JPH04202099A - Production of alkali titanate whisker - Google Patents
Production of alkali titanate whiskerInfo
- Publication number
- JPH04202099A JPH04202099A JP33005090A JP33005090A JPH04202099A JP H04202099 A JPH04202099 A JP H04202099A JP 33005090 A JP33005090 A JP 33005090A JP 33005090 A JP33005090 A JP 33005090A JP H04202099 A JPH04202099 A JP H04202099A
- Authority
- JP
- Japan
- Prior art keywords
- alkali
- source
- titanate
- mixture
- aspect ratio
- 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
Landscapes
- Inorganic Compounds Of Heavy Metals (AREA)
- Crystals, And After-Treatments Of Crystals (AREA)
Abstract
Description
【発明の詳細な説明】
[産業上の利用分野]
本発明はチタン酸アルカリウィスカー、詳しくは例えば
プラスチックス等の補強材、イオン吸着剤、イオン交換
材、分子吸着材、摩擦材、?濾過材、触媒担体、断熱材
その他種々の用途に供される繊維状特にアスペクト比の
高い繊維状チタン酸アルカリウィスカーの製造方法に関
する。[Detailed Description of the Invention] [Field of Industrial Application] The present invention relates to alkali titanate whiskers, specifically reinforcing materials such as plastics, ion adsorbents, ion exchange materials, molecular adsorbents, friction materials, etc. The present invention relates to a method for producing fibrous alkali titanate whiskers, particularly fibrous alkali titanate whiskers with a high aspect ratio, which are used as filtration media, catalyst carriers, heat insulating materials, and various other uses.
[従来の技術]
従来のチタン酸アルカリの製造方法としては、例えば原
料混合物を焼成し、固相反応により合成する焼成法(特
開昭53−26298)、融剤と共に溶融し、融剤中で
チタン酸アルカリの結晶を育成し、冷却後融剤を溶出除
去してチタン酸アルカリを得る融剤法(フラックス法)
(特開昭5l−122700)、主として化学量論的に
調合された混合物を溶融しこれを冷却固化して結晶化さ
せる溶融法(特開昭5l−89900)、溶媒を用いて
水の臨界点以上の高温高圧下で合成する水熱法(特開昭
50−64526号)等があげられる。[Prior Art] Conventional methods for producing alkali titanates include, for example, a firing method in which a raw material mixture is fired and synthesized by a solid phase reaction (Japanese Patent Application Laid-open No. 53-26298), and a method in which a raw material mixture is fired and synthesized by solid phase reaction, and a method in which a raw material mixture is fired and synthesized by solid phase reaction (Japanese Patent Application Laid-open No. 53-26298), and a method in which a raw material mixture is fired and synthesized by solid phase reaction, and Flux method (flux method) to obtain alkali titanate by growing crystals of alkali titanate and eluting and removing the flux after cooling.
(Japanese Patent Application Laid-Open No. 51-122700), a melting method in which a stoichiometrically prepared mixture is melted and then cooled and solidified to crystallize it (Japanese Patent Application Laid-Open No. 51-89900), which uses a solvent to reach the critical point of water. Examples include the hydrothermal method (JP-A-50-64526), which synthesizes under high temperature and high pressure.
[発明が解決しようとする課題]
上記のような従来の焼成法においては結晶性が低く得ら
れる繊維は数μmの短繊維であり、フラックス法ではフ
ラックスを除去する水洗工程が必要であり、かつフラッ
クスの回収設備を必要としコスト高となる。また溶融法
は結晶が互いに密着したまま成長するので解離処理が困
難であり、かつ得られる繊維は径が太くアスペクト比が
低く強度の点て補強材として好ましくない。[Problems to be solved by the invention] In the conventional firing method as described above, the fibers obtained are short fibers with low crystallinity of several micrometers, and in the flux method, a water washing step is required to remove the flux, and Flux recovery equipment is required, resulting in high costs. Furthermore, in the melting method, the crystals grow in close contact with each other, making dissociation treatment difficult, and the resulting fibers have large diameters, low aspect ratios, and poor strength, making them undesirable as reinforcing materials.
