Compressor installation with water-injected compressor element

Information

  • Patent Grant
  • 6409489
  • Patent Number
    6,409,489
  • Date Filed
    Wednesday, June 27, 2001
    23 years ago
  • Date Issued
    Tuesday, June 25, 2002
    22 years ago
Abstract
The invention concerns a compressor installation with a water-injected compressor element (1) having a water cycle (6) and a water supply device (15) for supplying water to the water cycle (6), containing a water supply line (16) with a controllable valve (18) and a reverse osmosis filter (17) therein. Onto the water cycle is connected a by-pass (21) in which are erected an ion exchanger (22) and a controllable valve (23). A valve (18) in the water supply line (16) is controlled by a device (20) for measuring the amount of water in the water cycle (6), and the valve (23) in the by-pass (21) is controlled by a device (24) for measuring the conductivity of the water.
Description




BACKGROUND OF THE INVENTION




1. Field of the Invention




The present invention concerns a compressor installation with at least one water-injected volumetric compressor element, provided with a suction line and a compressed air line, driving means for this compressor element, a water cycle in which the compressor element is erected, containing a water separator erected in the compressed air line and a return line for the separated water extending between the bottom side of said water separator and the inner space of the compressor element, and a water supply device for supplying water to the water cycle containing a water supply line with a controllable valve therein and a reverse osmosis filter, a device for measuring the amount of water in said water cycle and a device for measuring the conductivity of the water in this water cycle.




2. Discussion of the Related Art




With such compressor installations, water is injected on the compressing parts of the compressor element, to cool these parts as well as to lubricate them, and to fill the gaps between the mutual compressing parts as well as the gaps between the compressing parts and the housing of the compressor element.




Each compressor element can, depending on the temperature and the humidity of the sucked-in air, consume water or produce water, which is why a water supply device is provided with which, if necessary, water is supplied to the water cycle, usually via the inlet line of the compressor element.




The supplied water must be pure, and the mineral content must be sufficiently low in order to avoid deposits on seals, valves and the like. However, the mineral content should not be too low either, since the water can become corrosive then, for example as carbonic acid from the air can no longer be absorbed in the water and will be present in the water as free carbonic acid, as a result of which the pH will drop.




The corrosive character of the water can be determined on the basis of its conductivity. In order not to be corrosive, the conductivity of the water should be between 10 and 20 μS/cm at 25° C.




Distilled water is expensive. That is why the supplied water is usually treated on site, i.e. it is demineralized in a demineralization device.




A compressor installation with such a demineralization device is described in WO-A-99/02863.




This compressor installation has a single demineralization device which can be a reverse osmosis filter as well as an ion exchanger.




The demineralization device is connected to the rest of the compressor installation via lines with valves, in such a manner that the same device can be placed in the water supply line as well as in a by-pass bridging the water cycle.




The quality of the incoming water has little influence on the life of a reverse osmosis filter, but it does influence its yield. When the quality is bad, the output of the useful permeate will drop, and the output of the concentrate, which is to be removed, will rise.




A reverse osmosis filter is not particularly fit to reduce the conductivity of the water in the water cycle. A major part of the water cycle has to be discharged as a concentrate and hence has to be replaced by fresh water which has not been treated yet, with a relatively high conductivity, whose conductivity has to be reduced in the reverse osmosis filter.




Replacing a reverse osmosis filter as a demineralization device by an ion exchanger is not much better.




An ion exchanger is very well fit to reduce the conductivity of the water cycle, since it is relatively low already, but its life can be strongly reduced when fresh water of bad quality, and thus with a high conductivity, has to be treated.




SUMMARY OF THE INVENTION




The invention aims a compressor installation which does not have the above-mentioned and other disadvantages.




This aim is reached according to the invention in that a by-pass is connected to the water cycle in which are erected an ion exchanger and a controllable valve, whereby the valve in the water supply line is controlled by the device for measuring the amount of water in the water cycle, and the valve in the by-pass is controlled by the device for measuring the conductivity of the water.




