WATER SOFTENER FOR THE DOMESTIC LINEN WASH

Abstract: Water softener for domestic use, adapted to be attached also to the usual washing machines. operating on the principle of ion exchange by means of resins, with automatic regeneration cycle in pre-established and constant conditions, comprising a tank (11) for the regeneration saline solution, an impulse-actuated dispens­ ing valve (13), a float (14) level-regulator connected to the valve (13) which controls the flow of saline solution through a calibrated hole (10) in the bottom of the tank (11). Fixed within the tank (11) is a perforated container (12) which contains the sodium chloride required for forming the saline solution for regenerating the resins. The assembly comprises, finally, a container (3) for the ion exchange resins, and a three-way distribution valve (1) having two operating positions, namely one for the exchange cycle and one for the regeneration cycle.

Description: Water softener for the domestic linen wash. This invention relates to a small-sized, easily attached device, intended for domestic use in softening a sufficient quantity of the supply water required for a normal linen washing operation, either manual or mechanical in a washing machine, to optimum technical and economic conditions. The importance and usefulness of softening the water used for domestic linen washing are apparent, in that it permits to "relieve" the task of a detergent in neutralizing the negative effect of the water hardness on the performance and results of a washing operation. As a consequence, the "cleansing force" of a detergent can be utilized to a greater extent in that the requirements of seizing action on the salts of calcium and magnesium (hardness producers) will be limited. A final result can be a reduction, in the present formulations, of the builders having a seizing action, such as polyphosphates, the use of which is being discouraged by regulations all over the world for ecological reasons, due to the well -known eutrophication effects on sea water and lake water adjacent to the coasts. The device according to the invention substantially comprises an upper tank for the regeneration brine, which includes a basket-like container for the crystals of salt, a float level-regulator connected to a valve which controls the inlet of water, a cover with a vent pushbutton, and a lower tank containing, in a suitably-sized tube, the ion exchange resins. The device is connected at one side, through a two-position distributing valve, to the water supply or to the discharge, and at the other side to the user (usually a washing machine). By virtue of its small size (width about 15 cm. and height 50 to 65 cm.), the device can be advantageously fixed to wall near the utilization spot, or directly to the frame of a common washing machine. The basic and distinctive characteristic of this system with respect to those existing and known at present is its low cost, due to the simple automatic regeneration cycle and the reduced amount of salt, proportionate to the required specific exchange capacity, together with high performance and efficiency of ion exchange, The ion-exchange water-softening has been widely applied both in the industrial and civil fields, and has been carried out by several devices having different technical and constructional characteristics, often complicated and expensive. The resins generally used for this purpose are formed by polymers of high molecular weight such as styrens/ /divinylbenzene, insoluble in water which serve as supports receiving, during the step of preparation or polymerization, active functional groups, of anionic characteristics, generally sulfonic groups, that after salification into sodium form, can exchange their cations with the Ca++ and Mg++ cations present in hard water. EMI3.1 When all the available exchange groups have been exhausted, the resins must be regenerated by means of concentrated solutions of NaCl; the contact between the resins and the regeneration solution should last a sufficient period of time, such as 30 to 60 minutes. EMI3.2 "Exchange capacity" can be defined as the eauivalent in CaCO3 of the calcium and magnesium salts (expressed in g) existing in the water and that is exchanged or "seized" by 1 litre of resin; "regenerative level" can be defined as the quantity of NaCl used in the regeneration cycle. These values can be used to calculate the "efficiency" of the complete cycle of exchange and regenerationj the theoretical value being given by the following formula: Equivalent weight of CaCO3 Y = - = 0.855 Equivalent weight of NaCl Practically, this ratio is always lower than the theoretical value because the regeneration reaction will not saturate all the exchange groups, and because as the resin saturation increases, the "force" of the solution ions to remove the ions fixed on the resin decreases. As a consequence, the amount of NaCl is, practically, greater than the theoretical stoichiometric value. The economic cost of the process substantially depends upon the value of Y and hardness of the water to be treated. Several types of devices based on the ion exchange principle are presently used. In the industrial field, for example, plants of high capacity for the treatment of boiler feed-water at 4 to 5,cm0 1/h or more have been installed in power plants. Other types of softeners of smaller size and capacity, ard flow-rates up to 3,000 l/h, have been used to soften the water for several civil purposes, including alimentary purposes, at home. The plants of this latter type are designed so that the operations concerning the whole cycle of the resin take place automatically and require no action of the operator. The opening and closing of the hydraulic circuits are effected by electrically-operated valves under the