WO2020168604A1 - Mixed chloride molten salt having high thermal conductivity, preparation method therefor and application thereof - Google Patents

Mixed chloride molten salt having high thermal conductivity, preparation method therefor and application thereof Download PDF

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WO2020168604A1
WO2020168604A1 PCT/CN2019/078264 CN2019078264W WO2020168604A1 WO 2020168604 A1 WO2020168604 A1 WO 2020168604A1 CN 2019078264 W CN2019078264 W CN 2019078264W WO 2020168604 A1 WO2020168604 A1 WO 2020168604A1
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molten salt
chloride
thermal conductivity
mixed
mixture
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PCT/CN2019/078264
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French (fr)
Chinese (zh)
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杨波
翟伟
李茂东
李仕平
王志刚
黄国家
张双红
李悦
文芳
郭华超
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广州特种承压设备检测研究院
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Publication of WO2020168604A1 publication Critical patent/WO2020168604A1/en

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    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09KMATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
    • C09K5/00Heat-transfer, heat-exchange or heat-storage materials, e.g. refrigerants; Materials for the production of heat or cold by chemical reactions other than by combustion
    • C09K5/08Materials not undergoing a change of physical state when used
    • C09K5/10Liquid materials
    • C09K5/12Molten materials, i.e. materials solid at room temperature, e.g. metals or salts

Definitions

  • the invention belongs to the field of energy storage materials, and relates to a molten salt, in particular to a mixed chloride molten salt with high thermal conductivity and a preparation method and application thereof.
  • Renewable energy includes biomass energy, hydropower, wind energy, wave energy, and solar energy.
  • solar energy is the best energy source for safety, cleanliness, and permanence.
  • the annual sunshine hours of more than 2/3 of the country’s total area are more than 2200h, especially in western China, southeastern Xinjiang, western Qinghai, southern Yunnan and other regions with abundant solar resources, close to the world’s most famous African desert, ranking
  • the second place in the world, my country is very rich in solar energy resources. If this part of solar energy is used effectively, it will be of great significance to solve energy and environmental problems.
  • solar photovoltaic power generation has high production costs of polysilicon materials and serious environmental pollution.
  • Solar thermal power generation technology is considered to be one of the most promising technologies for solar power generation.
  • Due to the shortcomings of intermittent, low energy density, and poor stability of solar energy it is difficult to meet the demand for continuous energy consumption, and high temperatures will be generated after the sunlight is focused. Therefore, choosing reliable high-temperature heat transfer and heat storage materials will be one of the key technologies to improve the efficiency of solar thermal power generation and solar thermal chemical reaction energy storage.
  • molten salt As an inorganic compound, molten salt has low viscosity, good thermal conductivity, weak corrosiveness, low vapor pressure, wide operating temperature range, and low price, making it the first choice for medium and high temperature heat transfer and heat storage materials. Studies have shown that, compared with high-temperature heat transfer oil, the use of molten salt (nitrate molten salt) can increase the maximum operating temperature of solar power stations to about 500°C and increase the power generation efficiency of steam turbines to 40%.
  • the most used molten salt for solar thermal power generation is nitrate molten salt as a heat transfer and storage material. It is disclosed that mixed nitrate molten salt (60% KNO 3 -40wt% NaNO 3 , Solar Salt) and ternary mixed nitrate molten salt (53 % KNO 3 -7% NaNO 3 -40 wt% NaNO 2 , Hitec).
  • the maximum operating temperature of the mixed nitrate molten salt system is generally 550°C.
  • CN 104109508 A discloses a nitrate system molten salt heat storage material consisting of potassium nitrate and sodium nitrate, the mass ratio of sodium nitrate and potassium nitrate is 30-70:30-70, and the potassium nitrate and sodium nitrate are the Ca 2+, Mg 2+, Cl - , SO 4 2- ion content of impurities each less than 100ppm, 100ppm, 200ppm and 300ppm.
  • the invention is based on Solar Salt molten salt, and improves the thermal stability of Solar Salt molten salt through purification process and impurity ion control, and extends the service life and operating cost of heat storage materials.
  • the molten salt provided by the invention has a low thermal conductivity and a relatively high melting point.
  • CN 107090273 A discloses a mixed molten salt heat transfer and heat storage working fluid, which is characterized in that it is composed of Ca(NO 3 ) 2 , KNO 3 , NaNO 3 and LiNO 3 , and the mass ratio of each component is: Ca( NO 3 ) 2 : 8.0wt%; KNO 3 : 55-60wt%; NaNO 3 : 7-12wt%; LiNO 3 : 18-25wt%.
  • the molten salt can be used in the fields of medium and high temperature heat transfer and heat storage, such as solar thermal power generation and energy storage, abandonment of wind and photovoltaic, "coal-to-electricity" heat storage and heating, or industrial waste heat recovery and storage.
  • thermophysical properties of the mixed molten salt are very stable, there will be no separation of a certain component during use, it has good heat transfer performance in the liquid temperature zone, and the saturated vapor pressure is lower than 2 atmospheres. Since the main raw material of the mixed molten salt is nitrate, its thermal conductivity is low, and there is a risk of decomposition at high temperatures, and the upper limit of use temperature is low.
  • the present invention provides a high thermal conductivity mixed chloride molten salt.
  • the molten salt reduces the melting point, increases the upper limit temperature of the work, and improves the power generation efficiency of solar thermal power generation.
  • the molten salt has Larger thermal conductivity, better heat transfer and heat storage performance, can avoid local overheating of the device, reduce the amount of heat transfer and heat storage media, reduce the volume of related transportation and storage equipment, and reduce operating costs.
  • One of the objectives of the present invention is to provide a mixed chloride molten salt with high thermal conductivity.
  • the raw materials of the molten salt include chloride, metal hydroxide and metal powder.
  • the chloride includes sodium chloride and/or potassium chloride.
  • the metal hydroxide is aluminum hydroxide.
  • the metal powder is metal aluminum powder.
