JPH0563216B2 - - Google Patents
Info
- Publication number
- JPH0563216B2 JPH0563216B2 JP59033300A JP3330084A JPH0563216B2 JP H0563216 B2 JPH0563216 B2 JP H0563216B2 JP 59033300 A JP59033300 A JP 59033300A JP 3330084 A JP3330084 A JP 3330084A JP H0563216 B2 JPH0563216 B2 JP H0563216B2
- Authority
- JP
- Japan
- Prior art keywords
- sieve
- ceramic
- stage
- granulated
- rolling
- 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.)
- Expired - Lifetime
Links
- 239000000919 ceramic Substances 0.000 claims description 32
- 238000005096 rolling process Methods 0.000 claims description 23
- 239000000843 powder Substances 0.000 claims description 22
- 239000008187 granular material Substances 0.000 claims description 19
- 238000000034 method Methods 0.000 claims description 16
- 229910010293 ceramic material Inorganic materials 0.000 claims description 13
- 238000007873 sieving Methods 0.000 claims 1
- 238000005469 granulation Methods 0.000 description 9
- 230000003179 granulation Effects 0.000 description 9
- 239000011230 binding agent Substances 0.000 description 5
- 238000000465 moulding Methods 0.000 description 5
- 239000002245 particle Substances 0.000 description 4
- 238000001694 spray drying Methods 0.000 description 3
- 239000004677 Nylon Substances 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 229920001778 nylon Polymers 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 239000002904 solvent Substances 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B28—WORKING CEMENT, CLAY, OR STONE
- B28C—PREPARING CLAY; PRODUCING MIXTURES CONTAINING CLAY OR CEMENTITIOUS MATERIAL, e.g. PLASTER
- B28C1/00—Apparatus or methods for obtaining or processing clay
- B28C1/10—Apparatus or methods for obtaining or processing clay for processing clay-containing substances in non-fluid condition ; Plants
Landscapes
- Chemical & Material Sciences (AREA)
- Dispersion Chemistry (AREA)
- Compositions Of Oxide Ceramics (AREA)
- Preparation Of Clay, And Manufacture Of Mixtures Containing Clay Or Cement (AREA)
Description
【発明の詳細な説明】
[技術分野]
本発明はセラミツク微粉末の造粒方法に関する
ものである。DETAILED DESCRIPTION OF THE INVENTION [Technical Field] The present invention relates to a method for granulating fine ceramic powder.
[従来技術]
金型プレス成形において、セラミツク粉末を造
粒処理したものを利用する場合が多い。その利点
としては、流動性が良く、金型内に均一に充填で
きるため、均一な成形体が得られることが挙げら
れる。[Prior Art] In mold press molding, granulated ceramic powder is often used. Its advantage is that it has good fluidity and can be filled uniformly into the mold, resulting in a uniform molded product.
ところで、セラミツク粉末の造粒方法として、
噴霧乾燥式が多用されているが、この噴霧乾燥式
によると以下に述べるような多くの問題点があ
り、その解決が望まれている。 By the way, as a method for granulating ceramic powder,
Although the spray drying method is often used, there are many problems with the spray drying method as described below, and it is desired to solve these problems.
(1) セラミツク粉末に混入する結合バインダーの
量、造粒装置の操作条件により、顆粒の大き
さ、強度、中空度にばらつきが発生する。(1) Depending on the amount of binder mixed into the ceramic powder and the operating conditions of the granulation equipment, variations occur in the size, strength, and hollowness of the granules.
(2) セラミツク構造物の成形後、脱バインダー工
程が必要である。(2) After molding the ceramic structure, a binder removal process is required.
(3) 造粒製造が大型なため、セラミツク粉末が数
Kg〜数十Kg必要で、少量の造粒が不可能であ
る。(3) Because the granulation process is large-scale, a large number of ceramic powders are produced.
Kg to several tens of Kg is required, making it impossible to granulate a small amount.