control of an electric timer. These plants are very expensive and can be compensated only in case of softening of large amounts of water required by big buildings or by a plurality of buildings. In case of particular uses, such as small consumers with a capacity lower than 1,000 litres, other types of automatic or manual softeners such as those mounted on some dishwashing -machines, can be used. These softeners utilize small amounts of resin (0.5 to 5 litres) which will be regenerated either by dissolving sodium chloride crystals in water or directly diluting concentrated solutions of sodium chloride. The regeneration, in the small softeners mounted on dishwashing machines, takes place usually at the end of the washing cycle, under the control of electn.cally-oerate valves that modify the path and flow-rates of the water to control the several cycles of the resin. In these small -capacity softeners, either automatic or manual, the regeneration takes place in a totally different way with respect to industrial plants and in a very different condition from the optimum conditions indicated in technical literature. Heretofore, in facts, the most common systems were influenced by several factors, so as to cause an approximate regeneration and require too high amounts of regenerating material, and entail, therefore, excessive waste. Generally, the regeneration cycle is carried out in too short periods of time (about 10 to 20 minutes) that are shorter than required (30 to 60 minutes), while the brine has a variable concentration that decreases from the beginning to the end of a cycle, and its amount changes depending on the pressure of the water supply. The proportioning or dosage of the regenerating material (NaCl), particularly in the softeners for dishwashing machines, is approximately constant regardless of the hardness of the water to be treated. Obviously, these conditions entail poor results, both in the exchange capacity and total performance and in the final hardness of the treated water. In case of a dishwashing machine, for ezazaple, the final hardness will not fall below 50F and the performance Y of the cycle is about 0.1. The softening system according to this invention is characterized by an optimized regeneration cycle so as to obtain an economic exchange process and a constantly concentrated brine throughout the regeneration cycle, the latter being regulated in accordance with the hardress of the water to be treated. The system is operative within a wide range of flow-rates of the water-supply, such as O to 700 litres/h, so as to include the flow-rates of the most common washing machines marketed at present. The requirement of resins is also very limited, that is about 1. litre, whereas other small-capacity plants require, for the same rate of exchange, much greater amounts, such as 5 to 10 litres. These features grant the same results as in the industrial and automated plants, even in the absence of complicated timing and automated systems. The lower initial cost and limited operating cost, granted by the "calibration" or regulation of the exchange process, especially with regard to the propcrtioning of the sal42 as a function of the initial hardness of the water to be treated, will provide a system which is more economic than any other softening system. An essential technical feature, also, is constituted by the high and constant value of the efficiency factor Y at any value of the initial hardness of the water to be treated and corresponding regeneration levels. Therefore, the economic cost of the softening process depends only on the hardness of the water to be treated. Another advantage is that the device according to the above system can be permanently cc=ected to the water -supply, to the washing machine and to the discharge outlet (the only requirement being to connect the resin-containing column in such a position as to locate its top edge at a higher level than the discharge) without any displacement or connection to external collection containers. Further features and advantages of this invention will be better understood in the course of the following detailed description of some preferred embodiments thereof, made with reference to the accompanying drawings wherein: Fig. 1 is a diagrammatic view of the device according to the invention; Fig. 2 is a crosssectional view of a detail of the device of Fig. 1 Fig. 3 is a second embodiment of the device of Fig. 2; Fig. 4 is a graphical representation of the diagram of te hardness of the water eluded through the resins fo the three regeneration levels illustrated in Example 1. The ordinate indicates the hardnoss in French degrees (op) and the abscissa indicates the volume of the eluted water; Fig, 5 shows te operative exchange capacity and plots the exchanged amounts of CaCO3 (calculated from the difference of hardness between supplied water and eluted water) as a function of the proportioning of regenerating material as in Example 1; Figs, 6 and 7 show respectively, the diagrams of the residual hardness of the eluted water and operative exchange capacity in Example 2. The researches to design and manufacture a;a experimental device were carried out assuming to have to soften 50 to 100 litres of water (that is the average quantity of water recuired only in the steps of pre--ashing, washing and first rinsing in a common domestic washing machi ze). so as to obtain a residual hardness not high than 5oF, which valus is considered as acceptable for washing purposes. In the total quantity of 120-150 litres required for a complete washing cycle, the softenirg process is limited only to the amount of water required for the above-specified steps occurring in the presence of a detergent, to eliminate the inconveniences caused by hardness in the presence of a