JPH01226723A - Method for synthesizing particulate oxide raw material - Google Patents
Method for synthesizing particulate oxide raw materialInfo
- Publication number
- JPH01226723A JPH01226723A JP5458888A JP5458888A JPH01226723A JP H01226723 A JPH01226723 A JP H01226723A JP 5458888 A JP5458888 A JP 5458888A JP 5458888 A JP5458888 A JP 5458888A JP H01226723 A JPH01226723 A JP H01226723A
- Authority
- JP
- Japan
- Prior art keywords
- soln
- water
- spray
- dielectric constant
- solution
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
- 239000002994 raw material Substances 0.000 title claims abstract description 11
- 230000002194 synthesizing effect Effects 0.000 title claims abstract description 5
- 238000000034 method Methods 0.000 title claims description 22
- MUBZPKHOEPUJKR-UHFFFAOYSA-N Oxalic acid Chemical compound OC(=O)C(O)=O MUBZPKHOEPUJKR-UHFFFAOYSA-N 0.000 claims abstract description 22
- 229910052751 metal Inorganic materials 0.000 claims abstract description 17
- 239000002184 metal Substances 0.000 claims abstract description 17
- 239000002887 superconductor Substances 0.000 claims abstract description 8
- 235000006408 oxalic acid Nutrition 0.000 claims abstract description 5
- ATRRKUHOCOJYRX-UHFFFAOYSA-N Ammonium bicarbonate Chemical compound [NH4+].OC([O-])=O ATRRKUHOCOJYRX-UHFFFAOYSA-N 0.000 claims abstract description 4
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 claims abstract description 4
- 235000012501 ammonium carbonate Nutrition 0.000 claims abstract description 4
- 239000001099 ammonium carbonate Substances 0.000 claims abstract description 4
- VBIXEXWLHSRNKB-UHFFFAOYSA-N ammonium oxalate Chemical compound [NH4+].[NH4+].[O-]C(=O)C([O-])=O VBIXEXWLHSRNKB-UHFFFAOYSA-N 0.000 claims abstract description 4
- 229910052797 bismuth Inorganic materials 0.000 claims abstract description 4
- 229910052791 calcium Inorganic materials 0.000 claims abstract description 4
- 229910052802 copper Inorganic materials 0.000 claims abstract description 4
- 239000010949 copper Substances 0.000 claims abstract description 4
- 238000002156 mixing Methods 0.000 claims abstract description 4
- 229910052712 strontium Inorganic materials 0.000 claims abstract description 4
- 239000000243 solution Substances 0.000 claims description 15
- 239000000203 mixture Substances 0.000 claims description 12
- 239000003960 organic solvent Substances 0.000 claims description 10
- 239000007864 aqueous solution Substances 0.000 claims description 4
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 claims description 3
- JCXGWMGPZLAOME-UHFFFAOYSA-N bismuth atom Chemical compound [Bi] JCXGWMGPZLAOME-UHFFFAOYSA-N 0.000 claims description 3
- 239000011575 calcium Substances 0.000 claims description 3
- CIOAGBVUUVVLOB-UHFFFAOYSA-N strontium atom Chemical compound [Sr] CIOAGBVUUVVLOB-UHFFFAOYSA-N 0.000 claims description 3
- 239000012266 salt solution Substances 0.000 claims 1
- 239000002245 particle Substances 0.000 abstract description 17
- 239000002904 solvent Substances 0.000 abstract description 9
- 239000002244 precipitate Substances 0.000 abstract description 6
- 150000003839 salts Chemical class 0.000 abstract description 6
- 238000001694 spray drying Methods 0.000 abstract description 6
- 239000013078 crystal Substances 0.000 abstract description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 5
- 229910002651 NO3 Inorganic materials 0.000 abstract description 3
- NHNBFGGVMKEFGY-UHFFFAOYSA-N Nitrate Chemical compound [O-][N+]([O-])=O NHNBFGGVMKEFGY-UHFFFAOYSA-N 0.000 abstract description 3
- 230000007423 decrease Effects 0.000 abstract description 3
- 239000000463 material Substances 0.000 abstract description 3
- QTBSBXVTEAMEQO-UHFFFAOYSA-M Acetate Chemical compound CC([O-])=O QTBSBXVTEAMEQO-UHFFFAOYSA-M 0.000 abstract description 2
- 239000000523 sample Substances 0.000 description 9
- 239000010419 fine particle Substances 0.000 description 8
- 239000012071 phase Substances 0.000 description 8