The compressor installation thus has a separate demineralization device for the fresh water which is supplied to the water cycle and for reducing the conductivity of the water in the water cycle, so that both demineralization devices can function optimally and have a long life.




The by-pass can bridge the compressor element and thus extend between the return line and the suction line.




The device for measuring the conductivity is preferably provided in the return line.




The water supply device can be connected to the suction line.




The device for measuring the amount of water in the water cycle can be a hypsometer provided in or on the water separator.











BRIEF DESCRIPTION OF THE DRAWINGS




In order to better explain the characteristics of the invention, the following preferred embodiment of a compressor installation according to the invention is described as an example only without being limitative in any way, with reference to the accompanying drawing, which schematically represents a compressor installation according to the invention.




The compressor installation represented in

FIG. 1

contains a water-injected volumetric compressor element


1


, for example a screw-type compressor element, which is provided with a suction line


2


containing an air filter


3


, and a compressed air line


4


, driving means consisting of a motor


5


for this compressor element


1


, and a water cycle


6


in which the compressor element


1


is erected and which further consists of a water separator


7


erected in the compressed air line


4


, which in the given example forms an air receiver, the part of the compressed air line


4


situated between the compressor element


1


and said water separator


7


, and a return line


8


for the separated water which extends between the bottom side of the water separator


7


and the water injection openings opening into the inner space of the compressor element


1


.




In the return line


8


is erected a water cooler


9


.




Downstream to the water separator


7


are successively erected an after-cooler


10


and a second smaller water separator


11


in the compressed air line


4


.




A second return line


12


extends between the bottom side of this water separator


11


and the suction line


2


.




Depending on the atmospheric conditions of the air which is sucked-in via the suction line


2


, the compressor element


1


can consume water or produce it.




Onto the water cycle


6


is connected a discharge line


13


to this end, connected to the bottom side of the water separator


7


, and provided with a controllable valve


14


.




Of course, it is possible for the discharge line to be provided in another place in the water cycle


6


, for example between the water cooler


9


and the compressor element


1


.




In order to supply water to the water cycle


6


, the compressor installation comprises a water supply device


15


containing a water supply line


16


which is not directly connected to the water cycle


6


but to the suction line


2


.




In this water supply line


16


are provided a reverse osmosis filter


17


and a two-way valve


18


.




The concentrate flows away from this reverse osmosis filter


17


via the concentrate line


19


. The permeate flows towards the suction line


2


.




The water supply device


15


contains a measuring device


20


to measure the amount of water which is present in the water cycle


6


and which controls the valves


14


and


18


.




This amount of water can be determined by measuring the amount of water which is present in the first water separator


7


, which can be determined by measuring the water level.




The term ‘measuring’ is understood in the broadest sense here, since not the exact amount of water needs to be known; by ‘measuring’ can also be understood determining when the level drops below a certain minimum value.




The measuring device


20


can possibly also determine when said level rises above a certain higher level to control the valve


14


as a function thereof.




In the given example, the measuring device


20


is thus formed of at least one or several level detectors.




The compressor element


1


is bridged by a by-pass


21


which is connected to the return line


8


between the compressor element


1


and the water cooler


9


on the one hand, and which is connected to the suction line


2


on the other hand.




In this by-pass


21


are erected an ion exchanger


22


and a controllable valve


23


.




This valve


23


is controlled by a device


24


for measuring the conductivity of the water, erected in the return line


8


.




When the device


20


for measuring the amount of water in the water cycle


6


detects that there is too little water, or in other words when it detects that the level in the water separator


7


has dropped under a minimum level, it will order the valve


18


to open until a sufficient amount of water has been supplied to the water cycle


6


via the water supply line


16


.




This supplied water has been purified in the reverse osmosis filter


17


.




When the device


24


for measuring the conductivity measures a readout which is too high, it will order the valve


23


to open, as a result of which water flows from the return line


8


via the by-pass


21


and thus over the ion exchanger


22


to the suction line


2


.




No water from the water cycle is lost hereby.




