CN111947118A

CN111947118A - Device for heating molten salt

Info

Publication number: CN111947118A
Application number: CN202010849737.6A
Authority: CN
Inventors: 丁晓彬; 韩围棋; 刘安全; 张荣发; 杨广亮
Original assignee: Beijing Zeta Energy Technology Co ltd
Current assignee: Beijing Zeta Energy Technology Co ltd
Priority date: 2020-08-21
Filing date: 2020-08-21
Publication date: 2020-11-17

Abstract

The invention relates to a device for heating molten salts, comprising: a first salt solution tank; 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-feed insulated conduits fluidly communicating the second molten salt tank and the molten salt electrode; at least one set of outlet electrode insulated conduits fluidly communicating the molten salt electrode with the first salt tank; and a power supply device including a multi-phase alternating current and having the same number of phases as 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.

Description

Device for heating molten salt

Technical Field

The invention relates to the field of molten salt heating, in particular to a device for heating molten salt by using an electrode.

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 forms the prior art already known to a person skilled in the art.

Disclosure of Invention

The invention aims to provide a device for heating molten salt by using an electrode. The invention can successfully solve the technical problem of realizing low-current-density work of the electrode in various ionic conductors under any voltage, is not only suitable for electrode type heating of molten salt, but also suitable for electrode type heating of other ionic conductors with fluidity, and can design and manufacture molten salt electric heating equipment with various power sizes and suitable for various voltage ranges by utilizing the invention.

To achieve the above object, the present invention provides an apparatus for heating molten salt, comprising: a first salt solution tank; 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 electrode inlet insulating pipelines, wherein the number of pipelines in each group of electrode inlet insulating pipelines is the same as that of a plurality of molten salt electrode tanks in each group of molten salt electrodes, and the electrode inlet insulating pipelines are used for communicating the second molten salt tank with the molten salt electrodes; the number of pipelines in each group of the outlet electrode insulated pipelines is the same as that of the plurality of molten salt electrode boxes in each group of the molten salt electrodes, and the outlet electrode insulated pipelines are used for communicating the molten salt electrodes with the first salt solution boxes in a fluid mode; and a power supply device including a multi-phase alternating current and having the same number of phases as 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.

The apparatus for heating molten salt according to the present invention further comprises: at least one pre-heater disposed at least inside the first saltwater tank; a connecting conduit fluidly connecting the first saltwater tank to the second saltwater tank; and a molten salt circulation pump disposed in the connection pipe and configured to pump the molten salt in the first salt liquid tank to the second salt liquid tank.

The apparatus for heating molten salt according to the present invention further comprises: 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.

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-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".

In the above apparatus for heating molten salt, the electrode-feeding insulated pipes are inclined at a specific included angle with the horizontal plane, the included angle of each pipe in each group of electrode-feeding insulated pipes with respect to the horizontal plane is the same, the length of each pipe in each group of electrode-feeding insulated pipes is the same, and the flow cross-sectional area of each pipe in each group of electrode-feeding insulated pipes is the same, so as to ensure that the flow rate of each pipe in each group of electrode-feeding insulated pipes is the same.

In the above apparatus for heating molten salt, the electrode outlet insulating pipes are inclined at a specific included angle with the horizontal plane, the included angle of each pipe in each group of electrode outlet insulating pipes with respect to the horizontal plane is the same, the length of each pipe in each group of electrode outlet insulating pipes is the same, and the flow cross-sectional area of each pipe in each group of electrode outlet insulating pipes is the same, so as to ensure that the flow rate of each pipe in each group of electrode outlet insulating pipes is 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, the electrode-inlet insulated pipe is fluidly connected to the electrode-inlet insulated pipe connection port of the corresponding molten salt electrode box, and 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.

