[go: up one dir, main page]

JPH03215631A - Disintegrating method for dehydrated cake of filter press - Google Patents

Disintegrating method for dehydrated cake of filter press

Info

Publication number
JPH03215631A
JPH03215631A JP2008930A JP893090A JPH03215631A JP H03215631 A JPH03215631 A JP H03215631A JP 2008930 A JP2008930 A JP 2008930A JP 893090 A JP893090 A JP 893090A JP H03215631 A JPH03215631 A JP H03215631A
Authority
JP
Japan
Prior art keywords
dehydrated cake
dry dust
cake
dehydrated
primary
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.)
Pending
Application number
JP2008930A
Other languages
Japanese (ja)
Inventor
Masao Kawashima
川島 正男
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Nippon Steel Corp
Original Assignee
Sumitomo Metal Industries Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Sumitomo Metal Industries Ltd filed Critical Sumitomo Metal Industries Ltd
Priority to JP2008930A priority Critical patent/JPH03215631A/en
Publication of JPH03215631A publication Critical patent/JPH03215631A/en
Pending legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P10/00Technologies related to metal processing
    • Y02P10/20Recycling

Landscapes

  • Manufacture And Refinement Of Metals (AREA)

Abstract

PURPOSE:To form dehydrated cake to finer and to adjusts its moisture in such a manner that the dehydrated cake can be utilized for sintering by adding dry dust to the dehydrated cake after primary disintegration and subjecting this cake to secondary disintegration, thereby simultaneously executing uniform mixing and disintegrating to fine grains. CONSTITUTION:The slurry in a storage tank 1 is dehydrated to about 20% moisture content by a filter press 2 and is transferred to a coarse disintegrator 3. The dehydrated cake subjected to the coarse disintegrating is sent to a primary disintegrator 5 by which the cake is primarily disintegrated. The dry dust 4 is fed by a rotary valve 6 and is dropped onto the dehydrated cake subjected to the primary disintegrating and is sent to a secondary disintegrator 7. The dehydrated cake after the primary disintegrating and the dropped dry dust 4 are simultaneously mixed and finely disintegrated by the secondary disintegrator 7. The mixture is sent to a hopper 9. The dust is mixed in the form of sticking to the surface of the dehydrated cake 8 at the time when the dehydrated cake 8 is finely disintegrated and, therefore, the sticking to the interior of the machine does not arise. The mixing ratio of the dehydrated cake 8 and the dry dust 4 is preferably 10:5 to 10:7.

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は、製鉄所内で発生するスラリーを、焼結で有効
利用可能な水分及び粒度のケーキとするのに適した脱水
ケーキの解砕方法に関するものである。
Detailed Description of the Invention (Industrial Application Field) The present invention provides a method for crushing a dehydrated cake suitable for turning slurry generated in a steel mill into a cake with moisture and particle size that can be effectively used in sintering. It is related to.

(従来の技術) 製鉄所内で発生するスラリーを脱水するには、通常、フ
ィルタープレスが使用されているが、この脱水されたケ
ーキ中にはまだ20%程度の水分が含有されているため
、このままの状態ではハンドリング及びホッパー詰り等
の問題がある。従って、この脱水ケーキに乾ダストを混
合させて水分調整を行う必要がある。
(Prior technology) A filter press is usually used to dewater slurry generated in steel plants, but this dehydrated cake still contains about 20% water, so it is not possible to remove water as is. Under this condition, there are problems such as handling and hopper clogging. Therefore, it is necessary to mix dry dust into this dehydrated cake to adjust the moisture content.

また、この水分調整された脱水ケーキは粗解砕されただ
けであるので粒径10lml以上のものが90%と粗粒
が多く、このままでは焼結として利用できない。従って
、前記乾ダストと混合した後に解砕して細粒化している
Moreover, since this moisture-adjusted dehydrated cake has only been coarsely crushed, it has a large proportion of coarse particles (90% of which have a particle size of 10 lml or more), and cannot be used as it is for sintering. Therefore, after mixing with the dry dust, it is crushed into fine particles.

