CN215295378U - Solar photo-thermal power station salt melting system based on natural gas heat-conducting oil furnace - Google Patents

Abstract

A solar photo-thermal power station salt melting system based on a natural gas heat-conducting oil furnace belongs to the technical field of photo-thermal salt melting production. The utility model discloses a shorten salt dissolving cycle, reduce salt dissolving cost. The utility model discloses a change salt stove, heat exchanger and fused salt storage tank, change the low temperature fused salt entry that the salt stove passes through fused salt pipeline intercommunication heat exchanger, change the salt stove and pass through delivery pump and fused salt storage tank intercommunication, the high temperature fused salt export and the salt stove intercommunication of heat exchanger, the heat exchanger establishes the relation of connection with natural gas heat conduction oil furnace, and natural gas heat conduction oil furnace is used for providing the heat transfer heat source for the heat exchanger, and the heat exchanger can be the oil salt heat exchanger, also can be replaced by electric heater, also can be the solar collecting system of light and heat direct heating fused salt. The utility model discloses a light and heat mode realizes changing salt, and its salt speed is showing and is improving to this system simple structure, the system operation is simple and convenient, and the security is high, energy-concerving and environment-protective, clean high-efficient.

Description

Solar photo-thermal power station salt melting system based on natural gas heat-conducting oil furnace

Technical Field

The utility model relates to a solar energy light and heat power station salt melting system based on natural gas heat conduction oil furnace belongs to salt melting system technical field.

Background

Before being put into a solar photo-thermal power station, the molten salt is mainly supplied in a solid form (because the molten salt is solid at normal temperature), and the molten salt is conveniently transported and stored by adopting the solid form. When the fused salt needs to be put into a solar photo-thermal power station for heat storage, a large amount of solid fused salt needs to be converted into high-temperature liquid fused salt, the fused salt is subjected to initial melting, the initial melting of the fused salt is a key procedure before a fused salt heat storage system of the photo-thermal power station enters debugging operation, the fused salt is changed into liquid high-temperature fused salt from a solid state through the flow, the fused salt enters the system to start circulation, and the fused salt is kept in a liquid state in the service life of the whole power station.

In the existing photothermal solar thermal power station, two schemes for realizing salt melting are available, one scheme is that after an electric heater is adopted for salt initialization, a molten salt circulating pump is used for pumping low-temperature liquid molten salt into a natural gasified salt furnace, and high-temperature flue gas generated by burning natural gas is used for heating the molten salt in a coil pipe in the molten salt furnace to a high-temperature state and then conveying the molten salt back to a molten salt tank. Adding sodium nitrate and potassium nitrate (solid molten salt) into the molten salt tank in proportion, and when the temperature of the molten salt in the molten salt tank meets the requirement, conveying the molten salt to a molten salt tank through another molten salt conveying pump; and secondly, sodium nitrate and potassium nitrate are crushed and mixed in proportion and then directly enter a natural gasified salt furnace, a heat exchange coil is arranged in a hearth, high-temperature flue gas is contained in the heat exchange coil, the flowing direction of the high-temperature flue gas is opposite to the stirring direction of liquid in the furnace, and melted liquid molten salt overflows into a buffer tank through an overflow pipe and then is pumped into a molten salt tank from the buffer tank. The two traditional salt melting modes both use flue gas obtained after natural gas combustion as a heat source for heating solid molten salt particles, and a large amount of natural gas is consumed in the salt melting process. The salt melting speed is about 30-40t/h due to the technical limit of the natural gas furnace and the safety consideration. After salt dissolving is finished, the matched salt dissolving equipment has no utilization value in the project, and can only be used for the next project to carry out secondary salt dissolving or waste after shelving.

In addition to the above statements, the conventional salt formation process has the following disadvantages:

1. the built salt melting furnace system for melting salt by using a natural gas heating mode has higher cost, and after primary salt melting is realized, the molten salt is put into a solar photo-thermal system for use, and secondary salt melting is not needed, so that matched natural gas salt melting furnace system equipment cannot be reasonably used;

2. when the natural gasified salt furnace system is used for realizing salt melting, natural gas needs to be combusted, and the cost of the consumed natural gas is high in a tens of thousands of tons of large-scale photo-thermal power station molten salt projects;

3. the natural gasified salt furnace system is used for burning natural gas, so that the discharged carbon dioxide is large, and the environment is polluted to a certain extent;

4. the temperature raising capability of a natural gasification salt furnace system is limited, and the salt melting speed is low and the salt melting period is long in a tens of thousands-ton large-scale photo-thermal power station molten salt project.

