SAID SYSTEM

The present invention relates to a thermal exchange and thermal stratification system for the fluid to be heated, in particular sanitary water, within a storage tank. Moreover, the present invention relates to a boiler comprising said system.

More specifically, the present invention concerns to a thermal stratification system that allows to input inside a tank a secondary fluid heated following heat exchange with a primary fluid outside of said tank. Such inlet happening with flow rate and temperature such as not to create mixing and preserving the thermal stratification of the secondary fluid inside the tank.

By thermal stratification it is meant the natural tendency of a fluid to "stratify" inside a container, e.g. a tank, its temperature so as to increase from bottom to top and with high temperature gradients between the upper, warmer parte, and the lower, colder part.

In order to preserve the thermal stratification, it is tried preventing the fluid introduced into the tank from having different temperatures, thus generating a mixing and turbulence inside the tank itself, and compromising its efficiency.

The present invention is included in the closed vessel heating systems field, in which the tank containing the fluid to be heated is always under pressure.

Under the present state of the art, there are thermal stratification systems of the fluid contained in closed vessel tanks, employing pipes and heat exchangers aimed at and configured so as to input the heated fluid at different heights of the tank, so as to present the same temperature of the fluid already contained in the tank, to avoid the mixing and turbulence within said tanks.

However, such known systems require a system to regulate the inlet of said fluid inside said tank so as to preserve the thermal stratification, since said fluid as a consequence of said thermal exchange could be under different conditions and variations of flow rate and temperature which, if not regulated, do not allow to maintain the thermal stratification. At the state of the art these known systems require, therefore, suitably designed heat exchange systems and piping and circuits outside or inside the tank. Document EP 2873933 A1 , which is considered the most relevant document with respect to the inventive solution, describes a solution according to the preamble of claim 1 of the present patent application. Also document EP 2848875 A1 describes a solution according to the above preamble of claim 1 of the present application.

It is the object of the present invention solving the problems of the known art, in order to obtain a heat exchange and stratification system that we can be easily applied to boiler tanks or existing heat exchange systems, ensuring optimal thermal stratification of the fluid contained within the tank. It is the object of the present invention a thermal exchange and thermal stratification system for a secondary fluid contained in a tank of a boiler, said tank having a top portion and a lower portion, said system comprising a secondary circuit, for the flow of the secondary fluid, said secondary circuit being apt at being in fluid connection with the top portion and the lower portion of said tank, said system further comprising a circulation pump, apt to act on said secondary circuit for the circulation of said secondary fluid from the lower portion to the top portion of said tank through said secondary circuit, a thermal exchanger, apt to act on a portion of said secondary circuit for heating said secondary fluid before its introduction into the top portion of said tank, and a thermostatic valve, apt to act on said secondary circuit so that, during use, said thermostatic valve adjusts the temperature and the flow rate of said secondary fluid through said secondary circuit according to the thermal exchange with said heat exchanger for keeping the thermal stratification of the secondary fluid within said tank.said system being characterized in that said thermostatic valve is configured so that, during use, when the temperature of the secondary fluid in correspondence of said thermostatic valve equals to or is lower than a first pre-set temperature, said thermostatic valve prevents the flow, or flow rate, of said secondary fluid from the lower portion of said tank, in order to allow the remaining secondary fluid to circulate in said secondary circuit for heating said secondary fluid, when the temperature of the secondary fluid in correspondence of said thermostatic valve is higher than said first pre-set temperature, said thermostatic valve varies the flow rate of said secondary fluid through it in a way proportional to the difference between the temperature of the secondary fluid and the pre-set temperature, for the introduction of said secondary fluid in the top portion of said tank for preserving the thermal stratification of said secondary fluid within said tank.

Still according to the invention, said thermostatic valve has a first inlet opening or warm inlet opening, a second inlet opening or cold inlet opening, and an outlet opening, in that said secondary circuit has a first opening or lower opening, apt at being in fluid connection with the lower part of the tank for the intake of the secondary fluid from said tank, and a second opening or top opening, apt at being in fluid connection with the top part of the tank for the introduction of the secondary fluid in the tank, in that said secondary circuit further comprises a first portion or thermal exchange portion in correspondence of said heat exchanger for heating said secondary fluid, a second portion, able to put in fluid connection said lower opening with said second intake opening of said thermostatic valve, a third portion, able to put in fluid connection said outlet opening of said thermostatic valve and said first portion of the secondary conduit, and a fourth portion able to put in fluid connection said first portion both with said warm inlet opening of said thermostatic valve and both with said top opening, said system being configured so that, during use, said thermostatic valve adjusts the temperature and the flow rate of said secondary fluid by opening/partially or totally closing said second inlet opening according to the temperature of said secondary fluid in correspondence of said first inlet opening for preserving the thermal stratification of the secondary fluid within said tank.

