CN212339188U - Device for heating molten salt - Google Patents

Abstract

The utility model relates to a device for heating fused salt. The device comprises: a first brine tank provided with at least one preheater; a second salt solution tank disposed at a higher position than the first salt solution tank; at least one set of molten salt electrodes, each set of molten salt electrodes comprising a plurality of molten salt electrode tanks disposed at a higher level than the first molten salt tank and at a lower level than the second molten salt tank; at least one group of inlet electrode insulated pipelines; at least one group of electrode-outlet insulated pipelines; a power supply device, each phase of the multiphase alternating current of which is electrically connected to a corresponding one of a plurality of molten salt electrode tanks; a first connecting conduit fluidly connecting the first saltwater tank to the second saltwater tank; a molten salt circulation pump provided in the first connecting pipe; and a controller electrically connected to the pre-heater, the power supply device and the molten salt circulating pump to control the on or off of the pre-heater, the power supply or cut-off of the power supply device and the rotating speed of the molten salt circulating pump.

Description

Device for heating molten salt

Technical Field

The utility model relates to a fused salt heating field, more specifically relate to use device of electrode heating fused salt.

Background

The fused salt is a heat transfer and storage medium with excellent fluidity, has the characteristics of low steam pressure, wide applicable temperature range, stable chemical property, large heat capacity, no combustion, low price, easy preparation and the like, and has wide application prospect in the field of heat storage, particularly in the field of medium-high temperature heat storage.

At present, the molten salt is heated by adopting an electric bar in an indirect heat conduction mode, the higher the working temperature of the electric heating wire is, the shorter the service life of the electric heating wire is, the better the insulation between the electric heating wire and the outer sleeve is, the worse the heat transfer is, and the electric heating wire is not beneficial to being applied to the high-temperature high-power electric heating of the molten salt.

The electrode type heating method is characterized in that current directly passes through the molten salt to generate heat, the molten salt is a heating body, and the problems caused by indirect heating do not exist, but because the molten salt has high conductivity, the current density on the surface of an electrode cannot be controlled within a reasonable range by the conventional electrode heating technical means, and the corrosion of electrode materials and the electrolysis of the molten salt are difficult to avoid.

The information disclosed in this background section is only for enhancement of understanding of the general background of the invention and should not be taken as an acknowledgement or any form of suggestion that this information constitutes prior art already known to a person skilled in the art.

SUMMERY OF THE UTILITY MODEL

The utility model aims at providing an use device of electrode heating fused salt. The utility model discloses can successfully solve the difficult problem of the technique of realizing electrode low current density work in various ionic conductor under arbitrary voltage, not only be applicable to fused salt electrode formula heating, also be applicable to other ionic conductor's that have mobility electrode formula heating, utilize the utility model discloses can the manufacturing and designing be applicable to the fused salt electric heating equipment of the various power size of various voltage range.

To achieve the above object, the present invention provides an apparatus for heating molten salt, comprising: the first salt solution tank is internally provided with at least one preheater; a second salt solution tank disposed at a higher position than the first salt solution tank; at least one set of molten salt electrodes, each set of molten salt electrodes comprising a plurality of molten salt electrode tanks disposed at a higher level than the first molten salt tank and at a lower level than the second molten salt tank; at least one set of electrode-entering insulated pipes, the number of pipes in each set of electrode-entering insulated pipes being the same as the number of the plurality of molten-salt electrode tanks in each set of molten-salt electrodes, a first end of the electrode-entering insulated pipes being fluidly connected to the second molten-salt tank, a second end of the electrode-entering insulated pipes being fluidly connected to a corresponding one of the plurality of molten-salt electrode tanks, so that molten salt can flow through the electrode-entering insulated pipes; at least one group of outlet electrode insulated pipelines, wherein the number of the pipelines in each group of outlet electrode insulated pipelines is the same as that of the plurality of molten salt electrode boxes in each group of molten salt electrodes, the first end of each outlet electrode insulated pipeline is communicated with a corresponding one of the plurality of molten salt electrode boxes in a fluid mode, and the second end of each outlet electrode insulated pipeline is communicated with the first salt liquid box in a fluid mode, so that molten salt can flow through the outlet electrode insulated pipelines; a power supply device including a multi-phase alternating current, the number of phases of the multi-phase alternating current being the same as the number of the plurality of molten salt electrode tanks, each phase of the multi-phase alternating current of the power supply device being electrically connected to a corresponding one of the plurality of molten salt electrode tanks; a first connecting conduit fluidly connecting the first saltwater tank to the second saltwater tank; a molten salt circulation pump provided in the first connection pipe and adapted to pump molten salt in the first salt liquid tank to the second salt liquid tank; and a controller electrically connected to the pre-heater, the power supply device and the molten salt circulating pump to control the on or off of the pre-heater, the power supply or cut-off of the power supply device and the rotating speed of the molten salt circulating pump.