更に水熱法は、高圧下で高アルカリ溶液中で合成操作が
行われるものであるから保安装置を必要とし設備全体と
して費用が高くなり、またAg等の特殊材質を必要とし
、かつ連続操業が難しい。Furthermore, in the hydrothermal method, synthesis operations are carried out in a highly alkaline solution under high pressure, which requires safety equipment, increases the cost of the entire facility, requires special materials such as Ag, and requires continuous operation. difficult.
従来法にはそれぞれ上記のような問題点があり、かつい
ずれもアスペクト比の高いウィスカーを得ることはでき
ない。Each of the conventional methods has the above-mentioned problems, and none of them makes it possible to obtain whiskers with a high aspect ratio.
本発明者らは高度のアスペクト比を有する高品質のチタ
ン酸アルカリウィスカーを得る方法について鋭意研究の
結果、ハロゲン化アルカリと炭素とを粉末状で共存せし
めたチタン源とアルカリ源の混合粉体を焼成するとアス
ペクト比の高いチタン酸アルカリウィスカーが容易に得
られることを見出し本発明を完成した。As a result of intensive research into a method for obtaining high-quality alkali titanate whiskers with a high aspect ratio, the present inventors have developed a mixed powder of a titanium source and an alkali source in which an alkali halide and carbon coexist in powder form. The present invention was completed by discovering that alkali titanate whiskers with a high aspect ratio can be easily obtained by firing.
質のチタン酸アルカリウィスカーを高収率で得ることが
でき、成形、水洗その他従来法のような特定の前後処理
工程を要することなく短縮化された工程により効率よく
製造する方法を提供するにある。To provide a method for efficiently producing high-quality alkali titanate whiskers by a shortened process without requiring specific pre-processing steps such as molding, washing with water, and other conventional methods. .
[課題を解決するための手段1
上記目的を達成するため、本発明の方法はチタン源とア
ルカリ源の混合物を焼成して繊維状のチタン酸アルカリ
を製造するに当り、該混合物中に炭素原料及びハロゲン
化アルカリを共存せしめ焼成することを特徴とするもの
である。[Means for Solving the Problems 1] In order to achieve the above object, the method of the present invention involves adding a carbon raw material to the mixture when firing a mixture of a titanium source and an alkali source to produce a fibrous alkali titanate. and an alkali halide, and are then fired.
チタン源としては例えばTiO□、TiOH<等があげ
られ、アルカリ源としては例えばM2CO3(但しMは
アルカリ金属)があげられる。炭素原料としては主成分
を炭素とする原料であればよく、例えばカーボンブラッ
ク(チャンネルブラック、サーマルブラック、ファーネ
スブラック等)、グラファイト活性炭などがあげられ、
特に限定されるものではないが、灰分やその他の不純物
等が少いものが純度の高い製品を得るためには好ましい
。Examples of the titanium source include TiO□ and TiOH<, and examples of the alkali source include M2CO3 (where M is an alkali metal). The carbon raw material may be any raw material whose main component is carbon, such as carbon black (channel black, thermal black, furnace black, etc.), graphite activated carbon, etc.
Although not particularly limited, it is preferable to use a material with low ash content and other impurities in order to obtain a highly pure product.
ハロゲン化アルカリとしては、KCj2、KF、NaC
l2、NaF等があげられ1種又は2種以上を用いるこ
とができ、焼成により蒸発するものが純度の高い製品が
得られるので望ましい。通常これらの原料は通常粉状で
混合して焼成する。As alkali halides, KCj2, KF, NaC
12, NaF, etc., and one or more of them can be used, and those that evaporate during calcination are preferred because they yield products with high purity. These raw materials are usually mixed in powder form and fired.
