The invention relates to a method for cleaning the plates or fins of heat exchangers, which could also have larger depths, wherein the invention also relates to a device for cleaning such surfaces.
It is already known to supplementally use compressed air in high pressure cleaning equipment (from 800 bar pressure). In this case, larger amounts of water are charged with relatively small amounts of air in order to obtain a higher cleaning effect. Because here overwhelmingly water quantities are ejected with high pressure, a considerable force is applied to the parts to be cleaned, which can cause damage. For many surfaces only a low water pressure is manufacturer-approved, which mostly does not develop enough cleaning power. A water pressure of for example greater than 10 bar or the addition of abrasives, even the softer kind, can here already lead to the destruction of parts or an undesirable roughening of the surfaces.
Cleansing of plate or finned heat exchangers with a high pressure cleaner can lead to considerable damage, especially when the jet device is not angled exactly 90° to the sensitive fins. Here, the high-pressure stream of water emitted from the nozzle impinges obliquely on the sensitive fins, which can lead to significant damage.
Chemical cleaning agents are also used for cleansing, which then need to be removed again by water jet cleaning, wherein here larger amounts of chemical contaminated wastewater is produced. This effluent has to be caught—if at all possible—on the Earth's surface. For this purpose, the area around the finned heat exchanger must be protected to prevent damage to the environment.
Cleaning a plate or finned heat exchanger with only a water jet has, for the most part, not produced a satisfying cleaning effect.
Aim and purpose of the invention is to provide a method and a device for cleaning heat exchanger plates or fins, having a gentle yet effective cleaning effect at a low application of water and with the avoidance of chemicals.
According to the invention this problem is solved by the features of claims 1 and 11, advantageous embodiments and further developments of the invention will become apparent from the subsequent dependent claims.
The advantages achieved with the invention are comprised thereof, that by means of a low-pressure cleaning process using compressed air and small amounts of water as blasting medium, a cleaning method is provided which is particularly suitable for the cleaning of heat exchanger plates or fins. Since compressed air with a small amount of water has a much lower density than a jet of water, and in addition can be brought to a very high speed by a corresponding nozzle, full penetration of the heat exchanger is achieved even at low pressure of the carrier gas.
The use of a low pressure jet, which is generated only by means of compressed air and a small amount of pure water with no additives, allows a gentle but effective cleaning of the fins in the entire construction depth of the heat exchanger. The surfaces of fins to be cleaned are aligned parallel to the jet. Since, in contrast to the use of the method on other surfaces, such as graphite or foils, the beam angle of the surfaces to be cleaned is near to 0°, the jet pressure exerted on the surfaces is very low here. The surprising cleaning effect here can not be attributed to the impact of the jet on the surface, but rather results surprisingly from the friction effect of the jet on the surfaces of the plates or fins A pulsating of the jet contributes here to the cleaning action. The problem is inventively overcome in that compressed air is supplied to a jet nozzle which has a converging throat portion and an adjoining diverging section, and that the water is introduced into the carrier gas stream preferably before the constriction, or where appropriate in or downstream of the throat of the nozzle, and is accelerated to a high speed, at least close to the speed of sound or supersonic speed. Tests have shown that even at a relatively low pressure of the compressed air starting from 1 bar, preferably from 1.5 bar, and thus a low jet impact pressure, complete penetration of the jet through the finned heat exchanger is achieved. For the cleaning of heat exchangers with larger construction depths, of the jet pressure can be increased the jet pressure can be increased to the extent tolerated by the fins. Thereby even solidified or sticky layers of dirt are removed without bending or otherwise damaging the thin fins. To achieve a uniform cleaning with little overlap areas a flat nozzle is preferably used. A flat nozzle when used in the cleaning of “normal” surfaces often exhibits a smaller cleaning effect when compared to a circular nozzle, however, in the cleaning of finned heat exchangers, the jet passes more effectively into the narrow channels of the plate-fin heat exchanger, since the impact effect on the front side of the exchanger is strongly reduced. This leads to an improved and more uniform cleaning effect.
