CN202267054U - Superheated steam generating device of photo-thermal generating molten salt energy storage system - Google Patents
Superheated steam generating device of photo-thermal generating molten salt energy storage system Download PDFInfo
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- CN202267054U CN202267054U CN2011203912824U CN201120391282U CN202267054U CN 202267054 U CN202267054 U CN 202267054U CN 2011203912824 U CN2011203912824 U CN 2011203912824U CN 201120391282 U CN201120391282 U CN 201120391282U CN 202267054 U CN202267054 U CN 202267054U
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Abstract
The utility model relates to a superheated steam generating device of a photo-thermal generating molten salt energy storage system, which is composed of a steam generating stage tank body, a superheated steam generating stage tank body and a steam drying stage tank body. When the superheated steam generating device operates, high temperature heating mediums preheat the three stages of tank bodies and a spiral coil pipe to required temperatures through communicating pipelines; and then molten slat heat carriers are injected through the spiral coil pipe; next, high temperature water is injected through a sprayer and converted into steam in the steam generating stage tank body; and needed high temperature and high pressure superheated steam is obtained by a saturated steam generating stage tank body and the drying stage tank body. The superheated steam generating device of the photo-thermal generating molten salt energy storage system disclosed by the utility model can generate high temperature superheated steam; furthermore, molten salts are applied to heat exchange, therefore, the superheated steam generating device has excellent corrosion resistance and abrasion resistance; meanwhile, the sprayer and a filter screen device are employed to instantaneously gasify water which enters a generator, thereby greatly increasing generation efficiency of steam; and the tank bodies can preheat, so that the problem that equipment stops for being blocked as the molten salts are high in solidification point and are solidified when entering a heat exchange pipe is avoided.
Description
Technical field
The utility model relates to the photo-thermal power generation field, especially a kind of photo-thermal power generation fused salt energy-storage system superheated steam producer.
Background technology
The high temperature heat utilization technology is a Chinese national economy STRATEGIES OF SUSTAINABLE DEVELOPMENT property new energy technology as clean energy technology low-cost and that have the scale prospect in light, the heat energy.Moderate-high temperature heat utilization systems mainly is made up of condenser system, endothermic system, hold over system and heat utilization device in light, the heat energy.Because light, heat energy have intermittence and unstability, are difficult to satisfy the requirement of large-scale industrialization continous-stable energy supply, therefore must develop the high-efficiency thermal storage technology, could effectively solve solar energy conversion, transmission and storage problem.
Fused salt is heat transfer and the heat storage medium that extensively adopts at present middle high temperature light, the heat energy heat utilization system owing to having the significant advantage that thermal capacitance is big, stability is high, operating temperature range is wide.Because transporting with easy to use of steam, steam is widely used in industries such as generating, chemical industry, food at present, and therefore how being converted into steam to the fused salt accumulation of heat also just becomes one of key technology that elevated temperature heat is utilized in the solar energy.
Light, heat energy producing steam are the important form that the solar energy scale utilizes, and multiple steam generator based on the glass-vacuum tube thermal-arrest is arranged at present, and based on the steam generator of fused salt heat transfer heat accumulation function the bushing type steam generating device is arranged.The molten salt sleeve pipe type steam generating device uses the high temperature resistant selective coating of chuck outer wall to absorb solar radiant energy, and will absorb the fused salt in the heat transferred fused salt sleeve pipe, and the water of further passing to coiled inner tube forms steam.In the solar energy of scales such as solar energy thermal-power-generating in the moderate-high temperature heat utilization systems; There are some defectives in the molten salt sleeve pipe type steam generating device: (1) because the heat energy that tube wall absorbs was escaped in the sleeve pipe fused salt directly pass to water conservancy project matter in the pipe; Fused salt mainly plays heat transfer effect; And because the amount of stored heat of fused salt is less in the sleeve pipe, the heat accumulation function of fused salt working medium and fused salt groove is not fully used; (2) because the real-time change of the outer solar radiation of sleeve pipe can change with evaporation process being coupled in the fused salt in the sleeve pipe, the parameter of whole diabatic process of cannula system and water vapour is wayward; (3) because snakelike endothermic tube body construction is comparatively complicated, and the difficulty of processing of its sleeve pipe is big, therefore be difficult to the scale utilization; (4) system is single-stage mostly, can't produce superheated steam.
The utility model content
The technical problem that the utility model will solve is: provide a kind of and can produce hyperthermia and superheating steam, safe and reliable photo-thermal power generation fused salt energy-storage system superheated steam producer.