Particularly, according to the invention, said thermostatic valve is configured so that, during use, when the temperature of the secondary fluid in correspondence of the warm inlet opening of said thermostatic valve is equal or is lower than a first pre-set temperature, said thermostatic valve closes or maintains closed said second inlet opening, preventing the flow, or the flow rate, of said secondary fluid from the lower opening, in order to allow the secondary fluid to flow between the third, first and fourth portion of the secondary circuit for heating said secondary fluid within said secondary circuit, when the temperature of the secondary fluid in correspondence of the warm inlet opening of said thermostatic valve is higher than said pre-set temperature, said thermostatic valve opens or maintains partially or totally opened said second inlet opening, varying the flow-rate of said secondary fluid through said second inlet opening in a way proportional to the difference between the temperature of the secondary fluid in correspondence of the warm inlet opening and the preset temperature, for the introduction of said heated secondary fluid in said second opening for the thermal stratification within said tank.

Always according to the invention, said heat exchanger comprises a primary circuit for the flow of a heated primary thermal-carrier fluid by means of external heating means, for example a heat pump, said primary circuit being in direct or indirect thermal contact with said thermal exchange portion of said secondary circuit in correspondence of said heat exchanger for heating said secondary fluid.

Preferably, according to the invention, said circulation pump is arranged in correspondence of the third portion of the secondary circuit in order to intake the secondary fluid from the second portion and/or from the fourth portion of the secondary circuit.

Still according to the invention, said system can further comprise an adjustment system of the temperature of said secondary fluid in said secondary circuit according to the temperature detected at one or more height levels of said tank, in order to interrupt the heating of said secondary fluid in correspondence of said heat exchanger when reaching a second pre-set temperature at a determined level of said tank.

Particularly, according to the invention, said adjustment system comprises detecting means, for example probes, arranged at one or more levels of said tank, able to detect the temperature of said secondary fluid at the respective level of said tank.

Furthermore, according to the invention, said second portion of the secondary circuit is apt at being inserted within said tank or is apt at being arranged outside said tank.

Preferably, according to the invention, said thermostatic valve is directly connected to said circulation pump.

Further it is an object of the present invention a boiler comprising a tank, having a lower portion and a top portion, and a thermal exchange and thermal stratification system according to any one of the previous claims.

Finally, according to the invention, said tank is of a closed vessel type.

The invention will be now described, for illustrative but not limitative purposes, with particular reference to the figures of the enclosed drawings, wherein:

figure 1 shows a hydraulic diagram of the thermal exchange and stratification system for tanks according to the invention;

figure 2 shows a perspective view of a first embodiment of the thermal exchange and stratification system according to the invention applied to a boiler;

figure 3 shows a top view of the thermal exchange system of figure 2;

figure 4 shows a perspective view of a second embodiment of the thermal exchange and stratification system according to the invention;

figures 5a - 5f show front views in thermo graphic vision during different time phases in succession of the inlet of a fluid inside the tank following to the heating by a thermal exchange system according to the prior art;

figures 6a - 6f show front views in thermo graphic vision during different time phases in succession of the inlet of a fluid inside the tank following to the heating by a thermal exchange system according to the invention;

figure 7 shows a first graph of the temperature variation, as a function of time, of the secondary fluid heated by said thermal exchange system according to the prior art; and

figure 8 shows a second graph of the temperature variation, as a function of time, of the secondary fluid heated by heat exchange under the same conditions of said heat exchange system according to the known technique and input in the tank by said heat exchange system and the stratification thermal system according to the invention.

Making reference to figures 1 - 3, it is observed the thermal exchange and stratification system according to the invention, indicated by the reference number 1. Said system 1 is adapted to be applied to a storage tank 2 in a closed vessel boiler containing a fluid to be heated, for example sanitary water. In the specific embodiment, the fluid to be heated is a secondary fluid to be heated through thermal exchange with a further heat transfer fluid, known as primary fluid.

