DE202014001981U1 - Plant for separating paint particles from an air stream - Google Patents

Abstract

System for separating paint particles (43) from an air stream (5), in particular from a coating system (2), the air stream (5) being able to be fed via a feed (15) to a separating device (10) in which the paint particles (43) are separable from the air, characterized in that an ice-making device is provided, by means of which ice-crystal particles (1) can be produced, and that at least one injection unit (27) is arranged on the feed (15) and / or the separating device (10) which the ice crystal particles (1) can be introduced into the air stream (5).

Description

The invention relates to a system for separating paint particles from an air stream according to the preamble of claim 1.

In the mass production of motor vehicle, a considerable partial flow of the paint is not applied to the body of the motor vehicle during painting despite many optimizations. Depending on the type of application process, this amount can amount to up to 50% of the paint outflow. The relevant portion, which is called Lackoverspray is detected in the paint booth by the air flow and fed to a separator. However, current state-of-the-art methods, in addition to high operating, energy and investment costs, have a high degree of complexity in process engineering.

The DE 10 2010 041 552 A1 describes a method based on a transmission filter principle, wherein the contaminated with paint particles air flow is passed through a filter with a suitable pore size. To avoid contamination of the filter, it is supplied with an auxiliary material, such as stone dust. This additive is fluidized in a separator and may deposit on the surface of the filter. Here, the overspray material combines primarily with the stone meal, so that contamination of the filter is reduced. If the filter load is correspondingly high and the pressure difference increases, the filter is cleaned with compressed air. If the maximum load of stone powder is reached with paint material, it is disposed of and replaced with new material.

A major disadvantage of this method is that the stone powder must be specifically designed and tuned to each paint material and thus high costs incurred in its production and disposal after use. In particular, the disposal is problematic here from an environmental point of view. In addition, due to the moving parts in the separator maintenance and repair is problematic and in case of failure there is a high risk of cabin contamination. In addition, the power and compressed air consumption is very high.

The DE 10 2007 036 553 A1 discloses a method based on the principle of electrostatic deposition. The contaminated air stream is in this case passed through a separating module, which consists of a high voltage and a grounded element. The paint particles are charged and attracted by the directional electric field to the grounded plate. A coolant flows through the grounded plate, causing crystallization of the water in the air stream on the surface of the separation plate. The resulting ice layer binds the paint particles and thus counteracts sticking. In order to clean the plate, it is flowed through with a heated cooling medium, so that the paint-meltwater mixture can flow into an underlying drip tray.

This process is also costly and complex and requires a high consumption of consumables for the coolant supply and the high voltage module. In addition, there is a high maintenance and repair costs and a risk of high voltage and leakage of the coolant supply. Furthermore, a high power requirement is required for the generation of high voltage and plate cooling.

The DE 10 2010 051 085 A1 describes a method in which the contaminated with Lackoverspray air flow from the Fahrzeuglackierkabinen is guided past a transverse to the flow tube bundle, which is not only electrostatically charged, but its additional surface is also coated with an adhesive material. The system is cleaned via a slidable plate along the tubes, which scrapes off the deposited layer of paint particles.

Also, this method requires for the coolant supply and the high-voltage module expensive and complex process technology and a high maintenance and upkeep, especially for the arranged in the air duct with adhesive particles loaded moving parts. In addition, a high energy requirement is necessary for static charging and cooling.

The invention is therefore based on the object to provide a system for separating paint particles from an air stream, which is particularly economical to operate and at the same time simple.

According to the invention, the object is achieved by a system for separating paint particles from an air stream, in particular from a coating system, with the features of claim 1. Preferred embodiments of the invention are indicated in the dependent claims.

Starting from a deposition of paint particles from an air stream, in particular from a coating plant, wherein the air stream is fed to a separation device in which the paint particles are separated from the air, it is provided according to the invention that in the air flow ice crystal particles for binding and / or Agglomerate the paint particles are injected.

The invention is based on the recognition that the particle sizes of Overspraylackmaterials are often too small for effective separation. This applies, for example, to inertial separators, which require a minimum mass of the particles. By injecting ice crystal particles into the air stream it is achieved that in the paint particles in an artificially generated turbulence by a mutual agglomeration by attaching the particles to the ice crystals, a volume and mass increase is generated. The larger particles formed in this way can be deposited in a subsequent inertial separator or in a filter with larger filter openings with high reliability.