By the various exemplary embodiments described above, the advantages of utilizing the present invention are: 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 electrode type molten salt heating device adopts the molten salt as a heating body, has no heat conduction loss and no risk of dry burning of the heating wire, and the only moving part is the molten salt circulating pump, so that the heating is stopped once the pump stops running. The invention successfully solves the technical problem of realizing low-current-density work of the electrode in various high-conductivity ionic conductors under any working voltage.

Drawings

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

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

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

Fig. 3A and 3B are schematic sectional views of an electrode-entering insulated pipe and/or an electrode-exiting insulated pipe in the apparatus for heating molten salt of 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 sectional view of fig. 4A.

Fig. 4C and 4D illustrate 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.

It is to be understood that the drawings are not to scale, but rather illustrate various features which are presented in a somewhat simplified form to illustrate 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 invention, examples of which are illustrated in the accompanying drawings and described below. While the invention will be described in conjunction with the exemplary embodiments of the invention, it will be understood that the 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. 1A shows an apparatus 100 for heating molten salt according to an exemplary embodiment of the present invention, which may include:

a first salt solution tank 10 made of a high temperature resistant and corrosion resistant material and grounded;

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 group of electrode-feeding insulated pipelines 40, wherein the number of pipelines in each group of electrode-feeding insulated pipelines is the same as that of a plurality of molten salt electrode boxes in each group of molten salt electrodes, and the electrode-feeding insulated pipelines 40 are used for fluidly communicating the second molten salt box 20 with the molten salt electrodes 30; specifically, a first end (upper end) of the electrode inlet insulating conduit 40 is fluidly connected to the second molten salt tank 20, and a second end (lower end) of the electrode inlet insulating conduit 40 is fluidly connected to a corresponding one of the plurality of molten salt electrode tanks, such that molten salt may flow through the electrode inlet insulating conduit 40;

at least one group of outlet electrode insulated pipelines 50, wherein the number of pipelines in each group of outlet electrode insulated pipelines is the same as that of a plurality of molten salt electrode boxes in each group of molten salt electrodes, and the outlet electrode insulated pipelines 50 are used for fluidly communicating the molten salt electrodes 30 with the first salt solution box 10; specifically, a first end (upper end) of the outlet electrode insulation pipe 50 is fluidly connected to a corresponding one of the plurality of molten salt electrode tanks, and a second end (lower end) of the outlet electrode insulation pipe 50 is fluidly connected to the first salt solution tank 10, so that the molten salt can flow through the outlet electrode insulation pipe 50; and

and a power supply device 60 that includes a multi-phase alternating current and has the same number of phases 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.

Further, as shown in fig. 1A, the apparatus 100 for heating molten salt according to an exemplary embodiment of the present invention further includes: a connecting conduit 12 fluidly connecting the first saltwater tank 10 to the second saltwater tank 20; and 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.

Further, as shown in fig. 1B, the apparatus 100 for heating molten salt according to another exemplary embodiment of the present invention may further include: at least one preheater 11, said at least one preheater 11 being arranged at least inside the first saltwater tank 10, in other embodiments the preheater may also be arranged inside the second saltwater tank 20. Further, the present invention further comprises a controller 70, the controller 70 being electrically connected to the pre-heater 11, the power supply device 60 and the molten salt circulation pump 13 to control the turning on or off of the pre-heater 11, the supply or cut-off of the power supply device 60 and the rotation speed of the molten salt circulation pump 13.

Specifically, in the exemplary embodiment of the present invention, the plurality of molten salt electrode tanks of each group of molten salt electrodes 30 is three (denoted by

reference numerals

31, 32, 33 in fig. 1A and 1B, respectively), the multiphase alternating current is a three-phase alternating current (denoted by L1, L2, L3), each group of incoming electrode insulation piping 40 includes three incoming electrode insulation piping (denoted by

reference numerals

41, 42, 43 in fig. 1A and 1B, respectively), and each group of outgoing electrode insulation piping 50 includes three outgoing electrode insulation piping (denoted by