  • the use of aluminum powder can increase the thermal conductivity of the mixed molten salt, thereby improving the heat transfer efficiency and the power generation efficiency.
  • the raw materials of the molten salt include sodium chloride, potassium chloride, aluminum hydroxide and metal aluminum powder.
  • the present invention overcomes the problems of low working temperature upper limit and low thermal conductivity of the existing nitrate molten salt.
  • components such as aluminum hydroxide and metal aluminum powder with higher thermal conductivity on the basis of simple sodium chloride and potassium chloride, a new mixed chloride molten salt is formed.
  • the melting point of aluminum hydroxide is 300°C
  • the melting point of metal aluminum powder is 660°C, both of which are lower than simple inorganic sodium chloride and potassium chloride mono-salts, they can form mixed chloride molten salts with lower melting points and higher working temperature limits.
  • the thermal conductivity of metal aluminum powder is 270W/(m ⁇ K), and a small amount of addition can increase the thermal conductivity of molten salt.
  • the raw materials of the molten salt in terms of mass fraction include:
  • the mass fraction of sodium chloride can be 40%, 45%, 50%, 55%, 60%, 65% or 70%, etc.
  • the mass fraction of potassium chloride can be 25%, 26%, 28%, 30%. %, 32%, 35%, 38%, 40%, 42% or 45%, etc.
  • the mass fraction of aluminum hydroxide can be 2%, 3%, 4%, 5%, 6%, 7%, 8%, 9% or 10%, etc.
  • the mass fraction of metal aluminum powder can be 2%, 3%, 4%, 5%, 6% or 7%, etc., but it is not limited to the numerical values listed. The values listed also apply.
  • the mass fraction of metal aluminum powder in the molten salt is less than 2%, which cannot improve the thermal conductivity of the mixed molten salt, and has little effect on its thermal conductivity; the mass fraction is greater than 7%, and the molten salt causes mixed melting. Salt cannot form a communicative mixture.
  • the raw materials of the molten salt in terms of mass fraction include:
  • the second object of the present invention is to provide a method for preparing the above-mentioned molten salt, the preparation method being:
  • the metal powder is mixed with the chloride and the metal hydroxide to obtain a mixture; the mixture is heated to a molten state for calcination, and the molten salt is obtained after cooling.
  • the calcination temperature is 780 to 850°C, such as 780°C, 790°C, 800°C, 810°C, 820°C, 830°C, 840°C or 850°C, etc., but is not limited to For the listed values, other unlisted values within the range of values also apply.
  • the calcination temperature is higher than 850°C, which will cause the molten salt to deteriorate and decompose, and the thermal stability is poor; the calcination temperature is lower than 780°C, which will result in low power generation temperature and low power generation efficiency.
  • the calcination time is 12-16h, such as 12h, 12.5h, 13h, 13.5h, 14h, 14.5h, 15h, 15.5h or 16h, etc., but not limited to the listed values , Other unlisted values within this value range also apply.
  • the metal powder In the preparation method of the present invention, if the particles of the metal powder are too large, the metal powder needs to be ball-milled and refined.
  • the molten salt obtained after calcination and cooling has a relatively large particle size and needs to be crushed and ground into smaller particles for storage and transportation.
  • the third object of the present invention is to provide an application of the above-mentioned chlorinated modified molten salt, which is used in the field of solar thermal power generation.
  • the present invention has at least the following beneficial effects:
  • the mixed chloride molten salt of the present invention can lower the melting point and increase the upper limit operating temperature, improve the power generation efficiency of solar thermal power generation, and reduce the melting point to save operation and insulation costs; at the same time, it also expands the use temperature range of the molten salt and can be applied Solar thermal power generation, solar hydrogen production reaction and industrial waste heat recovery and other fields;
  • the mixed chloride molten salt of the present invention has higher thermal conductivity, good heat transfer performance, better heat transfer and heat storage effect, and can also avoid local overheating problems of the device.
  • This embodiment provides a mixed chloride molten salt with high thermal conductivity.
  • the raw materials of the molten salt in terms of mass fraction include:
  • the metal aluminum powder is ball-milled and mixed with sodium chloride, potassium chloride and aluminum hydroxide to obtain a mixture; the mixture is heated to a molten state and calcined at 800°C for 16 hours, and the mixture is obtained after cooling Said molten salt.
  • This embodiment provides a mixed chloride molten salt with high thermal conductivity.
  • the raw materials of the molten salt in terms of mass fraction include:
  • the metal aluminum powder is ball-milled and mixed with sodium chloride, potassium chloride and aluminum hydroxide to obtain a mixture; the mixture is heated to a molten state and calcined at 830°C for 12 hours, and the mixture is obtained after cooling Said molten salt.
  • This embodiment provides a mixed chloride molten salt with high thermal conductivity.
  • the raw materials of the molten salt in terms of mass fraction include:
  • the metal aluminum powder is ball-milled and mixed with sodium chloride, potassium chloride and aluminum hydroxide to obtain a mixture; the mixture is heated to a molten state and calcined at 800°C for 12 hours, and after cooling, the mixture is obtained Said molten salt.
  • This embodiment provides a mixed chloride molten salt with high thermal conductivity.
  • the raw materials of the molten salt in terms of mass fraction include:
  • the metal aluminum powder is ball-milled and mixed with sodium chloride, potassium chloride and aluminum hydroxide to obtain a mixture; the mixture is heated to a molten state and calcined at 820°C for 15 hours, and the mixture is obtained after cooling Said molten salt.
  • This embodiment provides a mixed chloride molten salt with high thermal conductivity.
  • the raw materials of the molten salt in terms of mass fraction include:
  • the metal aluminum powder is ball-milled and mixed with sodium chloride, potassium chloride and aluminum hydroxide to obtain a mixture; the mixture is heated to a molten state and calcined at 810°C for 13 hours, and the mixture is obtained after cooling Said molten salt.
  • This embodiment provides a mixed chloride molten salt with high thermal conductivity.