チタン源とアルカリ源の混合比は好ましくは酸化ヂタ:
/ (T i 02 ) 、酸化フルカリ(R20)換
算モル比でTiO□/R20=2〜8を主原料として、
炭素原料及びハロゲン化アルカリをそれぞれ0.1〜2
0重量%添加混合して900〜1200°Cで焼成する
。The mixing ratio of titanium source and alkali source is preferably oxidized titanium:
/ (T i 02 ), using TiO□/R20 = 2 to 8 as the main raw material in terms of molar ratio in terms of fulkaline oxide (R20),
Carbon raw material and alkali halide each from 0.1 to 2
0% by weight is added and mixed and fired at 900-1200°C.
[作用]
焼成により形成されるTiO2粒子と溶融アルカリとの
固液界面反応が重要であるとの知見を基に研究を重ねた
結果本発明に到達したものであり、本発明における炭素
原料の役割は、瞬間的な燃焼と発生するCOガスの還元
雰囲気が固液界面反応を促進するものと推定される。又
焼成物を多孔質化しウィスカーの成長を助長するすなわ
ち極く少いハロゲン化アルカリでありながら、その作用
はハロゲン化アルカリをチタン酸アルカリの結晶成長の
フラックスとして働かせ、反応育成を促し径方向への成
長を抑制し高アスペクト比化させるものである。[Function] The present invention was arrived at as a result of repeated research based on the knowledge that the solid-liquid interface reaction between TiO2 particles formed by firing and molten alkali is important, and the role of the carbon raw material in the present invention is It is presumed that the instantaneous combustion and the reducing atmosphere of the generated CO gas promote the solid-liquid interfacial reaction. In addition, it makes the fired product porous and promotes the growth of whiskers.Although the amount of alkali halide is extremely small, its action is to make the alkali halide act as a flux for crystal growth of alkali titanate, promoting reaction growth and increasing the growth of whiskers in the radial direction. This suppresses the growth of the metal and increases the aspect ratio.
M20 ・nT 102 (Mはアルカリ金属)で示
されるチタン酸アルカリ金属に相当する組成を形成する
チタン源とアルカリ源の原料に加える炭素原料及びハロ
ゲン化アルカリの量は、焼成条件により蒸発可能な添加
量で行なえば、焼成物はチタン酸アルカリのみであるか
ら水洗工程は必要としないものである。The amount of carbon raw material and alkali halide added to the titanium source and alkali source raw materials to form a composition corresponding to an alkali metal titanate represented by M20 ・nT 102 (M is an alkali metal) is an addition that can be vaporized depending on the firing conditions. In terms of quantity, since the fired product consists only of alkali titanate, a water washing step is not necessary.
なお、この焼成に当ってはトンネル炉等が使用できるの
で、連続焼成を行なうことができる。Incidentally, since a tunnel furnace or the like can be used for this firing, continuous firing can be performed.
[実施例1]
炭酸カリウム]、、15kg、酸化チタン4.00kg
、カーボンブラック、0.36kg、塩化カリウム0.
40kgを、20℃ヘンシエルミキザーで混合し、11
00°Cで2時間焼成した。焼成物をX線回折で同定し
たところ、六チタン酸カリウムであった。又、走査型電
子顕微鏡で拡大してみると、平均繊維径07μm、平均
繊維長30μmの単繊維状態にある高アスペクト比のも
のであった。[Example 1] Potassium carbonate], 15 kg, titanium oxide 4.00 kg
, carbon black, 0.36 kg, potassium chloride 0.
Mix 40 kg with a Henschel mixer at 20°C,
It was baked at 00°C for 2 hours. The fired product was identified by X-ray diffraction and was found to be potassium hexatitanate. Further, when magnified with a scanning electron microscope, it was found to be a single fiber with a high aspect ratio, with an average fiber diameter of 07 μm and an average fiber length of 30 μm.