(発明が解決しようとする課題) ところで、前記脱水ケーキと乾ダストを均一に混合する
手段として、パグミルやミキサー等の混合機を使用する
のが一般的であるが、これら混合機を使用した場合、フ
ィルターによって圧縮された脱水ケーキはその内部に含
有した水分が表面に浸出するため、羽根や軸に脱水ケー
キが容易に付着し、均一な混合ができなくなるという問
題がある。そして均一混合ができ゜なくなると、含有水
分が20%程度と高い状態のままの部分が存在し、次の
ような問題も生じる。
(Problem to be Solved by the Invention) By the way, as a means for uniformly mixing the dehydrated cake and dry dust, it is common to use a mixer such as a pug mill or a mixer. Since the moisture contained in the dehydrated cake compressed by the filter leaks to the surface, there is a problem that the dehydrated cake easily adheres to the blades and shafts, making it impossible to mix uniformly. If uniform mixing is no longer possible, there will be parts where the moisture content remains as high as about 20%, causing the following problems.

すなわち、細粒化する手段としては、高速回転する刃と
固定刃とで剪断する解砕機が一般に使用されているが、
前記したように20%程度の含有水分を含む部分では解
砕機で細粒化することが困難となる。
In other words, a crusher that uses a high-speed rotating blade and a fixed blade to shear the particles is generally used as a means of reducing the size of the particles.
As mentioned above, it is difficult to reduce the part containing about 20% water into fine particles using a crusher.

本発明は以上述べたような従来の解砕方法にあった問題
点を解決できる方法を提供することを目的としている。
An object of the present invention is to provide a method capable of solving the problems of conventional crushing methods as described above.

(課題を解決するための手段) 上記目的を達成するために本発明は、スラリーをフィル
タープレスで脱水した後この脱水ケーキを粗解砕及び一
次解砕し、次にこれら解砕後の脱水ケーキに乾ダストを
添加した後これら脱水ケーキ、乾ダストを二次解砕機で
均一混合と細粒解砕を同時に行うこととしており、その
際の脱水ケーキと乾ダストとの混合割合が10:5〜1
0:7となるように乾ダストを添加するのである。
(Means for Solving the Problems) In order to achieve the above object, the present invention dehydrates the slurry with a filter press, then roughly crushes and primary crushes the dehydrated cake, and then crushes the dehydrated cake after crushing. After adding dry dust, these dehydrated cakes and dry dust are simultaneously mixed uniformly and finely crushed in a secondary crusher, and the mixing ratio of the dehydrated cake and dry dust is 10:5 to 10:5. 1
Dry dust is added so that the ratio is 0:7.

かかる本発明方法によれば、脱水ケーキの水分含有率が
20%程度であっても一次解砕は可能である。これは混
合機と異なり解砕機が高速剪断によって細粒化を行うか
らであり、多少の粗粒が残存しても次の二次解砕機で十
分細粒化される。
According to the method of the present invention, primary crushing is possible even if the moisture content of the dehydrated cake is about 20%. This is because, unlike a mixer, a crusher uses high-speed shear to refine the particles, and even if some coarse particles remain, they will be sufficiently refined in the next secondary crusher.

そして、一次解砕後の脱水ケーキと乾ダストの混合も、
二次解砕機を使用することにより、脱水ケーキが細粒化
される時に脱水ケーキの表面に乾ダストが付着するよう
な形で混合されるため解砕機内への付着は起こらず均一
に混合できる。
Also, the mixing of the dehydrated cake and dry dust after the primary crushing,
By using a secondary crusher, when the dehydrated cake is pulverized, it is mixed in such a way that dry dust adheres to the surface of the dehydrated cake, so it does not adhere to the inside of the crusher and can be mixed uniformly. .