In the above apparatus for heating molten salt, the number of the plurality of molten salt electrode boxes of each group of molten salt electrodes is three, the multiphase alternating current is a three-phase alternating current, each group of the electrode-entering insulating pipelines includes three electrode-entering insulating pipelines, and each group of the electrode-exiting insulating pipelines includes three electrode-exiting insulating pipelines.

In the above apparatus for heating molten salt, the molten salt flowing in each of the pipelines in each of the groups of the electrode-inlet insulated pipelines generates a first resistance value resistance having the same resistance value, and the molten salt flowing in each of the pipelines in each of the groups of the electrode-outlet insulated pipelines generates a second resistance value resistance having the same resistance value.

Further, the first resistance value and the second resistance value are also the same.

In the above apparatus for heating molten salt, the molten salt electrode box is made of a corrosion-resistant and high-temperature-resistant metal material into a container having a specific internal surface area, and has an electrode-inlet insulated pipe connection port and an electrode-outlet insulated pipe connection port, a second end of the electrode-inlet insulated pipe is fluidly connected to the electrode-inlet insulated pipe connection port of the corresponding molten salt electrode box, and a first end of the electrode-outlet insulated pipe is fluidly connected to the electrode-outlet insulated pipe connection port of the corresponding molten salt electrode box; and the outer wall of the fused salt electrode box is connected with a conductive copper bar.

In the above-described apparatus for heating molten salt, the electrode-entering insulated pipe and the electrode-exiting insulated pipe are formed in the form of "pipes" or "tanks"; the electrode inlet insulating pipelines and the horizontal plane form a specific included angle and incline, the included angle of each pipeline in each group of electrode inlet insulating pipelines relative to the horizontal plane is the same, the length of each pipeline in each group of electrode inlet insulating pipelines is the same, and the flow cross-sectional area of each pipeline in each group of electrode inlet insulating pipelines is the same, so that the flow of each pipeline in each group of electrode inlet insulating pipelines is ensured to be the same; the electrode outlet insulating pipelines are inclined at a specific included angle with the horizontal plane, the included angle of each pipeline in each group of electrode outlet insulating pipelines relative to the horizontal plane is the same, the length of each pipeline in each group of electrode outlet insulating pipelines is the same, and the flow cross-sectional areas of the pipelines in each group of electrode outlet insulating pipelines are the same, so that the flow of each pipeline in each group of electrode outlet insulating pipelines is ensured to be the same.

According to the utility model discloses a device for heating fused salt, it is further provided with: a molten salt storage tank having a volume greater than the first salt solution tank, the molten salt storage tank having a plurality of pre-heaters disposed therein; a second connecting conduit fluidly connecting the first salt tank to the molten salt storage tank; a molten salt return pump provided in the second connecting pipe and used for pumping the molten salt in the first salt liquid tank to the molten salt storage tank; a third connecting conduit fluidly connecting the molten salt storage tank to the second brine tank; and a flow control valve provided in the third connecting pipe; wherein the controller is further electrically connected to the plurality of pre-heaters in the molten salt storage tank, the molten salt return pump, and the flow control valve to control opening or closing of the plurality of pre-heaters in the molten salt storage tank, a rotational speed of the molten salt return pump, and an opening degree of the flow control valve.

With the above-described respective exemplary embodiments, the advantages of the present invention are utilized: the insulated pipeline and the fused salt electrode can be designed according to any power voltage and heating power to form the applicable fused salt heating device. The utility model discloses a device of electrode formula heating fused salt adopts fused salt self to be the heat-generating body, no heat conduction loss, also does not have the heating wire risk of burning futilely, and only moving part is the fused salt circulating pump, in case the pump shut down heating also stops thereupon. Most importantly, the utility model discloses successfully solved under arbitrary operating voltage the technical problem who realizes the work of electrode low current density in various high conductivity ionic conductor.

Drawings

Fig. 1 is a schematic view of an apparatus for heating molten salt according to an exemplary embodiment of the present invention.

Fig. 2 is a schematic view of an apparatus for heating molten salt according to another exemplary embodiment of the present invention.

Fig. 3A and 3B are schematic cross-sectional views of the electrode-entering insulated pipe and/or the electrode-exiting insulated pipe in the apparatus for heating molten salt according to the present invention.

Fig. 4A and 4B illustrate an example of a molten salt electrode tank in an apparatus for heating molten salt according to an exemplary embodiment of the present invention, in which fig. 4B is a schematic cross-sectional view of fig. 4A.

Fig. 4C and 4D show another example of a molten salt electrode tank in an apparatus for heating molten salt according to an exemplary embodiment of the present invention, in which fig. 4D is a side view of fig. 4C.

