FIELD OF THE INVENTION
[0001] The present invention concerns a method to control the functioning of a heating apparatus,
which is advantageously used to reduce phenomena of corrosion connected to the continued
use of said apparatus.
[0002] In particular, the method according to the present invention can be implemented in
a heating apparatus that comprises electric cathodic protection devices against the
corrosion of containers, tanks or metal parts containing water, such as for example
boilers.
BACKGROUND OF THE INVENTION
[0003] Devices are known, for the cathodic protection of heating apparatuses against corrosion,
applicable to boilers or water-heaters.
[0004] In particular, a boiler-type apparatus is known for heating water, in which an electrode,
also called anode, made for example of titanium, is immersed in the water contained
in the boiler. An electric energy generator is connected with the positive pole to
the anode and with the negative pole to the boiler to be protected from corrosion.
[0005] The current that is established between the anode and the boiler is periodically
varied over time, in its intensity, for a determinate interval, with respect to the
normal operating value and, during this variation, the difference in potential that
is established between the two poles of the generator is measured.
[0006] The difference in potential measured is compared with a predetermined reference value,
corresponding to a known value at which corrosion is impeded; any deviation with respect
to this reference value is used to determine a current intensity to be applied between
anode and boiler in order to obtain a difference in potential substantially equal
to the predetermined reference value.
[0007] The known difference in potential value, hereafter referred to as protection potential,
is determined in a known manner for example with reference to the Pourbaix diagram,
or potential/pH diagram, which is a representation of the possible stable conditions
at balance of an electrochemical system in aqueous solution. This model is used to
predict the behavior of a metal material regarding corrosion, in this case referred
to iron alloys but also applicable for other metals, although with the adoption of
different potentials.
[0008] Knowing the material that the boiler is made of, it is therefore possible to determine
the protection potential to be applied between anode and boiler.
[0009] This method of protection, although it guarantees adequate protection against corrosion
in the boiler, is a system that is closed upon itself, and is not able to detect possible
influences due to factors outside the heating apparatus, such as for example electrostatic
loads, electric dispersions or other.
[0011] One purpose of the present invention is to perfect a method to control the functioning
of a heating apparatus that is efficient and that allows to increase the working life
of the heating apparatus in which it is applied.
[0012] Another purpose of the present invention is to perfect a method that increases the
safety of the heating apparatus.
[0013] The Applicant has devised, tested and embodied the present invention to overcome
the shortcomings of the state of the art and to obtain these and other purposes and
advantages.
SUMMARY OF THE INVENTION
[0014] The present invention is set forth and characterized in the independent claims, while
the dependent claims describe other characteristics of the invention or variants to
the main inventive idea.
[0015] In accordance with the above purposes, a method according to the present invention
is applied to control the functioning of a heating apparatus in which the heating
apparatus comprises:
- a tank containing an electrolytic solution, for example water,
- an electrode immersed in the electrolytic solution,
- an electric energy generator connected to the electrode and to the tank,
- a controller provided with a measurer which measures at least one electric quantity
which is established between the electrode and the tank.
[0016] The method provides to regulate the electric energy generator so as to keep in the
electrolytic solution a protection potential having a first known value, substantially
constant over time, suitable to guarantee the tank is protected from corrosion.
[0017] According to one aspect of the present invention, the method comprises a step of
detecting electric dispersions present in the tank, during which the measurer measures
at least one electric quantity and the controller processes the at least one electric
quantity in order to determine the presence of electric dispersions, which are to
be avoided since they are the cause of the corrosive effect generated on the walls
of the tank.
[0018] According to a first form of embodiment of the present invention, the detection step
provides to detect direct currents of electric dispersion present in the tank. According
to this form of embodiment, the direct currents detection step comprises:
- a step of temporary interruption or reduction of the electric energy supplied by the
electric energy generator;
- a step of measuring the residual potential, having a second value, which is established
between the electrode and the tank;
- a step of comparing the second value of the residual potential measured and a third
value of a reference potential;
and wherein, if the second value measured is greater than the third value of the reference
potential, the controller recognizes a functioning condition that is within the norm,
and wherein, if the second value measured is less than the third value of the reference
potential, the controller recognizes the presence of electric dispersions deriving
from direct currents in the tank.