なお、一次解砕機と二次解砕機とで解砕歯の間隙に差は
ないが、本発明のように二段に解砕することによって細
粒化が可能となる。しかし、水分含有率が20%程度の
脱水ケーキのみの場合には二段に解砕しても細粒化がで
きないため、本発明では二次解砕機で乾ダストと混合さ
せて水分含有率を低下させ細粒化を行っている。
Although there is no difference in the gap between the crushing teeth between the primary crusher and the secondary crusher, finer particles can be obtained by crushing in two stages as in the present invention. However, in the case of only a dehydrated cake with a moisture content of about 20%, it cannot be made into fine particles even if it is crushed in two stages. Therefore, in the present invention, the moisture content is reduced by mixing it with dry dust in a secondary crusher. The grain size is reduced and refined.

本発明において、脱水ケーキと乾ダストとの混合割合を
10:5〜10:7としたのは、混合後の水分が11%
以下では発塵し、また16%以上では搬送装置等への付
着があるためである。
In the present invention, the mixing ratio of dehydrated cake and dry dust is set to 10:5 to 10:7 because the water content after mixing is 11%.
This is because if it is less than 16%, dust will be generated, and if it is more than 16%, it will adhere to the conveying device, etc.

(実 施 例) 以下本発明方法を添付図面に示す一実施例に基づいて説
明する. 図面において、1は製鉄所で発生したスラリーの貯槽で
あり、この貯槽1内のスラリーはフィルタープレス2で
水分含有率が20%程度迄脱水された後粗解砕機3に送
られ、ここで粗解砕される。
(Example) The method of the present invention will be explained below based on an example shown in the attached drawings. In the drawing, 1 is a storage tank for slurry generated at a steelworks. The slurry in this storage tank 1 is dehydrated in a filter press 2 to a water content of about 20%, and then sent to a coarse crusher 3, where it is coarsely crushed. It is disintegrated.

そして粗解砕された脱水ケーキは次に乾ダスト4との混
合を良好にするため一次解砕機5に送られ、ここで一次
解砕される。その後、一次解砕された脱水ケーキの量に
合わせてその混合率が10:5〜10:7となるように
乾ダスト4をロータリーバルプ6で切出し調整して前記
一次解砕された脱水ケーキ上に落とし、この状態で二次
解砕機7に送られる。二次解砕機7では、一次解砕後の
脱水ケーキ8と、この上に落下された乾ダスト4を同時
に混合・細粒化してホッパ−9に送る。この二次解砕機
7では脱水ケーキ8が細粒化される時脱水ケーキ8の表
面に乾ダスト4が付着するような形で混合されるため、
機内への付着は起こらない。
The coarsely crushed dehydrated cake is then sent to a primary crusher 5 for good mixing with the dry dust 4, where it is primarily crushed. Thereafter, the dry dust 4 is cut out and adjusted with the rotary valve 6 so that the mixing ratio is 10:5 to 10:7 according to the amount of the primary crushed dehydrated cake, and then the dry dust 4 is adjusted on the primary crushed dehydrated cake. and sent to the secondary crusher 7 in this state. In the secondary crusher 7, the dehydrated cake 8 after the primary crushing and the dry dust 4 dropped thereon are simultaneously mixed and pulverized and sent to a hopper 9. In this secondary crusher 7, when the dehydrated cake 8 is pulverized, it is mixed in such a way that the dry dust 4 adheres to the surface of the dehydrated cake 8.
No adhesion to the interior of the aircraft.

次に本発明方法を用いて実際にフィルタープレス脱水ケ
ーキを解砕した際の結果を説明する。
Next, the results of actually crushing a filter press dehydrated cake using the method of the present invention will be explained.

使用に供した脱水ケーキと乾ダストの主成分と水分含有
率は下記第1表に示す如くである。
The main components and moisture content of the dehydrated cake and dry dust used are as shown in Table 1 below.