reference numerals

51, 52, 53 in fig. 1A and 1B, respectively). 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. 1A and 1B, 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). In application, taking three-phase alternating current as an example, in the case of including three groups 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 group 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 group 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 group of molten salt electrodes 30, respectively. Further, fig. 1A and 1B show only one set of the electrode-entering insulated pipes 40 and one set of the electrode-exiting insulated pipes 50, that is, for one set of the molten salt electrodes 30, one set of the electrode-entering insulated pipes 40 and one set of the electrode-exiting insulated 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 exemplary embodiment of the present invention, the molten salt flowing inside the respective pipes in each set of the electrode-entering insulated pipes 40 generates the first resistance-value resistances having the same resistance value, that is, the resistance values generated by the molten salt flowing inside the respective electrode-entering

insulated 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. An embodiment in which the electrode-feeding insulated pipe is vertically disposed may be as shown in fig. 1A and 1B, and an embodiment in which the electrode-feeding insulated pipe is inclined at a specific angle to the horizontal plane may be as 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. An embodiment in which the outlet electrode insulating pipe is vertically disposed may be as shown in fig. 1A and 1B, and an embodiment in which the outlet electrode insulating pipe is inclined at a specific angle to the horizontal plane may be as 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 tanks

31, 32, 33 are containers made of a corrosion-resistant, high-temperature-resistant metal material having a specific inner surface area, and have 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 corresponding molten salt electrode tank, and the first end of the electrode-outlet insulated pipe being fluidly connected to the electrode-outlet insulated pipe connection port of the corresponding molten salt electrode tank. 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.

Next, an exemplary manner of heating the molten salt using the above-described apparatus for heating the molten salt is described: 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 10; 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 invention takes three-phase alternating current as an example, uses electrodes to heat molten salt, and 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 200-275 ℃ to be in a molten state in which the salt can flow, thereby enabling the above-described circulation; further, after the power supply device 60 is turned on, the molten salt may be heated to 300-.

In the preferred embodiment of the invention, the molten salt electrode 30 is connected with three-phase alternating current, the molten salt is heated in the circulation process, the heated high-temperature molten salt flows into the first salt liquid tank, the molten salt is conveyed to a high position by the molten salt circulating pump from the first salt liquid tank and flows into the second salt liquid tank for continuous circulation, and the molten salt simultaneously carries out heat in the circulation process.

The molten salt heated by the present invention 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 invention can utilize the power of peak shaving of the power plant to convert the electricity into heat for storage or use. The invention can also directly convert the electricity generated by the waste clean energy into heat for storage or direct use.

In the exemplary embodiment of the present invention, after the molten salt circulation pump 13 is stopped, all, or substantially all, of the molten salt in the second molten salt tank 20, the electrode-entering insulated pipe 40, the molten salt electrode tank, and the electrode-exiting insulated pipe 50 falls back into the first molten salt tank 10 under the action of gravity, and the heating is stopped accordingly. Specifically, the molten salt electrode box has a container shape, a partition plate or a conduit is arranged inside the molten salt electrode box to form a siphon flow channel with the electrode insulating pipeline connecting port 35, a sufficient liquid level height inside the electrode is ensured during heating so as to ensure a sufficient contact area between the electrode and the molten salt, and the molten salt can completely or substantially completely flow out of the electrode under the siphon action to prevent freezing when the heating is stopped. 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 method for heating molten salt described above, when the heating is ready to be ended, the rotation speed of the molten salt circulation pump 13 may be controlled so that the amount of molten salt flowing into the second molten salt tank 20 is smaller than the amount of molten salt flowing out of 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.

By the various exemplary embodiments described above, the advantages of utilizing the present invention are: 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 electrode type molten salt heating device and method provided by the invention adopt the molten salt as a heating body, have no heat conduction loss and no risk of electric heating wire dry burning, and the only moving part is a molten salt pump (comprising a molten salt circulating pump and/or a molten salt return pump), so that the heating is stopped once the pump stops running. The invention successfully solves the technical problem of realizing low-current-density work of the electrode in various high-conductivity ionic conductors under any working voltage.

