CN115385307A - Preparation method and application of bismuth telluride micro-nano powder material - Google Patents
Preparation method and application of bismuth telluride micro-nano powder material Download PDFInfo
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- 229910052797 bismuth Inorganic materials 0.000 title claims abstract description 77
- JCXGWMGPZLAOME-UHFFFAOYSA-N bismuth atom Chemical compound [Bi] JCXGWMGPZLAOME-UHFFFAOYSA-N 0.000 title claims abstract description 77
- XSOKHXFFCGXDJZ-UHFFFAOYSA-N telluride(2-) Chemical compound [Te-2] XSOKHXFFCGXDJZ-UHFFFAOYSA-N 0.000 title claims abstract description 77
- 239000000463 material Substances 0.000 title claims abstract description 56
- 239000011858 nanopowder Substances 0.000 title claims abstract description 36
- 238000002360 preparation method Methods 0.000 title claims abstract description 28
- XEKOWRVHYACXOJ-UHFFFAOYSA-N Ethyl acetate Chemical compound CCOC(C)=O XEKOWRVHYACXOJ-UHFFFAOYSA-N 0.000 claims abstract description 93
- 238000000498 ball milling Methods 0.000 claims abstract description 47
- 239000002245 particle Substances 0.000 claims abstract description 44
- 239000000843 powder Substances 0.000 claims abstract description 36
- 238000000034 method Methods 0.000 claims abstract description 31
- 238000001035 drying Methods 0.000 claims abstract description 16
- 229910045601 alloy Inorganic materials 0.000 claims abstract description 13
- 239000000956 alloy Substances 0.000 claims abstract description 13
- 238000007599 discharging Methods 0.000 claims abstract description 4
- 238000000227 grinding Methods 0.000 claims description 22
- 238000005245 sintering Methods 0.000 claims description 13
- 239000000203 mixture Substances 0.000 claims description 6
- 238000007731 hot pressing Methods 0.000 claims description 5
- 239000010453 quartz Substances 0.000 claims description 5
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N silicon dioxide Inorganic materials O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 5
- 238000010438 heat treatment Methods 0.000 claims description 4
- 238000003892 spreading Methods 0.000 claims description 3
- 230000007480 spreading Effects 0.000 claims description 3
- 238000001816 cooling Methods 0.000 claims description 2
- 238000007789 sealing Methods 0.000 claims 2
- 238000005303 weighing Methods 0.000 claims 2
- 238000002156 mixing Methods 0.000 claims 1
- 230000002776 aggregation Effects 0.000 abstract description 17
- 230000008569 process Effects 0.000 abstract description 9
- 238000003723 Smelting Methods 0.000 abstract description 6
- 238000004220 aggregation Methods 0.000 abstract description 6
- 238000005265 energy consumption Methods 0.000 abstract description 4
- 239000006185 dispersion Substances 0.000 abstract description 3
- 239000004065 semiconductor Substances 0.000 abstract description 2
- 238000005266 casting Methods 0.000 abstract 1
- 230000010354 integration Effects 0.000 abstract 1
- 238000009826 distribution Methods 0.000 description 16
- 238000005054 agglomeration Methods 0.000 description 11
- 230000000052 comparative effect Effects 0.000 description 8
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 6
- 238000000926 separation method Methods 0.000 description 6
- 238000010586 diagram Methods 0.000 description 5
- 230000000694 effects Effects 0.000 description 4
- 239000002270 dispersing agent Substances 0.000 description 3
- VLKZOEOYAKHREP-UHFFFAOYSA-N n-Hexane Chemical compound CCCCCC VLKZOEOYAKHREP-UHFFFAOYSA-N 0.000 description 3
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 2
- 229910000617 Mangalloy Inorganic materials 0.000 description 2
- 238000002074 melt spinning Methods 0.000 description 2
- 238000002844 melting Methods 0.000 description 2
- 230000008018 melting Effects 0.000 description 2
- 230000035699 permeability Effects 0.000 description 2
- 230000002829 reductive effect Effects 0.000 description 2
- 238000001878 scanning electron micrograph Methods 0.000 description 2
- 239000010935 stainless steel Substances 0.000 description 2
- 229910001220 stainless steel Inorganic materials 0.000 description 2
- 238000009423 ventilation Methods 0.000 description 2
- 150000001345 alkine derivatives Chemical class 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000011362 coarse particle Substances 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 239000013078 crystal Substances 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 150000002148 esters Chemical class 0.000 description 1
- -1 high surface tension Chemical compound 0.000 description 1
- 239000004615 ingredient Substances 0.000 description 1
- 238000005551 mechanical alloying Methods 0.000 description 1
- 238000003801 milling Methods 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 238000010248 power generation Methods 0.000 description 1
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- 238000005057 refrigeration Methods 0.000 description 1
- 239000011435 rock Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
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Abstract
Description
技术领域technical field
本发明属于热电半导体材料制备技术领域,具体涉及一种碲化铋微纳米粉体材料的制备方法及应用。The invention belongs to the technical field of preparation of thermoelectric semiconductor materials, and in particular relates to a preparation method and application of a bismuth telluride micronano powder material.