第1表 (単位二%) そして上記第1表に示す成分、水分含有率の脱水ケーキ
を粗解砕した後、一次解砕した。粗解砕後の粒度分布を
下記第2表に、又一次解砕後の粒度分布を下記第3表に
示す。
Table 1 (Unit: 2%) The dehydrated cake having the components and water content shown in Table 1 above was roughly crushed and then primary crushed. The particle size distribution after coarse crushing is shown in Table 2 below, and the particle size distribution after primary crushing is shown in Table 3 below.

第2表 (単位二%) 第3表 (単位二%) 上記第3表に示す粒度に一次解砕した脱水ケーキに、乾
ダストの混合比率を変えて二次解砕した際の粒度分布と
、水分含有率を下記第4表に示す。
Table 2 (Unit: 2%) Table 3 (Unit: 2%) Particle size distribution when the dehydrated cake that has been primarily crushed to the particle size shown in Table 3 above is subjected to secondary crushing by changing the mixing ratio of dry dust. The moisture content is shown in Table 4 below.

上記第4表より明らかなように本発明方法によって解砕
した脱水ケーキは、その粒度分布が焼結受入基準の粒径
10m以上がlO%以下を全て満足する。
As is clear from Table 4 above, the particle size distribution of the dehydrated cake crushed by the method of the present invention satisfies the sintering acceptance standard of particle diameters of 10 m or more and 10% or less.

また水分含有率については、乾ダスト添加率を上げると
水分の含有率が低下するのは当然であるが、ハンドリン
グ上及びホッパー詰まり等の防止の為、脱水ケーキ10
に対して乾ダストを5〜7の割合で添加することにより
、焼結利用可能な水分含有率(11〜16%)になり得
る。
Regarding the moisture content, it is natural that the moisture content will decrease as the dry dust addition rate increases, but for handling reasons and to prevent hopper clogging, we
By adding dry dust at a ratio of 5 to 7, the moisture content (11 to 16%) that can be used for sintering can be achieved.

なお、混合機と解砕機を使用した従来方法で上記第1表
に示す成分、水分含有率の脱水ケーキと乾ダストを使用
した結果、混合が不均一で水分が23%の部分もあり解
砕が困難となり、焼結に利用できなかった。
In addition, as a result of using the dehydrated cake and dry dust with the ingredients and moisture content shown in Table 1 above using a conventional method using a mixer and a crusher, the mixture was uneven and there were parts with a moisture content of 23%, which resulted in the crushing. This made it difficult to use for sintering.

(発明の効果) 以上説明したように本発明方法によれば、焼結に利用可
能なようにフィルタープレス脱水ケーキを細粒化しかつ
水分調整ができる。
(Effects of the Invention) As explained above, according to the method of the present invention, a filter press dehydrated cake can be made into fine particles and its water content can be adjusted so that it can be used for sintering.

【図面の簡単な説明】[Brief explanation of drawings]

第1図は本発明方法の説明図で、(イ)は概略全体図、
(口)はその要部詳細図である.2はフィルタープレス
、3は粗解砕機、4は乾ダスト、5は一次解砕機、6は
ロータリーバルプ、7は二次解砕機、8は脱水ケーキ.
FIG. 1 is an explanatory diagram of the method of the present invention, where (a) is a schematic overall diagram;
(opening) is a detailed diagram of its main parts. 2 is a filter press, 3 is a coarse crusher, 4 is a dry dust, 5 is a primary crusher, 6 is a rotary valve, 7 is a secondary crusher, 8 is a dehydrated cake.

