The present invention relates to a device, a system, and a method for dissolving a solid chemical substance in water.
The present invention finds advantageous application in the treatment of water for swimming pools, drinking water, industrial water, and water in general, in particular, but not exclusively, for dissolving in an optimal way solid derivatives of chlorine (calcium hypochlorite, isocyanides, mixtures or derivatives thereof, etc.), to which the ensuing description will make explicit reference without this implying any loss of generality.
In the field of devices for dissolving a solid chemical substance in water, in particular in the field of water chlorination, it is known to use a device for dissolving solid substances in water comprising: a container, which has a collection portion for containing an aqueous solution; perforated supporting means (or in any case means permeable to liquids), which are set above the collection portion and are designed to support the solid chemical substance; and water-feeding means set above the supporting means for directing at least one jet of water onto the solid chemical substance to be dissolved.
The chlorinated water obtained by said dissolving process is currently left in the aforesaid container until it is fed into the swimming pool; for this reason, the solid chemical substances dissolved can precipitate, creating deposits inside the container. Normally, the solid chemical substances comprise calcium hypochlorite, and, consequently, within the container there may form deposits principally of calcium sulphate and calcium carbonate. Said undesirable deposits have the tendency to accumulate, in particular, around the connections that set the portion for collection of the chlorinated water in hydraulic communication with the ducts of an external hydraulic circuit that comprises the aforesaid swimming pool.
To overcome the periodic need to eliminate said deposits by means of manual intervention on the part of an operator, an intervention that involves interruption of operation of the device and, hence, of the treatment of the water of the swimming pool, it has been proposed in the past to provide mixing means, such as mechanical agitators, with propellers or blades, or nozzle agitators (supplied by a respective blower or by a pump), which are arranged at the collection portion and are designed to keep the chlorinated water contained therein in a state of agitation.
The above solution, albeit effective, entails additional installation costs and only manages to reduce, without eliminating altogether, the need to suspend operation of the chlorination device periodically and the feed of the chlorinated water to the swimming pool in order to carry out the operations of cleaning and maintenance of the mechanical members that constitute the agitators or the blower/pump for supplying the flow to the nozzles. Furthermore, said solution may involve a considerable expenditure in terms of energy, especially in the case where the volume of water to be kept in agitation is large.
It is moreover to be noted that, frequently, known dissolving devices comprise floats, the mechanisms of which are at least partially immersed in the chlorinated water. Said mechanisms tend to get damaged with particular frequency both on account of phenomena of corrosion and on account of salt deposits.
The document No. WO2005/070837 describes a device for dissolving a solid substance in water equipped with a mechanical agitator (FIG. 1, reference number 8), a spray agitator (FIG. 1, reference number 29) and floats with mechanisms immersed in the water. The device disclosed in WO2005/070837 envisages discontinuous feed and discharge of water (see page 11, lines 5-23). In particular, the discharge of water is performed only when the concentration of solute in the external circuit is lower than a reference quantity; and feed occurs only in an intermittent way.
The document No. US2005/244315 describes different embodiments of a device for dissolving solid chemical substances. All the devices referred to in US2005/244315 have only feeding means for bringing the water into contact with the solid chemical substance and not further units (different from the feeding means) for keeping the solution containing the chemical substance in agitation (see the figures). According to some embodiments, constant amounts of water are fed into the device intermittently (in particular, see paragraph [0070] and the first three lines of paragraph [0068]). According to another embodiment, feed of water is continuous but constant.
The document No. WO99/35078 describes a system for water treatment. The system described in WO99/35078 envisages feed of water through a sprayer. The sprayer is operated intermittently (see in particular, page 7, lines 7-14; page 7, line 30; page 8, lines 11-14).
The aim of the present invention is to provide a device, a system, and a method for dissolving a solid chemical substance that will overcome at least partially the drawbacks of the prior art and will be, at the same time, simple and inexpensive to produce.
In accordance with the present invention a device, a system, and a method for dissolving a solid chemical substance are provided according to what is recited in the ensuing independent claims and, preferably, in any one of the subsequent claims that depend either directly or indirectly upon the independent claims.
The present invention will now be described with reference to the annexed drawings, which illustrate non-limiting examples of embodiment thereof and in which:
Designated as a whole by 1 in
The container 3 is set vertically, is provided with a collection portion 8 (
The device 1 further comprises a charging chamber 10, which is set above the collection portion 8 within the container 3 and is designed to contain the solid chemical substance 2 for chlorination. In particular, the solid chemical substance 2 is in the form of tablets and may contain calcium hypochlorite, or isocyanides, and/or mixtures and/or derivatives thereof.