Based on the above situation, the research work of the salt dissolving technical scheme is developed, and the method has very important significance for shortening the salt dissolving period, reducing the salt dissolving cost, improving the salt dissolving speed and quality and ensuring that both the photo-thermal power generation and the salt dissolving are not wrong.

SUMMERY OF THE UTILITY MODEL

The utility model discloses a shorten salt dissolving cycle, reduce salt dissolving cost. A brief summary of the present invention is provided below in order to provide a basic understanding of some aspects of the present invention. It should be understood that this summary is not an exhaustive overview of the invention. It is not intended to identify key or critical elements of the invention or to delineate the scope of the invention.

The technical scheme of the utility model:

the utility model provides a solar energy light and heat power station salt melting system based on natural gas heat conduction oil furnace, is including melting salt furnace, heat exchanger, fused salt storage tank and natural gas heat conduction oil furnace, the heat exchanger has fused salt entry, fused salt export, heat source export and heat source entry, the fused salt furnace passes through the fused salt entry of fused salt pipeline intercommunication heat exchanger, and the molten salt furnace passes through delivery pump and fused salt storage tank intercommunication, and the fused salt export of heat exchanger communicates with the melting salt furnace through first pipeline, the heat source export of heat exchanger, heat source entry and natural gas heat conduction oil furnace establish the relation of connection, and natural gas heat conduction oil furnace is used for providing the heat transfer heat source for the heat exchanger.

Preferably: the auxiliary electric heater is characterized by further comprising an auxiliary electric heater, an inlet of the auxiliary electric heater is communicated with the molten salt pipeline, and an outlet of the auxiliary electric heater is communicated with the salt melting furnace through a second pipeline.

Preferably: and the first pipeline and the second pipeline are respectively provided with a valve and a temperature measuring instrument.

Preferably: the electric energy used in the auxiliary electric heater is derived from abandoned wind power, abandoned light power or off-peak power.

Preferably: the number of the heat exchangers is multiple, and the heat exchangers are installed in a parallel mode.

Preferably: the number of the heat exchangers is multiple, and the heat exchangers are installed in series.

Preferably: two adjacent heat exchangers are communicated through a secondary molten salt pipeline.

Preferably: and the secondary molten salt pipeline is provided with a valve and a temperature measuring instrument.

Preferably: the heat exchanger is a shell-and-tube heat exchanger, a shell-and-tube heat exchanger or a plate heat exchanger.

The utility model discloses following beneficial effect has:

1. the utility model discloses a salt melting system has solved conventional light and heat power station solid-state fused salt and has all gone on melting salt through dedicated natural gasification salt stove system, and conventional dedicated natural gasification salt stove realizes the salt melting process, receives factors such as stove heating power, natural gas quantity to restrict, and salt melting efficiency is not high, and whole salt melting cycle can not obtain the guarantee, and salt melting fuel is with high costs.

2. The utility model utilizes the photo-thermal power generation system to carry out salt melting work, thus the power generation and the salt melting are both not wrong, and the salt melting capacity is much larger than that of a special natural gas salt melting furnace system;

3. the utility model discloses when having the sun daytime, with light and heat salt, when not having the sun night, utilize the electrical heating absorption to abandon electricity or low ebb electricity and carry out salt, effectively shortened the cycle of salt.

4. The utility model discloses compare with conventional salt melting mode, realize salt melting through the light and heat mode, its salt melting speed is showing and is improving to this system is simple, and the system operation is simple and convenient, and the security is high, and is energy-concerving and environment-protective.

5. Adopt the utility model discloses a salt melting scheme carries sodium nitrate and the broken back of potassium nitrate in proportion to the salt melting furnace, adopts electric heater to carry out the initialization salt after, utilizes the low temperature liquid fused salt pump in the salt melting furnace to go into the oil salt heat exchanger, carries back to the salt melting furnace after heating the high temperature state through the molten salt of natural gas heat conduction oil furnace in with the oil salt heat exchanger, forms the liquid fused salt of low temperature more than 270 ℃ after high temperature liquid salt mixes with the solid fused salt to carry and store to the fused salt storage tank in.