(4) 特に顆粒強度が強過ぎると、成形時に顆粒が
破壊せず、身成形体が得られない。(4) In particular, if the granule strength is too strong, the granules will not break during molding and a molded body will not be obtained.
[発明の目的]
本発明は、上述した従来技術の問題点を解決す
るためになされたもので、強度が適度で中空では
ない大きさのそろつたセラミツク顆粒が、簡単か
つ迅速に少量のセラミツク粉末ででも造粒でき、
得られたセラミツク粉末の顆粒による成形体にお
いて、脱バインダー工程を不要とすることができ
るセラミツク微粉末の造粒方法を提供することを
目的とする。[Object of the Invention] The present invention was made in order to solve the problems of the prior art described above, and it is possible to easily and quickly produce ceramic granules of a uniform size with appropriate strength and no hollows into a small amount of ceramic powder. It can be granulated even with
It is an object of the present invention to provide a method for granulating fine ceramic powder, which can eliminate the need for a binder removal step in a molded article of ceramic powder granules obtained.
[発明の構成]
上記目的は、本発明によれば、比較的篩目の大
きな第1段部分、この第1段部分に比して比較的
篩目の小さな第2段部分および受皿を有する振動
篩を用い、前記第1段部分に造粒すべきセラミツ
ク材料とともに転動体を入れ、振動篩を所定の振
動数で振動させることにより、第1段部分の篩目
より転動体により押し出されたセラミツク材料を
第2段部分の篩目により分級し、第2段部分上お
よび受皿上に存在するセラミツク材料を振動によ
るころがりにより造粒することを特徴とするセラ
ミツク微粉末の造粒方法によつて達成される。[Structure of the Invention] According to the present invention, the above-mentioned object is to provide a vibrator having a first stage portion with a relatively large sieve mesh, a second stage portion with a relatively small sieve mesh compared to the first stage portion, and a saucer. Using a sieve, a rolling element is placed in the first stage part together with the ceramic material to be granulated, and the vibrating sieve is vibrated at a predetermined frequency to extrude the ceramic through the sieve openings of the first stage part by the rolling element. Achieved by a method for granulating fine ceramic powder, which is characterized in that the material is classified by the sieve mesh in the second stage part, and the ceramic material present on the second stage part and on the tray is granulated by rolling with vibration. be done.
以下に本発明を更に詳細に説明する。 The present invention will be explained in more detail below.
本発明で用いるセラミツク材料は特に限定され
ることなく、一般に用いられているセラミツク材
料において、これを上述した目的に適うよう造粒
成形する。 The ceramic material used in the present invention is not particularly limited, and is a commonly used ceramic material that is granulated and molded to meet the above-mentioned purpose.
本発明のセラミツク微粉末の造粒方法は、以下
に述べる工程を経てセラミツク顆粒を得る。本発
明においては、造粒に際して多段の振動篩を用
い、分級を行いつつ分級された粉体のころがり造
粒により所望のセラミツク顆粒を得る。各工程を
第1図を参照しつつ説明する。 In the method for granulating ceramic fine powder of the present invention, ceramic granules are obtained through the steps described below. In the present invention, a multistage vibrating sieve is used during granulation, and desired ceramic granules are obtained by rolling and granulating the classified powder while performing classification. Each step will be explained with reference to FIG.
セラミツク原材料2が導入される振動篩1の第
1段部分3は、比較的荒いメツシユのものが用い
られる。篩目は20〜40メツシユの範囲が好まし
い。 The first stage portion 3 of the vibrating sieve 1 into which the ceramic raw material 2 is introduced has a relatively rough mesh. The sieve size is preferably in the range of 20 to 40 mesh.