背景技术Background technique
热电材料可直接实现热和电的转换,在发电和制冷应用上有巨大潜力,对能源和环境问题的解决发挥重要作用,现在常用的热电材料主要是碲化铋。热电材料的热电性能由Seebeck系数、电导率和热导率之间相互制约,难以独立调控。由于微纳米粉末可增加晶界面,导致声子散射增加,有效降低材料晶格热导率,且热导的降低程度大于电性能变化程度,固可增强材料热电性能。Thermoelectric materials can directly realize the conversion of heat and electricity, have great potential in power generation and refrigeration applications, and play an important role in solving energy and environmental problems. Now the commonly used thermoelectric materials are mainly bismuth telluride. The thermoelectric properties of thermoelectric materials are restricted by the Seebeck coefficient, electrical conductivity, and thermal conductivity, which are difficult to control independently. Since the micro-nano powder can increase the crystal interface, resulting in increased phonon scattering, effectively reducing the thermal conductivity of the material lattice, and the reduction in thermal conductivity is greater than the change in electrical properties, which can enhance the thermoelectric properties of the material.
目前微纳米热电材料的制备方法有机械合金法、熔体旋甩法等,然而熔体旋甩法的设备昂贵,能耗高,机械合金法的长时间球磨容易导致粉体污染较为严重,晶粒取向不高,因此发展效率高、能耗低、可批量制备微纳米粉末的方法显得尤为重要。采用熔炼结合球磨制粉的方式,可有效避免上述问题。球磨存在湿法球磨和干法球磨之分,湿法球磨需要采用高纯酒精、己烷、丙酮等作为湿磨介质,因添加的介质量较大,且有刺激性气味,球磨过程中容易导致粉体氧化,且存在后续分离复杂等问题。干法球磨不需要引入大量的湿磨介质,操作方便,但是干法球磨过程中,则时间延长,物料容易出现聚结块,粒径分布不均匀的问题。At present, the preparation methods of micro-nano thermoelectric materials include mechanical alloying method, melt spinning method, etc. However, the equipment of the melt spinning method is expensive, and the energy consumption is high. The particle orientation is not high, so it is particularly important to develop methods with high efficiency, low energy consumption, and batch preparation of micro-nano powders. The method of smelting combined with ball milling can effectively avoid the above problems. Ball milling can be divided into wet ball milling and dry ball milling. Wet ball milling needs to use high-purity alcohol, hexane, acetone, etc. The powder is oxidized, and there are problems such as subsequent separation complexity. Dry ball milling does not need to introduce a large amount of wet milling media, and is easy to operate. However, during the dry ball milling process, the time is prolonged, and the materials are prone to agglomeration and uneven particle size distribution.