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 description 6
- 150000004703 alkoxides Chemical class 0.000 description 5
- 239000011259 mixed solution Substances 0.000 description 4
- 239000000843 powder Substances 0.000 description 4
- 239000007921 spray Substances 0.000 description 4
- 230000015572 biosynthetic process Effects 0.000 description 3
- 238000000975 co-precipitation Methods 0.000 description 3
- 238000001035 drying Methods 0.000 description 3
- 238000010298 pulverizing process Methods 0.000 description 3
- 239000012488 sample solution Substances 0.000 description 3
- 239000012047 saturated solution Substances 0.000 description 3
- 238000005118 spray pyrolysis Methods 0.000 description 3
- 238000003786 synthesis reaction Methods 0.000 description 3
- 238000005979 thermal decomposition reaction Methods 0.000 description 3
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 2
- 238000001354 calcination Methods 0.000 description 2
- 150000004649 carbonic acid derivatives Chemical class 0.000 description 2
- 238000011109 contamination Methods 0.000 description 2
- 238000002425 crystallisation Methods 0.000 description 2
- 230000008025 crystallization Effects 0.000 description 2
- 238000001704 evaporation Methods 0.000 description 2
- 238000010304 firing Methods 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 238000001556 precipitation Methods 0.000 description 2
- 239000011164 primary particle Substances 0.000 description 2
- 238000003746 solid phase reaction Methods 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 229910001111 Fine metal Inorganic materials 0.000 description 1
- 238000002441 X-ray diffraction Methods 0.000 description 1
- 238000004458 analytical method Methods 0.000 description 1
- 238000000889 atomisation Methods 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000003153 chemical reaction reagent Substances 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- -1 concentration Substances 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- AEDZKIACDBYJLQ-UHFFFAOYSA-N ethane-1,2-diol;hydrate Chemical compound O.OCCO AEDZKIACDBYJLQ-UHFFFAOYSA-N 0.000 description 1
- IDGUHHHQCWSQLU-UHFFFAOYSA-N ethanol;hydrate Chemical compound O.CCO IDGUHHHQCWSQLU-UHFFFAOYSA-N 0.000 description 1
- 230000001747 exhibiting effect Effects 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 239000011361 granulated particle Substances 0.000 description 1
- 238000000227 grinding Methods 0.000 description 1
- 230000003301 hydrolyzing effect Effects 0.000 description 1
- 229910001960 metal nitrate Inorganic materials 0.000 description 1
- 239000004570 mortar (masonry) Substances 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 238000000197 pyrolysis Methods 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 239000007858 starting material Substances 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 238000000859 sublimation Methods 0.000 description 1
- 230000008022 sublimation Effects 0.000 description 1
- 238000001308 synthesis method Methods 0.000 description 1
- 230000007704 transition Effects 0.000 description 1
- 239000011882 ultra-fine particle Substances 0.000 description 1
Landscapes
- Inorganic Compounds Of Heavy Metals (AREA)
- Superconductors And Manufacturing Methods Therefor (AREA)
Abstract
Description
【発明の詳細な説明】
「産業上の利用分野」
本発明は酸化物高温超伝導体の原料合成法に関するもの
である。DETAILED DESCRIPTION OF THE INVENTION "Field of Industrial Application" The present invention relates to a method for synthesizing raw materials for oxide high temperature superconductors.
1°「i技術及びその問題点」
従来、酸化物高温超伝導材料の化学的手法による合成法
としては、(1)固相°反応法、(2)蒸発法、(3)
共沈法、(4)金属アルコキシド法等が知られている。1° "i-Technology and its Problems" Conventionally, chemical methods for synthesizing oxide high-temperature superconducting materials include (1) solid phase reaction method, (2) evaporation method, and (3)
Co-precipitation method, (4) metal alkoxide method, etc. are known.