The utility model discloses owing to utilize the original indirect heating equipment of light and heat power station, saved the construction cost. After salt melting is finished, the matched feeding system can be detached and recycled, and the salt melting furnace and the electric heater can be directly converted into a high-temperature energy storage system for absorbing waste wind and light and realizing energy storage.

6. Adopt the utility model discloses a salt melting system, its salt melting speed exceeds 210 tons/hour, five times faster than traditional salt melting speed, can exceed 4000 tons every day, be more than four times of single day salt world record before, if melt 7 ten thousand tons of salt in succession and only need two weeks half, two months faster than traditional salt melting mode, save fossil fuel ten thousand yuan of salt, equipment investment also saves 20% than traditional salt melting system, calculate according to 100MW10 hour energy storage light and heat power station, realize in advance two months that energy storage power generation can create 6000 ten thousand power generation income.

Drawings

FIG. 1 is a schematic diagram of a salt melting system for a natural gas-based heat transfer oil furnace;

FIG. 2 is a schematic diagram of a salt neutralization system according to a second embodiment;

FIG. 3 is a schematic diagram of a salt dissolving system of a heat exchanger according to a second embodiment;

FIG. 4 is a schematic diagram showing the relationship between the salt dissolving amount and the salt dissolving period in the conventional salt dissolving mode and the salt dissolving mode of the present invention;

in the figure, 1-salt melting furnace, 2-heat exchanger, 3-molten salt storage tank, 4-molten salt pipeline, 5-delivery pump, 6-natural gas heat-conducting oil furnace, 7-secondary molten salt pipeline, 8-valve, 9-temperature measuring instrument, 10-auxiliary electric heater, 11-first pipeline, 12-second pipeline, 21-molten salt inlet, 22-molten salt outlet, 23-heat source outlet, 24-heat source inlet and 14-circulating pump.

Detailed Description

In order to make the objects, technical solutions and advantages of the present invention more apparent, the present invention will be described below with reference to specific embodiments shown in the accompanying drawings. It should be understood that the description is intended to be illustrative only and is not intended to limit the scope of the present invention. Moreover, in the following description, descriptions of well-known structures and techniques are omitted so as to not unnecessarily obscure the concepts of the present invention.

The first embodiment is as follows:

referring to fig. 1, the solar photo-thermal power station salt melting system based on the natural gas heat conduction oil furnace includes a salt melting furnace 1, a heat exchanger 2, a molten salt storage tank 3 and a natural gas heat conduction oil furnace 6, wherein the heat exchanger 2 has a molten salt inlet 21, a molten salt outlet 22, a heat source outlet 23 and a heat source inlet 24, the salt melting furnace 1 is communicated with the molten salt inlet 21 of the heat exchanger 2 through a molten salt pipeline 4, the salt melting furnace 1 is communicated with the molten salt storage tank 3 through a delivery pump 5, the molten salt outlet 22 of the heat exchanger 2 is communicated with the salt melting furnace 1 through a first pipeline 11, the heat source outlet 23 and the heat source inlet 24 of the heat exchanger 2 are connected with the natural gas heat conduction oil furnace 6, and the natural gas heat conduction oil furnace 6 is used for providing a heat exchange heat source for the heat exchanger 2.

In the salt melting furnace 1, solid salt and high-temperature molten salt are mixed in the salt melting furnace 1 to form intermediate-temperature liquid molten salt, one part of the intermediate-temperature liquid molten salt is sent into a molten salt storage tank 3 through a delivery pump 5 to be stored, the other part of the intermediate-temperature liquid molten salt is sent into a heat exchanger 2 through a circulating pump, the intermediate-temperature molten salt is heated to the high-temperature molten salt through the heat exchanger 2, then the high-temperature molten salt is sent into the salt melting furnace 1 through the circulating pump to be used for salt melting again, and therefore circulating salt melting work is formed;