发明内容Contents of the invention
针对干法球磨过程中容易出现物料结块,粒径分布不均匀等问题,本发明的目的为提供一种碲化铋微纳米粉体的制备方法,熔炼结合球磨制粉,球磨时加入乙酸乙酯干法球磨,避免干法球磨的结块现象,所得碲化铋微纳米粉体的粒径分布均匀。Aiming at the problems of material agglomeration and uneven particle size distribution in the dry ball milling process, the purpose of the present invention is to provide a preparation method of bismuth telluride micro-nano powder, smelting combined with ball milling to make powder, adding ethyl acetate during ball milling Ester dry ball milling avoids the agglomeration phenomenon of dry ball milling, and the particle size distribution of the obtained bismuth telluride micro-nano powder is uniform.
本发明提供如下的技术方案:The present invention provides following technical scheme:
一种碲化铋微纳米粉体材料的制备方法,将碲化铋的合金铸锭破碎成颗粒,置于球磨装置中,加乙酸乙酯干法球磨,出料、干燥,其中碲化铋与乙酸乙酯的质量比≥5:1。A preparation method of bismuth telluride micro-nano powder material, the alloy ingot of bismuth telluride is broken into particles, placed in a ball milling device, added with ethyl acetate for dry ball milling, discharging and drying, wherein bismuth telluride and The mass ratio of ethyl acetate is ≥5:1.
本发明的制备方法中,以熔炼铸锭和干法球磨相结合的方式制备碲化铋微纳米粉体,熔炼铸锭可以提升合金成分的均匀性。在干法球磨时加入乙酸乙酯,利用乙酸乙酯的表面张力大,渗透性强、易分离等特点,可有效改善干法球磨中出现的粉体聚集成块现象,提高粉体粒径的均匀性,而且可明显减小粉体粒径。In the preparation method of the present invention, the bismuth telluride micro-nano powder is prepared by combining ingot melting and dry ball milling, and the ingot melting can improve the uniformity of alloy composition. Adding ethyl acetate during dry ball milling can effectively improve the phenomenon of powder agglomeration in dry ball milling and improve the particle size of the powder by taking advantage of the characteristics of ethyl acetate, such as high surface tension, strong permeability, and easy separation. Uniformity, and can significantly reduce the particle size of the powder.
作为本发明方法的优选,碲化铋破碎后的颗粒的粒径为1~2mm。As a preference of the method of the present invention, the crushed bismuth telluride particles have a particle size of 1-2 mm.
作为本发明方法的优选,碲化铋的合金铸锭经过以下过程制备得到:As a preferred method of the present invention, the alloy ingot of bismuth telluride is prepared through the following process:
按名义组成的摩尔计量比取Bi粉、Sb粉和Te粉,称量并混合均匀,密封于真空度小于2Pa内的真空石英管中,封管,然后以12~18℃/min的速率升温至780~800℃,保温1~1.5h,接着摇摆2~3h,摇摆频率为5~8rpm/min,摇摆角度60°~65°,然后冷却。在制备合金铸锭时选用纯度为99.99%的Bi粉、Sb粉和Te粉。Take Bi powder, Sb powder and Te powder according to the molar ratio of the nominal composition, weigh and mix them evenly, seal them in a vacuum quartz tube with a vacuum degree of less than 2 Pa, seal the tube, and then raise the temperature at a rate of 12-18°C/min Heat to 780-800°C, keep warm for 1-1.5 hours, then rock for 2-3 hours, the rocking frequency is 5-8 rpm/min, the rocking angle is 60°-65°, and then cool. Bi powder, Sb powder and Te powder with a purity of 99.99% are selected when preparing the alloy ingot.
作为本发明方法的优选,碲化铋与乙酸乙酯的质量比为5~10:1。引入的乙酸乙酯的量不宜过多,也不能过少,过少起不到分散作用,仍易发生团聚现象,过多则分离复杂,而且材料易污染,影响材料性能。As a preference of the method of the present invention, the mass ratio of bismuth telluride to ethyl acetate is 5-10:1. The amount of ethyl acetate introduced should not be too much, nor too little, too little will not achieve the dispersing effect, and agglomeration is still prone to occur, and too much will cause complicated separation, and the material is easy to be polluted, which will affect the material performance.