The thermal exchange and stratification system 1 according to the invention provides a heat exchanger 7, comprising a primary circuit 10, through which flows a primary heat transfer medium heated, for example by means of heating pumps or other heating systems. Said primary fluid being water and being for example aimed at heating a house. In other embodiments, said heat exchanger 7 may provide other heating systems for the secondary fluid. Furthermore, the system 1 provides a secondary circuit 11 , for the flowing of the fluid to be heated or secondary fluid, having a first portion 18 in direct or indirect thermal contact with said primary circuit 10 in correspondence of said heat exchanger 7, for heating said secondary fluid. Said secondary circuit 11 is configured so as to put in fluid communication a lower opening 14 connected to the lower portion of said tank 2 and an upper opening 15 connected to the upper portion of said tank 2. In correspondence of said secondary circuit 11 it is provided a circulation pump 19 able to circulate the secondary fluid in said secondary circuit 11.

Furthermore, the system 1 according to the invention provides a thermostatic mixing valve 5 suitable to act on said secondary circuit 11 so that, during use, said thermostatic valve 5 regulates the temperature and the flow rate of said fluid through said secondary circuit secondary 11 as a function of the thermal exchange with said heat exchanger 7 to maintain the thermal stratification of the secondary fluid inside said tank 2.

In the specific embodiment, the thermostatic valve 5 has a first delivery or warm opening 3, a second delivery or cold opening 4, and an outlet opening 6.

Said secondary circuit 11 has a second portion 12 able to put in fluid communication of said lower opening 14 connected to the lower portion of said tank 2 with said second delivery opening 4 of said mixing valve 5. Furthermore, said secondary circuit 11 has a third portion 16 able to put in fluid communication of said outlet flow 6 of said mixing valve 5 and the first portion 18, and a fourth portion 17 able to put in fluid communication with said first portion 18 of said hot flow of said mixing valve 3 and with said upper opening 15 connected with the upper portion of said tank 2.

In particular, the circulating pump 19 is preferably positioned in correspondence of the third portion 16 of the secondary circuit 11 to suck the fluid to be heated from the first opening 14 and/or of the fourth portion 17 of the secondary circuit 11.

The thermal exchange system 1 according to the invention is configured in such a way that when the temperature TC of the secondary fluid at the warm outlet 3 of said mixing valve 5 equals or is lower than a first set temperature T1 for the fluid temperature TU in correspondence of the outlet opening 6 of said thermostatic mixing valve 5, said mixing valve 5 closes or keeps closed said second delivery opening 4, preventing the flow, i.e. the flow rate, of said secondary fluid, the low temperature, through the lower opening 14 connected to the lower portion of the tank 2 and through the upper opening 15 connected to the upper portion of the tank 2. In this condition the secondary fluid circulates only between the heat exchanger 7 and the thermostatic mixing valve 5 passing entirely by the warm outlet 3 to the outlet opening 6 and thus there is no flow, or flow rate, to and from said tank 2.

When, as a result of the thermal exchange, the temperature TC of the warm opening 3 exceeds said first temperature T1 , said thermostatic mixing valve 5 partially or totally opens the cold opening flow 4 by varying the flow rate of the flow in a manner proportional to the difference between the temperature TC of the warm opening 3 and the set temperature T1 for the temperature TU of the fluid at the outlet opening 6.

In consequence of the above, there is a flow, or a flow rate, through said lower opening 14 and the upper opening 15 which involves inlet of said secondary fluid in said tank 2 through the upper opening 15 at the temperature TC of the warm opening 3, that, on the basis of the operation described in the above, is higher or equal to the set temperature T1 for the output 6 temperature TU of the thermostatic mixing valve 5 and with a flow, or flow rate, partial with respect to the total flow at the opening 6, used to obtain the thermal exchange of said secondary fluid with said primary fluid and proportional to the difference between said temperature TC and said set temperature T1 .