第1段部分3にはナイロンボール4のような転
動体が所要個数入れられ、セラミツク粉末あるい
は凝集体であるセラミツク原材料2を破砕すると
ともに、1段部分3の篩目5より2′で示すよう
に所望粒径として強制的に第2段部分6上に押し
出す作用をする。第1段部分は少なくとも1個の
篩により構成され、その篩目は同一でも多少異な
らせても良い。 A required number of rolling elements such as nylon balls 4 are placed in the first stage section 3 to crush the ceramic raw material 2, which is ceramic powder or aggregates, and pass through the sieve mesh 5 of the first stage section 3 as shown at 2'. The desired particle size is forcibly extruded onto the second stage portion 6. The first stage portion is constituted by at least one sieve, and the sieve size may be the same or slightly different.
第2段部分6は第1段部分より細かい目の篩で
構成され、篩目は40〜60メツシユの範囲にするの
が良い。第2段部分6上ではその篩目7より細か
いセラミツク材料2″は次の受け皿8上に落下し、
篩目7より大きいセラミツク材料9は第2段部分
6上で振動により矢印10で示すように転動さ
れ、ころがりにより造粒される。第2段部分は少
なくとも1個の篩により構成され、その篩目は同
一でも多少異ならせても良い。 The second stage portion 6 is composed of a sieve with finer mesh than the first stage portion, and the sieve mesh is preferably in the range of 40 to 60 mesh. On the second stage portion 6, the ceramic material 2'' finer than the sieve mesh 7 falls onto the next tray 8,
The ceramic material 9, which is larger than the sieve size 7, is rolled on the second stage part 6 by vibration as shown by the arrow 10, and is granulated by rolling. The second stage portion is composed of at least one sieve, and the sieve size may be the same or slightly different.
受皿8上に落下したセラミツク材料2″は振動
により矢印11で示すように転動され、ころがり
により造粒される。第2段部分6および受皿8上
でころがり造粒されたセラミツク材料9および
2″がセラミツク造粒品として回収される。 Ceramic material 2'' that has fallen onto saucer 8 is rolled by vibration as shown by arrow 11 and is granulated by rolling. Ceramic materials 9 and 2 are granulated by rolling on second stage portion 6 and saucer 8. '' is recovered as ceramic granules.
[発明の作用]
振動篩1の第1段部分3上にセラミツク粉末が
入れられ、振動が与えられると、次のようにして
分級されつつころがりにより造粒される。[Operation of the Invention] Ceramic powder is placed on the first stage portion 3 of the vibrating sieve 1, and when vibration is applied, it is classified and granulated by rolling as follows.
(1) セラミツク粉体が乾燥凝集体の場合
(a) セラミツク粉末(凝集体)が転動体4のころ
がりにより粉砕される。(1) When the ceramic powder is a dry aggregate (a) The ceramic powder (aggregate) is crushed by the rolling of the rolling elements 4.
(b) 粉砕されたセラミツク粉末は第1段部分3の
篩目5(例えば32メツシユ)に詰まるが、転動
体の重みにより強制的に押し出され、例えば32
メツシユの目開き程度まで小さくなり、次の第
2段部分6上に落下する。(b) The pulverized ceramic powder gets stuck in the sieve mesh 5 (for example, 32 mesh) of the first stage portion 3, but is forcibly pushed out by the weight of the rolling elements.
It becomes as small as the opening of the mesh and falls onto the next second stage portion 6.
(c) さらに、第2段部分6上ではその篩目7(例
えば60メツシユ)より大きいものは残留して転
動により造粒され、その篩目より小さく微粉化
されたものは次の受け皿8上に落下し、ここで
転動により造粒される。(c) Further, on the second stage part 6, particles larger than the sieve mesh 7 (for example, 60 mesh) remain and are granulated by rolling, and particles smaller than the sieve mesh and pulverized are transferred to the next receiving tray 8. It falls to the top where it is granulated by rolling.
(d) 第2段部分6および受け皿8上で造粒された
ものをセラミツク顆粒として得る。(d) Granules granulated on the second stage portion 6 and tray 8 are obtained as ceramic granules.