Finally, in order to more clearly illustrate the invention, the applicant has illustrated the following in connection with examples. The size of the insulating tube is designed, the fused salt flowing through the insulating tube is regarded as a cylindrical resistor, the resistance value of the resistor is R ═ rho L/S, wherein R is the resistance value of the cylindrical resistor, rho is the conductivity of the fused salt, L is the length of the insulating tube, and S is the inner diameter area of the cross section of the insulating tube.

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

1. An apparatus for heating molten salts, comprising:

a first salt solution tank;

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 electrode inlet insulating pipelines, wherein the number of pipelines in each group of electrode inlet insulating pipelines is the same as that of a plurality of molten salt electrode tanks in each group of molten salt electrodes, and the electrode inlet insulating pipelines are used for communicating the second molten salt tank with the molten salt electrodes;

the number of pipelines in each group of the outlet electrode insulated pipelines is the same as that of the plurality of molten salt electrode boxes in each group of the molten salt electrodes, and the outlet electrode insulated pipelines are used for communicating the molten salt electrodes with the first salt solution boxes in a fluid mode; and

a power supply device that includes a multi-phase alternating current and has the same number of phases as 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.

2. The apparatus for heating molten salts of claim 1 further comprising:

at least one pre-heater disposed at least inside the first saltwater tank;

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

a molten salt circulation pump disposed in the connection pipe and configured to pump the molten salt in the first salt liquid tank to the second salt liquid tank.

3. The apparatus for heating molten salts of claim 2 further comprising:

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.

4. The apparatus for heating molten salt of claim 1 wherein the plurality of molten salt electrode tanks of each set of molten salt electrodes are three, the multiphase alternating current is a three-phase alternating current, each set of in-electrode insulated conduits includes three in-electrode insulated conduits, and each set of out-electrode insulated conduits includes three out-electrode insulated conduits.

5. An apparatus for heating molten salt according to claim 1, wherein molten salt flowing in each of the conduits in each of the sets of inlet electrode insulated conduits produces a first resistance value resistance having the same resistance value, and molten salt flowing in each of the conduits in each of the sets of outlet electrode insulated conduits produces a second resistance value resistance having the same resistance value.

6. The apparatus for heating molten salt of claim 5 wherein the first and second electrical resistance values are also the same.

7. An apparatus for heating molten salt according to claim 5, wherein the inlet and outlet electrode insulated pipes are formed in the form of "pipes" or "troughs".

8. An apparatus for heating molten salt according to claim 7, wherein the electrode-entering insulated pipes are inclined at a specific angle to the horizontal, the angle of each pipe in each group of electrode-entering insulated pipes to the horizontal is the same, the length of each pipe in each group of electrode-entering insulated pipes is the same, and the cross-sectional flow area of each pipe in each group of electrode-entering insulated pipes is the same to ensure that the flow rate of each pipe in each group of electrode-entering insulated pipes is the same.

9. An apparatus for heating molten salt according to claim 7, wherein the outlet electrode insulated pipes are inclined at a specific angle to the horizontal, the angle of each pipe in each group of outlet electrode insulated pipes to the horizontal is the same, the length of each pipe in each group of outlet electrode insulated pipes is the same, and the cross-sectional flow area of each pipe in each group of outlet electrode insulated pipes is the same to ensure that the flow rate of each pipe in each group of outlet electrode insulated pipes is the same.

10. The apparatus for heating molten salt of any one of claims 1 to 9 wherein the molten salt electrode tanks are made of a corrosion-resistant, high temperature resistant metal material into a vessel having a specific internal surface area and have an electrode inlet insulated pipe connection port fluidly connected to the electrode inlet insulated pipe connection port of the respective molten salt electrode tank and an electrode outlet insulated pipe connection port fluidly connected to the electrode outlet insulated pipe connection port of the respective molten salt electrode tank; and the outer wall of the fused salt electrode box is connected with a conductive copper bar.