• 专利附录
  • 专利说明
  • 权利要求
  • 类似技术
  • 同族专利
  • 引用文献
  • 法律状态
  • 优先权
    • 专利摘要:
    Apparatus for drying a nonwoven web comprising a fan (6), a furnace (3) for heating, an outlet duct (C2) which puts the furnace outlet (3) in communication with the suction of the ventilator (6), a bypass duct (C3), in branch of the input duct (C1) upstream of the heat source (4), putting the duct (C1) in communication with the input of a device ( 10, 11), an air extraction duct (C4) of the drying device (10, 11) and a humidity sensor (13) mounted in the extraction duct (C4). .
    公开号:FR3016374A1
    申请号:FR1400077
    申请日:2014-01-15
    公开日:2015-07-17
    发明作者:Laurent Schmit；Xavier Ayrault
    申请人:Andritz Perfojet SAS；
    IPC主号:
    专利说明:

    [0001] Method and installation for drying a wet veil In the field of papermaking, and in the field of the production of nonwovens using water-jet bonding technology, the veils have the particularity of coming out wet after the training and consolidation phase. Indeed: - The production of paper requires mixing the paper fiber with water so as to deliver it on a forming conveyor and promote the bonding of the fibrous web by hydrogen bonds. - The water jet binding process uses pressurized water jets to interlace the fibers and thus moistens the fibrous web. In these processes, the webs produced need to be evaporatively dried before they can be coiled. To do this, it is common to use through air ovens (OMEGA type or flat) to perform this in-line drying operation. Figure 1 shows the flow diagram of a through air oven. The web to be dried 1 circulates around a drum 2 (or on a conveyor in the case of a flat oven).
    [0002] Pressurized hot air is injected into the hood 3 by means of a fan V1 6 (called the main fan) and a heat source 4 which heats the air. This heat source 4 may for example be a gas burner or a heat exchanger (oil, air or water). The temperature of the hot air injected into the hood 3 is regulated by the action of the heat source 4.
    [0003] This hot air then passes through the wet web and the drum 2 (or the conveyor in the case of a flat oven): by this method, the water contained in the web is evaporated as the web progresses on the drum 2 (or on the conveyor in the case of a flat oven). The air that has passed through the veil has cooled down and has become wet. It is then sucked inside the drum 2 (or on the conveyor in the case of a flat oven) by the fan V1 6, and reheated by the heat source 4 and reinjected into the loop and so after. The heat source 4 may be placed upstream or downstream of the fan V1 6. Preferably, it is placed upstream in the case of a gas burner and downstream in the case of a heat exchanger. Part of the cold, moist air must be evacuated outside the loop in order not to concentrate the moisture in the circulation loop. Part of the cold and humid air (5 to 30% of the total flow) is thus discharged through the branch pipe 5 thanks to the pressure generated by the fan V1 6 if it is sufficient or by means of a bypass fan additional V2 8 if the pressure generated by the fan V1 6 is not sufficient. The bypass piping can be connected upstream of V1. The flow of the bypass air is regulated either by acting on the speed of rotation of the fan V2 8, or by acting on the opening of the regulating flaps 9. To fill this air deficit in the loop, it draws in the production room or outside the building of make-up air upstream of the fan V1 6 by the additional piping 7. In the case of paper production, l The air in the hood is usually heated to temperatures of about 200-250 ° C. The air that is extracted from the oven comes out at a temperature ranging between 150 and 180 ° C. In the case of nonwoven production using the water jet bonding method, the air in the hood is usually heated to temperatures of about 100150 ° C. The air which is extracted from the furnace is rather evacuated at a temperature varying between 70 and 120 ° C. Drying temperatures for the nonwoven production using the water-jet bonding process are lower because some fibers constituting the nonwoven (POLYPROPYLENE or POLYESTER for example) are sensitive to exposure to too much water. temperature (narrowing in width of the sheet, decrease