Fig. 5 is a schematic view of an apparatus for heating molten salt according to yet another exemplary embodiment of the present invention.

It is to be understood that the appended drawings are not to scale, but rather illustrate various features which are, presented in a somewhat simplified form, and which are indicative of the basic principles of the invention. In the drawings of the present invention, like reference numerals designate like or equivalent parts of the invention.

Detailed Description

Reference will now be made in detail to various embodiments of the present invention, examples of which are illustrated in the accompanying drawings and described below. While the present invention will be described in conjunction with exemplary embodiments thereof, it will be understood that the present description is not intended to limit the invention to those exemplary embodiments. On the contrary, the invention is intended to cover not only the exemplary embodiments of the invention, but also various alternatives, modifications, equivalents and other embodiments, which are included within the spirit and scope of the invention as defined by the appended claims.

Hereinafter, various exemplary embodiments of the present invention will be described in more detail with reference to the accompanying drawings.

Fig. 1 shows an apparatus 100 for heating molten salt according to an exemplary embodiment of the present invention, which may include:

the first salt solution tank 10 is made of high-temperature-resistant and corrosion-resistant materials and is grounded, and at least one preheater 11 is arranged inside the first salt solution tank 10;

a second brine tank 20 made of a high temperature-resistant, corrosion-resistant material and grounded, the second brine tank 20 being disposed at a higher position than the first brine tank 10;

at least one set of molten salt electrodes 30, each set of molten salt electrodes 30 comprising a plurality of molten salt electrode tanks disposed at a higher level than the first molten salt tank 10 and at a lower level than the second molten salt tank 20;

at least one set of electrode-entering insulated pipes 40, the number of pipes in each set of electrode-entering insulated pipes being the same as the number of the plurality of molten-salt electrode boxes in each set of molten-salt electrodes, a first end (an upper end) of the electrode-entering insulated pipes 40 being fluidly connected to the second molten-salt box 20, and a second end (a lower end) of the electrode-entering insulated pipes 40 being fluidly connected to a corresponding one of the plurality of molten-salt electrode boxes, so that molten salt can flow through the electrode-entering insulated pipes 40;

at least one group of outlet electrode insulated pipelines 50, wherein the number of the pipelines in each group of outlet electrode insulated pipelines is the same as that of the plurality of molten salt electrode boxes in each group of molten salt electrodes, a first end (the upper end) of each outlet electrode insulated pipeline 50 is in fluid communication with a corresponding one of the plurality of molten salt electrode boxes, and a second end (the lower end) of each outlet electrode insulated pipeline 50 is in fluid communication with the first salt liquid box 10, so that the molten salt can flow through the outlet electrode insulated pipelines 50;

a power supply device 60 that includes a multi-phase alternating current and the number of phases of the multi-phase alternating current is the same as the number of the plurality of molten salt electrode tanks, each phase of the multi-phase alternating current of the power supply device 60 being electrically connected to a corresponding one of the plurality of molten salt electrode tanks;

a first connecting conduit 12 fluidly connecting the first saltwater tank 10 to the second saltwater tank 20;

a molten salt circulation pump 13 provided in the first connection pipe 12 and adapted to pump the molten salt in the first salt tank 10 to the second salt tank 20; and

a controller 70 electrically connected to the preheater 11, the power supply device 60 and the molten salt circulation pump 13 to control turning on or off of the preheater 11, power supply or cut-off of the power supply device 60 and rotation speed of the molten salt circulation pump 13.

Specifically, in the present exemplary embodiment, the plurality of molten salt electrode tanks of each group of molten salt electrodes 30 are three (denoted by reference numerals 31, 32, 33, respectively, in fig. 1), the multiphase alternating current is a three-phase alternating current (denoted by reference numerals L1, L2, L3), each group of incoming electrode insulation piping 40 includes three incoming electrode insulation piping (denoted by reference numerals 41, 42, 43, respectively, in fig. 1), and each group of outgoing electrode insulation piping 50 includes three outgoing electrode insulation piping (denoted by reference numerals 51, 52, 53, respectively, in fig. 1). Specifically, each phase L1, L2, L3 of the three-phase alternating current is electrically connected to the three molten salt electrode tanks 31, 32, 33, respectively. It will be appreciated by those skilled in the art that three-phase ac is merely an example, and more or less phase ac is possible, e.g., two-phase ac is also possible.