[0019] The present invention also concerns an electric cathodic protection device to be
associated with a heating apparatus comprising a tank containing an electrolytic solution.
The device comprises an electrode immersed during use in the electrolytic solution,
an electric energy generator connected to the electrode and, during use, to the tank,
and a controller provided with a measurer configured to measure an electric quantity
which is established between the electrode and the tank. According to one feature
of the invention, the controller comprises a processing unit configured to receive
the data of the electric quantity detected by the measurer and to process the electric
quantity in order to determine the presence of electric dispersions. The device also
comprises indicators associated to the controller in order to indicate the presence
of electric dispersions.
BRIEF DESCRIPTION OF THE DRAWINGS
[0020] These and other characteristics of the present invention will become apparent from
the following description of a preferential form of embodiment, given as a non-restrictive
example with reference to the attached drawings wherein:
- fig. 1 is a schematic representation of a heating apparatus that uses a control method
according to the present invention;
- fig. 2a is a graph showing the development of potential over time that is applied
to the heating apparatus during normal functioning, according to a first form of embodiment;
- fig. 2b is a graph showing the difference of potential over time that is measured
in the heating apparatus according to the first form of embodiment;
- fig. 3a is a graph showing the development of potential over time that is applied
to the heating apparatus during normal functioning, according to a second form of
embodiment that is not part of the present invention;
- fig. 3b is a graph showing the development of electric currents over time, which is
detected in the heating apparatus according to the second form of embodiment and in
a functioning condition;
- fig. 3c is a graph showing the development of electric currents over time, which is
detected in the heating apparatus according to the second form of embodiment and in
another functioning condition.
[0021] To facilitate comprehension, the same reference numbers have been used, where possible,
to identify identical common elements in the drawings. It is understood that elements
and characteristics of one form of embodiment can conveniently be incorporated into
other forms of embodiment without further clarifications.
DETAILED DESCRIPTION OF SOME FORMS OF EMBODIMENT
[0022] A heating apparatus according to the present invention is indicated in its entirety
by the reference number 10 and comprises an electric cathodic protection device 11
against corrosion.
[0023] In particular, the heating apparatus 10 comprises a tank 12 having a metal surface
in contact with an electrolytic solution, such as water.
[0024] The electric cathodic protection device 11 in turn comprises an electrode 13 or anode,
an electric energy generator 14 and a controller 16.
[0025] The electrode 13 can comprise a titanium bar, possibly activated with noble materials.
[0026] One form of embodiment of the present invention provides that the electric energy
generator is a generator controlled in direct current, indicated hereafter as current
generator 14.
[0027] The current generator 14 is in turn connected to the controller 16 which controls
and manages the functioning of the current generator 14, and possibly signals particular
functioning conditions of the heating apparatus 10, like the presence of electric
dispersions.
[0028] More specifically, the controller 16 is provided with a measurer 15 that measures
at least one electric quantity, configured to detect, for example, the values of current
or electric voltage that are established in the electric cathodic protection device
11, in this case between the electrode 13 and the tank 12.
[0029] The measurer 15 can be a voltmeter, an amperometer, a wattmeter or simply a device
to compare at least one of the electric quantities that are to be detected.
[0030] Some forms of embodiment provide that the controller 16 comprises a processing unit
19, provided to process the data detected by the measurer 15 and to signal possible
anomalous functioning conditions due to the presence of electric dispersions.
[0031] To this purpose, the controller 16 can be associated to indicators 17, for example
luminous indicators, each of which identifies a functioning condition of the heating
apparatus 10.
[0032] In order to guarantee adequate protection against corrosion of the tank 12, during
normal functioning of the heating apparatus 10, the current generator 14 maintains,
between the electrode 13 and the tank 12, a protection potential that is substantially
constant over time, indicated in fig. 2a as protection potential Vp.
[0033] The protection potential Vp is a known value, determined as described above as a
function of the material that the tank 12 is made of, and with reference to the Pourbaix
diagram.