  • the raw materials of the molten salt in terms of mass fraction include:
  • the metal aluminum powder is ball-milled and mixed with sodium chloride, potassium chloride and aluminum hydroxide to obtain a mixture; the mixture is heated to a molten state and calcined at 820°C for 14 hours, and the mixture is obtained after cooling Said molten salt.
  • This embodiment provides a mixed chloride molten salt with high thermal conductivity.
  • the raw materials of the molten salt in terms of mass fraction include:
  • the metal aluminum powder is ball-milled and mixed with sodium chloride, potassium chloride and aluminum hydroxide to obtain a mixture; the mixture is heated to a molten state and calcined at 820°C for 14 hours, and the mixture is obtained after cooling Said molten salt.
  • This embodiment provides a mixed chloride molten salt with high thermal conductivity.
  • the raw materials of the molten salt in terms of mass fraction include:
  • the metal aluminum powder is ball-milled and mixed with sodium chloride, potassium chloride and aluminum hydroxide to obtain a mixture; the mixture is heated to a molten state and calcined at 820°C for 14 hours, and the mixture is obtained after cooling Said molten salt.
  • This embodiment provides a mixed chloride molten salt with high thermal conductivity.
  • the raw materials of the molten salt in terms of mass fraction include:
  • Sodium chloride, potassium chloride and aluminum hydroxide are mixed to obtain a mixture; the mixture is heated to a molten state and calcined at 820° C. for 14 hours, and the molten salt is obtained after cooling.
  • This embodiment provides a mixed chloride molten salt with high thermal conductivity.
  • the raw materials of the molten salt in terms of mass fraction include:
  • the metal aluminum powder is ball-milled and mixed with sodium chloride and potassium chloride to obtain a mixture; the mixture is heated to a molten state and calcined at 820° C. for 14 hours, and the molten salt is obtained after cooling.
  • Example 1 778 980°C 3.638
  • Example 2 783 960°C 4.113
  • Example 3 790 960°C 4.526
  • Example 4 781 970°C 4.244
  • Example 5 779 980°C 4.471
  • Example 6 789 980°C 4.498
  • Example 7 791 960°C 4.642
  • Example 8 788 950°C 4.893 Comparative example 1 786 950°C 3.237 Comparative example 2 -(Cannot form a communion) - - -
  • the melting point of the molten salt obtained in Examples 1-8 of the present invention can be as low as 778°C, the upper working temperature can reach 980°C, and the thermal conductivity can reach 4.893W/(m ⁇ K) .
  • Comparative Example 1 no metal hydroxide and metal powder were added, and its thermal conductivity was only 3.237 W/(m ⁇ K), while the addition ratio of Comparative Example 2 could not form an eutectic.

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Abstract

Provided by the present invention is a mixed chloride molten salt having high thermal conductivity. The raw materials of the molten salt comprise a chloride, a metal hydroxide and a metal powder. The molten salt lowers the melting point, increases the upper working temperature limit, and improves the power generation efficiency of solar thermal power generation. At the same time, the molten salt has greater thermal conductivity, better heat transfer and heat storage performance, may avoid the problem of local overheating of an apparatus, may also reduce the amount of media for heat transfer and heat storage, reduce the volumes of related transportation and storage devices, and reduce operating costs.

Description

一种高导热的混合氯化物熔盐及其制备方法和应用High thermal conductivity mixed chloride molten salt and preparation method and application thereof 技术领域Technical field
本发明属于储能材料领域,涉及一种熔盐,尤其涉及一种高导热的混合氯化物熔盐及其制备方法和应用。The invention belongs to the field of energy storage materials, and relates to a molten salt, in particular to a mixed chloride molten salt with high thermal conductivity and a preparation method and application thereof.
背景技术Background technique
可再生能源包括生物质能、水能、风能、海浪能、和太阳能等。在绿色能源中,太阳能是安全性、清洁性、永久性等最好的能源。我国全国总面积2/3以上地区年日照时数均大于2200h,尤其是西藏西部、新疆东南部、青海西部、云南南部等地区太阳能资源尤为丰富,接近世界上最著名的非洲大沙漠,位居世界第二位,我国太阳能资源非常丰富。如果将该太阳能的一分部进行有效利用,对于解决能源与环境问题将有重大意义。目前太阳能利用方式主要有3种方式,分别是转化为电能、热能和化学能;其中应用最多是太阳能光伏发电和太阳能热发电。太阳能光伏发电存在多晶硅材料制备成本较高且对环境污染严重。太阳能热发电技术被认为是太阳能发电最有前途技术之一。但由于太阳能具有间歇性、能量密度低和稳定性差等缺点,难以满足连续用能的需求,且太阳光聚焦后会产生很高的温度。故选择性能可靠的高温传热蓄热材料将是提高太阳能热发电和太阳能热化学反应蓄能效率的关键技术之一。Renewable energy includes biomass energy, hydropower, wind energy, wave energy, and solar energy. Among green energy sources, solar energy is the best energy source for safety, cleanliness, and permanence. The annual sunshine hours of more than 2/3 of the country’s total area are more than 2200h, especially in western Tibet, southeastern Xinjiang, western Qinghai, southern Yunnan and other regions with abundant solar resources, close to the world’s most famous African desert, ranking The second place in the world, my country is very rich in solar energy resources. If this part of solar energy is used effectively, it will be of great significance to solve energy and environmental problems. At present, there are three main ways to use solar energy, which are converted into electric energy, thermal energy and chemical energy; among them, solar photovoltaic power generation and solar thermal power generation are the most used. Solar photovoltaic power generation has high production costs of polysilicon materials and serious environmental pollution. Solar thermal power generation technology is considered to be one of the most promising technologies for solar power generation. However, due to the shortcomings of intermittent, low energy density, and poor stability of solar energy, it is difficult to meet the demand for continuous energy consumption, and high temperatures will be generated after the sunlight is focused. Therefore, choosing reliable high-temperature heat transfer and heat storage materials will be one of the key technologies to improve the efficiency of solar thermal power generation and solar thermal chemical reaction energy storage.