(2) セラミツク粉末が粉末状の場合
(e) 振動により第1段部分(例えば篩目32メツシ
ユ)上で雪だるま式に集合するのを転動体4が
防止し、あとは上記(1)の(b)以下の工程と同様に
してころがり造粒される。(2) When the ceramic powder is in powder form (e) The rolling elements 4 prevent it from gathering in a snowball-like manner on the first stage part (for example, 32 meshes) due to vibration, and then the process described in (1) above is performed. b) It is rolled and granulated in the same manner as the following process.
[発明の効果]
上述した本発明の分級と同時にころがりにより
造粒する方法は、従来の噴霧乾燥造粒方式に比し
て以下に述べる多くの利点をもたらす。[Effects of the Invention] The above-mentioned classification and rolling granulation method of the present invention provides many advantages as described below compared to the conventional spray drying granulation method.
(1) 振動篩の第1および第2段部分で分級を行つ
た後、ころがり造粒を行うので、造粒されたセ
ラミツク顆粒の大きさ、強度にはバラツキが小
さく、また顆粒の中空という問題も小さくな
る。(1) Since rolling granulation is performed after classification in the first and second stages of the vibrating sieve, there is little variation in the size and strength of the granulated ceramic granules, and the problem of hollow granules is avoided. will also become smaller.
(2) セラミツクにバインダーを併用しないので、
成形後の脱バインダー工程が不要である。(2) Ceramic and binder are not used together, so
No binder removal process is required after molding.
(3) 造粒装置は以下の実施例に示すように小型に
もすることができ、少量の造粒が簡単にでき
る。(3) The granulation device can be made small as shown in the following examples, and can easily granulate a small amount.
(4) 顆粒強度は(1)でも述べたように、適当に調整
されるため、これを用いて成形した時、良好な
成形体が得られる。(4) As mentioned in (1), the granule strength is appropriately adjusted, so when molded using this, a good molded product can be obtained.
[実施例]
次に、本発明を実施例につき具体的に説明す
る。[Example] Next, the present invention will be specifically explained with reference to an example.
振動篩として、第1図に示すような上段、下段
および受皿よりなるものを用い、上段は32メツシ
ユの篩、下段は60メツシユの篩で、篩径は約20cm
のものを用いた。 The vibrating sieve consists of an upper stage, a lower stage, and a saucer as shown in Figure 1.The upper stage is a 32 mesh sieve, the lower stage is a 60 mesh sieve, and the sieve diameter is approximately 20 cm.
I used the one from
セラミツク材料としては、前工程で溶媒を用い
て粉砕し乾燥した凝集体(5〜10μm)および粉
末(約1μm)のものを用いた。セラミツクを上記
振動篩の上段に50〜100g入れ、次いでφ15mmの
ナイロンボールを約10個入れ、蓋をした後、
290rpmの振動数で5分程度ふるいにかけた。凝
集体および粉末状のものも、前記本発明の作用で
説明したようにして分級されつつころがり造粒さ
れ、平均粒径200〜500μmのセラミツク顆粒が得
られた。 The ceramic materials used were aggregates (5 to 10 μm) and powders (approximately 1 μm) that had been crushed using a solvent in the previous step and dried. Put 50-100g of ceramic into the upper part of the vibrating sieve, then put about 10 nylon balls with a diameter of 15mm, and put the lid on.
The material was sieved for about 5 minutes at a vibration frequency of 290 rpm. The agglomerates and powders were also classified and granulated by rolling as explained in the operation of the present invention to obtain ceramic granules with an average particle size of 200 to 500 μm.
下段および受皿上の造粒体を混合し、金型成形
に使用したところ、流動性が良く、均一な成形体
が得られた。 When the granules on the lower stage and on the saucer were mixed and used for mold molding, a uniform molded product with good fluidity was obtained.
さらに、振動篩としては、第1図に示すもの以
外に、同心状に内側より第1篩部分3、第2篩部
分6および受皿8を有する遠心力を利用する回転
振動型のものを用いて上記と同様の造粒を行なつ
たところ、同様の結果が得られた。 Furthermore, as the vibrating sieve, in addition to the one shown in FIG. 1, a rotating vibrating type that utilizes centrifugal force and has a first sieve part 3, a second sieve part 6, and a saucer 8 concentrically from the inside is used. When granulation was carried out in the same manner as above, similar results were obtained.