According to further embodiments (not illustrated), the solid chemical substance 2 may be in the form of powder or granules and may contain other types of salts.
The charging chamber 10 has substantially the shape of a truncated cone tapered downwards and is delimited by a perforated bottom wall 11 (which is hence permeable to liquids), designed to support at the bottom the solid chemical substance 2, and by a side wall 12, which is at least partially inclined and also partially perforated and is designed to contain the solid chemical substance 2 laterally. According to some embodiments, the holes in the side wall 12 extend up to a distance of 5-15 cm from the bottom wall 11.
The dimensions of the holes in the walls 11 and 12 are chosen according to the nature of the solid chemical substance 2; in particular, when the solid chemical substance 2 is in the form of tablets, the dimensions of the holes in the walls 11 and 12 are chosen as a function of the size of the tablets.
According to further embodiments (not illustrated), the charging chamber 10 has a shape chosen in the group consisting of: substantially conical, substantially frustopyramidal, and substantially pyramidal.
Advantageously, the angle of tapering is selected so as to favour progressive dropping, by gravity, of the tablets of the solid chemical substance 2 introduced into the charging chamber 10 in the direction of a dissolving portion 13 thereof. In this way, also in the case of a device 1 of large dimensions, it is sufficient to provide just one liquid-dispersing unit 14 in the dissolving portion 13, towards which, in use, the tablets progressively drop.
The solid chemical substance 2 is dissolved at said dissolving portion 13, which is delimited at the bottom by the bottom wall 11. The charging chamber 10 further comprises a storage portion 15, which is set above the dissolving portion 13 and is designed to contain the solid chemical substance 2 above the dissolving portion 13 itself.
The device 1 further comprises the unit 14 for dispersing the water, which is positioned above the bottom wall 11, in particular within the charging chamber 10, and is designed to direct at least one jet of water towards the solid chemical substance 2 contained in the dissolving portion 13. In particular, the liquid-dispersing unit 14 comprises a spray head 17 (advantageously adjustable in height with respect to the bottom 11), which is set at a top end of the dissolving portion 13 and is designed to direct the water downwards and/or laterally, but not upwards, in such a way as substantially not to wet the solid chemical substance 2 located above the spray head 17 and contained in the storage portion 15. In the presence of solid chemical substances with a high degree of solubility (such as calcium hypochlorite), the spray head 17 is positioned at 5-15 cm from the bottom wall 11. In the presence of solid chemical substances with low solubility (for example, trichloro-isocyanide), the spray head 17 can be located also in a higher position, even above the overall mass of the chemical substance to be dissolved.
In this way, dissolving of the solid chemical substance 2 occurs very gradually; advantageously, this determines a low development of ill-smelling gases and the right concentrations of the solute within the aqueous solution, with consequent limited possibility of formation of deposits due to the precipitation of the dissolved solid substances.
The position of the spray head 17 is consequently modifiable (as may, for example, be noted in the embodiment of
The collection portion 8 comprises a bottom portion 18 having a substantially conical shape or the shape of a truncated cone tapered downwards. Advantageously, the angle of tapering of the side wall of the bottom portion 18 favours the flow of the water charged with solute (for example, chlorinated water, in the case where chlorine-based substances are used) downwards and at inlet to the discharging unit 5 and then towards the external hydraulic circuit 6, thus considerably reducing the likelihood of formation of deposits of precipitated salts.
According to embodiments (not illustrated), the bottom portion 18 has a shape chosen in the group consisting of: pyramidal and frustopyramidal.
The feeding system 4 comprises a duct 19 (
The dispersion pipe 21 is in hydraulic communication with the liquid-dispersing unit 14. The recirculation pipe 22 has an end opening 23 set in the collection portion 8.
A flow of water coming from the external hydraulic circuit 6 and fed by means of a pump 24 into the feeding system 4 is divided, in use, between the dispersion pipe 21 and the recirculation pipe 22 as a function of the degree of opening of a regulating valve 25 provided on the dispersion pipe 22 itself. The degree of opening of the regulating valve 25 is governed, by means of manual intervention, by an operator or else, automatically, by a control unit 26 (
It is to be noted that the liquid-dispersing units 14 is different from the means for feeding the collection portion 8 (in particular, the pipe 22 and the opening 23). In this way, the liquid-dispersing unit 14 feeds the device 1 with a flow (i.e., at least one jet) of water different from a flow of water fed into the device 1 itself by the feeding means.