Claims (2)

【特許請求の範囲】[Claims] (1)スラリーをフィルタープレスで脱水した後この脱
水ケーキを粗解砕及び一次解砕し、次にこれら解砕後の
脱水ケーキに乾ダストを添加した後これら脱水ケーキ、
乾ダストを二次解砕機で均一混合と細粒解砕を同時に行
うことを特徴とするフィルタープレス脱水ケーキの解砕
方法。
(1) After dewatering the slurry with a filter press, this dehydrated cake is roughly crushed and primary crushed, and then dry dust is added to the dehydrated cake after crushing, and then these dehydrated cakes,
A method for crushing a filter press dewatered cake, which is characterized by uniformly mixing dry dust and crushing it into fine particles at the same time using a secondary crusher.
(2)脱水ケーキと乾ダストとの混合割合が10:5〜
10:7となるように乾ダストを添加することを特徴と
する請求項1記載のフィルタープレス脱水ケーキの解砕
方法。
(2) The mixing ratio of dehydrated cake and dry dust is 10:5~
2. The method for crushing a filter press dehydrated cake according to claim 1, wherein the dry dust is added in a ratio of 10:7.
JP2008930A 1990-01-17 1990-01-17 Disintegrating method for dehydrated cake of filter press Pending JPH03215631A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2008930A JPH03215631A (en) 1990-01-17 1990-01-17 Disintegrating method for dehydrated cake of filter press

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2008930A JPH03215631A (en) 1990-01-17 1990-01-17 Disintegrating method for dehydrated cake of filter press

Publications (1)

Publication Number Publication Date
JPH03215631A true JPH03215631A (en) 1991-09-20

Family

ID=11706380

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2008930A Pending JPH03215631A (en) 1990-01-17 1990-01-17 Disintegrating method for dehydrated cake of filter press

Country Status (1)

Country Link
JP (1) JPH03215631A (en)

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5245518A (en) * 1975-10-08 1977-04-11 Chikara Hidaka Production process of pellets using iron ore dust generated from raw m aterial for iron manufacture as raw material
JPS62267431A (en) * 1986-05-13 1987-11-20 Kawasaki Steel Corp Manufacture of minipellet
JPH01104723A (en) * 1987-10-15 1989-04-21 Kawasaki Steel Corp Production of sintering raw material from iron making dust

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5245518A (en) * 1975-10-08 1977-04-11 Chikara Hidaka Production process of pellets using iron ore dust generated from raw m aterial for iron manufacture as raw material
JPS62267431A (en) * 1986-05-13 1987-11-20 Kawasaki Steel Corp Manufacture of minipellet
JPH01104723A (en) * 1987-10-15 1989-04-21 Kawasaki Steel Corp Production of sintering raw material from iron making dust

Similar Documents

Publication Publication Date Title
US4464479A (en) Method for treating red mud
CN1086560C (en) Konjaku fine flour wet processing method using water as medium
JPH03215631A (en) Disintegrating method for dehydrated cake of filter press
CN216727410U (en) Preparation high-quality calcium aluminate is raw material crushing device for powder
JPH01312036A (en) Manufacture of raw material for sintering from dust from iron manufacture and fine iron ore
JPS6152199B2 (en)
CA1297673C (en) Water slurry of carbonized substances, and process of manufacturing the same
CN221472987U (en) Straw screening and crushing system
JP4441715B2 (en) Method for producing coal ash slurry material for ground material
JPS59157185A (en) Preparation of coal-water slurry
JPS63172789A (en) Production of coal-water slurry
JPH04234969A (en) Method for homogeneously mixing feed stocks and equipment therefor
JP2840976B2 (en) Cement finish grinding method using high pressure roll mill
JPS63172792A (en) Production of coal slurry
KR19990064745A (en) The provender making apparatus and making method using food garbage
JPS6297700A (en) Apparatus for treating dehydrated cake
JPS6135208Y2 (en)
CN1387955A (en) Combined processing method of superfine crushing and preservative coating of plant material
KR200258459Y1 (en) Differentiate powdering machine)
JPH0576518B2 (en)
JPS5980322A (en) Granulation of coal
GB509991A (en) Improvements in and relating to the treatment of zein
JPH02116652A (en) Production of hydraulic cement board
JPH0150450B2 (en)
JPS5676490A (en) Coal slurry