detergent to a washing machine and washed linen due to tha deposits of incrustation materials The values of the water hardness change considerably from region to region; in Italy average values of 25 to 30 F have been reported, with maximum values of 70 to 80 F. In case of these maximum values, the 50 to 50 litres of water to be treated would require a maximum amotnt of 40 to 50 g. With reference to the drawings, and partifcularly to Fig the numeral 1 indicates a three-way valve .;th two oparactive positions, connected directly to th watersupply SO This valve is actuated by means of a knob 101 so as to s'titcm it from the wash position, wherein the water fron the supply 2 is fed to the ion exchange column 3 contained in a tank 4, to the regeneration position wherein the valve discharges through an outlet 5. With the valve in the ash position the water from the supply 2 flows through the pipe 6 and into the ion exchange collumn 4, and then through the pipe 7 and connecting piece 8 into the waching machine. During this step, a portion of the water ron the pipe 7 flora through the pipe 9 with calibrated hole 10 into G tank 11 containing a basket 12 for the sodium chloride crystals. The tank 11 is sealingly closed at the ton by a these cover 111 having a central vent or bleed hole 211 that can be closed by a valve member 13 supported Th: a flost 14. Therefore, when the water in the tank 11 has resached -est blished level, the valve menber 13 cleses than hole i and thus prevents any further entramee of water into the tank 11. A puschbutton 113, connscted to the flcat 14 and associated valve member 13, when deprassed, opens again the communication betwean the tank 11 and anmospere end thus parmits the brine formed in the tank 11 to discharge therefrom, through the calibrated hale 10 pips 9 and pipe 7, into the ion exchange columm 3 for rege@erating the ion exchange resins, and thereform, through the pipe 6 and outlet 5 to waste, when the valve 1 is in the regeneration position. Fig. 2 shows the tank 11 and associated elements with more detail. As better shown in this 2 re, fixed to the inn-r side of the cover 111 are two upright parallel guides 311 for guiding the float 14o Suspended from the free ends of these guides is a basket 12 for the sodium chloride0 Pivoted on the top side of the float 14 is one end of a lever 114, the other end of which is pivoted to the lower side of the cover 111, so that the lever is inclined with respect to the vertical axis of the tank 11. Pivoted at & an intermediate portion of the lever 114 is another upright lever 214 the top end of which is pivotably connected to the valve member 13 cooperating with the valve seat 213 communicating through a conduit in the cover 111 with the vent hole 211. A pushbutton 113 for opening the comnunication to the atmosphere is connected to the valve member 13 through a small stem 313. Fig. 3 shows a modification of the device of Figs, 1 and 2. In this modification, the valve member 13 is constantly biased against the valve seat 213 by a spring 413 interposed between the valve seat 213 and an abutment member 513 secured to the end of the stem 313 opposed to the end carrying the valve member 13. A lever 314 is pivoted at one end to the cover 111 and at the other end to the float 14. This lever cooperates with an abutment head 613 secured to the lower side of the valve member 13 whereby when the float is in a low position @@ lever holds the valve member 13 away from the E salt 213, whereas when the float is in the upper position sai lever permits the valve member to contact the valve seat Under all other respects, this device operates as that of Fig. 2. The operation of the device is now apparent. Before starting the device (already connected to the water supply and to the washing machine), the required amount of sodium chloride crystals is introduced in the filter -container 12 after unscrewing and removing the plug 11). After re-inserting the plug, the water supply can be open by rotating the valve 1 from the closed position to the wash position; water flows into the tank 4 through the resins and into the tank 11 through calibrated hole 10. The water fills up the tank completely, dissolving the sodium chloride therein, until it is automatically shut off by the float 14 that closes the valve 13-213. The washing cycle of the washing machine can now begin. All the water flowing into the washing machine is softened during the passage through the resins; during the step, the sodium chloride solution (brine) formed in the tankk @: cannot flow out therefrom because the pressure in the system is sufficient to hold it therein even er the washing machine is open to the water supply. On completion of the washing cycle of the machine, the valve 1 must be rotated manually to the regeneration position; the pressure of the water is thus relieved through the outlet 5. By depressing now the vent or bleed pushbutton 113 on the cover of the tank, the brine is permitted to flow out the tank 11 and drop into the resins so as to regenerate them. The duration of the regeneration depends upon the emptying time of the tank 11 and is about 50 minutes. On completion of the regeneration a new exchange cycle amS simultaneous washing cycle can be started, by rotating the valve 1 to the wash position after supplying the tank 11 with the required amount of sodium chloride, The proportioning of the salt, in the range of 50 to 150 g, can be facilitated by indications or marks on the tank 11 at various voletric levels of the basket, corresponding to various possible values of the supply water, which, obviously, must be knc-rn0 In the use of the device, the ion exchange system has been evaluated and analyzed, using different volumes of resin and different regenerative levels and with inCretSinJ amounts