According to specific embodiments, the regulating valve 25 is of the open/close type. When the sensor 27 detects a concentration lower than a given value, the regulating valve 25 opens; when the sensor 27 detects a concentration higher than a given value, the regulating valve closes.
According to one aspect of the present invention, the device 1 further comprises a regulating unit 29 for regulating the passage of water through the recirculation pipe 22, in particular through the connection 20. Said regulating unit 29 comprises a maximum-level/minimum-level control valve 30 and a differential float 31, which is located preferably in the proximity of a wall of the collection portion 8 and movement of which determines the degree of opening of the valve 30 (and hence of the connection 20).
In other words, the regulating unit 29 regulates the amount of water that is fed into the pipes 21 and 22.
The regulating unit 29 is then designed to prevent emptying and overflow of the collection portion 8 through the discharging unit 5.
In particular, the valve 30 is a differential valve (namely, it is able to present different degrees of opening).
The float 31 is mobile between a respective lowered position and a respective raised position—in use, the float 31 is in the raised position when the aqueous solution reaches or exceeds a given maximum level.
The float 31 and the control valve 30 are connected by means of a mechanism (in itself known and not illustrated). In this way, the control valve 30 regulates the opening of the connection 20 as a function of the position of the float 31.
The float 31 opens the connection 20 progressively as a function of the level reached by the water charged with solute (for example, chlorinated water) in the collection portion 8. The greater the height of the float 31, the less the water that is fed in through the connection 20.
Once the connection 20 is opened, the float 31 enables feed of water from the recirculation branch into the collection portion 8 until the given maximum level is reached (raised position). When the float 31 is in the completely raised position, the connection 20 is completely closed (this, however, does not occur during normal operation, but only in the case of arrest or of poor operation due, for example, to a breakdown in the system).
In particular, the regulating unit 29 is designed so that the control valve 30 and the mechanism of connection to the float 31 are always above said given maximum level, i.e., always above the free surface of the aqueous solution contained in the collection portion 8. In this way, advantageously, the valve 30 with the corresponding hydraulic and/or mechanical connections never comes into contact with very concentrated aqueous solutions, even during the step of dissolving of the solid chemical substance 2 and, consequently, cannot be the site of undesirable deposits of saline precipitates potentially having a corrosive effect on their surfaces.
In use, the flow of water fed into the device 1 through the feeding system 4 is regulated in response to the variations in level of the aqueous solution in the collection portion 8. In use, the discharging unit 5 is substantially always open and enables substantially continuous discharge of the aqueous solution (chlorinated water) to the external hydraulic circuit 6.
In other words, during operation of the device 1, there is a substantially continuous (constant) flow of aqueous solution leaving the collection portion 8 through the discharging unit 5. It is to be noted that, advantageously, the flow rate of the discharging unit 5 is smaller than the maximum flow rate of the feeding system 4 (namely, of the duct 19).
Furthermore, in use, there is a flow at inlet into the collection portion 8 that is given by the sum of:
It should be emphasized that the flow of water coming from the external hydraulic circuit 6 through the pipe 22 is maintained substantially continuous (albeit not always constant). In this regard, it should be noted that, in use, when the level of the aqueous solution within the collection portion 8 increases, the float 31 rises and gradually reduces the amount of liquid that is fed in through the recirculation pipe 22. When the flow of water fed in is less than the amount discharged, the float 31 again drops, opening more the connection 20. In this way, a sort of dynamic balance is achieved that enables a substantially continuous inflow and outflow of liquid into/from the collection portion 8.
The continuous flow thus brought about through the collection portion 8 keeps the aqueous solution contained therein advantageously in agitation, thus rendering superfluous the presence of mixers.
In this way, the precipitation of salts, chiefly calcium carbonate and calcium sulphate (in the case where calcium hypochlorite or similar products are used), and consequently the formation of deposits within the collection portion 8, becomes relatively unlikely.
The sensor 27 is designed for detecting the concentration of solute within the aqueous solution present in the external hydraulic circuit 6 upstream of a duct 32 of the discharging unit 5 (
The concentration sensor 28 is designed for detecting the concentration of solute within the aqueous solution present in the collection portion 8.
Advantageously, where, in use, the sensor 28 detects a concentration of solute outside a given range (in particular, when the concentration is too low), an alarm device (of a type in itself known and not illustrated) is activated, and the entire device 1 is blocked.
The control unit 26 is electrically connected to the regulating valve 25, to the pump 24, and to the sensors 27 and 28.