In the embodiment shown in FIG. 1, only one set of molten salt electrodes 30 is shown, but it will be understood by those skilled in the art that two, three or more sets of molten salt electrodes 30 may be provided, and that each set of molten salt electrodes 30 includes a plurality of molten salt electrode tanks (illustrated as each set of molten salt electrodes 30 including three molten salt electrode tanks 31, 32, 33). Accordingly, taking a three-phase alternating current as an example, in the case of including three sets of molten salt electrodes 30, L1 phases of the three-phase alternating current are electrically connected to the first molten salt electrode tank 31 of each set of molten salt electrodes 30, L2 phases of the three-phase alternating current are electrically connected to the second molten salt electrode tank 32 of each set of molten salt electrodes 30, and L3 phases of the three-phase alternating current are electrically connected to the third molten salt electrode tank 33 of each set of molten salt electrodes 30, respectively. Further, fig. 1 shows only one set of the inlet electrode insulating pipes 40 and one set of the outlet electrode insulating pipes 50, that is, for one set of the molten salt electrodes 30, one set of the inlet electrode insulating pipes 40 and one set of the outlet electrode insulating pipes 50 are provided. However, it will be understood by those skilled in the art that two or more sets of the electrode-inlet insulating pipes 40 and two or more sets of the electrode-outlet insulating pipes 50 may be provided in parallel for one set of the molten salt electrode 30, as required.

Specifically, in the present exemplary embodiment, the molten salt flowing inside the respective pipes in each set of the electrode-entering insulating pipes 40 produces the first resistance-value resistances having the same resistance value, that is, the resistance values produced by the molten salt flowing inside the respective electrode-entering insulating pipes 41, 42, 43 are the same as each other. The molten salt flowing through the respective outlet electrode insulated pipes 50 of each group generates a second resistance value resistance having the same resistance value, that is, the resistance values generated by the molten salt flowing through the respective outlet electrode insulated pipes 51, 52, 53 are the same as each other.

In order to make the resistance values generated by the molten salt flowing in the electrode-entering insulated pipelines 41, 42 and 43 equal to each other, the electrode-entering insulated pipelines may have a cross section in a circular, oval, rectangular, hexagonal or other closed shape, each insulated pipeline is a complete pipeline or is formed by combining a plurality of short pipes, and each group of electrode-entering insulated pipelines has the same flow cross section and the same length, so as to ensure that the pipelines of each group of electrode-entering insulated pipelines have the same resistance values after being filled with the molten salt liquid. Furthermore, the electrode insulating pipeline is vertically arranged or obliquely arranged with a specific included angle formed between the electrode insulating pipeline and the horizontal plane, so that the fused salt flowing by means of gravity has enough flow and can take out all heat. The embodiment that the electrode insulation pipe is vertically arranged can be shown in fig. 1, and the embodiment that the electrode insulation pipe is obliquely arranged at a specific included angle with the horizontal plane can be shown in fig. 2. In fig. 2, the included angle of each pipe in each group of electrode-entering insulating pipes with respect to the horizontal plane is the same, so as to ensure that each group of electrode-entering insulating pipes has the same flow cross-sectional area and the same length, thereby ensuring that each pipe in each group of electrode-entering insulating pipes has the same resistance value after being filled with molten salt liquid.

Similarly, in order to make the resistance values generated by the molten salt flowing in the outlet electrode insulated pipes 51, 52 and 53 equal to each other, the outlet electrode insulated pipes may have a cross section in a circular shape, an oval shape, a rectangular shape, a hexagonal shape or other closed shapes, each insulated pipe is a complete pipe or is formed by combining a plurality of short pipes, and each outlet electrode insulated pipe has the same flow cross section and the same length, so as to ensure that each pipe of each outlet electrode insulated pipe has the same resistance value after being filled with the molten salt liquid. Furthermore, the electrode outlet insulating pipeline is vertically arranged or obliquely arranged at a specific included angle with the horizontal plane, so that the fused salt flowing by gravity has enough flow and can take out all heat. The embodiment in which the outlet electrode insulating pipe is vertically arranged can be shown in fig. 1, and the embodiment in which the outlet electrode insulating pipe is obliquely arranged at a specific included angle with the horizontal plane can be shown in fig. 2. In fig. 2, the included angles of the pipelines in each group of the electrode outlet insulating pipelines with respect to the horizontal plane are the same, so as to ensure that each group of the electrode outlet insulating pipelines has the same flow cross-sectional area and the same length, thereby ensuring that each pipeline of each group of the electrode outlet insulating pipelines has the same resistance value after being filled with the molten salt liquid.

Preferably, in the embodiment shown in fig. 2, the included angle of each pipe in each group of the electrode-entering insulated pipes relative to the horizontal plane is the same as the included angle of each pipe in each group of the electrode-exiting insulated pipes relative to the horizontal plane.

Further, as shown in fig. 3A and 3B, the electrode-entering insulating conduit 40 and/or the electrode-exiting insulating conduit 50 may not have a closed-shaped cross section, but may be formed in the form of a "groove", and specifically, an insulating tube groove. The insulating pipe groove has a bottom with a semicircular section or an inverted trapezoidal section, or has a section with an open form with other shapes. Similarly, each insulating pipe groove is a complete pipe groove or formed by overlapping a plurality of sections of short grooves, each group of electrode inlet insulating pipe grooves have the same flow cross section area and the same length, so that the molten salt in the electrode inlet insulating pipe grooves has the same resistance value when flowing, and each group of electrode outlet insulating pipe grooves have the same flow cross section area and the same length, so that the molten salt in the electrode outlet insulating pipe grooves has the same resistance value when flowing.