[実施例2]
炭酸ナトリウム0.88kg、酸化チタン4.00kg
、人造黒鉛6.70kg、塩化ナトリウム0.20kg
、弗化カリウム0.40kg混合し、1100°Cて1
5時間焼成した。X線回折で、得られた生成相は、六チ
タン酸ナトリウムで、平均繊維径0.8μm、平均繊維
長40μmの単繊維状態の高アスペクト比のものである
。[Example 2] Sodium carbonate 0.88 kg, titanium oxide 4.00 kg
, artificial graphite 6.70kg, sodium chloride 0.20kg
, 0.40 kg of potassium fluoride was mixed and heated at 1100°C.
It was baked for 5 hours. The generated phase obtained by X-ray diffraction is sodium hexatitanate, and has a high aspect ratio in the form of single fibers with an average fiber diameter of 0.8 μm and an average fiber length of 40 μm.
[実施例3]
炭酸カリウム1.72kg、酸化チタン3.97kg、
カーボンブラック0.03kg、弗化カリウム0.02
に、gの混合物を、1000°Cで30分間焼成、得ら
れた生成相は、匹チタン酸カリウムで、平均繊維径0
51tm、平均繊維長50μmの単繊維状態の高アスペ
クト比のものである。[Example 3] Potassium carbonate 1.72 kg, titanium oxide 3.97 kg,
Carbon black 0.03kg, potassium fluoride 0.02
The mixture of g was calcined at 1000°C for 30 minutes, and the resulting phase was potassium titanate with an average fiber diameter of 0.
51 tm, average fiber length 50 μm, single fiber state, high aspect ratio.
[比較例11
炭酸カリウム1.15kg、酸化チタン400kgを実
施例1と同様に、混合、焼成を行ない、評価を行なった
。[Comparative Example 11 1.15 kg of potassium carbonate and 400 kg of titanium oxide were mixed and fired in the same manner as in Example 1, and evaluated.
生成相は、六チクン酸カリウムであるが、平均繊維径1
.5μm、平均繊維長2.0μmの棒状が焼結した塊状
のものである。The generated phase is potassium hexticunate, but the average fiber diameter is 1
.. It is a block of sintered rods with an average fiber length of 5 μm and an average fiber length of 2.0 μm.
[比較例21
炭酸カリウム1.1’5kg、酸化チタン400kg、
カーボンブラック0.36kgを同様の混合、焼成を行
ない評価した。[Comparative Example 21 Potassium carbonate 1.1'5 kg, titanium oxide 400 kg,
0.36 kg of carbon black was mixed and fired in the same manner and evaluated.
生成相は、六チタン酸カリウムであるが、平均繊維径1
3μm、平均繊維長2.5μmの棒状が焼結した塊状の
ものである。The generated phase is potassium hexatitanate, but the average fiber diameter is 1
It is a sintered block of rods with a diameter of 3 μm and an average fiber length of 2.5 μm.
[比較例3〕
炭酸カリウム1.15kg、酸化チタン4.00kg、
塩化カリウム0.40kgを同様の混合、焼成を行ない
評価した。[Comparative Example 3] Potassium carbonate 1.15 kg, titanium oxide 4.00 kg,
0.40 kg of potassium chloride was mixed and fired in the same manner and evaluated.
生成相は、六チクン酸カリウムであるが、平均繊維径1
.0μm、平均繊維長5μmの棒状が焼 結した塊状
のものである。The generated phase is potassium hexticunate, but the average fiber diameter is 1
.. It is a block of sintered rods with an average fiber length of 0 μm and an average fiber length of 5 μm.
以上、説明した様に本発明により、得られるチタン酸ア
ルカリは、その応用として、利用されやすい高アスペク
ト比の繊維形状として容易に得られるものである。As explained above, the alkali titanate obtained by the present invention can be easily obtained in the form of a fiber with a high aspect ratio, which is easy to use for its applications.
又、本発明によるチタン酸アルカリウィスカーは、欠陥
の少ない高品質のものと1で得られるのも特徴である。Furthermore, the alkali titanate whisker according to the present invention is characterized in that it can be obtained in one step with high quality and few defects.