in the embodiment, the heat exchanger 2 is a heat conduction oil heat exchanger, when the system performs salt melting operation, solid salt and 300-plus-400-degree high-temperature molten salt are mixed in the salt melting furnace 1 to form 280-plus-340-degree medium-temperature liquid molten salt, one path of the formed medium-temperature liquid molten salt is sent into the molten salt storage tank 3 for storage through the transfer pump 5, the other portion of the formed medium-temperature liquid molten salt is sent into the heat exchanger 2 through the circulating pump from the molten salt inlet 21, meanwhile, the natural gas heat conduction oil furnace 6 is communicated with the heat source outlet 23 and the heat source inlet 24 of the heat exchanger 2, the high-temperature heat conduction oil which absorbs heat in the natural gas heat conduction oil furnace 6 is sent into the heat exchanger 2, the heat is transferred to the medium-temperature molten salt entering the heat exchanger 2 through the high-temperature heat conduction oil inside the heat exchanger 2, so that the temperature of the medium-temperature molten salt (280-plus-340 ℃) reaches the high-temperature molten salt (300-plus-400 ℃), and then, conveying the high-temperature molten salt into the salt melting furnace 1 through the first pipeline 11 for completing salt melting again, wherein the conveying amount ensures that the solid molten salt newly added into the salt melting furnace 1 can reach a certain temperature, melting the solid molten salt, and repeating the steps to realize circulating salt melting.

The salt melting system in the embodiment solves the problem that the conventional photo-thermal power station solid-state molten salt is melted through the natural gasified salt furnace system, the conventional natural gasified salt furnace realizes the salt melting process and is limited by factors such as furnace heating capacity and natural gas consumption, the whole salt melting period is long, and the construction and operation costs of the salt melting cost are high.

By adopting the salt melting system, the salt melting work is carried out by utilizing the power generation and heat storage system of the optical-thermal power station, so that the power generation and the salt melting are both correct, and the salt melting capacity is far greater than that of the traditional natural gasification salt furnace system;

inside the heat exchanger 2, high-temperature heat conduction oil is used for exchanging heat to the medium-temperature molten salt entering the heat exchanger 2, so that the temperature of the medium-temperature molten salt reaches the high-temperature molten salt, wherein the heat conduction oil is derived from a natural gas heat conduction oil furnace 6. Wherein the heat conducting oil in the heat exchanger 2 is from a natural gas heat conducting oil furnace.

In the present embodiment, the salt melting furnace 1 is used for converting the pulverized solid molten salt into a liquid state melt, and the salt melting furnace 1 is a container for realizing salt melting; the heat exchanger 2 is a shell-and-tube heat exchanger, a shell-and-tube heat exchanger or a plate heat exchanger.

The second embodiment is as follows:

referring to fig. 1 and 2, on the basis of the first embodiment, the salt melting furnace further comprises an auxiliary electric heater 10, an inlet of the auxiliary electric heater 10 is communicated with the molten salt pipeline 4, and an outlet of the auxiliary electric heater 10 is communicated with the salt melting furnace 1 through a second pipeline 12;

specifically, the method comprises the following steps: a part of the medium-temperature molten salt in the salt melting furnace 1 flows into the heat exchanger 2 and/or the auxiliary electric heater 10, the medium-temperature molten salt is heated to high-temperature molten salt by the heat exchanger 2 and/or the auxiliary electric heater 10, and then the high-temperature molten salt is conveyed into the salt melting furnace 1 through the circulating pump 14, so that the circulating salt melting work is realized;

when the system works for melting salt, solid salt and 300-400 ℃ high-temperature molten salt are mixed in a melting salt furnace 1 to form 280-340 ℃ medium-temperature liquid molten salt, one path of the formed medium-temperature liquid molten salt is sent to a molten salt storage tank 3 through a delivery pump 5 for storage, the other portion of the formed medium-temperature liquid molten salt is pumped into a heat exchanger 2 or an auxiliary electric heater 10 through a circulating pump 14, the medium-temperature liquid molten salt (280-340 ℃) is heated and converted into the high-temperature liquid molten salt (300-400 ℃) through the heat exchanger 2 or the auxiliary electric heater 10, then the high-temperature molten salt is delivered into the melting salt furnace 1 to realize cyclic salt, and the delivery amount ensures that the solid molten salt newly added into the melting salt furnace 1 can reach a certain temperature and melt the solid molten salt.