[0034] Merely by way of example, if the tank 12 is made of steel, the protection potential
Vp assumes a value comprised between 900mV and 1200mV.
[0035] The protection potential Vp to be established in the electrolytic solution can be
generated iteratively by regulating the current supplied by the current generator
14 and detecting with the measurer 15 the establishment of electric currents inside
the electric cathodic protection device 11.
[0036] The detection of electric currents identifies an unstable condition of the potential
in the tank 12.
[0037] If the measurer 15 detects a considerable deviation in the electric currents with
respect to the previous measurement, the controller 16 regulates the current supplied
by the current generator 14 to take it to a constant value corresponding to a balanced
current. With reference to figs. 2a, 2b, 3a, 3b and 3c, a method is described to control
the functioning of the heating apparatus 10 and, in particular, to detect possible
electric dispersions, for example stray currents that affect the tank 12 and that
can contribute significantly to the corrosion inside it.
[0038] The stray currents may be small in entity, and therefore not produce a direct intervention
of the electric safety devices, such as circuit breakers normally provided in the
electric network.
[0039] Although they do not prejudice the overall safety of the electric network or the
heating apparatus 10, stray currents are an important factor with regard to the creation
of corrosive phenomena.
[0040] Such problems occur both with dispersions of direct current and also with dispersions
of alternating current.
[0041] With reference to figs. 2a and 2b, a first form of embodiment is described of the
method according to the present invention, used to detect electric dispersions in
direct current.
[0042] During the normal functioning of the heating apparatus 10, the controller 16 regulates
the current supplied by the current generator 14, as described above, to maintain
a balanced condition of the protection potential Vp between the electrode 13 and the
tank 12.
[0043] There then follows a step to detect electric dispersions during which a controlled
variation of the electric energy supplied by the current generator is provided.
[0044] As shown in fig. 2a, the detection step occurs for an interval of time T shorter
than the overall functioning time of the heating apparatus 10 according to the invention.
Merely by way of example, it may be provided that the time interval T lasts about
one minute and is executed with a cyclicity of twelve hours, that is, the detection
is performed periodically twice a day.
[0045] Some forms of embodiment provide that, during the detection step, the supply of electric
current to the current generator 14 is temporarily interrupted, and a measurement
is made by the measurer 15.
[0046] It is clear that a temporary interruption of the time interval T, in the normal functioning
of the heating apparatus 10, does not influence the protective effect against corrosion
normally performed by the heating apparatus 10.
[0047] Other forms of embodiment provide only a reduction in the current supplied by the
current generator 14, and not an interruption thereof.
[0048] During the detection, the measurer 15 detects the difference in potential, indicated
hereafter as measured potential Vm. The measured potential Vm corresponds to the residual
potential that is established between the electrode 13 and the tank 12.
[0049] From experiment analysis, Applicant has found that, in the absence of electric dispersions,
the measured potential Vm or residual potential quickly moves to an asymptotic value
substantially stable over time, as shown in fig. 2b, similarly to the curve in which
the measured potential Vm1 is detected.
[0050] If there are electric dispersions in the heating apparatus 10, it should be noted
that the development of the measured potential Vm, instead of moving to an asymptotic
potential over time, rapidly decreases, consequently facilitating corrosive action.
This condition is shown by the curve in fig. 2b, in which the potential value Vm2
is detected.
[0051] On the basis of these observations, the method according to the present invention
provides that the value of measured potential Vm is compared by the controller 16
with a reference potential Vr. Merely by way of example, the reference potential Vr
is comprised between 20% and 40% of the protection potential Vp.
[0052] If the measured potential Vm is greater than the reference potential Vr, the controller
16 recognizes a functioning condition within the norm. To this end, in fig. 2b, the
measured potential is indicated as Vm1 and it can be seen that Vm1>Vr.
[0053] If the measured potential Vm is less than the reference potential Vr, the controller
16 recognizes the presence of harmful electric dispersions in the tank 12 and commands
the activation of the indicators 17. In this condition, in fig. 2b the measured potential
is indicated as Vm2 and it can be seen that Vm2<Vr.