しかして上述(1)の固相反応法は、酸化物、炭酸塩等
の形でビスマス、ストロンチウム、カルシウム、銅等の
試薬を乳鉢、ボールミル等で混合し、仮焼、粉砕の過程
を繰り返すことによって目的とする相の均質な粉体を得
ようとするものであるが、生成粒子径は一般に大きくな
り、粉砕過程において試料汚染の問題が避けられない。However, the solid phase reaction method described in (1) above involves mixing reagents such as bismuth, strontium, calcium, copper, etc. in the form of oxides, carbonates, etc. in a mortar, ball mill, etc., and repeating the steps of calcining and pulverizing. Although this method attempts to obtain a powder with the desired phase homogeneity, the resulting particle size generally increases, and the problem of sample contamination during the grinding process is unavoidable.
(2)の蒸発法は、所定の組成比の金属塩の混合溶液を
加熱して、溶媒を除去することにより乾燥試料を得、こ
れを粉砕、焼成することにより原料粉末を得る方法であ
るが、溶媒除去に際して各成分の溶解度差、分解・昇華
等の影響で組成の不均一性や組成全体の変動が生じやす
いことや、粉砕工程が必要かつ試料汚染の問題が起こる
。The evaporation method (2) is a method in which a dry sample is obtained by heating a mixed solution of metal salts with a predetermined composition ratio to remove the solvent, and a raw material powder is obtained by pulverizing and calcining this. When removing the solvent, non-uniformity of the composition and fluctuations in the overall composition tend to occur due to differences in solubility of each component, decomposition, sublimation, etc., and a pulverization process is required, resulting in the problem of sample contamination.
(3)の共沈法は、金属酸塩の混合溶液に沈澱剤を加え
て単塩または複塩の沈欄粒子を形成させ、これをろ過、
乾燥、焼成することにより比較的容易に1μm以下〜数
μmの微粒子原料を合成することが可能である。しかし
、多成分系の場合、完全同時沈澱は理論上不可能であり
、希望する組成比の沈澱を得ることは困難である。In the coprecipitation method (3), a precipitant is added to a mixed solution of metal salts to form precipitated particles of a single or double salt, which are then filtered,
By drying and firing, it is possible to synthesize fine particle raw materials with a size of 1 μm or less to several μm relatively easily. However, in the case of a multi-component system, complete simultaneous precipitation is theoretically impossible, and it is difficult to obtain a precipitate with a desired composition ratio.
(4)の金属アルコキシド法は、金属アルコキシド溶液
の加水分解により数10nm程度の超微粒子を合成する
ことが可能であるが、出発原料の金属アルコキシドが非
常に高価であり、多成分系の場合は、それぞれの金属の
溶解度が実用上問題がない程度に高い有機溶媒が必要と
なり、また複合アルコキシドの合成が困難であるため、
沈澱粒子の組成の不均一性に関して共沈法と同様の欠点
を持つ。In the metal alkoxide method (4), it is possible to synthesize ultrafine particles of several tens of nanometers by hydrolyzing a metal alkoxide solution, but the metal alkoxide as a starting material is very expensive, and in the case of a multicomponent system, , an organic solvent is required in which the solubility of each metal is high enough to cause no practical problems, and synthesis of composite alkoxides is difficult.
It has the same drawbacks as the coprecipitation method regarding the non-uniformity of the composition of precipitated particles.
「発明の概要」
本発明はこれらの欠点を解消し、微粒で均質な、低温で
の合成が可能で易焼結性を有する、酸化物高温超伝導体
用の合成原料を提供することを目的とする。"Summary of the Invention" The purpose of the present invention is to eliminate these drawbacks and provide a synthetic raw material for oxide high-temperature superconductors that is fine-grained and homogeneous, can be synthesized at low temperatures, and has easy sinterability. shall be.