The number of the auxiliary electric heaters 10 is multiple, and the multiple auxiliary electric heaters 10 are arranged in the whole salt dissolving system in a parallel or series mode;

in this embodiment, the salt melting system of this embodiment is adopted, the salt melting speed exceeds 210 tons/hour, which is five times faster than the conventional salt melting speed, and can exceed 4000 tons per day, which is four times or more of the previous single-day salt melting world record, if 7 ten thousand tons of salt are melted continuously, only two weeks and half are needed, which is two months faster than the conventional salt melting method, the heat storage island can generate electricity in advance to save ten thousand yuan fossil fuel of salt, the equipment investment is also saved by 20% compared with the conventional salt melting system, and the specific comparison is shown as follows:

TABLE 1 comparison of photothermolysis of salt System with classical salt System

It should be noted that, in a solar power generation project, a natural gasified salt furnace is adopted in a conventional salt system in the world at present, and flue gas generated after combustion of natural gas is used for providing heat to melt solid molten salt into liquid.

When salt melting is needed in a certain solar power generation project, a conventional mode is to purchase a molten salt furnace, and then provide heat by using flue gas generated after natural gas combustion to melt solid molten salt into liquid;

different from the conventional salt dissolving mode, in this embodiment, the salt dissolving operation is performed by using the original equipment of the solar power plant, for example, the heat exchanger 2 and the natural gas heat-conducting oil furnace 6 used in this embodiment are the existing equipment of the power plant, and the original function of this equipment is used for solar power generation, in this embodiment, the salt dissolving system is formed according to the matching and connecting mode of the technical features in this embodiment, and is used for salt dissolving, so that the cost of purchasing and building a natural gasified salt furnace is saved, the carbon dioxide emission in the salt dissolving process is reduced, and the salt dissolving speed and the salt dissolving period are increased by using the existing equipment to realize salt dissolving (as shown in fig. 4);

it should be noted that: the heat storage medium used in the photo-thermal power station project is high-temperature molten salt, taking a 100 MW-level groove type heat conduction oil photo-thermal power generation project in Wulat as an example, the power station is provided with a high-temperature molten salt heat storage system, and the high-temperature molten salt used by the system is a mixture of potassium nitrate with the mass fraction of 40% and sodium nitrate with the mass fraction of 60%. Before the molten salt energy storage system is put into operation, solid molten salt is melted and injected into the cold salt tank, and the step (salt melting) plays a crucial role in smooth debugging and formal operation of the heat storage system. At present, the international conventional salt melting system adopts a natural gasified salt furnace, and uses the smoke generated after the combustion of natural gas to provide heat so as to melt solid molten salt into liquid. The conventional salt dissolving system not only has low salt dissolving rate and cannot normally put the heat storage system into operation in a short time, but also needs to consume a large amount of fossil fuel, which is contrary to the promise of 'double carbon'. But is limited by the characteristics of high melting temperature of molten salt, more technical difficulties of salt melting systems and the like, and the practical exploration of high-speed and low-carbon novel salt melting technology at home and abroad is almost zero.

The salt melting system of the embodiment can ensure that both photo-thermal power generation and salt melting are not wrong, and has very important significance for realizing salt melting in photo-thermal power generation projects.

The third concrete implementation mode:

referring to fig. 1 and 2, on the basis of the first embodiment and the second embodiment, a valve 8 and a temperature measuring instrument 9 are respectively installed on the first pipeline 11 and the second pipeline 12, the valve 8 is used for controlling the opening and closing of the pipelines, and the temperature measuring instrument 8 is used for measuring the temperature of fluid in the pipelines. The opening and closing of the molten salt in the first pipeline 11 and the second pipeline 12 are monitored in real time by utilizing the information interaction of the valve 8 and the temperature measuring instrument 9, so that the smooth proceeding of the molten salt work is ensured.

The fourth concrete implementation mode:

on the basis of the second embodiment, the electric energy used by the auxiliary electric heater 10 is derived from low-cost electricity such as abandoned wind electricity, abandoned light electricity, and off-peak electricity, and the cost of the electric energy is lower than that of the electric energy provided by a conventional power station.

The fifth concrete implementation mode:

referring to fig. 3, the present embodiment provides a salt melting system for a solar thermal power station based on a natural gas heat-conducting oil furnace, which is different from the first embodiment in that the number of heat exchangers 2 is multiple, and the multiple heat exchangers 2 are installed in parallel. The heat exchangers 2 arranged in parallel can heat the medium-temperature liquid molten salt with the temperature of 280 plus 340 ℃ simultaneously so as to achieve the high-temperature molten salt with the temperature of 300 plus 400 ℃, in addition, the work/close of any one heat exchanger 2 can be independently controlled, and the work of other heat exchangers 2 is not influenced, in the whole system, the mode of connecting the heat exchangers 2 in parallel has the advantages of flexibility, convenient use and no influence on the operation of the whole salt melting system when an accident occurs to a single heat exchanger 2.