in the thickness of the veil, yellowing of the veil, alteration of the mechanical properties of the veil). Several enhancers describe different ways of utilizing the heat energy of the air that is rejected by the furnace through the extraction piping. In particular, as part of the production of paper, one of the improvement devices (see patent DE2802156B1 and US6551461) injects this bypass air still hot above a drying box located upstream of the oven in order to get started. upstream of the oven the drying process of the veil (and thus reduce the rate of load of the veil at the entrance of the oven). The bypass air is delivered through a diffusion box 10 above a drying box 11 on which the web passes. This drying crate 11 can be integrated in a conveyor or in a cylinder. The still hot air thus delivered will pass through the veil and will evaporate part of the water contained in the veil. The air recovered by drying box 11 (cold and wet) is then discharged to the outside (by a final exhaust fan for example). The system described above works perfectly well when the temperature of the air discharged by the furnace is higher than 150 ° C. (in the case of paper production). Indeed, at these temperatures, the relative humidity of the air flow that is rejected by the oven will remain low (<5%). As this air stream passes through the wet veil on the drying crate, its temperature will be further lowered and the air will be further loaded with moisture. However, because of the favorable upstream conditions (high temperature, low relative humidity), it is not possible for the sucked air to reach saturation by crossing the veil over the drying box and regenerating water on the veil. by condensation. In the case of a nonwoven web from a water jet bonding process, this drying enhancement system described in DE2802156B1 and US6551461 does not work well. There is a moistening of the veil rather than drying. The invention overcomes this disadvantage by a method of drying a wet web of nonwoven by passing through an oven, through the wet web moved by a means of transport, hot air which thereby moistens By heating a first portion of the humidified air and returning it to the oven through the wet web and passing through a drying device, upstream of the oven in the direction of travel of the web, through the wet sail moved, a second portion of the humidified air, characterized in that the relative humidity of the humidified air leaving the drying device is set to a set rate less than 100%.
    [0004] It has been found that since the temperatures of the air stream discharged by the furnace are much lower (7000-12000) than in paper production, the relative humidity of this stream can be quite great (20%). -40%). As a result, there is a high risk that the air stream will reach the saturation state by passing through the veil on the drying crate, causing the veil to be rewetted rather than removing a portion of the veil. the water contained in the veil. In addition this condensation 10 can continue in the suction box, and in the duct leading to the exhaust fan, preventing its proper operation. By adjusting the relative humidity of the humidified air leaving the dryer at a set rate below 100%, rewetting of the web is avoided. The energy expenditure will be minimized to dry the product by setting the set point between 70 and 99% and preferably between 96 and 98%. The absence of water in liquid form at the inlet of the final exhaust fan eliminates the need to install an air / water separator upstream of the fan. The relative humidity can be prevented from exceeding the set point by raising the temperature of the hot air. It can also be done by increasing the flow of hot air and / or the flow rate of the first part of the humidified air. The air in the bypass duct may contain flue gas (NOx, CO) hazardous to the operators. It is good that all the blown air is sucked in order not to diffuse polluted air into the production room. For this purpose, the flow rate of the humidified air leaving the drying device is adjusted so that it is greater than the flow rate of the second part of the humidified air. For example, Q extraction = K * Q derivation will be imposed, with K> 1.