熔融盐作为一种无机化合物,粘度小、导热性能好、腐蚀性弱、蒸汽压低、使用温度范围广、价格便宜,成为中高温传热蓄热材料的首选。研究表明,与高温导热油相比,运用熔融盐(硝酸熔盐)可以使太阳能电站最高工作温度提高到500℃左右,使得蒸汽轮机发电效率提高到40%。As an inorganic compound, molten salt has low viscosity, good thermal conductivity, weak corrosiveness, low vapor pressure, wide operating temperature range, and low price, making it the first choice for medium and high temperature heat transfer and heat storage materials. Studies have shown that, compared with high-temperature heat transfer oil, the use of molten salt (nitrate molten salt) can increase the maximum operating temperature of solar power stations to about 500°C and increase the power generation efficiency of steam turbines to 40%.
目前,太阳能热发电使用最多的熔盐是硝酸熔盐作为传热蓄热材料,公开 混合硝酸熔盐有(60%KNO 3-40wt%NaNO 3,Solar Salt)和三元混合硝酸熔盐(53%KNO 3-7%NaNO 3-40wt%NaNO 2,Hitec)。混合硝酸熔盐体系存在上限使用温度一般在550℃。如果要用到运行温度更高的塔式太阳能发电和热化学热解制氢等会出现高温分解和劣化等问题,且硝酸熔盐存在导热系数很低,一般在0.4~0.6W/(m·K)之间,再同一热功率下,需要更多传热蓄热材料,增大了储热系统尺寸,增加了电站的运行难度,提高了成本。 At present, the most used molten salt for solar thermal power generation is nitrate molten salt as a heat transfer and storage material. It is disclosed that mixed nitrate molten salt (60% KNO 3 -40wt% NaNO 3 , Solar Salt) and ternary mixed nitrate molten salt (53 % KNO 3 -7% NaNO 3 -40 wt% NaNO 2 , Hitec). The maximum operating temperature of the mixed nitrate molten salt system is generally 550°C. If tower solar power generation with higher operating temperature and hydrogen production by thermochemical pyrolysis are to be used, problems such as high temperature decomposition and degradation will occur, and molten nitrate salts have very low thermal conductivity, generally 0.4~0.6W/(m· K), under the same thermal power, more heat transfer and heat storage materials are needed, which increases the size of the heat storage system, increases the difficulty of power station operation, and increases the cost.
CN 104109508 A公开了一种硝酸盐体系熔盐储热材料由硝酸钾和硝酸钠组成,所述硝酸钠和硝酸钾的质量比为30~70∶30~70,所述硝酸钾和硝酸钠中的Ca 2+、Mg 2+、Cl -、SO 4 2-杂质离子含量分别小于100ppm、100ppm、200ppm以及300ppm。该发明已Solar Salt熔盐为基础,通过提纯工艺和杂质离子控制提高了Solar Salt熔盐的热稳定性,延长储热材质的使用寿命和运行成本。但是该发明提供的熔盐的导热系数较低,熔点也相对偏高。 CN 104109508 A discloses a nitrate system molten salt heat storage material consisting of potassium nitrate and sodium nitrate, the mass ratio of sodium nitrate and potassium nitrate is 30-70:30-70, and the potassium nitrate and sodium nitrate are the Ca 2+, Mg 2+, Cl - , SO 4 2- ion content of impurities each less than 100ppm, 100ppm, 200ppm and 300ppm. The invention is based on Solar Salt molten salt, and improves the thermal stability of Solar Salt molten salt through purification process and impurity ion control, and extends the service life and operating cost of heat storage materials. However, the molten salt provided by the invention has a low thermal conductivity and a relatively high melting point.
CN 107090273 A公开了一种混合熔盐传热蓄热工质,其特征在于,由Ca(NO 3) 2、KNO 3、NaNO 3和LiNO 3组成,各组分的质量配比为:Ca(NO 3) 2:8.0wt%;KNO 3:55~60wt%;NaNO 3:7~12wt%;LiNO 3:18~25wt%。该熔盐可应用于太阳能热发电储能、弃风弃光电及“煤改电”蓄热供热或工业余热回收储存等中高温传热蓄热领域。该混合熔盐热物性性能非常稳定,使用过程中不会出现某一成分的分离现象,在液态温区具有良好的传热性能,且饱和蒸汽压力低于2个大气压。由于该混合熔盐的主要原料为硝酸盐,其导热系数较低,且在高温下有分解风险,使用上限温度低。 CN 107090273 A discloses a mixed molten salt heat transfer and heat storage working fluid, which is characterized in that it is composed of Ca(NO 3 ) 2 , KNO 3 , NaNO 3 and LiNO 3 , and the mass ratio of each component is: Ca( NO 3 ) 2 : 8.0wt%; KNO 3 : 55-60wt%; NaNO 3 : 7-12wt%; LiNO 3 : 18-25wt%. The molten salt can be used in the fields of medium and high temperature heat transfer and heat storage, such as solar thermal power generation and energy storage, abandonment of wind and photovoltaic, "coal-to-electricity" heat storage and heating, or industrial waste heat recovery and storage. The thermophysical properties of the mixed molten salt are very stable, there will be no separation of a certain component during use, it has good heat transfer performance in the liquid temperature zone, and the saturated vapor pressure is lower than 2 atmospheres. Since the main raw material of the mixed molten salt is nitrate, its thermal conductivity is low, and there is a risk of decomposition at high temperatures, and the upper limit of use temperature is low.
目前,迫切需要工作温度上限高、熔点低些、导热系数高等优点的熔盐来代替现有硝酸熔盐,从而提高太阳能热发电的发电效率,降低传热蓄热的运行成本。At present, there is an urgent need for molten salt with the advantages of high operating temperature, lower melting point, and high thermal conductivity to replace the existing nitrate molten salt, so as to improve the power generation efficiency of solar thermal power generation and reduce the operating cost of heat transfer and heat storage.