In a preferred embodiment, the first resistance value and the second resistance value are also the same. That is, the resistance value of the molten salt flowing through the electrode-inlet insulated pipes 41, 42, and 43 and the resistance value of the molten salt flowing through the electrode-outlet insulated pipes 51, 52, and 53 are also the same.

In an exemplary embodiment of the present invention, the molten salt electrode box 31, 32, 33 is a container made of a corrosion-resistant and high-temperature-resistant metal material and having a specific inner surface area, and has an electrode-insulated pipe connection port and an electrode-insulated pipe connection port, the second end of the electrode-insulated pipe is fluidly connected to the electrode-insulated pipe connection port of the corresponding molten salt electrode box, and the first end of the electrode-insulated pipe is fluidly connected to the electrode-insulated pipe connection port of the corresponding molten salt electrode box. Further, fused salt electrode incasement portion can be equipped with baffle or pipe and go out electrode insulation pipeline connection port and form the siphon runner to thereby guarantee that fused salt electrode incasement portion keeps certain liquid level height when the fused salt flows and guarantee that electrode and fused salt have sufficient area of contact, and fused salt electrode incasement portion does not basically have the fused salt to be detained or only a small amount of fused salt is detained when the stop heating, and furtherly, fused salt electrode incasement portion outer wall is connected with electrically conductive copper bar.

Specifically, as shown in fig. 4A and 4B, there is shown an example of a molten salt electrode tank in an apparatus for heating molten salt according to an exemplary embodiment of the present invention. The molten salt electrode tank shown in fig. 4A and 4B has an electrode-inlet insulated pipe connection port 34 and an electrode-outlet insulated pipe connection port 35, a second end (lower end) of the electrode-inlet insulated pipe 40 is fluidly connected to the electrode-inlet insulated pipe connection port 34 of the molten salt electrode tank, and a first end (upper end) of the electrode-outlet insulated pipe 50 is fluidly connected to the electrode-outlet insulated pipe connection port 35 of the molten salt electrode tank. In the embodiment shown in fig. 4A and 4B, the inside of the molten salt electrode tank is provided with a partition plate 36 which forms a flow channel with the electrode inlet insulated pipe connection port 34 and the electrode outlet insulated pipe connection port 35 to ensure that a certain liquid level height is maintained inside the molten salt electrode tank when molten salt flows so as to ensure that the electrode has a sufficient contact area with the molten salt, and that substantially no molten salt or only a small amount of molten salt is retained inside the molten salt electrode tank when heating is stopped. Further, the copper busbar connected to the outer wall of the molten salt electrode box is not shown in fig. 4A and 4B, and is of a conventional design known to those skilled in the art and is therefore not shown.

Further, as shown in fig. 4C and 4D, it shows another example of a molten salt electrode tank in an apparatus for heating molten salt according to an exemplary embodiment of the present invention. The molten salt electrode tank shown in fig. 4C is a vessel having a specific internal surface area and has an inlet electrode insulated pipe connection port 34 and an outlet electrode insulated pipe connection port 35. In the embodiment shown in fig. 4C, no partition is arranged inside the molten salt electrode box, which relies on its own volume to ensure that the inside of the molten salt electrode box is maintained at a certain liquid level height when the molten salt flows so as to ensure that the electrode has a sufficient contact area with the molten salt, and that substantially no molten salt remains inside the molten salt electrode box when heating is stopped.

Hereinafter, a method of heating molten salt using the above-described apparatus for heating molten salt is specifically described, the method including the steps of: the salt in the first salt solution tank 10 is heated by a preheater 11 and heated to a molten state in which the salt can flow; after the salt is in a molten state capable of flowing, turning off the preheater 11; pumping the molten salt in the first salt solution tank 10 to the second salt solution tank 20 by using the molten salt circulating pump 13, and controlling the rotating speed of the molten salt circulating pump 13 so that the amount of the molten salt entering the second salt solution tank 20 is more than the amount of the molten salt flowing away from the second salt solution tank 20 through the electrode-feeding insulated pipeline 40; after the molten salt flowing through the electrode inlet insulating pipeline 40 enters the molten salt electrode box and correspondingly flows through the electrode outlet insulating pipeline 50 into the first salt solution box 10, the power supply device 60 is started to supply power, so that the molten salt is heated; when the molten salt in the second molten salt tank 20 reaches a predetermined liquid level height, the rotating speed of the molten salt circulating pump 13 is controlled so that the amount of the molten salt entering the second molten salt tank 20 is equal to the amount of the molten salt flowing away from the second molten salt tank 20 through the electrode-entering insulating pipe 40.