Thus, according to the invention, by setting a suitable temperature T1 as outlet 6 temperature TU of the thermostatic mixing valve 5, it is obtained by introducing said secondary fluid in the upper part of said tank 2, at the wished temperature, greater than or equal to the set temperature T1 , and with a flow, or flow rate, automatically and simultaneously set by the thermostatic mixing valve 5 in such a way not to influence the thermal stratification of the tank, regardless of the temperature and flow, or flow rate, conditions, of said secondary fluid and primary heat exchange, i.e. irrespective of the conditions to which said thermal exchange takes place, such as changes in temperature and/or flow rate of the primary fluid and the secondary fluid.

Therefore, the system according to the invention advantageously allows providing a system for adjusting the flow and the temperature when entering into a tank of a secondary fluid which is heated by means of a any generic thermal exchange system with a primary fluid under variable conditions and non-controlled flow rate and temperature, so that said input preserves the thermal stratification inside said tank.

Comparing the figures 5a - 5f with the figures 6a - 6f it is noted that, in the absence of said thermal stratification system according to the invention, the secondary fluid coming directly from said thermal exchange with said primary fluid, and introduced in the upper portion of the tank 2 through the opening 15 with temperature and flow, or flow rate, deriving from said thermal exchange and not adjusted by the thermostatic mixing valve 5 of the system 1 according to the invention, creates a mixing within the tank and does not allow the thermal stratification.

As can be observed from a comparison of graphs of figures 7 and 8, in the thermal exchange and stratification exchange system according to the invention, the temperature TC of the warm opening 3 rises much more quickly (Figure 8) compared to the same temperature TC in the same thermal exchange system according to the prior art (figure 7), which indicates that the heating of the fluid placed in the tank is quicker.

Furthermore, in the thermal exchange and thermal stratification system according to the invention, said temperature TC (figure 8) is constantly included between the delivery and return temperatures of the primary fluid, respectively T1 FL1 and T2 FL1 , while in the thermal exchange system according to the prior art under the same conditions, without said thermal stratification system (figure 7), said temperature TC is almost coincident with the return temperature T2 FL1 of the primary fluid, indicating that in the thermal and stratification exchange system according to the invention (fig. 8) said secondary fluid reaches, under the same conditions, higher temperatures, i.e. the thermal exchange is more efficient.

Furthermore, from the comparison of the graphs of figures 7 and 8, it can be noted that, in the thermal exchange and thermal stratification system according to the invention (figure 8) the temperature Tsb, detected in the lower part of the tank, increases quite some time after the temperature Tsa, detected in the upper part of the tank, maintaining a high temperature gradient between the upper part and the lower part of the tank for the entire first period until TSB does not begin increasing, indicating that there is a perfect thermal stratification. Conversely, in the thermal exchange system according to the prior art without said thermal stratification system (figure 7) said temperatures Tsa and Tsb increase simultaneously, maintaining a low temperature gradient between the upper part and the lower part of the tank, indicating that there is not a good thermal stratification, confirming the above, evidenced by a comparison of figures 5a - 5f with figures 6a - 6f.

Preferably, the thermal and stratification exchange system according to the invention may further comprise an adjustment and control system of the thermal exchange of said secondary fluid with said primary fluid, as a function of the temperature detected by detection means, such as probes, provided in a plurality of positions of said tank, so as to stop said thermal exchange to reach the wished temperature at a given level of said tank, corresponding to the position of a specific probe, allowing, by virtue of the thermal stratification in said tank, of not having to heat said fluid even below said level of said probe.

Particularly, the regulation and control system is able to stop said thermal exchange by electronic, electro-mechanical, or thermo mechanical actuators, when a second set temperature T2 is reached in correspondence of one or more set levels of said tank.

The embodiment of the thermal exchange and thermal stratification system 1 according to the invention of figure 4 differs from the previously described system by the fact that said second portion 12 of the secondary circuit 11 is inserted inside said tank 2 instead of being outside the same, in order to have an easier production, as to realize said second portion 12, which connects the lower opening 14 with the delivery opening 4 of the mixing valve 5, it is not necessary to suitably align a pipe so that it passes outside the tank. Said second portion 12 passing through the tank 2 is in any case accessible for inspection and replacement while remaining within the maximum dimensions of the whole product.

Furthermore, in the embodiment of figure 4, the mixing valve 5 is directly connected to the circulating pump 19, thus reducing the overall dimensions and optimizing the fittings.

In the foregoing preferred embodiments and the variants of the present invention have been suggested, but it is to be understood that one skilled in the art can introduce modifications and changes, without departing from the relevant scope, as defined by the enclosed claims.