发明内容Summary of the invention
为解决上述技术问题,本发明提供一种高导热的混合氯化物熔盐,所述熔盐降低了熔点,提高了工作上限温度,提高了太阳能热发电的发电效率,同时所述熔盐就有较大的导热系数,传热蓄热性能更好,能避免装置局部出现过热问题,也可以减少传热蓄热介质用量,减少有关运输、储存设备的体积,降低运行成本。In order to solve the above technical problems, the present invention provides a high thermal conductivity mixed chloride molten salt. The molten salt reduces the melting point, increases the upper limit temperature of the work, and improves the power generation efficiency of solar thermal power generation. At the same time, the molten salt has Larger thermal conductivity, better heat transfer and heat storage performance, can avoid local overheating of the device, reduce the amount of heat transfer and heat storage media, reduce the volume of related transportation and storage equipment, and reduce operating costs.
本发明目的之一在于提供一种高导热的混合氯化物熔盐,所述熔盐的原料包括氯化物、金属氢氧化物以及金属粉。One of the objectives of the present invention is to provide a mixed chloride molten salt with high thermal conductivity. The raw materials of the molten salt include chloride, metal hydroxide and metal powder.
作为本发明优选的技术方案,所述氯化物包括氯化钠和/或氯化钾。As a preferred technical solution of the present invention, the chloride includes sodium chloride and/or potassium chloride.
作为本发明优选的技术方案,所述金属氢氧化物为氢氧化铝。As a preferred technical solution of the present invention, the metal hydroxide is aluminum hydroxide.
优选地,所述金属粉为金属铝粉。Preferably, the metal powder is metal aluminum powder.
本发明中,使用铝粉能提高混合熔盐的导热系数,从而提高热传递效率,提高发电效率。In the present invention, the use of aluminum powder can increase the thermal conductivity of the mixed molten salt, thereby improving the heat transfer efficiency and the power generation efficiency.
作为本发明优选的技术方案,所述熔盐的原料包括氯化钠、氯化钾、氢氧化铝以及金属铝粉。As a preferred technical solution of the present invention, the raw materials of the molten salt include sodium chloride, potassium chloride, aluminum hydroxide and metal aluminum powder.
本发明为了克服现有硝酸熔盐工作温度上限不高,导热系数低等问题。通过在简单氯化钠、氯化钾的基础上添加导热系数更高的氢氧化铝、金属铝粉等成分,形成新的混合氯化物熔盐。由于氢氧化铝熔点为300℃,金属铝粉的熔点为660℃,都低于简单无机氯化钠、氯化钾单盐,能形成更低熔点、工作温度上限更高的混合氯化物熔盐,其中金属铝粉的导热系数为270W/(m·K),微量的添加就能提高熔盐的导热系数。The present invention overcomes the problems of low working temperature upper limit and low thermal conductivity of the existing nitrate molten salt. By adding components such as aluminum hydroxide and metal aluminum powder with higher thermal conductivity on the basis of simple sodium chloride and potassium chloride, a new mixed chloride molten salt is formed. Since the melting point of aluminum hydroxide is 300°C, and the melting point of metal aluminum powder is 660°C, both of which are lower than simple inorganic sodium chloride and potassium chloride mono-salts, they can form mixed chloride molten salts with lower melting points and higher working temperature limits. Among them, the thermal conductivity of metal aluminum powder is 270W/(m·K), and a small amount of addition can increase the thermal conductivity of molten salt.
作为本发明优选的技术方案,按照质量分数计所述熔盐的原料包括:As a preferred technical solution of the present invention, the raw materials of the molten salt in terms of mass fraction include:
Figure PCTCN2019078264-appb-000001
Figure PCTCN2019078264-appb-000001
Figure PCTCN2019078264-appb-000002
Figure PCTCN2019078264-appb-000002
其中,氯化钠的质量分数可以是40%、45%、50%、55%、60%、65%或70%等,氯化钾的质量分数可以是25%、26%、28%、30%、32%、35%、38%、40%、42%或45%等,氢氧化铝的质量分数可以是2%、3%、4%、5%、6%、7%、8%、9%或10%等,金属铝粉的质量分数可以是2%、3%、4%、5%、6%或7%等,但并不仅限于所列举的数值,上述各数值范围内其他未列举的数值同样适用。Among them, the mass fraction of sodium chloride can be 40%, 45%, 50%, 55%, 60%, 65% or 70%, etc., and the mass fraction of potassium chloride can be 25%, 26%, 28%, 30%. %, 32%, 35%, 38%, 40%, 42% or 45%, etc. The mass fraction of aluminum hydroxide can be 2%, 3%, 4%, 5%, 6%, 7%, 8%, 9% or 10%, etc. The mass fraction of metal aluminum powder can be 2%, 3%, 4%, 5%, 6% or 7%, etc., but it is not limited to the numerical values listed. The values listed also apply.
本发明中,所述熔盐中金属铝粉的质量分数小于2%,起不到提高混合熔盐的导热系数作用,对其导热性能影响不大;质量分数大于7%,熔盐造成混合熔盐无法形成共融的混合物。In the present invention, the mass fraction of metal aluminum powder in the molten salt is less than 2%, which cannot improve the thermal conductivity of the mixed molten salt, and has little effect on its thermal conductivity; the mass fraction is greater than 7%, and the molten salt causes mixed melting. Salt cannot form a communicative mixture.
作为本发明优选的技术方案,按照质量分数计所述熔盐的原料包括:As a preferred technical solution of the present invention, the raw materials of the molten salt in terms of mass fraction include:
Figure PCTCN2019078264-appb-000003
Figure PCTCN2019078264-appb-000003
本发明目的之二在于提供一种上述熔盐的制备方法,所述制备方法为:The second object of the present invention is to provide a method for preparing the above-mentioned molten salt, the preparation method being:
将金属粉与氯化物以及金属氢氧化物混合,得到混合料;将所述混合料加热至熔融状态进行煅烧,冷却后得到所述熔盐。The metal powder is mixed with the chloride and the metal hydroxide to obtain a mixture; the mixture is heated to a molten state for calcination, and the molten salt is obtained after cooling.