By the above method of heating the molten salt, the molten salt is pumped from the first salt solution tank 10 to the second salt solution tank 20, then the molten salt in the second salt solution tank 20 flows into the molten salt electrode tank through the electrode inlet insulation pipe 40 by gravity, and then the molten salt in the molten salt electrode tank flows into the first salt solution tank 10 through the electrode outlet insulation pipe 50 by gravity, thereby forming a cycle. Simultaneously with the above-described cycle, the power supply device 60 is turned on to supply power, so that the molten salt is heated.

The utility model takes three-phase alternating current as an example, and uses electrodes to heat fused salt, which is equivalent to a star connection method using three-phase alternating current. The star connection method is characterized in that the current can be circulated between phase lines when the connection is not connected with a zero line, if three-phase loads are the same, the vector sum of the three-phase currents is zero, and therefore the neutral line current is zero. Therefore, the electrodes can heat the molten salt as long as the phase balance between the electrodes is ensured, namely the flow rate and the flow velocity of the molten salt flowing through the electrodes are the same, and the size of the electrodes is the same.

In an exemplary embodiment of the present invention, upon heating by the preheater 11, the salt may be heated to 200-; further, after the power supply device 60 is turned on, the molten salt may be heated to 300-.

The utility model discloses an in the preferred embodiment, three-phase alternating current is connected to fused salt electrode 30, and the fused salt is heated at the in-process of above-mentioned circulation, and the high temperature fused salt after being heated flows into first salt solution case, and the fused salt is carried to the high-order and flows into the continuous circulation of second salt solution case by the fused salt circulating pump from first salt solution case, and the fused salt is taken the heat out simultaneously in the circulation process.

Through the utility model discloses the fused salt that is heated can be applied to: the heat exchanger is used for providing industrial high-temperature steam at different temperatures, directly providing high-temperature steam for a steam turbine of a power plant, and also providing steam at different temperatures for wine making, pharmacy, mining industry and the like. Further, the utility model discloses can utilize the electric power of power plant's peak shaving, convert the electricity into heat storage or use. The utility model discloses also can directly utilize the electric power that the discarded clean energy produced to directly change into heat storage or directly use.

In the exemplary embodiment of the present invention, after the molten salt circulating pump 13 is stopped, the molten salt in the second molten salt tank 20, the electrode-entering insulating pipe 40, the molten salt electrode tank, and the electrode-exiting insulating pipe 50 all or substantially all fall back into the first molten salt tank 10 under the action of gravity, and the heating is also stopped accordingly. Specifically, the utility model discloses a fused salt electrode case has the container shape, and fused salt electrode incasement portion is equipped with baffle or pipe and goes out electrode insulating tube way connection port 35 and forms the siphon runner, thereby ensures that the electrode is inside to have sufficient liquid level height when the heating and guarantees that electrode and fused salt have sufficient area of contact, can make the fused salt all or basically all flow out in the electrode in order to prevent freezing under the siphon effect again when the stop heating. In certain embodiments, there may be a small amount of molten salt retained inside the molten salt electrode compartment, but there is no adverse effect as long as the flow of molten salt is not affected upon reuse, where hot molten salt melts the retained frozen molten salt, thereby keeping it flowing.

In an exemplary embodiment of the present invention, according to the above-described method for heating molten salt, when the heating is ready to be finished, the rotation speed of the molten salt circulation pump 13 may be controlled so that the amount of molten salt entering the second molten salt tank 20 is smaller than the amount of molten salt flowing away from the second molten salt tank 20 through the electrode-entering insulating pipe 40. In this way, the liquid level in the second brine tank 20 can be gradually lowered, and heating is ended again when lowered to a certain height, thereby further improving the effect and more easily preventing the molten salt from freezing.

Further, as shown in fig. 5, there is shown a schematic view of an apparatus for heating molten salt according to still another exemplary embodiment of the present invention.

In an apparatus for heating molten salt according to still another exemplary embodiment of the present invention, it is further provided with:

a molten salt storage tank 80 having a larger volume than the first salt solution tank 10, the molten salt storage tank 80 being provided with a plurality of preheaters (not shown) inside;

a second connecting conduit 81 fluidly connecting the first salt tank 10 to the molten salt storage tank 80;

a molten salt return pump 82 provided in the second connecting pipe 81 and adapted to pump the molten salt in the first salt liquid tank 10 to the molten salt storage tank 80;

a third connecting conduit 83 fluidly connecting the molten salt storage tank 80 to the second brine tank 20; and

a flow control valve 84 provided in the third connecting pipe 83;

wherein the controller 70 is further electrically connected to the plurality of pre-heaters in the molten salt storage tank 80, the molten salt return pump 82, and the flow control valve 84 to control the opening or closing of the plurality of pre-heaters in the molten salt storage tank, the rotational speed of the molten salt return pump 82, and the opening degree of the flow control valve 84.