The sixth specific implementation mode:

referring to fig. 3, the present embodiment provides a salt melting system for a solar thermal power station based on a natural gas heat-conducting oil furnace, and is different from the first embodiment in that the number of the heat exchangers 2 is multiple, and the plurality of heat exchangers 2 are installed in series. The intermediate-temperature liquid molten salt with the temperature of 280 plus 340 ℃ can flow through a passage to exchange heat for many times by adopting the heat exchangers 2 in series so as to achieve the high-temperature molten salt with the temperature of 300 plus 400 ℃, and the whole system only has one passage by adopting the series connection mode, thereby being convenient for controlling the whole system by a switch.

The seventh embodiment:

referring to fig. 3, on the basis of the fifth embodiment, two adjacent heat exchangers 2 are communicated through a secondary molten salt pipeline 7. And a valve 8 for opening/closing the secondary molten salt pipeline 7 and a temperature measuring instrument 8 for measuring the temperature of the liquid molten salt flowing through the secondary molten salt pipeline 7 are installed on the secondary molten salt pipeline 7. According to the arrangement, the 280-DEG C340-DEG C intermediate temperature liquid molten salt flowing out of the molten salt furnace 1 enters the heat exchanger 2, and the 280-DEG C340-DEG C intermediate temperature liquid molten salt is increased to 300-DEG C400-DEG C high temperature molten salt in the heat exchanger 2; if the medium temperature liquid molten salt in the heat exchanger 2 can not effectively exchange heat to the high temperature molten salt temperature value state, the secondary molten salt pipeline 7 is opened, the liquid molten salt is conveyed into the other heat exchanger 2 connected in parallel again, and heat exchange is further carried out on the liquid molten salt until the high temperature molten salt state of 300-400 ℃ is achieved.

The specific implementation method nine:

referring to fig. 1 and 3, based on the fifth embodiment, the heat exchanger 2 is used for heating and converting the intermediate-temperature liquid molten salt (280-.

In the present embodiment, the temperature of the high-temperature molten salt can be varied up and down to 370 degrees, the range of 70 degrees (not more than 600 degrees at the maximum), the temperature of the medium-temperature salt can be varied up and down to 310 degrees, and the range of 30 degrees.

The detailed implementation mode is ten:

with reference to the first embodiment, the heat exchanger 2 is a shell-and-tube heat exchanger, or a plate heat exchanger.

It is noted that the terminology used herein is for the purpose of describing particular embodiments only and is not intended to be limiting of example embodiments according to the present application. As used herein, the singular forms "a", "an" and "the" are intended to include the plural forms as well, and it should be understood that when the terms "comprises" and/or "comprising" are used in this specification, they specify the presence of stated features, steps, operations, devices, components, and/or combinations thereof, unless the context clearly indicates otherwise.

Unless specifically stated otherwise, the relative arrangement of the components and steps, the numerical expressions, and numerical values set forth in these embodiments do not limit the scope of the present invention. Meanwhile, it should be understood that the sizes of the respective portions shown in the drawings are not drawn in an actual proportional relationship for the convenience of description. Techniques, methods, and apparatus known to those of ordinary skill in the relevant art may not be discussed in detail but are intended to be part of the specification where appropriate. In all examples shown and discussed herein, any particular value should be construed as merely illustrative, and not limiting. Thus, other examples of the exemplary embodiments may have different values. It should be noted that: like reference numbers and letters refer to like items in the following figures, and thus, once an item is defined in one figure, further discussion thereof is not required in subsequent figures.

In the description of the present invention, it should be understood that the orientation or positional relationship indicated by the orientation words such as "front, back, up, down, left, right", "horizontal, vertical, horizontal" and "top, bottom" etc. are usually based on the orientation or positional relationship shown in the drawings, and are only for convenience of description and simplification of description, and in the case of not making a contrary explanation, these orientation words do not indicate and imply that the device or element referred to must have a specific orientation or be constructed and operated in a specific orientation, and therefore, should not be interpreted as limiting the scope of the present invention; the terms "inner and outer" refer to the inner and outer relative to the profile of the respective component itself.