作为本发明方法的优选,球磨所用磨球与碲化铋的球料比为2~3:1。As a preference of the method of the present invention, the ball-to-material ratio of the ball milling balls to the bismuth telluride is 2-3:1.
作为本发明方法的优选,As preferred method of the present invention,
磨球的大小为0.6~1.2mm;The size of the grinding ball is 0.6~1.2mm;
和/或球磨转速为350~500rpm/min;And/or the ball milling speed is 350-500rpm/min;
和/或单周期研磨时间为30~40min,研磨1~2h。优选的,研磨时至少按单周期研磨时间研磨两周,更优选的中间间隔10~20min左右。And/or the single-cycle grinding time is 30-40 minutes, and the grinding time is 1-2 hours. Preferably, grinding is performed for at least two weeks in a single-cycle grinding time, and more preferably, the intermediate interval is about 10 to 20 minutes.
作为本发明方法的优选,干燥物料的方式为:将物料摊开后室温通风干燥,再加热至40~50℃干燥。乙酸乙酯分散剂带有微果香的气味,沸点低、易分离:将出料置于筛网上分离磨球和粉体,然后摊开粉体置于通风口处干燥10~20min,再鼓风烘箱干燥20~30min。As a preferred method of the method of the present invention, the method of drying the materials is as follows: after spreading the materials, they are ventilated and dried at room temperature, and then heated to 40-50°C for drying. Ethyl acetate dispersant has a slightly fruity smell, low boiling point, and easy separation: put the discharged material on a sieve to separate the grinding balls and powder, then spread the powder and dry it at the vent for 10-20 minutes, then blow Dry in an air oven for 20-30 minutes.
一种上述制备方法得到的碲化铋微纳米粉体材料。所得碲化铋微纳米粉体的粒径分布均匀,粒径小,无结块,无污染。A bismuth telluride micronano powder material obtained by the above preparation method. The obtained bismuth telluride micronano powder has uniform particle size distribution, small particle size, no agglomeration, and no pollution.
一种提高碲化铋块体热电性能的方法,所述碲化铋块体由上述碲化铋微纳米粉体材料真空热压烧结得到。所制备的碲化铋块体常温下的zT值得到提升。A method for improving the thermoelectric performance of a bismuth telluride block, the bismuth telluride block is obtained by vacuum hot-pressing sintering of the above-mentioned bismuth telluride micro-nano powder material. The zT value of the prepared bismuth telluride block at room temperature is improved.
作为本发明的优选,真空热压烧结的压强为70~100MPa,烧结温度420~500℃,热压烧结时间60~120min。As a preference of the present invention, the pressure of vacuum hot-press sintering is 70-100 MPa, the sintering temperature is 420-500° C., and the hot-press sintering time is 60-120 min.
本发明的有益效果如下:The beneficial effects of the present invention are as follows:
本发明的碲化铋微纳米粉体的制备方法中,采用熔炼铸锭和干法球磨结合的方式,在球磨过程中采用加入乙酸乙酯助分散,有效避免了干法球磨过程中的粉体聚集成块,提高了粉体粒径的均匀性,并且制备过程的效率高,能耗低。同时所制备的碲化铋微纳米粉体制备成碲化铋块体后,所得碲化铋块体的热电性能得到明显的提升,热电优值zT得到提高。In the preparation method of the bismuth telluride micro-nano powder of the present invention, the method of combining smelting ingot and dry ball milling is adopted, and ethyl acetate is used to assist dispersion during the ball milling process, which effectively avoids powder formation during the dry ball milling process. Aggregation into blocks improves the uniformity of the particle size of the powder, and the preparation process has high efficiency and low energy consumption. At the same time, after the prepared bismuth telluride micro-nano powder is prepared into a bismuth telluride block, the thermoelectric performance of the obtained bismuth telluride block is obviously improved, and the thermoelectric figure of merit zT is improved.