The utility model solves the technical scheme that its technical problem adopted: a kind of photo-thermal power generation fused salt energy-storage system superheated steam producer; Comprise outer dry stage tank body, saturated vapor level tank body and 3 built-in tank bodies of steam generation level tank body of reinforcing tank body and being arranged in the outer reinforcing tank body, being interconnected, described 3 built-in tank bodies and outer the reinforcing between the tank body are filled with heat-insulation layer; Be provided with spiral coil in described 3 built-in tank bodies, and 3 interior spiral coils of built-in tank body are connected through connecting line; The steam that described steam generation level tank body produces converts the high pressure superheater dry steam successively into and passes through the outer tank body outside that reinforces of steam (vapor) outlet discharge that dry stage tank body top is provided with behind supersaturated vapor level tank body and steam generation level tank body.
Specifically, for can high-temperature steam, the inner chamber upper end of the described steam generation level of the utility model tank body be provided with spray thrower, and an end of described spray thrower is arranged on outer high-temperature water import of reinforcing the tank body outer surface through pipeline connection; The top of spray thrower, below spiral coil are provided with high temperature atomizing filter screen;
For the flow of better controlled high-temperature water in the process of spray, the internal chamber wall of the described steam generation level of the utility model tank body is provided with the water level controller; Described water level controller is arranged on 1/3rd height place apart from steam generation level tank base.
The lower end of the described steam generation level of the utility model tank body is provided with the outlet of high-temperature molten salt thermophore, and described high-temperature molten salt thermophore outlet is communicated with the spiral coil of steam generation level tank inner chamber; The lower end of described steam generation level tank body also is provided with the heat media outlet.Interface channel between described steam generation level tank body and the saturated vapor level tank body is provided with the pressure instrumentation and the HTHP control valve of cooperating.
Say further that again the upper end of the described dry stage tank body of the utility model is provided with the high temperature preheating medium import that communicates with tank inner chamber; Spiral coil in the dry stage tank body is communicated with the outer high-temperature molten salt thermophore import that the tank body upper end is provided with of reinforcing, and adds nitrogen inlet in the described import.
Saying further, in order to save the space, the utility model described outer reinforce tank body with and 3 inner built-in tank bodies be vertical structure.
Simultaneously, the operation method of the described photo-thermal power generation fused salt of the utility model energy-storage system superheated steam producer is following:
1) in 3 built-in tank bodies, feeds the high temperature preheating medium from the high temperature preheating medium import of dry stage tank body and carry out preheating;
2) the high-temperature molten salt thermophore import from the dry stage tank body feeds the high-temperature molten salt thermophore, and thermophore promotes the tank body temperature of dry stage tank body, saturated vapor level tank body and steam generation level tank body successively through spiral coil;
3) inject high-temperature water to spray thrower through high-temperature water through import, spray thrower sprays high-temperature water to the filter screen that atomizes, and makes high-temperature-hot-water form tiny fog, and the spiral coil of heat fully contacts and converts high-temperature steam into;
4) when above-mentioned high-temperature steam pressure reached the rated value of setting, the HTHP control valve was opened, and high temperature and high pressure steam gets into saturated vapor level tank body, makes it be converted into saturated vapor through further heating;
5) saturated vapor gets into the dry stage tank body through interface channel, further converts the high pressure superheater dry steam into, flows out through steam (vapor) outlet.
Specifically; In the described step 3); When high-temperature water gets into the high-temperature water spray thrower through import, the lower end of the flow of import through being arranged on steam generation level tank body, regulate apart from the gauge tap on the water level controller at 1/3rd height place of steam generation level tank base.
When device when out of service, open the by-pass valve control in the outlet of heat WATER AS FLOW MEDIUM, by self steam pressure in the steam generator, condensate is all discharged through the heat media outlet; And from the nitrogen inlet nitrogen injection, the high-temperature molten salt thermophore is discharged in the boosting spiral coil.
The beneficial effect of the utility model is: 1, can produce hyperthermia and superheating steam; 2, use fused salt heat exchanging, and have good corrosion resistance and abrasion resistance; 3, adopt spray thrower and filter screen device, can let the instant water that gets into generator gasify, improved the efficient that steam produces greatly; 4, tank body can preheating, like this with regard to not producing because the freezing point height of fused salt get into heat exchanger tube will frozen plug and the problem that causes equipment to stop.
Description of drawings
Below in conjunction with accompanying drawing and embodiment the utility model is further specified.