In order to produce a particularly high effect and to reduce the adhesion of the paint material, ice crystal particles in the form of fine powder snow are injected into the exhaust air stream contaminated with paint particles. With a correspondingly high particle density and particle size, the effect of particle agglomeration increases statistically. In addition, water snow fulfills the physical-chemical requirements for combination with the generally water-based paint material. The thus purified air volume flow can be fed by Umluftverfahren and without further subsequent conditioning effort again the painting process.

A significant proportion of the energy applied to the production of the ice crystal particles leads to waste heat, which can be recovered and used in the painting process.

In current mass finishing processes, the air is heated and must then be cooled again upon deposition of the overspray particles. Due to the cold energy introduced by the snow and ice material, in this case cooling power can be saved. Due to the simple methodology of the invention, significant energy savings can be achieved as compared to conventional prior art technologies. This can amount to more than 50%. In addition, the snow-melt water paint material can be reused after an appropriate separation and a costly and expensive disposal can be omitted. In addition, there is no risk of contamination of paint booths in case of failure, since both paint and the water used pose no risk to the process technology.

The invention is particularly suitable for use in a painting process for motor vehicles, but can readily be used in all areas of series painting, for example for household goods or furniture in which deposition of the paint overspray is prescribed.

It is preferred that the ice crystal ponds be formed substantially of a fluid selected from water, alcohols, ethers, esters, carboxylic acids, carbon dioxide or mixtures thereof.

These compounds have a lower density of the solid phase compared to the liquid phase, so that the corresponding ice particles have a considerably larger collision surface. It can be done in this way a particularly efficient deposition of paint particles on the crystal particles of these compounds. In addition, the corresponding fluids are inexpensive to purchase on a large scale. The corresponding process technology for the conversion of the fluid phase into the solid is known and is based on mature process steps, which are largely optimized from an energetic point of view. In addition, the molecules of these fluids have a sufficiently large polarity to mix with the usually water-based paint material.

Suitably, further additives, in particular for changing the melting point, the viscosity or the wetting properties are added to the fluid.

By lowering the melting point, a reduction of the energy expenditure for cooling to the solid state of the fluid can be achieved. By a suitable choice of the viscosity, this can be optimized for the relevant geometry and flow guidance in the coating system. With a lower viscosity, the energy losses are reduced by the flow friction, while at an increased viscosity, a lighter transition to the solid state can be achieved. The wetting properties to be set depend on the surface properties of the coating system used, in particular with regard to their surface roughness and hydrophobic or hydrophilic character. To change the physical-chemical variables concerned, organic or inorganic salts and surface-active surfactants are suitable.

It is advantageous if the separating device has a filter or a separating surface, with which the ice crystal particles are separated with the paint particles in solid or molten form from the air stream.

As filter materials, for example, sieves, paper filters, glass fibers, nonwovens, ceramic filter elements of open-pore ceramic, open-pore sintered metal filter elements or needle felt can be used become. After the conversion of the ice crystal particles with the paint particles in the liquid phase, a separation of the relevant mixture in the fluid forming the crystal particles and in the paint material can be carried out and both components can be reused and recycled to the process. When using a Abscheidefläche the applied surface temperature can be adjusted to the effect that the respective phases are transferred separately from each other in the liquid state. The deposition surface may be smooth or have an increased surface roughness or other surface structuring in order to provide a high degree of adsorption surface to the ice crystal particles to be collected with the paint particles. The paint-liquid mixture can be easily removed from the separation surface.

It is preferable to use a cooling surface on which an ice layer is formed from the liquid, which is separated and crushed to form the ice crystal particles.

Suitable for this purpose are, in particular, rollers through which coolant flows in a water bath. The water freezes on the roll surface, is removed by means of brushes or a doctor blade and introduced directly into the generated turbulence. The particle size can be influenced by the corresponding process parameters such as roller temperature and rotational speed.

In a further preferred embodiment of the invention, the ice crystal particles are formed by means of a spraying device by spraying the liquid under heat removal. The spraying device may be the injection unit for feeding the ice crystals into the air stream.

In the case of water as the fluid used, the water needed for snow production is compressed and cooled to below 0 ° C without freezing. Using fan and cooled air, the supercooled water is finely atomized and introduced into a turbulence zone. The water crystallizes upon introduction into the agglomeration area. The generation of the snow crystals and in particular the crystal size can be targeted and controlled.