    [0005] Preferred value K = 1.1. The invention also relates to a drying installation of a nonwoven web comprising: a fan, a heating furnace having an inlet and an outlet, an inlet duct, which puts the discharge to the fan in communication with the inlet of the furnace and sends discharge air to the furnace inlet, - a heat source arranged in such a way that the air discharged into the inlet duct is heated, an outlet duct, which puts the outlet of the furnace in communication with the suction of the fan, - a bypass duct, in derivation of the inlet duct upstream of the heat source, putting the inlet duct in communication with the inlet of a drying device a transport means, which moves a web in the drying device and in the oven, the drying device being upstream of the oven in the direction of movement of the web, an air extraction duct of the device of drying, a moisture probe, mounted in the extraction duct and measuring the moisture content of the air evacuated from the drying device, - the probe being connected to a control unit which compares the relative humidity to a set point and which, if the humidity relative is above the set point, raises the temperature of the heat source and / or increases the air flow in the inlet duct and / or increases the air flow in the bypass duct. By mounting the humidity probe in the extraction duct, it is meant that the probe is mounted downstream in the direction of passage of the air of the nonwoven web in the drying device, the probe thus possibly being mounted in the drying device itself. An exhaust fan is preferably provided in the extraction duct, preferably just downstream in the direction of passage of the air from the drying device. It is also preferably provided a bypass fan mounted in the bypass duct and / or an air flow control flap in the bypass duct. It is also possible, preferably, to provide a flowmeter mounted in the extraction duct, a flowmeter mounted in the bypass duct and a control unit connected in signal technique to the two flowmeters and regulating the flow rate of the extraction duct. so that it is greater than the flow rate in the bypass duct. The regulation according to the invention acts on the drying temperature of the oven and / or on the speed of rotation of the main fan of the oven and / or on the speed of rotation of the furnace bypass fan and / or on the position of the flaps of the oven. setting. This regulation prevents the condensation of air on the veil, since the air will always be in the drying box or downstream of the drying box forming part of the drying device at a relative humidity of less than 100%. .
    [0006] For a given non-woven production: - The higher the drying temperature imposed in the oven, the higher the temperature of the air extracted from the oven and the lower its relative humidity and therefore the humidity of the oven. air recovered in the drying crate will be weak. - The greater the rotational speed of the furnace bypass fan, the greater the air flow to the furnace and the lower the relative humidity of the exhaust air stream and hence the lower the humidity of the furnace. air recovered in the drying crate will be weak. - The more the control flaps on the furnace bypass line are open, the greater the airflow from the furnace and the lower the relative humidity of the exhaust air stream and hence the lower the humidity of the furnace. the air recovered in the drying crate will be weak. - The greater the speed of rotation of the main fan of the oven, the greater the air flow rejected by the oven and the lower the relative humidity of the exhaust air stream and therefore the lower the humidity of the air recovered in the drying crate will be weak.
    [0007] In the accompanying drawings given solely by way of example: Figure 1 is a diagram illustrating the prior art, Figure 2 is a flow diagram illustrating the invention, and Figure 3 is a diagram similar to Figure 2 illustrating a variant. .
    [0008] In Figure 2, the web to be dried 1 circulates around a drum 2 (or on a conveyor). A hot inlet duct C1 is injected under pressure into the hood 3 by means of a fan V1 6 (called the main fan) and a heat source 4 which heats the air. This heat source 4 may be for example a gas burner or a heat exchanger (oil, air, water or electric). This hot air then passes through the wet web and the drum 2 (or the conveyor belt): by this process, the water contained in the web is evaporated as the web advances on the drum 2 (or on the conveyor). The air that has passed through the veil has cooled down and has become wet. It is then sucked by a conduit C2 extraction inside the drum 2 by the fan V1 6, and reheated by the heat source 4 and reinjected into the loop and so on. The heat source 4 can be placed upstream or downstream of the fan V 1 6. Preferably, it is placed downstream as described in the figure, in the case of an exchanger and upstream in the case of a burner. gas. The motor of this fan V1 6 is controlled by a frequency converter 14. The temperature of the hot air injected into the hood 3 is regulated by the action of the heat source 4. Part of the cooled and humid air is evacuated outside the loop so as not to concentrate the moisture in the circulation loop. Part of the cooled and humid air is thus evacuated via the bypass duct C3 by virtue of the pressure generated at the outlet by the fan V1 (6) if it is sufficient or by virtue of an additional bypass ventilator V2 (8). The bypass conduit C3 may be connected upstream of V1. Flaps 9 may be installed in the bypass conduit C3 in order to regulate the value of the extracted flow rate. In the case where there is a V2 branching fan (8), the motor of this fan can be controlled by frequency converter. If there are adjustment flaps 9, this drive control is not necessary. To fill this deficit of air in the loop, it sucks 25 in the production room of makeup air upstream of the fan V1 by the piping 7 booster. The cooled and wet air discharged through the bypass duct C3 is then injected into a diffusion box 10 which will diffuse the air over a drying crate 11 located upstream of the furnace 3, on which circulates the veil to dry.