第1図は、本実施例1で得られたものの透過型電子顕微
鏡写真である。従来のフラックス法で得られたものは、
第2図のように転位、欠陥がみられるが、本発明で得ら
れたものは、結晶欠陥はほとんどみられない。FIG. 1 is a transmission electron micrograph of the material obtained in Example 1. What was obtained by the conventional flux method is
Although dislocations and defects are observed as shown in FIG. 2, the crystals obtained by the present invention have almost no crystal defects.
[発明の効果]
本発明によれば、従来の方法では得られなかった直線状
でアスペクト比が極めて高い高品質のチタン酸アルカリ
ウィスカーが、焼成後水中ての水洗工程又は水中での解
離操作等特別の後処理を必要とせずに高収率に得られ、
工程も簡単で短縮され、低コストデ製造できるので極め
て有益である。また数ミリ以上の長繊維の製造も可能で
あり、利用分野の拡大が可能となる。[Effects of the Invention] According to the present invention, high-quality alkali titanate whiskers that are linear and have an extremely high aspect ratio, which could not be obtained by conventional methods, can be obtained by a washing process in water after calcination or a dissociation process in water, etc. Obtained in high yield without the need for special post-treatment,
The process is simple, shortened, and can be manufactured at low cost, making it extremely useful. It is also possible to produce long fibers of several millimeters or more, making it possible to expand the range of applications.
図面は透過型電子顕微鏡写真で、第1図は本発明方法で
得られたチタン酸アルカリウィスカーであり、第2図は
従来のフラックス法で得られたチタン酸アルカリ繊維で
ある。The drawings are transmission electron micrographs; FIG. 1 shows alkali titanate whiskers obtained by the method of the present invention, and FIG. 2 shows alkali titanate fibers obtained by the conventional flux method.
Claims (1)
チタン酸アルカリを製造するに当り、該混合物中に炭素
原料及びハロゲン化アルカリを共存せしめて焼成するこ
とを特徴とするチタン酸アルカリウィスカーの製造方法
。 2、チタン源とアルカリ源の混合比は、酸化チタン(T
iO_2)、酸化アルカリ(R_2O)換算モル比でT
iO_2/R_2O=2〜8である請求項1記載のチタ
ン酸アルカリウィスカーの製造方法。 3、M_2O・nTiO_2(但しMはアルカリ金属)
で示されるチタン酸アルカリ金属に相当する組成を形成
するチタン源とアルカリ源の原料に加える炭素原料及び
ハロゲン化アルカリの量は、それぞれ0.1〜20重量
%である請求項1記載のチタン酸アルカリウィスカーの
製造方法。[Claims] 1. In producing fibrous alkali titanate by firing a mixture of a titanium source and an alkali source, a carbon raw material and an alkali halide are allowed to coexist in the mixture before firing. A method for producing an alkali titanate whisker. 2. The mixing ratio of titanium source and alkali source is titanium oxide (T
iO_2), T in molar ratio converted to alkali oxide (R_2O)
The method for producing an alkali titanate whisker according to claim 1, wherein iO_2/R_2O=2 to 8. 3. M_2O・nTiO_2 (M is an alkali metal)
The titanic acid according to claim 1, wherein the amounts of the carbon raw material and the alkali halide added to the titanium source and alkali source raw materials forming the composition corresponding to the alkali metal titanate represented by are each 0.1 to 20% by weight. Method for producing alkali whiskers.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP33005090A JP3207850B2 (en) | 1990-11-30 | 1990-11-30 | Method for producing alkali titanate whiskers |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP33005090A JP3207850B2 (en) | 1990-11-30 | 1990-11-30 | Method for producing alkali titanate whiskers |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH04202099A true JPH04202099A (en) | 1992-07-22 |
| JP3207850B2 JP3207850B2 (en) | 2001-09-10 |
Family
ID=18228220
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP33005090A Expired - Lifetime JP3207850B2 (en) | 1990-11-30 | 1990-11-30 | Method for producing alkali titanate whiskers |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP3207850B2 (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2006335579A (en) * | 2005-05-31 | 2006-12-14 | Univ Nihon | Piezoelectric material and synthesis method thereof |
| WO2016194531A1 (en) * | 2015-06-02 | 2016-12-08 | 東邦チタニウム株式会社 | Alkali titanate and friction material |