These properties can be achieved by a defined setting of pressure, temperature and / or relative humidity. When using water as the fluid used, a temperature range of about 20 to 25 ° C and 60 to 70% relative humidity has been found to be particularly suitable. Furthermore, it should be noted that due to the large surface area of the numerous snow crystals there will be a snow melt between their introduction and the deposition in the separator, whereby a moisture increase of the air flow is achieved. This may require subsequent conditioning of the purified air to the process conditions. In addition to influencing the crystal size and geometry, the nucleation temperature for forming the snow phase can be additionally increased by further chemical aids, such as so-called snow-inducers. In particular proteins are suitable as snow inducer. On these proteins, small ice crystals form as crystallization nuclei, to which more water freezes. The lower the relative humidity, the better the cooling process. At a relative humidity of about 30%, this step already starts at 1 ° C, whereas at 80% relative humidity below -3 ° C is required.

It is also advantageous if the ice crystal particles are charged electrically.

The electrical charge can be either by ionization in a strong electric field or by a bombardment with electrically charged particles. The electrically charged ice crystal particles are particularly suitable for further agglomeration of the polar paint particles. Furthermore, the agglomerated particles can be efficiently collected in an electric and / or magnetic field.

In a further preferred embodiment of the invention, the air stream is pretreated before the supply of the separating device for agglomeration of the paint particles.

In this way, the mass of the paint particles is increased and a subsequent separation of the paint particles from the air flow can be carried out particularly efficiently in a Trägheitsabscheideeinrichtung. In addition to a pretreatment for agglomeration of the paint particles, an adjustment of the air flow in terms of flow velocity, temperature, pressure and relative humidity can be carried out. The flow direction and velocity of the air stream can be set defined with a larger particle size, wherein a uniform flow direction and speed also contributes to the agglomeration of the paint particles.

It is expedient if the pretreatment for agglomeration is carried out in a shear-layer channel.

Here, in the paint particles in an artificially generated turbulence by a mutual attachment, that is an agglomeration caused by particle collision, a volume and mass increase to them in a subsequent Inert separation, where further agglomeration effects are done to be able to completely separate. In a shear-layer channel, two particle-laden air streams flow at different speeds and mix in a subsequent mixing channel. Due to the different momentum input creates a turbulent shear layer and there is a turbulent mixing process. The air and particle mass flows mix with each other and the agglomeration process takes place. Decisive for the agglomeration process are the interactions and adhesion conditions between the paint particles or the paint particles and the ice crystal particles and the probability of collision, which in turn depends on the particle size, the density and the flow velocity. In addition, various agglomeration mechanisms may exist, which in turn affect the agglomeration process and its kinetics. To control the agglomeration process, the velocity ratios of the two air flows, the number of particles and the particle size distribution should be defined. The masses and volumes significantly enlarged from the mixing channel can then subsequently be separated and collected in accordance with their mass in an inertia separating device. The thus freed of the paint particles air can either be discharged or re-fed to the process as clean air.

The invention relates to a system for separating paint particles from an air stream, in particular from a coating plant, wherein the air flow can be supplied via a feed of a separating device, in which the paint particles are separable from the air. In the system according to the invention, an ice-making device is provided, by means of which ice-crystal particles can be produced, and at least one injection unit, with which the ice-crystal particles can be introduced into the air stream, is arranged on the feed and / or the separating device.

The ice or snow production can take place in various ways. Suitable is a snow production with cooled rolls, with rollers through which coolant flows in a water bath and the water frozen on the roll surface is removed by means of brushes or a doctor blade. In addition, a snow production with supercooled water can take place, which is compressed and cooled below 0 ° C, without freezing. The supercooled water is finely atomized in a dry and cooled air and introduced into the air stream. The atomization of the supercooled water can also be done directly with the Eindüseinheit. The feeding of the air stream into the separating device can particularly preferably be connected to a mixing channel of a shear layer channel in which the paint particles agglomerated from the mixing of the snow particles with the overspraylack particles laden with snow particles have formed. By introducing further ice crystal particles into the air flow through the injection unit, further agglomeration processes take place on the already occurring pre-agglomerated paint particles. In addition, a particle shell is formed by the overspray particles by the injected ice crystal particles, whereby the risk of sticking of the walls of the separator is reduced by the adhering paint particles. The location and arrangement of the injection unit depend on the ice and snow stability in the air stream as well as on the location of the most intensive turbulence development. The stability of the ice or snow particles and their agglomeration character can be influenced in addition to the thermodynamic parameters such as pressure, temperature and relative humidity on the geometry and dimensioning of the feed. In this case, the geometrically induced turbulence development can be adapted to the snow behavior by means of flow simulations. An optimal geometry of the shear layer channel as well as the location of the snow injection depends on agglomeration character, snow stability and turbulence intensity.

In a particularly preferred embodiment of the system according to the invention, the separating device has an inertia separating device, in particular a cyclone.