    [0009] This drying crate 11 can be located either in a conveyor (sail carrier = conveyor belt) or in a cylinder (sail carrier = nickel cylinder, perforated sheet, wire mesh). The air is sucked into the drying box 11 by a final exhaust fan V3 12. Preferably, this fan 12 is positioned closest to the drying box 11. A relative humidity measuring probe 13 is installed in the drying box 11 or downstream of the drying box 11. Preferably, it will be installed just upstream of the fan 12 in a conduit C4 extraction. This probe 13 measures the relative humidity of the air in the drying crate 11 or downstream of the drying crate. Preferably, the measurement is made just upstream of the final exhaust fan 12. The relative humidity measured in the drying box 11 or downstream of the drying box 11 (preferably just upstream of the exhaust fan) 12) is controlled at less than 100% per action on the oven drying temperature and / or on the speed of rotation of the oven main fan V1 6 and / or on the speed of rotation of the V2 bypass fan 8 The relative humidity signal is sent via a line L1 to a control unit UR which compares the signal with a set rate and sends the regulation signals. as a consequence to the fan 6 via the line L2, to the heat source 4 via the line L3 to the flap 9 by the line L4 and / or the fan 8 (to its variator 15) by the line L5. In another way of carrying out the invention (see FIG. 3), the following elements can be added to the configuration described in FIG. 2: The motor of the fan V3 12 is controlled by a frequency converter 16. A flowmeter 17 is the flow rate extracted by the furnace in the conduit C3 bypass. This flowmeter can be installed before or after the V2 branching fan 8. A flowmeter 18 measures the flow of air sucked by the drying box 11. This flowmeter can be installed before or after the final exhaust fan V3 12. The air extracted by the furnace may contain flue gas (NOx, CO) which may be hazardous to the operators working on the production line. In order for the system to work properly, it is absolutely necessary that 100% of the flow rate blown by the diffusion box is sucked up by the drying box, otherwise air will be released into the production room. To satisfy this condition, a control system will regulate the value of the flow sucked by the drying crate (measured by the flowmeter 18) as a function of the flow rate in the bypass duct (measured by the flowmeter 17) using lines L6 , L7 and L8. For example, Q extraction = K * Q derivation, with K> 1 will be required. Preferred value: K = 1.1 Examples: - Example of a production condition without the inventive system (corresponds to the configuration described in the figure 2): A sail 45 gsm 50% Viscose 50% PET is produced at 220 m / min over a width of 3500 mm.