Fig. 1 is the structural representation of the preferred embodiment of the utility model;
Among the figure: 1, high temperature preheating medium import; 2, high temperature preheating medium connecting pipeline; 3, heat media outlet; 4, dry stage tank body; 5, saturated vapor level tank body; 6, steam generation level tank body; 7, high-temperature molten salt thermophore import; 8, spiral coil; 9, connecting line; 10, the outer tank body of reinforcing; 11, heat-insulation layer; 13, high-temperature molten salt thermophore outlet; 14, side pressure instrument; 15, HTHP control valve; 16, interface channel; 17, high-temperature water import; 18, spray thrower; 19, high temperature atomizing filter screen; 20, steam (vapor) outlet; 21, water level controller; 22, nitrogen inlet.
The specific embodiment
Combine accompanying drawing and preferred embodiment that the utility model is done further detailed explanation now.These accompanying drawings are the sketch map of simplification, the basic structure of the utility model only is described in a schematic way, so it only show the formation relevant with the utility model.
A kind of photo-thermal power generation fused salt energy-storage system superheated steam producer; Form by steam generation level, superheated steam generation level and steam drying level; The heat medium until temperature required, injects fused salt thermophore (or other phase-change materials) through spiral coil through three grades of tank bodies of connecting pipeline preheating and coil pipe again during operation, then through spray thrower injection high-temperature water; Be converted into steam in the steam generation level, level and the required high-temperature high-pressure overheat steam of dry stage realization take place through saturated vapor.
As shown in Figure 1, design steam generation level tank body 6, saturated vapor level tank body 5 and oval (or the non-ellipse) tank bodies of 4 three high pressure-bearings of dry stage tank body in skin is reinforced tank body 10, three grades of tank bodies are through the flange connection and communicate external high-temperature-resistant thermal-insulation layer 11; Dry steam level tank body 4 tops are provided with steam (vapor) outlet 20, high temperature preheating medium import 1 and high-temperature molten salt thermophore import 7, and high-temperature molten salt thermophore import 7 places are provided with nitrogen inlet 22; Three grades of tank bodies connect high temperature preheating medium connecting pipeline 2, the built-in spiral coil 8 of oval (or the non-ellipse) tank body of each high pressure-bearing, and through connecting line 9 connections.Steam generation level tank body 6 tops are provided with high-temperature water import 17; Built-in spray thrower 18 and high temperature atomizing filter screen 19; Tank body 1/3rd highly locates to be provided with water level controller 21, and top and saturated vapor level tank body 5 junctions are provided with HTHP control valve 15 and pressure instrumentation 14; Steam generation level tank body 6 lower ends are provided with heat media outlet 3 and high-temperature molten salt thermophore outlet 13.
The high temperature preheating medium gets into steam drying level tank body 4 through import 1; And, tank body and internal helicoid coil pipe are preheated to temperature required back through exporting 3 discharges through interface channel 16 and connecting pipeline 2 entering saturated vapors generation level tank body 5 and steam generation level tank bodies 6.
Tank bodies at different levels are heated in fluid interchange in spiral coil by high-temperature molten salt thermophore (or other phase-change materials); Its step is following: (1) high-temperature molten salt thermophore (or other phase-change materials) promotes this grade tank body temperature through the spiral coil of import 7 entering steam drying level tank bodies 4 through fluid interchange; (2) spiral coil through connecting line entering saturated vapor level tank body 5 promotes this grade tank body temperature through fluid interchange; (3) spiral coil through connecting line entering steam generation level tank body 6 promotes this grade tank body temperature through fluid interchange; (4) high-temperature molten salt thermophore (or other phase-change materials) flows out through outlet 13;
The high-temperature water of preheating gets into high-temperature water spray thrower 18 through import 17, and high-temperature water sprays to atomizing filter screen 19 through high-temperature water spray thrower 18, makes high-temperature-hot-water form tiny fog and gets into steam generation level tank body 6; Fully contact with the heat spiral coil and to convert high-temperature steam into; When steam pressure reaches the rated value of setting, HTHP control valve 15 is opened, and high temperature and high pressure steam gets into saturated vapor level tank body 5; Make it be converted into saturated vapor through further heating; And, further convert the high pressure superheater dry steam into through communication passage 16 entering dry stage tank bodies 4, flow out through exporting 20; When the high-temperature water of preheating got into high-temperature water spray thrower 18 through import 17, the flow of import 17 was regulated through the gauge tap on the water level controller 21.
When system is out of service, open the by-pass valve control of outlet on 3, by self steam pressure in the steam generator, condensate all discharged through exporting 3; And from import 22 nitrogen injections, high-temperature molten salt thermophore (or other phase-change materials) is discharged coil pipe in the boosting coil pipe, in order to avoid residual solidifying caused pipeline blockage in coil pipe.