附图说明Description of drawings
图1是实施例1制备的碲化铋微纳米粉末的SEM图。FIG. 1 is an SEM image of the bismuth telluride micro-nano powder prepared in Example 1.
图2是实施例1制备的碲化铋微纳米粉末的粒径分布图。2 is a particle size distribution diagram of the bismuth telluride micro-nano powder prepared in Example 1.
图3是对比例1制备的碲化铋微纳米粉末的粒径分布图。3 is a particle size distribution diagram of the bismuth telluride micro-nano powder prepared in Comparative Example 1.
图4是对比例2制备的碲化铋微纳米粉末的粒径分布图。4 is a particle size distribution diagram of bismuth telluride micro-nano powder prepared in Comparative Example 2.
具体实施方式Detailed ways
下面就本发明的具体实施方式作进一步说明。The specific embodiments of the present invention will be further described below.
如无特别说明,本发明中所采用的原料均可从市场上购得或是本领域常用的,如无特别说明,下述实施例中的方法均为本领域的常规方法。Unless otherwise specified, the raw materials used in the present invention can be purchased from the market or commonly used in the field. If not specified, the methods in the following examples are all conventional methods in the field.
本发明提供了一种碲化铋微纳米粉体材料的制备方法的实施方案,具体的为,将碲化铋的合金铸锭破碎成颗粒,置于球磨装置如球磨罐中,加乙酸乙酯干法球磨,出料、干燥,其中碲化铋与乙酸乙酯的质量比≥5:1。The present invention provides an embodiment of a preparation method of bismuth telluride micro-nano powder material, specifically, the bismuth telluride alloy ingot is broken into particles, placed in a ball milling device such as a ball milling tank, and ethyl acetate is added Dry ball milling, discharging and drying, wherein the mass ratio of bismuth telluride to ethyl acetate is ≥5:1.
在本发明提供的一些实施方案中,碲化铋合金铸锭的制备过程如下:按名义组成的摩尔计量比取Bi粉、Sb粉和Te粉,称量并混合均匀,密封于真空度小于2Pa内的真空石英管中,封管,然后以12~18℃/min的速率升温至780~800℃,保温1~1.5h,接着摇摆2~3h,摇摆频率为5~8rpm/min,摇摆角度60°~65°,然后冷却。In some embodiments provided by the present invention, the preparation process of the bismuth telluride alloy ingot is as follows: take Bi powder, Sb powder and Te powder according to the molar ratio of the nominal composition, weigh and mix them evenly, and seal them in a vacuum less than 2Pa In the vacuum quartz tube inside, seal the tube, then raise the temperature to 780-800°C at a rate of 12-18°C/min, keep it warm for 1-1.5h, then swing for 2-3h, the swing frequency is 5-8rpm/min, and the
优选的,合金铸锭的化学式为Bi0.5Sb1.5Te3,采用纯度为99.99%的Bi粉、Sb粉和Te粉制备。Preferably, the chemical formula of the alloy ingot is Bi 0.5 Sb 1.5 Te 3 , and it is prepared by using Bi powder, Sb powder and Te powder with a purity of 99.99%.
在本发明提供的一些实施方案中,碲化铋破碎后的颗粒的粒径为1~2mm。In some embodiments provided by the present invention, the particle size of the crushed bismuth telluride particles is 1-2 mm.
在本发明提供的一些实施方案中,碲化铋与乙酸乙酯的质量比为5~10:1,优选的如5:1、6:1、7:1、8:1、9:1、10:1。In some embodiments provided by the present invention, the mass ratio of bismuth telluride to ethyl acetate is 5-10:1, preferably such as 5:1, 6:1, 7:1, 8:1, 9:1, 10:1.
在本发明提供的一些实施方案中,球磨所用磨球与碲化铋的球料比为2~3:1。球磨时,投料顺序为:将碲化铋破碎颗粒按一定球料比称量至球磨罐中,投料顺序为先放磨球,再放碲化铋破碎颗粒,再加入乙酸乙酯,设置好球磨参数。In some embodiments provided by the present invention, the ball-to-material ratio of the balls used in the ball mill to the bismuth telluride is 2-3:1. During ball milling, the feeding sequence is: weigh the crushed bismuth telluride particles into the ball mill tank according to a certain ball-to-material ratio. parameter.