    [0010] 4 injectors are used to bind the web, at pressures of 50-80-120-120 bar with strips type 2J14-2J14-2J14-1J7 Strip 2J14 = 2 rows, hole diameter = 120pm, center distance holes = 1.4 mm Strip 1J7 = 1 row, Diameter of the holes = 120pm, distance between the holes = 0.7 mm The wet veil then passes on a vacuum void conveyor equipped with: - 1 so-called low void void box: slot width = 10 mm, empty = - 100 mbar - 1 so-called high vacuum void box: slot width = 8 mm, vacuum = - 400 mbar The conveyor belt has a permeability of about 800 cfm. In this conveyor, downstream of the two express boxes, the drying box (11) fed from above by the diffusion box (10) has been integrated. This drying crate has a slot width of 600 mm. Just upstream of this drying crate (after the 25 squeeze boxes), it is measured that the wear rate of the haze is 120% (= 120 g of water per 100 g of dry haze). When the veil is passed under the drying crate, it is then transported to the oven to be completely dried. The oven which is used to dry this veil is equipped with a V2 branching fan 8 and a main fan V1 6. The motors of these two fans are controlled by frequency converter. The heat source 4 is a gas burner. The by-pass piping of this furnace is connected to the diffusion box 10. In order to obtain a dry haze at the furnace outlet, the following instructions were applied in the oven: 25 T ° air setpoint in the hood 3: 120 ° C% V1 = 70% V2 = 85 30 The temperature and humidity of the air extracted by the bypass piping are recorded: T ° C = 82 ° C RH = 20% (ie 70 g of water / kg dry air) The temperature and humidity of the air are measured in the drying crate 11: T ° C = 43 ° C RH = 100% The presence of water droplets in this drying crate is noted. The air in the drying crate has arrived saturation. Just after the drying crate 11 (before the oven), it is measured that the load of the sail is 130%. This value is greater than the value measured just upstream of the drying crate (120%). The web was therefore re-wetted by the air flow coming from the furnace sheath. The diffusion box + drying box system could not lower the wear rate of the veil before the oven, therefore, does not give a satisfactory result. Under these conditions, the oven consumes a total of 2410 Kw, 25 distributed in: - 2320 Kw gas - 90 Kw electricity - Example of the same production condition with the inventive system (corresponds to the configuration described in Figure 3 or 4): the speed of the bypass fan V2 is controlled to obtain the desired relative humidity upstream of the final exhaust fan V3. A 45 gsm 50% Viscose 50% PET veil is produced at 220 5 m / min over a width of 3500 mm. 4 injectors are used to bind the web, at pressures of 50-80-120-120 bar with strips type 2J142J14-2J14-1J7 10 Strip 2J14 = 2 rows, hole diameter = 120pm, distance between holes = 1.4 mm Strip 1J7 = 1 row, diameter of the holes = 120pm, distance between the holes = 0.7 mm. The wet veil then passes over a vacuum void conveyor equipped with: 1 so-called low void void box: slot width = 10 mm, empty = - 100 mbar 20 - 1 high void void box: slot width = 8 mm, vacuum = - 400 mbar The conveyor belt has a permeability of about 800 cfm. In this conveyor, downstream of the two express boxes, the drying box 11 fed from above was integrated by the diffusion box 10. This drying box has a slot width of 600 mm. Just upstream of this drying crate (after the two boxes of squeezing), it is measured that the wear rate of the haze is 120% (= 120 g of water per 100 g of dry haze).
    [0011] When the veil is under the drying crate, it is then transported to the oven to be completely dried.
    [0012] The oven that is used to dry this veil is equipped with a V2 8 branch fan and a V1 6 main fan. The motors of these 2 fans are controlled by frequency converter.
    [0013] The heat source 4 is a gas burner. The bypass piping of this furnace is connected to the diffusion box 10.
    [0014] The drying box 11 is connected to a fan V3 12. There is installed just upstream of this fan a probe 13 which measures the relative humidity of the air stream. The speed of the bypass fan V2 is regulated to obtain the desired relative humidity upstream of the final exhaust fan V3. A set point of 95% is imposed for this relative humidity. In order to obtain a dry haze at the oven outlet, the following instructions were applied in the oven: T ° air set point in the hood 3: 120 ° C 30% V1 = 55% The regulation stabilized the value of the speed 95% V2 fan rotation.