Spatially relative terms, such as "above … …," "above … …," "above … …," "above," and the like, may be used herein for ease of description to describe one device or feature's spatial relationship to another device or feature as illustrated in the figures. It will be understood that the spatially relative terms are intended to encompass different orientations of the device in use or operation in addition to the orientation depicted in the figures. For example, if a device in the figures is turned over, devices described as "above" or "on" other devices or configurations would then be oriented "below" or "under" the other devices or configurations. Thus, the exemplary term "above … …" can include both an orientation of "above … …" and "below … …". The device may be otherwise variously oriented (rotated 90 degrees or at other orientations) and the spatially relative descriptors used herein interpreted accordingly.

It should be noted that the terms "first," "second," and the like in the description and claims of this application and in the drawings described above are used for distinguishing between similar elements and not necessarily for describing a particular sequential or chronological order. It is to be understood that the data so used is interchangeable under appropriate circumstances such that the embodiments of the application described herein are capable of operation in sequences other than those illustrated or described herein.

It should be noted that, in the above embodiments, as long as the technical solutions can be aligned and combined without contradiction, those skilled in the art can exhaust all possibilities according to the mathematical knowledge of the alignment and combination, and therefore the present invention does not describe the technical solutions after alignment and combination one by one, but it should be understood that the technical solutions after alignment and combination have been disclosed by the present invention.

This embodiment is only illustrative of the patent and does not limit the scope of protection thereof, and those skilled in the art can make modifications to its part without departing from the spirit of the patent.

Claims (9)

1. The utility model provides a solar energy light and heat power station salt melting system based on natural gas heat conduction oil stove which characterized in that: including melting salt stove (1), heat exchanger (2), fused salt storage tank (3) and natural gas heat conduction oil furnace (6), heat exchanger (2) have fused salt entry (21), fused salt export (22), heat source export (23) and heat source entry (24), melting salt stove (1) is through fused salt entry (21) of fused salt pipeline (4) intercommunication heat exchanger (2), and melting salt stove (1) is through delivery pump (5) and fused salt storage tank (3) intercommunication, and fused salt export (22) of heat exchanger (2) are through first pipeline (11) and melting salt stove (1) intercommunication, heat source export (23), heat source entry (24) and natural gas heat conduction oil furnace (6) of heat exchanger (2) establish the relation of connection, and natural gas heat conduction oil furnace (6) are used for providing the heat transfer heat source for heat exchanger (2).

2. The solar photo-thermal power station salt melting system based on the natural gas heat conduction oil furnace is characterized in that: the salt melting furnace is characterized by further comprising an auxiliary electric heater (10), wherein the inlet of the auxiliary electric heater (10) is communicated with the molten salt pipeline (4), and the outlet of the auxiliary electric heater (10) is communicated with the salt melting furnace (1) through a second pipeline (12).

3. The solar photo-thermal power station salt melting system based on the natural gas heat conduction oil furnace is characterized in that: and the first pipeline (11) and the second pipeline (12) are respectively provided with a valve (8) and a temperature measuring instrument (9).

4. The solar photo-thermal power station salt melting system based on the natural gas heat conduction oil furnace is characterized in that: the electric energy used in the auxiliary electric heater (10) is derived from abandoned wind power, abandoned light power or off-peak power.

5. The solar photo-thermal power station salt melting system based on the natural gas heat conduction oil furnace is characterized in that: the number of the heat exchangers (2) is multiple, and the heat exchangers (2) are installed in a parallel mode.

6. The solar photo-thermal power station salt melting system based on the natural gas heat conduction oil furnace is characterized in that: the number of the heat exchangers (2) is multiple, and the heat exchangers (2) are installed in series.

7. The solar photo-thermal power station salt melting system based on the natural gas heat conduction oil furnace is characterized in that: two adjacent heat exchangers (2) are communicated through a secondary molten salt pipeline (7).

8. The solar photo-thermal power station salt melting system based on the natural gas heat conduction oil furnace is characterized in that: and a valve (8) and a temperature measuring instrument (9) are arranged on the secondary molten salt pipeline (7).

9. The salt melting system of the solar photo-thermal power station based on the natural gas heat conduction oil furnace according to any one of claims 1-2 and 5-7, wherein: the heat exchanger (2) is a shell-and-tube heat exchanger, a shell-and-tube heat exchanger or a plate heat exchanger.

Images