在本发明提供的一些实施方案中,磨球的大小为0.6~1.2mm;球磨转速为350~500rpm/min;单周期研磨时间为30~40min,研磨1~2h。优选的,在两个单周期研磨操作之间有一段时间间隔,间隔时间10~20min,优选的为10min。In some embodiments provided by the present invention, the size of the balls is 0.6-1.2 mm; the rotational speed of the ball mill is 350-500 rpm/min; the single-cycle grinding time is 30-40 minutes, and the grinding time is 1-2 hours. Preferably, there is an interval between two single-cycle grinding operations, and the interval is 10-20 minutes, preferably 10 minutes.
在本发明提供的一些实施方案中,干燥物料的方式为:将物料摊开后室温通风干燥,再加热至40~50℃干燥。优选的,室温通风干燥的风速为2~3m/s,干燥时间10~20min,加热干燥的时间为10~20min。In some embodiments provided by the present invention, the method of drying the material is: spreading the material, ventilating and drying at room temperature, and then heating to 40-50° C. for drying. Preferably, the wind speed of ventilation drying at room temperature is 2-3 m/s, the drying time is 10-20 min, and the heating drying time is 10-20 min.
本发明提供的一些实施方案中为通过上述的制备方法得到的碲化铋微纳米粉体材料。Some embodiments provided by the present invention are bismuth telluride micro-nano powder materials obtained by the above-mentioned preparation method.
本发明提供了一种提高碲化铋块体热电性能的方法的实施方案,具体的为碲化铋块体采用上述获得的碲化铋微纳米粉体材料真空热压烧结得到。The present invention provides an embodiment of a method for improving the thermoelectric performance of a bismuth telluride block, specifically, the bismuth telluride block is obtained by vacuum hot-pressing sintering of the bismuth telluride micro-nano powder material obtained above.
在本发明提供的一些实施方案中,真空热压烧结的压强为70~100MPa,烧结温度420~500℃,热压烧结时间60~120min。In some embodiments provided by the present invention, the pressure of vacuum hot-press sintering is 70-100 MPa, the sintering temperature is 420-500° C., and the hot-press sintering time is 60-120 min.
实施例1Example 1
(1)配料熔炼/材料准备:(1) Ingredients smelting/material preparation:
将纯度99.99%的Bi粉、Sb粉和Te粉按名义组成为Bi0.5Sb1.5Te3的化学计量比,称量并均匀混合好,密封于真空度小于2Pa内的真空石英管中,用氧炔焰对石英管进行封管处理,然后以15℃/min的速率升温至780℃,然后保温1h,接着摇摆2h,摇摆频率为5rpm/min,摇摆角度60°,采用随炉冷却方式冷凝,得到碲化铋合金铸锭;The Bi powder, Sb powder and Te powder with a purity of 99.99% are composed into the stoichiometric ratio of Bi 0.5 Sb 1.5 Te 3 according to the name, weighed and mixed evenly, sealed in a vacuum quartz tube with a vacuum degree of less than 2 Pa, and used oxygen The alkyne flame seals the quartz tube, then raises the temperature to 780°C at a rate of 15°C/min, and then keeps it warm for 1h, then swings for 2h, the swing frequency is 5rpm/min, and the swing angle is 60°. It is condensed by furnace cooling. Obtain bismuth telluride alloy ingot;
(2)破碎颗粒:(2) Broken particles:
将所得合金铸锭在鄂式破碎机进行破碎,鄂板材料为锰钢,得到粒径1~2mm内的粗料颗粒;The obtained alloy ingot is crushed in a jaw crusher, and the material of the jaw plate is manganese steel to obtain coarse particles with a particle size of 1 to 2 mm;
(3)干法球磨:(3) Dry ball milling:
将粗料颗粒投放到球磨罐中,球磨罐内装有直径1mm的不锈钢磨球,球料质量比为1:1,向粗料颗粒内加入乙酸乙酯,乙酸乙酯与粗料颗粒的质量比为1:5,在转速400rpm/min,占空比为1:1,单周期磨30min下连续研磨2个周期1h;Put the coarse material particles into the ball milling tank, the ball milling tank is equipped with stainless steel grinding balls with a diameter of 1mm, the mass ratio of balls to materials is 1:1, add ethyl acetate to the coarse material particles, the mass ratio of ethyl acetate to coarse material particles 1:5, at a speed of 400rpm/min, a duty ratio of 1:1, continuous grinding for 2 cycles of 1h under a single-cycle grinding for 30min;
(4)乙酸乙酯分离:(4) Ethyl acetate separation:
球磨结束后出料,将所得出料置于850um筛网上进行磨球和粉体的分离,然后将分离后的粉体置于通风口处初步干燥10min,通风速率2m/s,然后再放入烘箱50℃烘干10min,完全除去乙酸乙酯,得到粒径分布均匀的碲化铋微纳米粉体。After the ball milling is finished, the material is discharged, and the resulting material is placed on an 850um sieve to separate the grinding ball and the powder, and then the separated powder is placed in the vent for preliminary drying for 10 minutes, and the ventilation rate is 2m/s, and then put into the Dry in an oven at 50°C for 10 minutes to completely remove ethyl acetate, and obtain bismuth telluride micro-nano powder with uniform particle size distribution.
所制备的碲化铋微纳米粉体的SEM图如图1所示,粒径分布图如图2所示。从图中可以看出,所得碲化铋微纳米粉体无聚集结块,粒径分布均匀,处于微纳米范围内,其中D(50)为1.2μm左右,D(100)为13.6μm左右。The SEM image of the prepared bismuth telluride micro-nano powder is shown in FIG. 1 , and the particle size distribution graph is shown in FIG. 2 . It can be seen from the figure that the obtained bismuth telluride micro-nano powder has no aggregation and agglomeration, and the particle size distribution is uniform in the micro-nano range, wherein D(50) is about 1.2 μm, and D(100) is about 13.6 μm.
实施例2Example 2
(1)配料熔炼/材料准备:与实施例1相同;(1) batching smelting/material preparation: same as
(2)破碎研磨:与实施例1相同;(2) crushing and grinding: same as
将所得合金铸锭在鄂式破碎机中破碎,鄂板材料为锰钢,得到粒径1~2mm内的粗料;The obtained alloy ingot is crushed in a jaw crusher, and the material of the jaw plate is manganese steel to obtain a coarse material with a particle size of 1 to 2 mm;
(3)干法球磨:(3) Dry ball milling:
将粗料颗粒投放到球磨罐中,球磨罐内装有直径1mm的不锈钢磨球,球料质量比为1:1,向粗料颗粒内加入乙酸乙酯,乙酸乙酯与粗料颗粒的质量比为1:10,在转速400rpm/min,占空比为1:1,单周期磨40min下连续研磨2个周期80min;Put the coarse material particles into the ball milling tank, the ball milling tank is equipped with stainless steel grinding balls with a diameter of 1mm, the mass ratio of balls to materials is 1:1, add ethyl acetate to the coarse material particles, the mass ratio of ethyl acetate to coarse material particles 1:10, at a speed of 400rpm/min, a duty ratio of 1:1, continuous grinding for 2 cycles of 80 minutes under a single-cycle grinding of 40 minutes;
(4)分散剂分离:与实施例1相同。(4) Separation of dispersant: same as Example 1.
所得碲化铋微纳米粉体无聚集结块,粒径分布均匀,处于微纳米范围内,其中D(50)为1.02μm左右,D(100)为12.8μm左右。The obtained bismuth telluride micro-nano powder has no aggregation and agglomeration, and the particle size distribution is uniform in the micro-nano range, wherein D(50) is about 1.02 μm, and D(100) is about 12.8 μm.