As the conductivity of the water from the water cycle is already relatively low and in any case lower than the conductivity of the fresh mains water, the ion exchanger


22


will only have to further reduce the conductivity of the water from the water cycle treated by it to a limited extent, which implies that the ion exchanger has a relatively long life and does not have to be replaced often.




Since, in order not to restrict the life of the ion exchanger


22


, the reverse osmosis filter


17


takes care of the purification of the supplied water, the latter will have to function optimally under all circumstances.




Thus, according to a variant, the water supply device


15


may contain a pump


25


which is provided upstream to the reverse osmosis filter


17


in the water supply line


16


to put the water under extra pressure. The osmotic pressure to be overcome depends on the concentration of dissolved salts in the water.




The extra pressure will ensure a good service of the membrane when the water supply line


16


is connected to the public water supply system and the water supply pressure is insufficient.




According to another variant, a decalcifier


26


is erected in the water supply line


16


, upstream to the reverse osmosis filter


17


.




If the feed water has a high conductivity, it will be due for more than 80% to the presence of calcium salts and magnesium salts.




They can be removed by means of the decalcifier


26


, which significantly improves the service of the osmosis membrane of the reverse osmosis filter


17


.




As is represented in the figure, this decalcifier


26


can be erected in the water supply line


16


together with the pump


25


, in particular upstream to the latter.




The volumetric compressor element


1


does not necessarily have to be a screw-type compressor element. It may just as well be a tooth compressor element, a spiral compressor element or a mono screw-type compressor element.




The invention is by no means limited to the above-described embodiment represented in the accompanying drawings; on the contrary, such a compressor installation can be made in all sorts of variants while still remaining within the scope of the invention, as specified in the following claims.



Claims
  • 1. A compressor installation withat least one water-injected volumetric compressor element, provided with a suction line and a compressed air line; driving means for this compressor element; a water cycle in which the compressor element is erected, containing a water separator erected in the compressed air line and a return line for the separated water, extending between the bottom side of said water separator and the inner space of the compressor element; a water supply device for supplying water to the water cycle containing a water supply line with a controllable valve therein and a reverse osmosis filter; a device for measuring the amount of water in said water cycle; a device for measuring the conductivity of the water in this water cycle, a by-pass connected to the water cycle in which are erected an ion exchanger and a controllable valve; whereby the valve in the water supply line is controlled by the device for measuring the amount of water in the water cycle, and the valve in the by-pass is controlled by the device for measuring the conductivity of the water.
  • 2. The compressor installation of claim 1, wherein the by-pass bridges the compressor element and thus extents between the return line and the suction line.
  • 3. The compressor installation of claim 1, wherein the device for measuring the conductivity is provided in the return line.
  • 4. The compressor installation of claim 1, wherein the water supply device is connected to the suction line.
  • 5. The compressor installation of claim 1, wherein the device for measuring the amount of water in the water cycle is a hypsometer provided in or on the water separator.
  • 6. The compressor installation claim 1, wherein the water supply device contains a pump which is erected in the water supply line, upstream to the reverse osmosis filter.
  • 7. The compressor installation of claim 1, wherein the water supply device contains a decalcifier which is erected in the water supply line, upstream to the reverse osmosis filter.
  • 8. The compressor installation of claim 1, wherein a discharge line is connected to the water cycle, provided with a valve which is controlled by the device for measuring the amount of water in the water cycle.
  • 9. The compressor installation of claim 8, wherein the discharge line is connected to the water separator.
Priority Claims (1)
Number Date Country Kind
000409 Jun 2000 BE
US Referenced Citations (6)
Number Name Date Kind
4968231 Zimmern et al. Nov 1990 A
5033944 Lassota Jul 1991 A
5174741 Tohgo Dec 1992 A
6016657 Buschur Jan 2000 A
6102683 Kirsten Aug 2000 A
6174148 Suzuki Jan 2001 B1
Foreign Referenced Citations (3)
Number Date Country
44 47 097 Jul 1996 DE
197 29 498 Feb 1999 DE
58-148287 Sep 1983 JP