作为本发明优选的技术方案,所述煅烧的温度为780~850℃,如780℃、790℃、800℃、810℃、820℃、830℃、840℃或850℃等,但并不仅限于所列举的数值,该数值范围内其他未列举的数值同样适用。As a preferred technical solution of the present invention, the calcination temperature is 780 to 850°C, such as 780°C, 790°C, 800°C, 810°C, 820°C, 830°C, 840°C or 850°C, etc., but is not limited to For the listed values, other unlisted values within the range of values also apply.
本发明中,煅烧温度大于850℃,会导致熔盐劣化与分解,热稳定性能较差; 煅烧温度低于780℃会导致发电温度时不高,发电效率偏低。In the present invention, the calcination temperature is higher than 850°C, which will cause the molten salt to deteriorate and decompose, and the thermal stability is poor; the calcination temperature is lower than 780°C, which will result in low power generation temperature and low power generation efficiency.
作为本发明优选的技术方案,所述煅烧的时间为12~16h,如12h、12.5h、13h、13.5h、14h、14.5h、15h、15.5h或16h等,但并不仅限于所列举的数值,该数值范围内其他未列举的数值同样适用。As a preferred technical solution of the present invention, the calcination time is 12-16h, such as 12h, 12.5h, 13h, 13.5h, 14h, 14.5h, 15h, 15.5h or 16h, etc., but not limited to the listed values , Other unlisted values within this value range also apply.
本发明所述制备方法中,如金属粉的颗粒度过大,则需要对金属粉进行球磨细化。煅烧冷却后得到的熔盐的颗粒度较大,需要经过粉碎以及研磨等处理成较小的颗粒以便储存和运输。In the preparation method of the present invention, if the particles of the metal powder are too large, the metal powder needs to be ball-milled and refined. The molten salt obtained after calcination and cooling has a relatively large particle size and needs to be crushed and ground into smaller particles for storage and transportation.
本发明目的之三在于提供一种上述氯化改性熔盐的应用,所述熔盐用于太阳能热发电领域。The third object of the present invention is to provide an application of the above-mentioned chlorinated modified molten salt, which is used in the field of solar thermal power generation.
与现有技术相比,本发明至少具有以下有益效果:Compared with the prior art, the present invention has at least the following beneficial effects:
(1)本发明混合氯化物熔盐能降低熔点和提高上限工作温度,提高太阳能热发电的发电效率,熔点的降低可以节省运行保温成本;同时也扩大了熔盐的使用温度范围,可以应用于太阳能热发电、太阳能制氢反应及工业余热回收等领域;(1) The mixed chloride molten salt of the present invention can lower the melting point and increase the upper limit operating temperature, improve the power generation efficiency of solar thermal power generation, and reduce the melting point to save operation and insulation costs; at the same time, it also expands the use temperature range of the molten salt and can be applied Solar thermal power generation, solar hydrogen production reaction and industrial waste heat recovery and other fields;
(2)本发明混合氯化物熔盐的导热系数更高,传热性好,传热蓄热效果更好,也能避免装置局部出现过热问题。(2) The mixed chloride molten salt of the present invention has higher thermal conductivity, good heat transfer performance, better heat transfer and heat storage effect, and can also avoid local overheating problems of the device.
具体实施方式detailed description
为便于理解本发明,本发明列举实施例如下。本领域技术人员应该明了,所述实施例仅仅是帮助理解本发明,不应视为对本发明的具体限制。To facilitate the understanding of the present invention, examples of the present invention are listed below. Those skilled in the art should understand that the described embodiments are only to help understand the present invention and should not be regarded as specific limitations to the present invention.
实施例1Example 1
本实施例提供一种高导热的混合氯化物熔盐,按照质量分数计所述熔盐的原料包括:This embodiment provides a mixed chloride molten salt with high thermal conductivity. The raw materials of the molten salt in terms of mass fraction include:
Figure PCTCN2019078264-appb-000004
Figure PCTCN2019078264-appb-000004
Figure PCTCN2019078264-appb-000005
Figure PCTCN2019078264-appb-000005
按照上述质量分数将金属铝粉球磨细化并与氯化钠、氯化钾和氢氧化铝混合,得到混合料;将所述混合料加热至熔融状态在800℃下煅烧16h,冷却后得到所述熔盐。According to the above mass fraction, the metal aluminum powder is ball-milled and mixed with sodium chloride, potassium chloride and aluminum hydroxide to obtain a mixture; the mixture is heated to a molten state and calcined at 800°C for 16 hours, and the mixture is obtained after cooling Said molten salt.
实施例2Example 2
本实施例提供一种高导热的混合氯化物熔盐,按照质量分数计所述熔盐的原料包括:This embodiment provides a mixed chloride molten salt with high thermal conductivity. The raw materials of the molten salt in terms of mass fraction include:
Figure PCTCN2019078264-appb-000006
Figure PCTCN2019078264-appb-000006
按照上述质量分数将金属铝粉球磨细化并与氯化钠、氯化钾和氢氧化铝混合,得到混合料;将所述混合料加热至熔融状态在830℃下煅烧12h,冷却后得到所述熔盐。According to the above mass fraction, the metal aluminum powder is ball-milled and mixed with sodium chloride, potassium chloride and aluminum hydroxide to obtain a mixture; the mixture is heated to a molten state and calcined at 830°C for 12 hours, and the mixture is obtained after cooling Said molten salt.
实施例3Example 3
本实施例提供一种高导热的混合氯化物熔盐,按照质量分数计所述熔盐的原料包括:This embodiment provides a mixed chloride molten salt with high thermal conductivity. The raw materials of the molten salt in terms of mass fraction include:
Figure PCTCN2019078264-appb-000007
Figure PCTCN2019078264-appb-000007
按照上述质量分数将金属铝粉球磨细化并与氯化钠、氯化钾和氢氧化铝混合,得到混合料;将所述混合料加热至熔融状态在800℃下煅烧12h,冷却后得到所述熔盐。According to the above mass fraction, the metal aluminum powder is ball-milled and mixed with sodium chloride, potassium chloride and aluminum hydroxide to obtain a mixture; the mixture is heated to a molten state and calcined at 800°C for 12 hours, and after cooling, the mixture is obtained Said molten salt.