    [0015] The temperature and the relative humidity of the air extracted by the extraction pipe are recorded: T ° C = 95 ° C RH = 10% (ie 57 g of water / kg of dry air) The temperature is measured and the humidity of the air in the drying box 11: T ° C = 47 ° C HR = 95% (ie 69 g of water / kg of dry air) The air, crossing the veil on the drying crate recovered 69-57 = 12 g of water / kg of air. This amount corresponds to the amount of water that has been extracted from the veil by evaporation on this drying crate. We then check the wear rate of the veil just after the drying crate: we measure 101%. This value is therefore much lower than the measured value just upstream of the drying crate (120%). The veil was thus this time partially dried by the air flow coming from the sheath of the oven! The air did not condense in the diffusion box. Under these conditions, the oven consumes a total of 1860 Kw, divided into: 30 - 1805 Kw gas - 55 Kw electricity - Example of the same production condition with the inventive system (corresponds to the configuration described in Figure 3 or 4): the temperature of the air injected into the hood is decreased to obtain the desired relative humidity upstream of the final exhaust fan V3.
    [0016] A sail 45 gsm 50% Viscose 50% PET is produced at 220 m / min over a width of 3500 mm. 4 injectors are used to bind the web, at pressures of 50-80-120-120 bar with strips type 2J1410 2J14-2J14-1J7 Strip 2J14 = 2 rows, hole diameter = 120pm, distance between holes = 1.4 mm Strip 1J7 = 1 row, diameter of the holes = 120pm, distance between the holes = 0.7 mm. The wet veil then passes over a vacuum void conveyor equipped with: 1 so-called low void void box: slit width = 20 mm, vacuum = - 100 mbar - 1 so-called high void void box: slot width = 8 mm, vacuum = - 400 mbar The conveyor belt has a permeability of about 800 cfm. In this conveyor, downstream of the two expressing crates, the drying crate 11 fed from above was integrated by the diffusion box 10. This drying crate has a slit width of 600 mm. Just upstream of this drying crate (after the two squeeze boxes), it is measured that the wear rate of the haze is 120% (= 120 g of water per 100 g of dry haze). When the veil is passed under the drying crate, it is then transported to the oven to be completely dried. The oven which is used to dry this veil is equipped with a V2 branching fan 8 and a main fan V1 6. The motors of these two fans are controlled by frequency converter. The heat source 4 is a gas burner.
    [0017] The bypass pipe of this furnace is connected to the diffusion box 10. The drying box 11 is connected to a fan V3 12. A probe 13 is installed just upstream of this fan which measures the relative humidity of the fan. air flow. The temperature of the air injected into the hood is regulated to obtain the desired relative humidity upstream of the final exhaust fan V3.
    [0018] A set point of 95% is imposed for this relative humidity. In order to obtain a dry haze at the furnace outlet, the following instructions were applied in the oven:% V1 = 50%% V2 - 85% The regulation stabilized the temperature of the air injected into the hood at 130 ° C. The temperature and the relative humidity of the air extracted by the bypass piping are recorded: T ° C = 99 ° C RH = 10% (ie 67 g of water / kg of dry air) The temperature is measured and the humidity of the air in the drying box 11: T ° C = 51 ° C HR = 95% (ie 82 g of water / kg of dry air) The air, crossing the veil on the drying crate recovered 82-67 = 15 g of water / kg of air. This amount corresponds to the amount of water that has been extracted from the veil by evaporation on this drying crate. We then check the wear rate of the veil just after the drying crate: 105% is measured. This value is therefore much lower than the value measured just upstream of the drying crate (120%). The veil was thus this time partially dried by the air flow coming from the furnace sheath !! The air did not condense in the diffusion box.
    [0019] Under these conditions, the oven consumes a total of 1935 Kw, divided into: - 1897 Kw in gas - 38 Kw in electricity.
    权利要求:
    Claims (10)
    [0001]
    REVENDICATIONS1. A method of drying a wet web of nonwoven by passing through an oven, through a wet web moved by a means of transport, hot air which thereby moistens, by heating a first part of the humidified air and by making it iron in the oven through the wet web and by passing through a drying device, upstream of the oven in the direction of movement of the web, through the wet web moved, a second part of the humidified air, characterized in that the relative humidity of the humidified air leaving the drying device is set at a set point of less than 100%.
    [0002]
    2. Method according to claim 1, characterized in that the set point is set between 70% and 99%.
    [0003]
    3. A method according to claim 1 or 2, characterized in that the relative humidity is prevented from exceeding the set point by raising the temperature of the hot air.