According to some embodiments, the control unit 26 is designed to actuate the regulating valve 25 on the basis of the detections made by the sensor 27 so as to maintain the concentration of solute in the water of the swimming pool (or tank) 7 (namely, in the water present in the external hydraulic circuit 6) between a minimum concentration and a maximum concentration. In particular, in use, when the concentration of solute detected by the sensor 27 is relatively close to the minimum concentration, the control unit 26 modifies the degree of opening of the regulating valve 25, thus altering the ratio between the flowrate of the contribution of dispersion and the flowrate of the contribution of recirculation so as to favour the contribution of dispersion. Consequently, a larger amount of solid chemical substance 2 is dissolved, thus obtaining a larger amount of concentrated aqueous solution that drops back into the collection portion 8 and, from there, proceeds continuously through the discharging unit 5 towards the external hydraulic circuit 6 (and then to the swimming pool or tank 7).
Instead, when the concentration of solute detected by the sensor 27 is relatively close to the maximum concentration, the control unit 26 modifies the degree of opening of the regulating valve 25, altering the ratio between the flowrate of the contribution of dispersion and that of the contribution of recirculation so as to favour the contribution of recirculation. Consequently, a smaller amount of solid substance 2 is dissolved, whilst a larger amount of water having low concentration of solute passes into the collection portion 8, as has been described previously.
The container 3 moreover has an overflow pipe 33 (
The device 1 further comprises a retention valve 34 (
The feeding system 4 comprises a manual valve 35, which is set along the duct 19 and the degree of opening of which determines the maximum flow rate of the feeding system 4 (namely, of the duct 19).
According to advantageous embodiments, the device 1 is made up of a plurality of modular components. According to the embodiment illustrated in
The various modular components described above (namely, the components 36, 37, 38 and the lid 9) can be connected to one another by means of fluid-tight couplings (for example, blocking mechanisms of the bayonet or frustoconical couplings, or other types of blocking mechanism) (examples of blocking mechanisms are illustrated in cross-sectional view and at an enlarged scale in
In particular, each top modular component can comprise one or more (in the case in point two) projections or tabs (i.e., keys) 39 (see, for example,
Each bottom modular component has an element 42 that projects upwards and is designed to be inserted in a respective seat 43 (illustrated in cross-sectional view and at an enlarged scale in
In this case, the charging chamber 10′ comprises: an auger feeder or else some other device designed for dispensing material in powder and/or granular form, at the same time preventing the effect of packing thereof within the chamber 10′ (said devices are in themselves known and are hence not illustrated), which is set in a housing 44; and a side seat 45, positioned in which is a motor for driving the auger feeder. The housing 44 has a side opening 46, through which, in use, the solid chemical substance 2 is directly fed into the collection portion 8.
The charging chamber 10′ moreover has a storage portion 15′, which is designed to contain the solid chemical substance in powder or granular form, is set, above the auger feeder (i.e., the housing 44), is delimited laterally by a wall 47, and is tapered in the direction of the housing 44.
The device 1 of
or else other products in the form of tablets with an extremely low solubility.
In this case, the spray head 17 is set above the storage portion 15. Like this, it is possible to moisten the solid chemical substance 2 for long periods, thus favouring dissolving thereof.
It should moreover be noted that the charging chamber 10″ of the device 1 of
The device 1 of
From what has been set forth above, it is clear that the modular structure of the device 1 (in particular of the container 3) enables, by adding and/or replacing a component, modification of the functionality of the device 1 itself, adapting it to the different types of solid chemical substance 2 in an extremely simple way.
According to a further aspect of the present invention, a system 49 is provided, comprising the device 1 and the external hydraulic circuit 6, as defined above. In particular, an embodiment of the system 49 is illustrated in
The degree of opening of the valve 51 defines the flow rate of the discharging unit 5 (i.e., of the duct 32).
Regulation of the valve 51 and of the manual valve 35 enables determination of the ratio between the flow rate of the discharging unit 5 and the maximum flow rate of the duct 19.
In particular, the valve 51 and the manual valve 35 are regulated (usually manually by an operator during installation of the device 1) so that, as has been said, the maximum flow rate of the duct 19 is greater than the flow rate of the discharging unit 5.
It is to be noted that the couplings of
Number | Date | Country | Kind |
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BO2009A000142 | Mar 2009 | IT | national |
Filing Document | Filing Date | Country | Kind | 371c Date |
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PCT/IB2010/000474 | 3/8/2010 | WO | 00 | 2/21/2012 |