[0054] One form of embodiment of the present invention provides that the potential is measured
after a period of time S from the moment when the controlled variation of the protection
potential Vp is commanded. The period of time S is evaluated, using theoretical experiments,
also in relation to the stabilization time of the potential to move to the asymptotic
value as described above.
[0055] One form of embodiment of the present invention provides that the period of time
S is comprised between 30secs and 60secs. The period of time S, before measuring,
prevents the detection of transitory effects and allows to temporarily stabilize the
functioning of the heating apparatus 10.
Example
[0056]
- Value of the protection potential maintained during normal functioning of the heating
apparatus 10, Vp = -1000mV;
- Value of the measured potential Vm, 60secs after the temporary interruption of the
current generator 14, without direct current dispersions: Vm1 = -750mV;
- Value of the measured potential Vm, 60secs after the temporary interruption of the
current generator 14, in the presence of direct current dispersions: Vm2 = - 290mV.
[0057] Once the measured potential Vm has been measured, that is, after time interval T
(fig. 2a), the heating apparatus 10 resume normal functioning, returning the difference
in potential to the value of protection potential Vp.
[0058] With reference to figs. 3a, 3b and 3c, another form of embodiment of the method that
is not part of the present invention is described, used to detect electric dispersions
in alternating current.
[0059] During the normal functioning of the heating apparatus 10, the controller 16 commands
the current generator 14 to generate, between the electrode 13 and the tank 12, a
difference in potential with a desired development and variable over time.
[0060] In particular, the current generator 14 alternates in very short times, that is,
about every 200µs, the generation of a first potential V1, and a second potential
V2 with a reduced intensity compared to the first potential V1.
[0061] The values of the first potential V1 and the second potential V2 are determined so
as to obtain a polarization of the electrolytic solution to a value corresponding
to the protection potential Vp.
[0062] Some forms of embodiment provide that the second potential V2 is comprised between
30% and 70% of the first potential V1.
[0063] The variation in potential between the first potential V1 and the second potential
V2 can occur with a square wave development of period P which can be for example about
200µs (fig. 3a).
[0064] In the normal functioning of the heating apparatus 10 and in the absence of electric
dispersions due to alternating currents, the controller 16 acts by modulating the
current to be supplied to the current generator 14 so as to guarantee said protection
potential Vp in the electrolytic solution.
[0065] During this step, the measurer 15 measures the electric quantities, in this case
the current circulating in the electric cathodic protection device 11, to evaluate
whether a balanced condition has been reached. The currents measured by the measurer
15 are indicated in figs. 3b and 3c, by Im.
[0066] The balanced condition is represented by the consecutive detection of measured currents
Im substantially uniform over time (fig. 3b).
[0067] The measurements are taken by the measurer 15 when the potential at the heads of
the current generator 14 assumes the value of said second potential V2.
[0068] In the absence of stray currents, therefore, the measured current values Im are not
subjected to big deviations, and remain confined in a band of values 18 that vary
around a balanced current Ie as represented in fig. 3b.
[0069] In the presence of alternating current dispersions, the measurer 15 detects a fluctuation
in the measured currents Im which varies with a periodicity near or comparable to
that of the alternating currents of electric dispersion.
[0070] To this purpose the data detected by the measurer 15 on each occasion are transmitted
to the processing unit 19 to reconstruct the development over time of the measured
currents Im. The processing unit 19 is able to identify the cyclicity of the values
detected which, in the presence of stray alternating currents, vary with a frequency
substantially equal to, or a multiple of, the latter, for example with a frequency
of 50Hz or 60Hz or multiples thereof.
[0071] It is quite clear that to allow a correct acquisition of the cyclicity of the stray
currents, the frequency at which the measurements are made must be greater than the
frequency of the stray currents.
[0072] If the processing unit 19 identifies a cyclical development of the measurements performed
as indicated above, it commands the activation of the indicators 17 to signal to the
user a condition of anomalous functioning.