-
1990
- 1990-11-30 JP JP33005090A patent/JP3207850B2/en not_active Expired - Lifetime
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2006335579A (en) * | 2005-05-31 | 2006-12-14 | Univ Nihon | Piezoelectric material and synthesis method thereof |
| WO2016194531A1 (en) * | 2015-06-02 | 2016-12-08 | 東邦チタニウム株式会社 | Alkali titanate and friction material |
| JPWO2016194531A1 (en) * | 2015-06-02 | 2018-03-22 | 東邦チタニウム株式会社 | Alkali titanate and friction material |
| US10156277B2 (en) | 2015-06-02 | 2018-12-18 | Toho Titanium Co., Ltd. | Alkali-metal titanate and friction material |
Also Published As
| Publication number | Publication date |
|---|---|
| JP3207850B2 (en) | 2001-09-10 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| Rao | Chemical synthesis of solid inorganic materials | |
| Vejux et al. | TEM study of interfacial relationships in the V2O5 TiO2 (anatase) system | |
| CN1035443C (en) | Potassium titanate crystal whiskers preparation method | |
| HU204235B (en) | Process for producing self-carrying ceramic products consisting of zones of different character | |
| JPH04202099A (en) | Production of alkali titanate whisker | |
| US4064224A (en) | Method of making fibrous alkali titanates | |
| WO2024037679A1 (en) | A method for the preparation of submicron and/or micron fibers formed by a mixture of crystalline tio2 and v2o5 and the submicron and/ or micron fibers prepared by this method | |
| JP2747916B2 (en) | Potassium titanate long fiber and method for producing titania fiber using the same | |
| CN109231208B (en) | Preparation method of transition metal carbide | |
| JPS62241819A (en) | Manufacture of high purity lithium oxide | |
| JPH0234888B2 (en) | SENIJOCHITANSANKARIUMUNOSEIZOHO | |
| JP2001316200A (en) | Manganese oxide single crystal particles and method for producing the same | |
| Wang et al. | Synthesis of potassium hexatitanate whiskers using hydrothermal method | |
| JPH0478731B2 (en) | ||
| JPS63239104A (en) | Production of fine silicon nitride powder containing beta-phase | |
| JPS62260796A (en) | Method for producing potassium hexatitanate fiber | |
| JPS60259627A (en) | Method for producing potassium hexatitanate fiber or potassium hexatitanate composite fiber | |
| JPH07330500A (en) | Method for manufacturing aluminum borate whiskers | |
| JPH0244774B2 (en) | ||
| JP2856636B2 (en) | Production method of ammonium cryolite | |
| JP2631859B2 (en) | Method for producing titania fiber | |
| JPH03279215A (en) | Production of potassium hexatitanate fiber | |
| JPS63134502A (en) | Sublimation purification of inorganic fluoride | |
| JPH10212625A (en) | Method for producing potassium titanate fiber | |
| JP3028398B2 (en) | Method for producing sodium titanate fiber |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
| R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
| R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
| FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20080706 Year of fee payment: 7 |
|
| FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20090706 Year of fee payment: 8 |
|
| FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20090706 Year of fee payment: 8 |
|
| FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20090706 Year of fee payment: 8 |
|
| FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20100706 Year of fee payment: 9 |
|
| FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20110706 Year of fee payment: 10 |
|
| EXPY | Cancellation because of completion of term | ||
| FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20110706 Year of fee payment: 10 |