Specifically, in the embodiment shown in fig. 5, the connection manner of the controller 70 and the plurality of pre-heaters in the molten salt storage tank 80, the molten salt return pump 82 and the flow control valve 84 is not specifically shown, but referring to the embodiment shown in fig. 1, the connection manner of the controller 70 and the plurality of pre-heaters in the molten salt storage tank 80, the molten salt return pump 82 and the flow control valve 84 is clearly known to those skilled in the art and is therefore not shown in fig. 5.

Further, in the embodiment shown in fig. 5, the first connection pipe 12 and the molten salt circulation pump 13 shown in fig. 1 are not shown, but those skilled in the art will appreciate that the embodiment shown in fig. 5 may have the first connection pipe 12 and the molten salt circulation pump 13.

Hereinafter, a method of heating the molten salt using the apparatus for heating a molten salt shown in fig. 5 is described in detail, the method including the steps of: using a pre-heater to heat the salt in the first salt liquid tank 10 and/or the molten salt storage tank 80 and to heat the salt to a molten state capable of flowing; after the salt is in a molten state capable of flowing, closing the preheater; adjusting the flow control valve 84 so that the molten salt in the molten salt storage tank 80 flows into the second molten salt tank 20, and controlling the opening degree of the flow control valve 84 so that the amount of the molten salt entering the second molten salt tank 20 is more than the amount of the molten salt flowing away from the second molten salt tank 20 through the electrode-entering insulating pipe 40; after the molten salt flowing through the electrode inlet insulating pipeline 40 enters the molten salt electrode box and correspondingly flows through the electrode outlet insulating pipeline 50 into the first salt solution box 10, the power supply device 60 is started to supply power, so that the molten salt is heated; pumping the molten salt in the first salt liquid tank 10 to a molten salt storage tank 80 by using a molten salt return pump 82, and controlling the rotating speed of the molten salt return pump 82 to ensure that the molten salt in the first salt liquid tank 10 keeps a certain liquid level height; when the molten salt in the second molten salt tank 20 reaches a predetermined liquid level height, the opening degree of the flow control valve 84 is controlled so that the amount of the molten salt entering the second molten salt tank 20 is equal to the amount of the molten salt flowing away from the second molten salt tank 20 through the electrode-entering insulating pipe 40.

With the above-described respective exemplary embodiments, the advantages of the present invention are utilized: the insulated pipeline and the fused salt electrode can be designed according to any power voltage and heating power to form the applicable fused salt heating device. The utility model discloses a device of electrode formula heating fused salt adopts fused salt self to be the heat-generating body, no heat conduction loss, also does not have the heating wire risk of burning futilely, and only moving part is the fused salt pump (including fused salt circulating pump and/or fused salt return pump), in case the pump shut down heating also stops thereupon. Most importantly, the utility model discloses successfully solved under arbitrary operating voltage the technical problem who realizes the work of electrode low current density in various high conductivity ionic conductor.

Finally, in order to illustrate the invention more clearly, the applicant has illustrated the following with reference to examples. The utility model discloses the big or small design of insulating tube is that the fused salt that will flow through the insulating tube is regarded as a cylindrical resistance, and its resistance is R rho L/S, and R is exactly the cylindrical resistance here, and rho is the fused salt conductivity, and L is insulating tube length, and S is insulating tube cross section internal diameter area, and when L/S reached certain numerical value, the resistance that can make the insulating tube fused salt of flowing through was very big, consequently after passing through the insulating tube, the fused salt electric current had just been very little.

The foregoing descriptions of specific exemplary embodiments of the present invention have been presented for purposes of illustration and description. They are not intended to be exhaustive or to limit the invention to the precise forms disclosed, and obviously many modifications and variations are possible in light of the above teaching. The exemplary embodiments were chosen and described in order to explain certain principles of the invention and its practical application to enable one skilled in the art to make and use various exemplary embodiments of the invention and various alternatives and modifications thereof. It is intended that the scope of the invention be defined by the following claims and their equivalents.