实施例4Example 4
本实施例提供一种高导热的混合氯化物熔盐,按照质量分数计所述熔盐的原料包括:This embodiment provides a mixed chloride molten salt with high thermal conductivity. The raw materials of the molten salt in terms of mass fraction include:
Figure PCTCN2019078264-appb-000008
Figure PCTCN2019078264-appb-000008
按照上述质量分数将金属铝粉球磨细化并与氯化钠、氯化钾和氢氧化铝混合,得到混合料;将所述混合料加热至熔融状态在820℃下煅烧15h,冷却后得到所述熔盐。According to the above mass fraction, the metal aluminum powder is ball-milled and mixed with sodium chloride, potassium chloride and aluminum hydroxide to obtain a mixture; the mixture is heated to a molten state and calcined at 820°C for 15 hours, and the mixture is obtained after cooling Said molten salt.
实施例5Example 5
本实施例提供一种高导热的混合氯化物熔盐,按照质量分数计所述熔盐的原料包括:This embodiment provides a mixed chloride molten salt with high thermal conductivity. The raw materials of the molten salt in terms of mass fraction include:
Figure PCTCN2019078264-appb-000009
Figure PCTCN2019078264-appb-000009
按照上述质量分数将金属铝粉球磨细化并与氯化钠、氯化钾和氢氧化铝混合,得到混合料;将所述混合料加热至熔融状态在810℃下煅烧13h,冷却后得到所述熔盐。According to the above mass fraction, the metal aluminum powder is ball-milled and mixed with sodium chloride, potassium chloride and aluminum hydroxide to obtain a mixture; the mixture is heated to a molten state and calcined at 810°C for 13 hours, and the mixture is obtained after cooling Said molten salt.
实施例6Example 6
本实施例提供一种高导热的混合氯化物熔盐,按照质量分数计所述熔盐的原料包括:This embodiment provides a mixed chloride molten salt with high thermal conductivity. The raw materials of the molten salt in terms of mass fraction include:
Figure PCTCN2019078264-appb-000010
Figure PCTCN2019078264-appb-000010
按照上述质量分数将金属铝粉球磨细化并与氯化钠、氯化钾和氢氧化铝混合,得到混合料;将所述混合料加热至熔融状态在820℃下煅烧14h,冷却后得到所述熔盐。According to the above mass fraction, the metal aluminum powder is ball-milled and mixed with sodium chloride, potassium chloride and aluminum hydroxide to obtain a mixture; the mixture is heated to a molten state and calcined at 820°C for 14 hours, and the mixture is obtained after cooling Said molten salt.
实施例7Example 7
本实施例提供一种高导热的混合氯化物熔盐,按照质量分数计所述熔盐的原料包括:This embodiment provides a mixed chloride molten salt with high thermal conductivity. The raw materials of the molten salt in terms of mass fraction include:
Figure PCTCN2019078264-appb-000011
Figure PCTCN2019078264-appb-000011
按照上述质量分数将金属铝粉球磨细化并与氯化钠、氯化钾和氢氧化铝混合,得到混合料;将所述混合料加热至熔融状态在820℃下煅烧14h,冷却后得到所述熔盐。According to the above mass fraction, the metal aluminum powder is ball-milled and mixed with sodium chloride, potassium chloride and aluminum hydroxide to obtain a mixture; the mixture is heated to a molten state and calcined at 820°C for 14 hours, and the mixture is obtained after cooling Said molten salt.
实施例8Example 8
本实施例提供一种高导热的混合氯化物熔盐,按照质量分数计所述熔盐的原料包括:This embodiment provides a mixed chloride molten salt with high thermal conductivity. The raw materials of the molten salt in terms of mass fraction include:
Figure PCTCN2019078264-appb-000012
Figure PCTCN2019078264-appb-000012
按照上述质量分数将金属铝粉球磨细化并与氯化钠、氯化钾和氢氧化铝混合,得到混合料;将所述混合料加热至熔融状态在820℃下煅烧14h,冷却后得到所述熔盐。According to the above mass fraction, the metal aluminum powder is ball-milled and mixed with sodium chloride, potassium chloride and aluminum hydroxide to obtain a mixture; the mixture is heated to a molten state and calcined at 820°C for 14 hours, and the mixture is obtained after cooling Said molten salt.
对比例1Comparative example 1
本实施例提供一种高导热的混合氯化物熔盐,按照质量分数计所述熔盐的原料包括:This embodiment provides a mixed chloride molten salt with high thermal conductivity. The raw materials of the molten salt in terms of mass fraction include:
氯化钠                    55%;Sodium chloride 55%;
氯化钾                    45%;Potassium chloride 45%;
将氯化钠、氯化钾和氢氧化铝混合,得到混合料;将所述混合料加热至熔融状态在820℃下煅烧14h,冷却后得到所述熔盐。Sodium chloride, potassium chloride and aluminum hydroxide are mixed to obtain a mixture; the mixture is heated to a molten state and calcined at 820° C. for 14 hours, and the molten salt is obtained after cooling.
对比例2Comparative example 2
本实施例提供一种高导热的混合氯化物熔盐,按照质量分数计所述熔盐的原料包括:This embodiment provides a mixed chloride molten salt with high thermal conductivity. The raw materials of the molten salt in terms of mass fraction include:
氯化钠                    50%;Sodium chloride 50%;
氯化钾                    40%;Potassium chloride 40%;
金属铝粉                  10%。Metal aluminum powder 10%.