实施例3Example 3
与实施例1不同之处为,在步骤(3)的干法球磨过程中,两个单周期研磨中间间隔10min。The difference from Example 1 is that in the dry ball milling process of step (3), the interval between two single-cycle milling is 10 minutes.
所得碲化铋微纳米粉体无聚集结块,粒径分布均匀,处于微纳米范围内,其中D(50)为1.1μm左右,D(100)为13.2μm左右。The obtained bismuth telluride micro-nano powder has no aggregation and agglomeration, and the particle size distribution is uniform in the micro-nano range, wherein D(50) is about 1.1 μm, and D(100) is about 13.2 μm.
对比例1Comparative example 1
与实施例1不同之处为,制备过程中未加入乙酸乙酯,所得粉体的粒径分布图如图3所示。The difference from Example 1 is that no ethyl acetate was added during the preparation process, and the particle size distribution diagram of the obtained powder is shown in FIG. 3 .
从图2看出,所制备的碲化铋微纳米粉体粒径分布均匀性降低,出现聚集结块,其中D(50)为7μm左右,D(100)为63μm左右。It can be seen from Fig. 2 that the particle size distribution uniformity of the prepared bismuth telluride micro-nano powder is reduced, and aggregation and agglomeration appear, wherein D(50) is about 7 μm, and D(100) is about 63 μm.
对比例2Comparative example 2
与实施例1不同之处为,制备过程中以酒精替代乙酸乙酯,粉体的粒径分布图如图4所示。The difference from Example 1 is that ethyl acetate is replaced by alcohol in the preparation process, and the particle size distribution diagram of the powder is shown in FIG. 4 .
从图中可以看出,所得碲化铋微纳米粉体出现聚集结块,其中D(50)为5.1μm左右,D(100)为20μm左右。It can be seen from the figure that the obtained bismuth telluride micro-nano powder is agglomerated, wherein D(50) is about 5.1 μm, and D(100) is about 20 μm.
将上述各实施例和对比例制备的碲化铋微纳米粉体(三个平行样)送入模具中,在压强100MPa、烧结温度500℃下保持100min,得到碲化铋块体,测试并计算室温298K下的碲化铋块体的zT值,结果如下表1所示。Put the bismuth telluride micro-nano powder (three parallel samples) prepared in the above-mentioned examples and comparative examples into a mold, keep it at a pressure of 100 MPa and a sintering temperature of 500°C for 100 minutes to obtain a bismuth telluride block, test and calculate The zT value of the bismuth telluride bulk at room temperature 298K, the results are shown in Table 1 below.
表1碲化铋块体的热电优值结果Table 1 Thermoelectric figure of merit results of bismuth telluride bulk
从上表中可以看出,当干法球磨过程中不添加乙酸乙酯等任何助分散试剂,如对比例1所示,由于出现结块,且粒径较大,分布不均,所得碲化铋块体的热电优值为0.917(均值),同时块体的zT值的波动性较大。而引入乙酸乙酯后,如实施例1和实施例2所示,zT值得到提升,且zT值的波动性降低,当单周期研磨间隔一段时间时,如实施例3所示,zT值的波动性进一步降低。而采用乙醇替代乙酸乙酯时,如对比例2所示,zT值相对对比例1稍有提升,但是波动性仍较大,效果低于乙酸乙酯。这可能是因为乙醇更容易挥发,而且渗透性等也不如乙酸乙酯所致,这表明湿法球磨所用的球磨介质更倾向于提供的是一种分散场合的作用,将其在干法球磨中使用时达不到理想的效果。It can be seen from the above table that when no ethyl acetate and other dispersing agents are added during the dry ball milling process, as shown in Comparative Example 1, due to agglomeration, large particle size and uneven distribution, the obtained telluride The thermoelectric figure of merit of the bismuth block is 0.917 (mean value), and the zT value of the block fluctuates greatly. And after introducing ethyl acetate, as shown in
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