本発明者は、酸化物高温超伝導体の原料合成方法の研究
を進める過程で、金属蓚酸塩沈澱生成時に■金属の硝酸
塩等の水溶液■蓚酸または蓚酸アンモニウムまたは炭酸
アンモニウムの両方または一方に、溶媒としてエタノー
ル等の誘電率が水より低い水溶性有機溶媒を添加するこ
とにより、■と■の混合時に生成する沈澱が微細化し、
これを噴霧乾燥することにより、出発溶液のpH1各成
分の仕込量の調節等の操作を必要とせずに容易に熱分解
の可能な微粒子を生じせしめることを見いだし本発明に
到達した。In the process of researching a raw material synthesis method for oxide high-temperature superconductors, the present inventor discovered that when metal oxalate precipitates are formed, a solvent is added to an aqueous solution of oxalic acid, ammonium oxalate, and/or ammonium carbonate. By adding a water-soluble organic solvent such as ethanol with a dielectric constant lower than that of water, the precipitate formed when mixing ■ and ■ becomes finer.
The inventors have discovered that by spray-drying this, fine particles that can be easily thermally decomposed can be produced without requiring operations such as adjusting the amount of each component at pH 1 of the starting solution, and have thus arrived at the present invention.
すなわち本発明は、■目的の酸化物高温超伝導体組成と
なるように酢酸塩、硝酸塩等の金属塩混合溶液を調製し
■これに蓚酸または蓚酸アンモニウムまたは炭酸アンモ
ニウム溶液を6口えるが、その際に誘電率50以下の水
溶性有機溶媒の少なくとも一種以上を含む水溶液を■、
■の両方または一方(こ加え、微粒の金属蓚酸塩沈澱を
含んだ溶液を合成する。That is, the present invention involves: (1) preparing a mixed solution of metal salts such as acetate and nitrate so as to have the desired composition of an oxide high-temperature superconductor; In particular, an aqueous solution containing at least one type of water-soluble organic solvent with a dielectric constant of 50 or less,
In addition to both or one of (2), a solution containing fine metal oxalate precipitates is synthesized.
さらに、この溶液を適当な条件下で噴霧乾燥することに
より容易に熱分解の可能な粒子を得、または噴霧熱分解
し、熱分解後の粒子径2〜3μm以下の微粒子原料粉末
を得ることを特徴とする。以下に本発明の詳細な説明す
る。Furthermore, by spray drying this solution under appropriate conditions, particles that can be easily thermally decomposed can be obtained, or by spray pyrolysis, it is possible to obtain fine particle raw material powder with a particle size of 2 to 3 μm or less after thermal decomposition. Features. The present invention will be explained in detail below.
まず、金属塩混合溶液及び蓚酸または蓚酸アンモニウム
または炭酸アンモニウムに加える水溶性有機溶媒の量は
、飽和溶液に対して全溶液中の水:有機溶媒比が1=5
〜lO:1、また飽和溶液:溶媒比が1:1〜1:10
とする。水溶性有機溶媒を加える理由は、第一に金属蓚
酸塩の溶解度を減少させ結晶核の発生数を増大させるた
め、第二に溶液の誘電率を減少させイオン会合体を形成
しやすくするためであり、いずれも結晶核発生数の増大
と沈澱粒子の微粒化に寄与する。ここで、水の対有機溶
媒比がこれより大きいと、溶解度と誘電率の減少程度が
小さくなり、逆にこれより小さいと処理中の晶析が起こ
りやすくなる。First, the amount of water-soluble organic solvent added to the metal salt mixed solution and oxalic acid, ammonium oxalate, or ammonium carbonate is such that the water:organic solvent ratio in the total solution is 1 = 5 with respect to the saturated solution.
~lO:1, and the saturated solution:solvent ratio is 1:1 to 1:10
shall be. The reasons for adding a water-soluble organic solvent are, firstly, to reduce the solubility of metal oxalate and increase the number of crystal nuclei, and secondly, to reduce the dielectric constant of the solution and facilitate the formation of ionic aggregates. Both contribute to an increase in the number of crystal nuclei generated and to the atomization of precipitated particles. Here, if the ratio of water to organic solvent is larger than this, the degree of decrease in solubility and dielectric constant will be small, whereas if it is smaller than this, crystallization will easily occur during treatment.