按照上述质量分数将金属铝粉球磨细化并与氯化钠和氯化钾混合,得到混合料;将所述混合料加热至熔融状态在820℃下煅烧14h,冷却后得到所述熔盐。According to the above mass fraction, the metal aluminum powder is ball-milled and mixed with sodium chloride and potassium chloride to obtain a mixture; the mixture is heated to a molten state and calcined at 820° C. for 14 hours, and the molten salt is obtained after cooling.
对实施例1-8以及对比例1和2提供的熔盐的熔点、工作上限温度以及导热 系数进行测试,结果如表1所示。The melting point, upper working temperature and thermal conductivity of the molten salt provided in Examples 1-8 and Comparative Examples 1 and 2 were tested. The results are shown in Table 1.
表1Table 1
 To 熔点/℃Melting point/℃ 工作上线温度/℃Working online temperature/℃ 导热系数/W/(m·K)Thermal conductivity/W/(m·K)
实施例1Example 1 778778 980℃980°C 3.6383.638
实施例2Example 2 783783 960℃960°C 4.1134.113
实施例3Example 3 790790 960℃960°C 4.5264.526
实施例4Example 4 781781 970℃970°C 4.2444.244
实施例5Example 5 779779 980℃980°C 4.4714.471
实施例6Example 6 789789 980℃980°C 4.4984.498
实施例7Example 7 791791 960℃960°C 4.6424.642
实施例8Example 8 788788 950℃950°C 4.8934.893
对比例1Comparative example 1 786786 950℃950°C 3.2373.237
对比例2Comparative example 2 -(不能形成共融物)-(Cannot form a communion) -- --
通过表1的测试结果可以看出,本发明实施例1-8得到的熔盐,其熔点可低至778℃,工作上限温度可达980℃,导热系数可达4.893W/(m·K)。而对比例1未添加金属氢氧化物以及金属粉,其导热系数仅为3.237W/(m·K),而对比例2的添加比例不能形成共融物。It can be seen from the test results in Table 1 that the melting point of the molten salt obtained in Examples 1-8 of the present invention can be as low as 778°C, the upper working temperature can reach 980°C, and the thermal conductivity can reach 4.893W/(m·K) . In Comparative Example 1, no metal hydroxide and metal powder were added, and its thermal conductivity was only 3.237 W/(m·K), while the addition ratio of Comparative Example 2 could not form an eutectic.
申请人声明,本发明通过上述实施例来说明本发明的详细工艺设备和工艺流程,但本发明并不局限于上述详细工艺设备和工艺流程,即不意味着本发明必须依赖上述详细工艺设备和工艺流程才能实施。所属技术领域的技术人员应该明了,对本发明的任何改进,对本发明产品各原料的等效替换及辅助成分的添加、具体方式的选择等,均落在本发明的保护范围和公开范围之内。The applicant declares that the present invention uses the above embodiments to illustrate the detailed process equipment and process flow of the present invention, but the present invention is not limited to the above detailed process equipment and process flow, which does not mean that the present invention must rely on the above detailed process equipment and process flow. The process can be implemented. Those skilled in the art should understand that any improvement to the present invention, the equivalent replacement of each raw material of the product of the present invention, the addition of auxiliary components, the selection of specific methods, etc. fall within the scope of protection and disclosure of the present invention.

Claims (10)

  1. 一种高导热的混合氯化物熔盐,其特征在于,所述熔盐的原料包括氯化物、金属氢氧化物以及金属粉。A high thermal conductivity mixed chloride molten salt, characterized in that the raw materials of the molten salt include chloride, metal hydroxide and metal powder.
  2. 根据权利要求1所述的熔盐,其特征在于,所述氯化物包括氯化钠和或氯化钾。The molten salt according to claim 1, wherein the chloride includes sodium chloride and or potassium chloride.
  3. 根据权利要求1或2所述的熔盐,其特征在于,所述金属氢氧化物为氢氧化铝;The molten salt according to claim 1 or 2, wherein the metal hydroxide is aluminum hydroxide;
    优选地,所述金属粉为金属铝粉。Preferably, the metal powder is metal aluminum powder.
  4. 根据权利要求2或3所述的熔盐,其特征在于,所述熔盐的原料包括氯化钠、氯化钾、氢氧化铝以及金属铝粉。The molten salt according to claim 2 or 3, wherein the raw materials of the molten salt include sodium chloride, potassium chloride, aluminum hydroxide and metal aluminum powder.
  5. 根据权利要求4所述的熔盐,其特征在于,按照质量分数计所述熔盐的原料包括:The molten salt according to claim 4, wherein the raw material of the molten salt in terms of mass fraction comprises:
    Figure PCTCN2019078264-appb-100001
    Figure PCTCN2019078264-appb-100001
  6. 根据权利要求5所述的熔盐,其特征在于,按照质量分数计所述熔盐的原料包括:The molten salt according to claim 5, wherein the raw material of the molten salt in terms of mass fraction comprises:
    Figure PCTCN2019078264-appb-100002
    Figure PCTCN2019078264-appb-100002
  7. 一种权利要求1-6任一项所述的熔盐的制备方法,其特征在于,所述制备方法为:A method for preparing molten salt according to any one of claims 1 to 6, characterized in that the preparation method is:
    将金属粉与氯化物以及金属氢氧化物混合,得到混合料;将所述混合料加热至熔融状态进行煅烧,冷却后得到所述熔盐。The metal powder is mixed with the chloride and the metal hydroxide to obtain a mixture; the mixture is heated to a molten state for calcination, and the molten salt is obtained after cooling.
  8. 根据权利要求7所述的制备方法,其特征在于,所述煅烧的温度为780~850℃。The preparation method according to claim 7, wherein the calcination temperature is 780-850°C.
  9. 根据权利要求7或8所述的制备方法,其特征在于,所述煅烧的时间为12~16h。The preparation method according to claim 7 or 8, wherein the calcination time is 12 to 16 hours.
  10. 一种权利要求1-6任一项所述的熔盐的应用,其特征在于,所述熔盐用于太阳能热发电领域。An application of the molten salt according to any one of claims 1-6, wherein the molten salt is used in the field of solar thermal power generation.
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