The utility model can produce hyperthermia and superheating steam, because general steam about 190 degree, uses but can't satisfy generating, so must realize heated drying, makes it reach the needs that could satisfy steam turbine more than 340 degree.The multistage steam generator of the utility model design can address this problem, and with being widely used in the power station afterwards.
Can use fused salt heat exchanging at present; Domestic manufacturer did not also produce, and the evaporimeter heat exchange coil that domestic manufacturer produces generally adopts the 12CrMo steel, and refractory salt corrosion and erosion are poor; The utility model adopts the 316L stainless-steel seamless pipe, has improved its corrosion resistant and anti-washing away.
The just specific embodiment of describing in the above specification of the utility model; The various fleshes and bloods that illustrate not the utility model constitute restriction; Under the those of ordinary skill of technical field after having read specification can to before the described specific embodiment make an amendment or be out of shape, and do not deviate from the essence and the scope of utility model.
Claims (6)
1. photo-thermal power generation fused salt energy-storage system superheated steam producer; It is characterized in that: comprise outer dry stage tank body, saturated vapor level tank body and 3 built-in tank bodies of steam generation level tank body of reinforcing tank body and being arranged in the outer reinforcing tank body, being interconnected, described 3 built-in tank bodies and outer the reinforcing between the tank body are filled with heat-insulation layer; Be provided with spiral coil in described 3 built-in tank bodies, and 3 interior spiral coils of built-in tank body are connected through connecting line; The steam that described steam generation level tank body produces converts the high pressure superheater dry steam successively into and passes through the outer tank body outside that reinforces of steam (vapor) outlet discharge that dry stage tank body top is provided with behind supersaturated vapor level tank body and steam generation level tank body.
2. photo-thermal power generation fused salt energy-storage system superheated steam producer as claimed in claim 1; It is characterized in that: the inner chamber upper end of described steam generation level tank body is provided with spray thrower, and an end of described spray thrower is arranged on outer high-temperature water import of reinforcing the tank body outer surface through pipeline connection; The below of spray thrower, spiral coil top are provided with high temperature atomizing filter screen; The internal chamber wall of described steam generation level tank body is provided with the water level controller; The lower end of described steam generation level tank body is provided with the outlet of high-temperature molten salt thermophore, and described high-temperature molten salt thermophore outlet is communicated with the spiral coil of steam generation level tank inner chamber; The lower end of described steam generation level tank body also is provided with the heat media outlet.
3. photo-thermal power generation fused salt energy-storage system superheated steam producer as claimed in claim 2 is characterized in that: described water level controller is arranged on 1/3rd height place apart from steam generation level tank base.
4. photo-thermal power generation fused salt energy-storage system superheated steam producer as claimed in claim 1 is characterized in that: the interface channel between described steam generation level tank body and the saturated vapor level tank body is provided with the pressure instrumentation and the HTHP control valve of cooperating.
5. photo-thermal power generation fused salt energy-storage system superheated steam producer as claimed in claim 1 is characterized in that: the upper end of described dry stage tank body is provided with the high temperature preheating medium import that communicates with tank inner chamber; Spiral coil in the dry stage tank body is communicated with the outer high-temperature molten salt thermophore import that the tank body upper end is provided with of reinforcing, and adds nitrogen inlet in the described import.
6. photo-thermal power generation fused salt energy-storage system superheated steam producer as claimed in claim 1 is characterized in that: described outer reinforce tank body with and 3 inner built-in tank bodies be vertical structure.
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| Application Number | Priority Date | Filing Date | Title |
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| CN2011203912824U CN202267054U (en) | 2011-10-14 | 2011-10-14 | Superheated steam generating device of photo-thermal generating molten salt energy storage system |
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| CN2011203912824U CN202267054U (en) | 2011-10-14 | 2011-10-14 | Superheated steam generating device of photo-thermal generating molten salt energy storage system |
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| CN202267054U true CN202267054U (en) | 2012-06-06 |
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| CN2011203912824U Withdrawn - After Issue CN202267054U (en) | 2011-10-14 | 2011-10-14 | Superheated steam generating device of photo-thermal generating molten salt energy storage system |
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-
2011
- 2011-10-14 CN CN2011203912824U patent/CN202267054U/en not_active Withdrawn - After Issue
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| CN105927954A (en) * | 2016-06-16 | 2016-09-07 | 赖正平 | Solid fuel and fused salt integrated steam boiler |
| CN105927954B (en) * | 2016-06-16 | 2017-11-03 | 赖正平 | The integrated steam boiler of solid fuel, fused salt |
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