また飽和溶液の対溶媒比がこれより大きいとり過ぎるた
め、噴霧乾燥後のサイクロンによる捕集が困難となり他
の回収方法が必要になると製造能率が低下するためであ
る。使用される水溶性有機溶媒の例と物性を第1表に示
す。In addition, if the ratio of the saturated solution to the solvent is too high, it becomes difficult to collect using a cyclone after spray drying, and if another collection method is required, the production efficiency will decrease. Table 1 shows examples and physical properties of the water-soluble organic solvents used.
沈澱粒子の微細・均質化のために、■と■の混合は撹拌
機等を用いて激しく撹拌した状趨で速やかに行う必要が
ある。In order to make the precipitated particles fine and homogeneous, it is necessary to mix (1) and (2) quickly with vigorous stirring using a stirrer or the like.
噴霧乾燥の条件としては、試料の乾燥が速やかに行われ
、造粒粒子が捕集可能な大きさでできるだけ微粒になる
ように乾燥チャンバ内への試料入口・出口温度、噴霧空
気量、試料送液量、さらここは収率よく呻子を捕集でき
るようにサイクロン入口での吸引空気量を調節する必要
がある。これらの条件は試料溶液の濃度、乾燥チャンバ
の容積、サイクロンの形状等により最適条件が異なる。The conditions for spray drying include sample inlet and outlet temperatures, atomizing air volume, and sample delivery so that the sample dries quickly and the granulated particles are as fine as possible with a collectable size. It is necessary to adjust the amount of liquid and the amount of air sucked at the cyclone inlet so that the larvae can be collected with good yield. The optimum conditions for these conditions differ depending on the concentration of the sample solution, the volume of the drying chamber, the shape of the cyclone, etc.
熱分解温度は試料の組成により異なるが、例えば
B14Sr3Ca3Cu40yの場合820℃3時間の
焼成で超伝導相の結晶構造を示すことがX線回折により
確かめられた(第1図)。Although the thermal decomposition temperature varies depending on the composition of the sample, for example, in the case of B14Sr3Ca3Cu40y, it was confirmed by X-ray diffraction that it exhibited a superconducting phase crystal structure after firing at 820°C for 3 hours (Figure 1).
噴霧熱分解の場合は、600〜1800℃程度の炉中や
プラズマ、化学炎等の高温条件下に導入する。この場合
も温度、噴霧液滴径、滞留時間等の噴霧に関する諸条件
は試料溶液の量、濃度、溶媒の種類、処理容器の形状、
試料の捕集方法等の条件に応じて最適条件を選ぶ必要が
ある。また得られた粒子の熱分解−結晶化が超伝導相合
成に至っていない場合は適当な加熱処理を行う。In the case of spray pyrolysis, it is introduced into a furnace at about 600 to 1800°C, or under high temperature conditions such as plasma or chemical flame. In this case as well, various conditions related to spraying, such as temperature, spray droplet diameter, and residence time, include the amount of sample solution, concentration, type of solvent, shape of processing container, etc.
It is necessary to select optimal conditions depending on conditions such as the sample collection method. Further, if the thermal decomposition and crystallization of the obtained particles have not led to superconducting phase synthesis, an appropriate heat treatment is performed.
噴霧乾燥−熱分解、噴霧熱分解答々の過程を経て得られ
た微粒子の粒子径は1次粒子径2〜3゛μm以下の微粒
子であり、分析電子顕微鏡によるバルク及び微小領域の
組成分析結果から、ストイキオメトリ−が保たれかつ均
一組成であることが確認された。The particle size of the fine particles obtained through the processes of spray drying-pyrolysis and spray pyrolysis is fine particles with a primary particle size of 2 to 3 μm or less, and the composition analysis results of the bulk and micro regions using an analytical electron microscope. It was confirmed that the stoichiometry was maintained and the composition was uniform.