第1図は本発明のセラミツク微粉末造粒方法を
説明するための線図的断面図である。
符号の説明、1……振動篩、2,2′,2″……
セラミツク材料、3……第1段部分、4……転動
体、5,7……篩目、6……第2段部分、8……
受皿、9……セラミツク造粒体、10,11……
ころがり方向。
FIG. 1 is a diagrammatic cross-sectional view for explaining the ceramic fine powder granulation method of the present invention. Explanation of symbols, 1... vibrating sieve, 2, 2', 2''...
Ceramic material, 3... First stage part, 4... Rolling element, 5, 7... Screen mesh, 6... Second stage part, 8...
Saucer, 9...Ceramic granules, 10, 11...
Rolling direction.
Claims (1)
部分に比して比較的篩目の小さな第2段部分およ
び受皿を有する振動篩を用い、前記第1段部分に
造粒すべきセラミツク材料とともに転動体を入
れ、振動篩を所定の振動数で振動させることによ
り、第1段部分の篩目より転動体により押し出さ
れたセラミツク材料を第2段部分の篩目により分
級し、第2段部分上および受皿上に存在するセラ
ミツク材料を振動によるころがりにより造粒する
ことを特徴とするセラミツク微粉末の造粒方法。1. Granules should be granulated in the first stage part using a vibrating sieve having a first stage part with a relatively large sieve mesh, a second stage part with a relatively small sieve mesh compared to this first stage part, and a saucer. By putting a rolling element together with the ceramic material and vibrating the vibrating sieve at a predetermined frequency, the ceramic material pushed out by the rolling element through the sieve openings in the first stage part is classified by the sieving openings in the second stage part. A method for granulating fine ceramic powder, characterized in that the ceramic material present on the two-stage portion and on the saucer is granulated by rolling by vibration.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP59033300A JPS60175534A (en) | 1984-02-23 | 1984-02-23 | Granulation of fine ceramic powder |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP59033300A JPS60175534A (en) | 1984-02-23 | 1984-02-23 | Granulation of fine ceramic powder |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS60175534A JPS60175534A (en) | 1985-09-09 |
JPH0563216B2 true JPH0563216B2 (en) | 1993-09-10 |
Family
ID=12382696
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP59033300A Granted JPS60175534A (en) | 1984-02-23 | 1984-02-23 | Granulation of fine ceramic powder |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS60175534A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US11701081B2 (en) | 2017-03-30 | 2023-07-18 | Koninklijke Philips N.V. | System and method for concurrent visualization and quantification of blood flow using ultrasound |
Families Citing this family (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2720123B2 (en) * | 1991-09-25 | 1998-02-25 | 三井造船株式会社 | Method for producing piezoelectric ceramic microspheres for piezoelectric elastomer |
US7858023B2 (en) | 2004-06-30 | 2010-12-28 | Tdk Corporation | Method for producing raw material powder for rare earth sintered magnet, method for producing rare earth sintered magnet, granule and sintered body |
JP4666145B2 (en) * | 2005-03-24 | 2011-04-06 | Tdk株式会社 | Rare earth sintered magnet manufacturing method and rare earth sintered magnet |
JP5466735B2 (en) * | 2012-07-18 | 2014-04-09 | 杉山重工株式会社 | Vibrating granulator |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS4843417A (en) * | 1971-09-30 | 1973-06-23 |
-
1984
- 1984-02-23 JP JP59033300A patent/JPS60175534A/en active Granted
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS4843417A (en) * | 1971-09-30 | 1973-06-23 |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US11701081B2 (en) | 2017-03-30 | 2023-07-18 | Koninklijke Philips N.V. | System and method for concurrent visualization and quantification of blood flow using ultrasound |
Also Published As
Publication number | Publication date |
---|---|
JPS60175534A (en) | 1985-09-09 |
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