[0073] Some forms of embodiment of the present invention can provide that the light indicators
comprise a plurality of light sources, in this case (fig. 1) a red led 17a, a green
led 17b and a yellow led 17c, each of which identifies a particular functioning condition
of the heating apparatus 10.
[0074] The controller 16 described above can also provide a function of counting the working
time of the electric cathodic protection device 11.
[0075] For example, it may provide that in the first electric feed to the heating apparatus
10, the indicators 17 indicate to the user said working time, for example an indication
of the years of work that corresponds to the number of flashes of the red led 17a,
and an indication of the months of work that corresponds to the number of flashes
of the green led 17b. To this purpose it may be provided that the controller 16 also
comprises timer means to determine the working time.
[0076] In the normal functioning of the heating apparatus 10, and if no electric dispersions
are detected, the green led 17b remains switched on.
[0077] If electric dispersions are detected, the yellow led 17c switches on and remains
on until a maintenance operation is requested.
[0078] The red led 17a can be used to indicate conditions of excessive electric absorption
by the heating apparatus 10, or to indicate short circuit conditions or an open circuit
in the heating apparatus 10.
[0079] It is clear that modifications and/or additions of parts may be made to the method
to control the functioning of a heating apparatus as described heretofore, without
departing from the field and scope of the present invention.
[0080] It is also clear that, although the present invention has been described with reference
to some specific examples, a person of skill in the art shall certainly be able to
achieve many other equivalent forms of method to control the functioning of a heating
apparatus, having the characteristics as set forth in the claims and hence all coming
within the field of protection defined thereby.
1. Method to control the functioning of a heating apparatus (10) which comprises a tank
(12) containing an electrolytic solution inside it, an electrode (13) immersed in
said electrolytic solution, an electric energy generator (14) connected to said electrode
(13) and to said tank (12), and a controller (16) provided with a measurer (15) which
measures at least one electric quantity which is established between said electrode
(13) and said tank (12), said method providing at least a protective step in which
said electric energy generator (14) is regulated to maintain, between said electrode
(13) and said tank (12), a protection potential with a first value (Vp), known and
substantially constant over time, suitable to guarantee the protection of said tank
(12) from corrosion, said protection step providing a regulation of a current supplied
by the electric energy generator (14), a detection, with said measurer (15), of electric
currents established, and a regulation of the current supplied by the electric energy
generator (14) to maintain a balanced condition of said protection potential to said
first value (Vp),
characterized in that it comprises at least a step of detecting direct currents of electric dispersions
present in said tank (12), wherein said detection step comprises:
- a step of temporary interruption or reduction of the electric energy supplied by
said electric energy generator (14);
- a step of measuring the residual potential, having a second value (Vm), which is
established between said electrode (13) and said tank (12), said step of measuring
the residual potential being performed during said step of temporary interruption
or reduction of the electric energy;
- a step of comparing said second value (Vm) of the residual potential measured and
a third value (Vr) of a reference potential;
wherein, if said second value measured (Vm) is greater than said third value (Vr)
of the reference potential, said controller (16) recognizes a functioning condition
that is within the norm, and wherein, if said second value measured (Vm) is less than
said third value (Vr) of the reference potential, said controller (16) recognizes
the presence of electric dispersions deriving from direct currents in said tank (12).
2. Method as in claim 1, characterized in that, if said second value (Vm) of the potential measured is less than the reference potential
(Vr), indicators (17) are activated to warn of the presence of electric dispersions.
3. Method as in claim 1 or 2, characterized in that said third value (Vr) of the reference potential is comprised between 20% and 40%
of said first value (Vp) of the protection potential.
4. Method as in any claim hereinbefore, characterized in that said interruption or reduction of electric energy supplied by said electric energy
generator (14) has a duration of an interval of time (T), and in that the detection of the second value (Vm) of said measured potential occurs after a
period of time (S) from the start of said interruption or reduction.
5. Method as in claim 4, characterized in that said period of time (S) is comprised between 30secs and 60secs.
6. Method as in claim 4, characterized in that after said interval of time (T), said protection potential is returned to said first
value (Vp).