このようにして得られた微粒子は低温で超伝導相が合成
され、微粒で易焼結性を有する。The thus obtained fine particles have a superconducting phase synthesized at low temperatures, and are fine and easily sinterable.
また他の化学°的な合成法に比べて途中での沈澱条件の
コントロールの必要や組成変動の心配もなく、対象とす
る元素や組成を変えた場合への応用も広い。また処理装
置のスケールアップによる量産化が容易である。In addition, compared to other chemical synthesis methods, there is no need to control precipitation conditions during the process and there is no need to worry about compositional fluctuations, and it can be widely applied to cases where the target element or composition is changed. Moreover, mass production by scaling up the processing equipment is easy.
「実施例」 次に実施例を挙げて本発明を説明する。"Example" Next, the present invention will be explained with reference to Examples.
(実施例1)
0.02M /IのBiaSr3CaaCu40yの硝
酸塩溶液5001を調製し、これに2倍体積の水−エタ
ノール=1:1溶液を混合した。0.5mol/ Iの
溶液を混合した。室温でこれらを急激に混合撹拌し、得
られた溶液を以下の条件で噴霧乾燥した。2流体ノズル
式噴霧、乾燥チャンバ入口温度200℃、出口温度10
0℃、噴霧空気圧1.5Kg/cm2、吸引空気量、0
.40m3/ min、試料送液量10cm3/ m
ino 捕集粒子は径2〜5μmの凝集粒子で、これ
を820℃3時間熱処理することにより、2〜3μm以
下の超伝導相結晶構造を示す粒子が得られた。この原料
を用いて作成された焼結体は超伝導転移温度Tc= 9
4Kを示し、理論密度の95%まで緻密化した。(Example 1) A nitrate solution 5001 of BiaSr3CaaCu40y of 0.02 M/I was prepared, and twice the volume of water-ethanol = 1:1 solution was mixed therein. A solution of 0.5 mol/I was mixed. These were rapidly mixed and stirred at room temperature, and the resulting solution was spray-dried under the following conditions. Two-fluid nozzle spray, drying chamber inlet temperature 200℃, outlet temperature 10
0℃, spray air pressure 1.5Kg/cm2, suction air amount, 0
.. 40m3/min, sample liquid flow rate 10cm3/m
The ino collection particles were agglomerated particles with a diameter of 2 to 5 μm, and by heat-treating them at 820° C. for 3 hours, particles exhibiting a superconducting phase crystal structure of 2 to 3 μm or less were obtained. The sintered body created using this raw material has a superconducting transition temperature Tc = 9
4K and was densified to 95% of the theoretical density.
(実施例2)
実施例1の金属硝酸塩水溶液及び蓚酸溶液に加える有機
溶媒としてエチレングリコールを用いた。水−エチレン
グリコール溶液の濃度は水: エチレングリコール=3
:1とした。(Example 2) Ethylene glycol was used as an organic solvent to be added to the metal nitrate aqueous solution and oxalic acid solution of Example 1. The concentration of water-ethylene glycol solution is water: ethylene glycol = 3
:1.
噴霧乾燥条件は実施例1と同様、但し試料溶液温度は5
0℃に保った。噴霧乾燥粒子を820℃3時間の熱処理
することにより、第1図に示したと同様の超伝導相の結
晶相が得られた。The spray drying conditions were the same as in Example 1, except that the sample solution temperature was 5.
It was kept at 0°C. By heat-treating the spray-dried particles at 820° C. for 3 hours, a superconducting crystalline phase similar to that shown in FIG. 1 was obtained.
粒子径は2〜3μmであった。The particle size was 2-3 μm.
