2017-12-08 Dispositif d'humidification d'un flux d'air
US16/469,755 US20200080736A1 (en) 2016-12-15 2017-12-08 Device for humidifying an air stream

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE102016124478.3A DE102016124478A1 (de) 2016-12-15 2016-12-15 Vorrichtung zum Befeuchten eines Luftstroms
DE102016124478.3 2016-12-15

Publications (1)

Publication Number Publication Date
WO2018108746A1 true WO2018108746A1 (fr) 2018-06-21

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Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/EP2017/082065 WO2018108746A1 (fr) 2016-12-15 2017-12-08 Dispositif d'humidification d'un flux d'air

Country Status (5)

Country Link
US (1) US20200080736A1 (fr)
EP (1) EP3704418A1 (fr)
CN (1) CN110073150A (fr)
DE (1) DE102016124478A1 (fr)
WO (1) WO2018108746A1 (fr)

Cited By (2)

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