of sodium chloride as regenerating material. The following example illustrate the operative conditions and performances that can be obtained to the invention. Example 1 Tank 11 (brine) volume 1500 ml Resin column column 500 ml height 47 cm diametre 307 cm supply-water hardness 17.5 F flowrate 300 lA Regeneration with 50 g NaCl (conc.brine 100 g NaCl (conc.brine 6.6,?3) 150 g NaCl (conc.brine 10.0%) Fig. 4 shows, for each type and amount of resin, the diagrams of the hardness of the water that has flowed through the resins for the three regeneration levels, employing 50, 100 and 150 g of NaCl, respectively; the ordinate indicates the hardness in French degrees (oF), and the abscissa shows the volume of treated water. Fig. 5 shows the operative exchange capacity and indicates the amounts of exchanged amounts of CaCO3, calculated on the basis of the difference of hardness between supply -water and eluted water, as a function of the proportioning of the regenerating material (Nacl). The exchange efficiences Y that can be calculated from the diagram of Fig. 5 are: with 50 g NaCl 28 g CaCO3 exchanged Y = 0o56 with 100 g NaCl 38.5 g CaCO3 exchanged Y = 0039 with 150 g NaCl 44.5 g CaCO3 exchanged Y = 0o31 These data indicate that the exchange efficiency, expressed by the factor Y, is not constant at the three considered regeneration levels, but decreases with the increase of the proportion of NaCl. The volume of the resin, therefore, is too low, with resultant saturation at high regener tion levels. Example 2 Operating conditions: Tank S (brine) volume 1500 ml Resin column volume 1000 ml height 47 cm diametre 5.2 cm Supply-water hardness 21.5 OF flowrate 540 l/h Regeneration with 50 g NaCl 75 g NaCl 100 g NaCl 150 g NaCl As in Example 1, diagrams have been plotted of the residual hardness of the treated water and the operative exchange capacity (see Figs. 6 and 7, respectively). The diagram of Fig. 7 shows the factors Y, i.e. the efficiences of the exchange: with 50 g NaCl 25.5 g CaCO3 exchanged Y = 0o51 with 75 g NaCl 38 g Ca exchanged Y = 0cSO with 100 g NaCl 53 g CaCo3 exchanged Y = 0053 with 150 g NaCl 65.8 g CaCO3 exchanged Y = 0S43 The substantial constance of the values Y meaning a good proportionality between regeneration level and hardness co the water to be treated, and the high exchange capacity (that with 100 g NaCi permits to exchange 53 g CaCO3, that is above 40-50 g which is the maximum value required in the most difficult conditions) demonstrate that the softening process, in the specified experimental conditiomsp is thoroughly satisfactory.

Claims: CLAIMS 1. A water softener for domestic purposes, adapted to be also attached to a common washing machine and operating on the principle of ion exchange through resins, characterized by a regeneration cycle occurring automatically and in constant and pre-establishe conditions, with regeneraticrz levels that can vary as a function of the exchange capacity required in accordance with the amount and hardness of the water to be treated. 2. A softener according to claim 1, characterized by the fact of comprising: a) a tank including a closure cover, an impulse-actuate dispensing valve, a level-regulating float connected to the valve controlling the flow of water through a calibrated hole in the bottom of the tank, and containing therein a perforated container for receiving the sodium chloride required for regenerating the resins; b) a three-way distributing valve having two operating positions, one for the ion exchange cycle (washing) and another for the regeneration cycle; c) a tank containing the resins within pipes of glass, plastics or other material, either of straight vertical shape or having a U shape. 3. A softener according to claims 1 and 2, wherein the regenerating brine is formed in the tank with homogenRous concentration within the range of 3 to 10%, depending on the amount of solid salt dosed in the container therefor by the action of the supply water flowing thereinto to fill it up completely. 4. A softener according to the preceding claims, characts- rized by the fact that it is adapted for operation with flow-rates of water in the range 0 to 700 1/h, with any value of hardness, generally in the range 0 to 100 op, with proportions of salts in the range 0 to 150 g, generally 5D to 100 g, and amounts of cationic exchange resin, of suitable shape and size, in the range 500 to 1000 ml. 5. A softener according to the preceding claims, characte rized by the fact that the regeneration cycle will cease automatically upon exhaustion of the brine, without any manual control. 6. A softener according to the preceding claims, charact-- rized by the fact that it comprises manually-controlled supplying and distributing three-:y valve having two operative positions and connected, respectively, to the water-supply, to a discharge and to the inlet of an ion exchanger, the outlet of this exchanger being connected to the user and to a tank containing the regeneration cryst-ls9 respectively, the latter tank being provided with a vent hole communicating with the atmosphere and cooperabine with a valve member controlled by a member responsive to the level of the liquid in the tank, so as to close said vent hole when a pre-established level in the tank is reached. means being provided that can be controlled for the outside to re-establish the communicstion bst.-een the tark and the atmosphere; and means to establish a communication between said tank and said ion exchanger in order to hav the regenerating. solution to flow through the exchanger when said distributing valve is switched to the discharge position,

Inventors: FAVARI, GIAN FRANCO, TONINELLI, GIUSEPPE
Applicants: MIRA LANZA S.P.A.
Application year: 1981
Main classification: C02F1
IPC codes: B01J49, D06F39, C02F1