    [0004]
    4. Process according to any one of claims 1 to 3, characterized in that the relative humidity is prevented from exceeding the set point by increasing the hot air flow and / or the flow rate of the first part. humidified air. 30
    [0005]
    5. Process according to any one of claims 1 to 4, characterized in that the flow rate of the humidified air leaving the drying device is adjusted so that it is greater than the flow rate of the second part. humidified air.
    [0006]
    6. Installation for drying a nonwoven web characterized in that it comprises: - a fan (6), - a furnace (3) for heating having an inlet and an outlet, - a duct (Cl) d an inlet which puts the discharge of the fan (6) in communication with the inlet of the oven (3) and sends discharge air to the inlet of the oven, - a source (4) of heat arranged in such a way that the air discharged into the inlet duct (C1) is heated, an outlet duct (C2) which puts the outlet of the oven (3) in communication with the suction of the fan (6), - a duct (C3) bypassing, in branching of the input duct (C1) upstream of the heat source (4), putting the inlet duct (C1) in communication with the inlet of a drying device (10, 11) a conveying means (2) which moves a web in the drying device (10, 11) and in the oven (3), the drying device (10, 11) being upstream of the oven (3) in the direction of movement of the veil, - a duct (C4) for extracting air from the drying device (10, 11), - a moisture level probe (13) mounted in the extraction duct (C4) and measuring the rate of humidity of the air evacuated from the drying device (10, 11), the probe (13) being connected to a control unit which compares the relative humidity to a deconsigned rate and which, if the relative humidity is greater than set point, raises the temperature of the heat source (4) and / or increases the air flow in the inlet duct (C1) and / or increases the air flow in the bypass duct (C3) .
    [0007]
    7. Installation according to claim 6, characterized by a fan (8) bypass mounted in the duct (C3) bypass.
    [0008]
    8. Installation according to claim 6 or 7, characterized by a flap (9) for adjusting the flow of air in the duct (C3) bypass.
    [0009]
    9. Installation according to one of claims 6 to 8, characterized by an exhaust fan mounted in the duct (C4) of extraction, preferably just downstream, in the direction of passage of air, the device (10, 11) drying.
    [0010]
    10. Installation according to one of claims 6 to 9, characterized by a flowmeter (18) mounted in the duct (C4) of extraction, by a flowmeter (17) mounted in the duct (C3) bypass and by a control unit (UC), connected in signal technique to the flow meters (17) and (18) and controlling the flow rate in the extraction duct (C4) so that it is greater than the flow rate in the duct ( C3) bypass.
    类似技术:
    公开号 | 公开日 | 专利标题
    EP2896730B1|2016-11-30|Method and installation for drying a wet sheet material
    EP3034976B1|2019-01-09|Installation for drying a wet non-woven web
    KR20130126664A|2013-11-20|Apparatus and method for controlling moisture in the manufacture of glass fiber insulation
    CN103459957A|2013-12-18|Dryer for a textile material web
    US20060070259A1|2006-04-06|Method of drying a web
    EP1747313B1|2016-02-03|Wide non-woven and methods therefor and production machine
    US20090100643A1|2009-04-23|Moisture conditioner for lint cotton
    CH619436A5|1980-09-30|
    CN110382983B|2022-01-07|Dryer for a textile web, method for operating the dryer and device for operating the dryer
    US5357881A|1994-10-25|Combined positive controlled sludge dryer and burner