Claims (7)

1. An apparatus for heating molten salts, comprising:

the first salt solution tank is internally provided with at least one preheater;

a second salt solution tank disposed at a higher position than the first salt solution tank;

at least one set of molten salt electrodes, each set of molten salt electrodes comprising a plurality of molten salt electrode tanks disposed at a higher level than the first molten salt tank and at a lower level than the second molten salt tank;

at least one set of electrode-entering insulated pipes, the number of pipes in each set of electrode-entering insulated pipes being the same as the number of the plurality of molten-salt electrode tanks in each set of molten-salt electrodes, a first end of the electrode-entering insulated pipes being fluidly connected to the second molten-salt tank, a second end of the electrode-entering insulated pipes being fluidly connected to a corresponding one of the plurality of molten-salt electrode tanks, so that molten salt can flow through the electrode-entering insulated pipes;

at least one group of outlet electrode insulated pipelines, wherein the number of the pipelines in each group of outlet electrode insulated pipelines is the same as that of the plurality of molten salt electrode boxes in each group of molten salt electrodes, the first end of each outlet electrode insulated pipeline is communicated with a corresponding one of the plurality of molten salt electrode boxes in a fluid mode, and the second end of each outlet electrode insulated pipeline is communicated with the first salt liquid box in a fluid mode, so that molten salt can flow through the outlet electrode insulated pipelines;

a power supply device including a multi-phase alternating current, the number of phases of the multi-phase alternating current being the same as the number of the plurality of molten salt electrode tanks, each phase of the multi-phase alternating current of the power supply device being electrically connected to a corresponding one of the plurality of molten salt electrode tanks;

a first connecting conduit fluidly connecting the first saltwater tank to the second saltwater tank;

a molten salt circulation pump provided in the first connection pipe and adapted to pump molten salt in the first salt liquid tank to the second salt liquid tank; and

a controller electrically connected to the pre-heater, the power supply device and the molten salt circulating pump to control the turning on or off of the pre-heater, the supply or cut-off of the power supply device and the rotation speed of the molten salt circulating pump.

2. An apparatus for heating molten salt as claimed in claim 1, wherein the number of molten salt electrode tanks of each group of molten salt electrodes is three, the multiphase alternating current is a three-phase alternating current, each group of the electrode-in insulated pipes includes three electrode-in insulated pipes, and each group of the electrode-out insulated pipes includes three electrode-out insulated pipes.

3. An apparatus as claimed in claim 1 for heating molten salt, in which molten salt flowing in respective ones of the inlet electrode insulated conduits of each group produces a first resistance value resistance of the same resistance value, and molten salt flowing in respective ones of the outlet electrode insulated conduits of each group produces a second resistance value resistance of the same resistance value.

4. An apparatus for heating molten salt as claimed in claim 3 where the first and second resistance values are also the same.

5. An apparatus for heating molten salt as claimed in claim 1 wherein the molten salt electrode boxes are made of corrosion resistant, high temperature resistant metal material into a vessel having a specific internal surface area and having an electrode inlet insulated pipe connection port and an electrode outlet insulated pipe connection port, the second end of the electrode inlet insulated pipe being fluidly connected to the electrode inlet insulated pipe connection port of the respective molten salt electrode box and the first end of the electrode outlet insulated pipe being fluidly connected to the electrode outlet insulated pipe connection port of the respective molten salt electrode box; and the outer wall of the fused salt electrode box is connected with a conductive copper bar.

6. An apparatus for heating molten salts as claimed in claim 3, characterized in that the inlet and outlet electrode insulated pipes are formed in the form of "pipes" or "troughs";

the electrode inlet insulating pipelines and the horizontal plane form a specific included angle and incline, the included angle of each pipeline in each group of electrode inlet insulating pipelines relative to the horizontal plane is the same, the length of each pipeline in each group of electrode inlet insulating pipelines is the same, and the flow cross-sectional area of each pipeline in each group of electrode inlet insulating pipelines is the same, so that the flow of each pipeline in each group of electrode inlet insulating pipelines is ensured to be the same;

the electrode outlet insulating pipelines are inclined at a specific included angle with the horizontal plane, the included angle of each pipeline in each group of electrode outlet insulating pipelines relative to the horizontal plane is the same, the length of each pipeline in each group of electrode outlet insulating pipelines is the same, and the flow cross-sectional areas of the pipelines in each group of electrode outlet insulating pipelines are the same, so that the flow of each pipeline in each group of electrode outlet insulating pipelines is ensured to be the same.

7. An apparatus for heating molten salt as claimed in any one of claims 1 to 6, characterized in that there is further provided:

a molten salt storage tank having a volume greater than the first salt solution tank, the molten salt storage tank having a plurality of pre-heaters disposed therein;

a second connecting conduit fluidly connecting the first salt tank to the molten salt storage tank;

a molten salt return pump provided in the second connecting pipe and used for pumping the molten salt in the first salt liquid tank to the molten salt storage tank;

a third connecting conduit fluidly connecting the molten salt storage tank to the second brine tank; and

a flow control valve provided in the third connecting pipe;

wherein the controller is further electrically connected to the plurality of pre-heaters in the molten salt storage tank, the molten salt return pump, and the flow control valve to control opening or closing of the plurality of pre-heaters in the molten salt storage tank, a rotational speed of the molten salt return pump, and an opening degree of the flow control valve.

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