In this way, the enlarged agglomerated paint particles can be separated from the air stream particularly efficiently. In this case, the separation is the more effective the greater the mass of the respective paint particles, and therefore the largest possible mass of the particles should be aimed for when entering the separation device.

On the other hand, the mass of the particles must not be too large to be transported in the air flow. By means of a cyclone particularly high fluid velocities can be achieved to achieve an optimum degree of separation. The fluid velocity can be defined by the geometry of the cyclone as well as the differential pressures at the inlet and outlet of the cyclone defined by the requirements, that is in particular the density, viscosity and wetting properties of the paint particles and the thermodynamic parameters such as pressure and temperature and humidity of the air flow be set. The air stream loaded with the agglomerated paint particles enters via a feed into the cyclone and is set in a three-dimensional, turbulent rotational spin flow, whereby the paint particles are forced outward by the action of the centrifugal forces become. There is a risk here that the paint particles could reach the cyclone walls and stick them together. This can be counteracted by forming a liquid envelope around the overspray particles by injecting snowflakes into the cyclone interior. The injected snow particles may in turn contribute to further agglomeration of the particles. The resulting low-viscosity suspension of snow or ice and paint material flows through a lower cylindrical cone opening from the cyclone. The cleared of the paint particles purified air flow can be discharged through a cylindrical dip tube, which projects centrally into the cyclone. If the original cleaning of the air stream is not sufficient, then another cyclone separator can be connected downstream or else a cascade of cyclone separation devices can be provided.

Overall, therefore, results in a change in the particle size of the paint material by agglomeration processes on the one hand by internal processes in the cyclone and by external process steps such as in the snow addition in an upstream shear layer channel. For the cyclone separation, it is important to set an optimum differential pressure and flow rate, which is a function of the size of the overspray particles. In this case, greenfield and brownfield observations can be made suitably, a collection device, in particular a filter or a Abscheidefläche, provided for collecting the bound or agglomerated paint particles on the separator.

Preferably, the collecting device is raised above the melting point of the carrier fluid used, so that a melting of the fluid at the filter or Abscheideflache can take place and a mixture of fluid and paint particle material is formed. These two phases can subsequently be separated from one another and treated separately from one another and, if appropriate, recirculated to the process. The filter material or the material of the Abscheidefläche and their surface properties should be selected depending on the polarity of the paint material or the carrier fluid suitable. For example, in the case of polar materials, a hydrophilic surface is to be preferred, while in the case of apolar substances a hydrophobic surface is more suitable. In this case, a coherent film of the paint particles or of carrier fluid compounds, which can flow off at a suitable location, forms on the collecting device.

Further, it is advantageous if a plurality of Eindüseinheiten are provided, which are controlled separately.

With several Eindüseinheiten a larger amount of snow and ice material can be evenly introduced into the separator in the same period. In addition, the inflow events occurring at various points improve the turbulence and mixing in the separator. Via a control and regulating device, the amount, flow velocity and, in the case of an alternating injection, the frequency of the introduced ice material can be specifically adapted to the respective requirements, that is to say in particular flow conditions and geometry of the separating device. In particular, it may be advantageous to initially inject a larger amount of snow material in the region of the supply of the air flow and to gradually reduce the amount of snow material introduced in the rear downstream of the separation device.

The invention will be explained in more detail with reference to a schematic embodiment with reference to the drawings. The same reference numerals designate the same elements.

It shows:

1 a schematic block diagram of the method according to the invention;

2 a cross section through the separator; and

3 a cross section through a shear layer channel of the system according to the invention.

There are various embodiments of the system according to the invention conceivable. In the following we describe a preferred embodiment.

In the in 1 schematically shown flow chart is exhaust air 5 , which with Overspraylackpartikeln 43 is loaded from a coating plant 2 For example, for the coating of automobiles, household goods or furniture, with a stream of ice crystal particles 1 merged to adsorb the paint particles 43 on the ice crystal particles 1 a paint particle agglomeration 3 to effect. The ice crystal particles 1 have a very high specific surface area compared to their mass and therefore can have a large number of overspray particles on their flow path 43 adsorb. These are bound on the surface and can partially combine to form larger agglomerates. The with the agglomerated paint particles 43 loaded ice crystal particles 1 are then used for paint separation 4 further treated. The paint separation 4 For example, by melting the Eiskristallteilchen 1 , wherein a phase separation in water and paint material takes place, take place. In the case of water-based paint material, the mixture of melt water and paint material is disposed of. In the in 2 shown separating device 10 that flows with paint particles 43 laden exhaust air 5 via a feeder 15 in the form of a cyclone separator 10 one. Due to the cyclone geometry, the exhaust air 5 around the dip tube projecting centrally into the cyclone 20 in a three-dimensional turbulent rotational spin flow 29 added. At various points within the cyclone there is a snow injection 27 , creating a shell of snow particles 44 around the paint particles 43 is formed. On the injected snow particles 44 store the paint particles 43 by adsorption, and there is an agglomeration process, which increases the mass of the particles consisting of paint and ice material. Due to the increased mass of the agglomerated paint particles 43 These are pressed by centrifugal forces, which are caused by the rotational spin flow in the outer region of the flow and at the same time remains the purified air 30 in the flow inside and is over the dip tube 20 dissipated. The with paint particles 43 loaded snow particles 44 adhere to the inner wall of the cone 25 and can flow as a low viscosity suspension through the lower cylindrical cone opening.