    EP3414208B1|2020-12-23|Method and facility for manufacturing cross-linked fiberglass materials
    WO2012009360A3|2012-05-24|Modulated air flow clothes dryer and method
    FR2499227A1|1982-08-06|APPARATUS AND METHOD FOR DRYING SHEET MATERIAL
    EA025306B1|2016-12-30|Method for starting a sintering furnace, and sintering equipment
    EP2337882B1|2013-02-20|Spunbond tower with an electrostatic device
    CN110914620A|2020-03-24|Machine and method for drying and treating fabrics
    WO2018134526A1|2018-07-26|Facility for consolidating and drying a web and consolidation and drying method implemented in such a facility
    CN206173596U|2017-05-17|Energy -efficient intensification water thorn system of preheating
    EP2334851B1|2013-07-03|Apparatus for producing a non-woven web with dust removal
    CN209699389U|2019-11-29|A kind of wet system of pre- thermal control of spreading machine
    US20190257006A1|2019-08-22|Installation for producing a textile web-shaped material and method for producing a textile web-shaped material
    RU2382306C1|2010-02-20|Automatic plant for drying non-woven fabric with fibrous and porous structure
    JP4692457B2|2011-06-01|Fiber mat drying method
    CN1903086A|2007-01-31|Method for lowering temp. of air flow for drying tobacco leaves scrap
    FR2516636A1|1983-05-20|ASPIRE AMBIENT AIR CONDITIONING METHOD AND DEVICE FOR CHEMICAL PLANTS STATIONING AT SEA
    同族专利:
    公开号 | 公开日
    FR3016374B1|2016-01-29|
    EP2896730A1|2015-07-22|
    US9885519B2|2018-02-06|
    EP2896730B1|2016-11-30|
    US20150198368A1|2015-07-16|
    IL236704A|2018-05-31|
    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    DE2802156B1|1977-12-23|1979-06-28|Escher Wyss Gmbh|Drying plant of a paper machine|
    US6551461B2|2001-07-30|2003-04-22|Kimberly-Clark Worldwide, Inc.|Process for making throughdried tissue using exhaust gas recovery|
    US20050132598A1|2003-12-19|2005-06-23|Kimberly-Clark Worldwide, Inc.|Method and system for heat recovery in a throughdrying tissue making process|
    DE102006062234A1|2006-12-22|2008-06-26|Voith Patent Gmbh|Method and device for drying a fibrous web|
    FR3030705A1|2014-12-17|2016-06-24|Andritz Perfojet Sas|INSTALLATION FOR DRYING A WET NON-WOVEN NET|
    DE102016108863A1|2016-05-13|2017-11-16|TRüTZSCHLER GMBH & CO. KG|Dryer for a textile web with a device for energy minimized operation and method for this purpose|
    FR3061916B1|2017-01-19|2019-04-05|Fives Dms|SAIL CONSOLIDATING AND DRYING INSTALLATION AND METHOD OF CONSOLIDATION AND DRYING USED IN SAID INSTALLATION|
    DE102017106887A1|2017-03-30|2018-10-04|Reifenhäuser GmbH & Co. KG Maschinenfabrik|Dryer for a textile web with a device for determining the residual moisture of a web and method, module and system for this purpose|
    WO2019212612A1|2018-05-01|2019-11-07|Valmet, Inc.|Through air drying systems and methods with hot air injection|
    法律状态:
    2015-12-16| PLFP| Fee payment|Year of fee payment: 3 |
    2017-01-20| PLFP| Fee payment|Year of fee payment: 4 |
    2018-11-02| ST| Notification of lapse|Effective date: 20180928 |
    优先权:
    申请号 | 申请日 | 专利标题
    FR1400077A|FR3016374B1|2014-01-15|2014-01-15|METHOD AND INSTALLATION FOR DRYING A WETWATER|FR1400077A| FR3016374B1|2014-01-15|2014-01-15|METHOD AND INSTALLATION FOR DRYING A WETWATER|
    EP15150143.4A| EP2896730B1|2014-01-15|2015-01-06|Method and installation for drying a wet sheet material|
    US14/592,061| US9885519B2|2014-01-15|2015-01-08|Method and installation for drying a damp web|
    IL236704A| IL236704A|2014-01-15|2015-01-13|Method and installation for drying a damp web|
    [返回顶部]