(実施例3)
実施例1と同様の条件で調製した金属蓚酸塩を:含む溶
液を900℃に保った電気炉の反応管中に噴霧し、サイ
クロン及びフィルタにて生成粒子を捕集した。1次粒子
径、は0.5〜2μmであった。この粒子はビスマス、
ストロンチウム、カルシウム、銅の酸化物及び炭酸塩で
あり、さらに800℃1時間の熱処理により超伝導相の
結晶相を示した。(Example 3) A solution containing metal oxalate prepared under the same conditions as in Example 1 was sprayed into a reaction tube of an electric furnace kept at 900°C, and generated particles were collected using a cyclone and a filter. The primary particle size was 0.5 to 2 μm. This particle is bismuth,
These are oxides and carbonates of strontium, calcium, and copper, and after being heat-treated at 800° C. for 1 hour, they exhibited a superconducting crystalline phase.
「発明の効果」
本発明は以上説明したように、信性に比べてより低温で
合成可能な、易焼結性の、酸化物高温超伝導体の均−組
成の微粒子原料を容易に製造するものであり、臨界電流
密度の向上など超伝導材料の実用化を促進するものとし
て期待される。"Effects of the Invention" As explained above, the present invention can easily produce a fine particle raw material with a homogeneous composition for an oxide high temperature superconductor that can be synthesized at a lower temperature than the conventional one, is easy to sinter, and is easy to sinter. This is expected to promote the practical application of superconducting materials, such as improving critical current density.
第1図は本方法により生成した超伝導相微粒子の粉末X
線回折パターンで、図中の(000)は各回折ピークに
相当する面指数を表す。Figure 1 shows superconducting phase fine particle powder X produced by this method.
In the line diffraction pattern, (000) in the figure represents the plane index corresponding to each diffraction peak.
Claims (1)
または炭酸アンモニウム溶液とを、誘電率50以下の水
溶性有機溶媒の少なくとも一種以上を含む水溶液中で混
合し、これを噴霧乾燥−熱分解または噴霧熱分解するこ
とによる、酸化物高温超伝導体に用いる微粒子原料の合
成法。[Claims] A metal salt solution such as bismuth, strontium, calcium, copper, etc. and an oxalic acid or ammonium oxalate solution or an ammonium carbonate solution are mixed in an aqueous solution containing at least one water-soluble organic solvent having a dielectric constant of 50 or less. A method for synthesizing particulate raw materials for use in oxide high-temperature superconductors by mixing and spray-drying-pyrolyzing or spray-pyrolyzing the mixture.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP5458888A JPH01226723A (en) | 1988-03-08 | 1988-03-08 | Method for synthesizing particulate oxide raw material |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP5458888A JPH01226723A (en) | 1988-03-08 | 1988-03-08 | Method for synthesizing particulate oxide raw material |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH01226723A true JPH01226723A (en) | 1989-09-11 |
JPH0572331B2 JPH0572331B2 (en) | 1993-10-12 |
Family
ID=12974879
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP5458888A Granted JPH01226723A (en) | 1988-03-08 | 1988-03-08 | Method for synthesizing particulate oxide raw material |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH01226723A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH03140472A (en) * | 1989-10-27 | 1991-06-14 | Agency Of Ind Science & Technol | Production of built-up film of oxide fine particle |
FR2659961A1 (en) * | 1990-03-23 | 1991-09-27 | Rhone Poulenc Chimie | PROCESS FOR THE PREPARATION OF SUPERCONDUCTING PHASES BASED ON BISMUTH, STRONTIUM, CALCIUM AND COPPER AND A STABILIZING ELEMENT. |
-
1988
- 1988-03-08 JP JP5458888A patent/JPH01226723A/en active Granted
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH03140472A (en) * | 1989-10-27 | 1991-06-14 | Agency Of Ind Science & Technol | Production of built-up film of oxide fine particle |
JPH0774454B2 (en) * | 1989-10-27 | 1995-08-09 | 工業技術院長 | Manufacturing method of oxide fine particle deposition film |
FR2659961A1 (en) * | 1990-03-23 | 1991-09-27 | Rhone Poulenc Chimie | PROCESS FOR THE PREPARATION OF SUPERCONDUCTING PHASES BASED ON BISMUTH, STRONTIUM, CALCIUM AND COPPER AND A STABILIZING ELEMENT. |
Also Published As
Publication number | Publication date |
---|---|
JPH0572331B2 (en) | 1993-10-12 |
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