In a practical embodiment the flow rate of the carrier gas is 4000 liter per min, preferably 6,000 liter per min. The amount of water supplied in liters should be, in proportion to the compressed air, preferably be less than 1:1000. The supplied water should be metered in at a distance of at least 30 mm upstream of the constriction of the jet at a pressure of at least 50% of the pressure of the compressed air, but preferably be similar to or higher than the pressure of the compressed air. In the case of a dosing in of the supplied water at a distance of less than 30 mm from the nozzle throat, and at or downstream of the nozzle throat, the water pressure can be reduced as a function of the decreasing pressure with increase in speed of the compressed air or introduced without pressure. The water is then sucked in by the high flow velocity of the water.
Tests have also shown that even at relatively low pressure of the compressed air of for example 1.5 bar and thus a relatively low jet impact pressure a high-pressure cleaner with superior high cleaning effect is already achieved, able to remove any solid or sticky dirt layers, without attacking the underlying surface or damaging the fins. In addition to the effect achieved by the high friction rate of the compressed air and the fine water droplets homogeneously distributed in the compressed air, the pulses of a pulsating jet also contribute in to the cleaning success.
In this advantageous embodiment of the invention, the jet may be induced to pulsate by the design of the water pump and/or with appropriate valves in the water and/or compressed air supply, which leads to an enhancing of the cleaning effect. In the case that the existing water pressure is adequate, an additional pump to increase the pressure of the water can also be dispensed with. An improvement of the cleaning effect can also be achieved by heating of the compressed air or medium, for example, by means of heat exchanger, to clean for example heavily oil-contaminated surfaces faster and more successfully. The required water preferably has drinking water quality, but also properties near to drinking water quality. For special requirements there is there is also the possibility of improvement in the effect by changing the pH of the water.
The objective and purpose of the invention is, in addition to the provision of the process, the provision of an device for carrying out the cleaning of the plates or fins of a plate or finned heat exchanger. For cleaning, preferably only compressed air and water are used. The device here comprises a jet nozzle with a source of compressed air, wherein the jet nozzle has a section converging to a throat section and a subsequent diverging section. Next a feed line for the water is provided, which is designed for the addition of water before, in or after the jet nozzle. At a feeder for the water which serves as an abrasive, the volume of the amount of water to the volume of the compressed air in the ratio is less than 1:1000, preferably less than 1:2000.
Herein the jet nozzle is preferably of a convergent-divergent design, preferably a Laval nozzle. In the liquid supply a suitable throttle valve is provided upstream of the jet device to regulate the amount of water. Thereby the water/liquid is fed to the carrier gas directly or via a distribution chamber with at least one outlet port. A diaphragm pump or a piston pump is preferably provided to transport the water/liquid. The displacement thereof should be less than 1.00 liter. A pressure amplifier may be arranged behind the membrane pump. Interrupter valves can be provided for generating a pulsed nozzle stream of water and/or compressed air, and in addition changing pipeline diameters from the water supply up to the pump can also bring about desired pressure changes of the water.
The transport of water can be facilitated through any kind of pumps, preferably by a membrane pump or piston pump, which suck the water, but can also occur under water hose pressure. An advantage of using a compressed air-powered water pump is that no additional electrical power supply is required, whereby hour meters, etc. can be powered by small batteries or other external power sources.
When installing a pressure amplifier downstream of the diaphragm pump or piston pump, the pressure of the control air can be kept small, whereby the water pressure can be increased, however, well above the control pressure.
The generation of a pulsed jet stream can hereby be by the design of the pump as a diaphragm pump and/or through the use of the interrupter valves for water and/or compressed air. The pipe from water supply up to the pump may have different diameters.
According to a further preferred embodiment of the device, demineralization of water takes place prior to being introduced into the device, or in a system in the device having (e.g. osmosis or ion exchange system).
The use of a flat nozzle is particularly advantageous for the device. For cleaning hard to reach areas, the use of an injection lance with adjustable jet angle is particularly advantageous.
An embodiment of the invention is illustrated purely schematically in the drawings and will be described in greater detail below. In the drawings:
In the inventive method and the device of the invention, a carrier gas other than air can and another liquid substance other than water can be used.
01 jet nozzle
02 line
03 distribution chamber
04 outlet
05 flow line
06 constriction
07 section
08 section
09 carrier gas/compressed air
10 pressure regulator or choke valve
Number | Date | Country | Kind |
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10 2012 014 605.1 | Jul 2012 | DE | national |
Filing Document | Filing Date | Country | Kind |
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PCT/DE2013/100273 | 7/23/2013 | WO | 00 |