The feeder 15 is a shear layer channel 40 upstream, which in cross section in 3 is shown. The shear layer channel 40 consists of two units, a paint particle flow channel 50 and a snow particle flow channel 60 , The paint particles 43 occur over the paint particle entry 41 into the paint particle flow channel 50 one while the snow particles 44 over the snow particle entry 42 into the snow particle flow channel 60 enter. Here is the volume flow 1 the with paint particles 43 laden exhaust air 5 much larger than the volume flow 2 the one with snow particles 44 laden air. The two flow channels 50 . 60 are over a partition 55 separated and united under rejuvenation to a mixing channel 70 in which the two particle-laden air flows enter at different speeds and mix. Due to the different momentum input creates a turbulent shear layer and there is a turbulent mixing process. In this case, air and particle mass flows mix with each other and there is an agglomeration process with the formation of particles laden with paint particles snow particles 72 instead of. These snow particles loaded with paint particles 72 occur at the end of the mixing channel 70 out and into the feeder 15 the separator 10 to be separated there.

QUOTES INCLUDE IN THE DESCRIPTION

This list of the documents listed by the applicant has been generated automatically and is included solely for the better information of the reader. The list is not part of the German patent or utility model application. The DPMA assumes no liability for any errors or omissions.

Cited patent literature

• DE 102010041552 A1 [0003]
• DE 102007036553 A1 [0005]
• DE 102010051085 A1 [0007]

Claims (12)

Plant for separating paint particles ( 43 ) from an air stream ( 5 ), in particular from a coating installation ( 2 ), whereby the air flow ( 5 ) via a feeder ( 15 ) a separator ( 10 ), in which the paint particles ( 43 ) are separable from the air, characterized in that an ice generating device is provided, through which ice crystal particles ( 1 ) are producible, and that at the feeder ( 15 ) and / or the separating device ( 10 ) at least one injection unit ( 27 ) is arranged, with which the Eiskristallteilchen ( 1 ) in the air stream ( 5 ) can be introduced. Plant according to claim 1, characterized in that the separating device ( 10 ) is a Trägheitsabscheideeinrichtung, in particular a cyclone, is. Plant according to claim 2, characterized in that the separating device ( 10 ) has a filter. Installation according to one of claims 1 to 3, characterized in that on the separating device ( 10 ) a collecting device for collecting the bound and / or agglomerated paint particles ( 43 ) is provided. Installation according to one of claims 1 to 4, characterized in that several Eindüseinheiten ( 27 ) are provided, which are controlled separately. Installation according to one of claims 1 to 5, characterized in that the ice crystal particles ( 1 ) are formed substantially from a liquid selected from water, alcohols, ethers, esters, carboxylic acids, carbon dioxide or mixtures thereof. Plant according to one of claims 1 to 6, characterized in that the liquid further additives, in particular for changing the melting point, the viscosity or the wetting properties, are added. Installation according to one of claims 1 to 7, characterized in that the separating device ( 10 ) has a filter or a deposition surface, with which the ice crystal particles with the paint particles ( 43 ) in solid or molten form from the air stream ( 5 ) are separable. Installation according to one of claims 1 to 8, characterized in that a cooling surface is provided, on which from the liquid an ice layer is formed, which is used to form the Eiskristallteilchen ( 1 ) is separated and crushed by means of a separating device. Plant according to one of claims 1 to 8, characterized in that the ice crystal particles ( 1 ) can be generated by means of a spray by spraying the liquid under heat removal. Installation according to one of claims 1 to 10, characterized in that the ice crystal particles ( 1 ) are electrically charged. Installation according to one of claims 1 to 11, characterized in that an agglomeration in a shear layer channel ( 40 ) is provided.

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