JPS6365379B2 - - Google Patents

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Publication number
JPS6365379B2
JPS6365379B2 JP59068227A JP6822784A JPS6365379B2 JP S6365379 B2 JPS6365379 B2 JP S6365379B2 JP 59068227 A JP59068227 A JP 59068227A JP 6822784 A JP6822784 A JP 6822784A JP S6365379 B2 JPS6365379 B2 JP S6365379B2
Authority
JP
Japan
Prior art keywords
titanium oxide
hopper
slurry
space
classification
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
Application number
JP59068227A
Other languages
Japanese (ja)
Other versions
JPS60212252A (en
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 filed Critical
Priority to JP6822784A priority Critical patent/JPS60212252A/en
Publication of JPS60212252A publication Critical patent/JPS60212252A/en
Publication of JPS6365379B2 publication Critical patent/JPS6365379B2/ja
Granted legal-status Critical Current

Links

Description

【発明の詳細な説明】 [産業上の利用分野] 本発明は酸化チタンスラリから粗大粒子を連続
的に分級除去することが可能な分級装置に関する
ものである。
DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field] The present invention relates to a classification device capable of continuously classifying and removing coarse particles from titanium oxide slurry.

酸化チタンスラリは、酸化チタン含有合成重合
体を製造する場合などに用いられる。特に、その
重合体を繊維とする場合には、酸化チタンは微細
粒子で分散していることが必要である。そのため
に、数μm程度のような粗大粒子も1μm未満のよ
うな微細粒子も共に含む酸化チタンスラリから粗
大粒子を分級除去することにより、微細粒子のみ
を含有する酸化チタンスラリを製造することが一
般に行われている。
Titanium oxide slurry is used when producing a titanium oxide-containing synthetic polymer. In particular, when the polymer is used as fiber, titanium oxide must be dispersed in fine particles. For this purpose, it is generally possible to produce a titanium oxide slurry containing only fine particles by classifying and removing coarse particles from a titanium oxide slurry that contains both coarse particles of several μm and fine particles of less than 1 μm. It is being done.

[従来の技術] その酸化チタンスラリの分級装置としては、一
定の空間を有する分級槽の上部にサイホン管を設
けた装置が知られている(特公昭57−5582号公
報)。この装置は、その上方からスラリ原液を供
給して一定時間放置した後、サイホン管を通して
微細粒子のみを含有する上澄液を抜出す方法によ
つて酸化チタンスラリの分級を行うものである。
[Prior Art] As a classification device for titanium oxide slurry, a device is known in which a siphon tube is provided at the top of a classification tank having a certain space (Japanese Patent Publication No. 57-5582). This device classifies titanium oxide slurry by supplying a slurry stock solution from above, leaving it for a certain period of time, and then extracting a supernatant liquid containing only fine particles through a siphon tube.

[発明が解決しようとする課題] ところが、この装置では、分級操作をバツチシ
ステムで行わざるを得ないので、微細粒子スラリ
を連続的に取出すことができず生産性が低い。
[Problems to be Solved by the Invention] However, in this apparatus, the classification operation must be performed in a batch system, and therefore the fine particle slurry cannot be taken out continuously, resulting in low productivity.

そこで、この酸化チタンスラリの分級を連続的
に行うため、多数の傾斜板を有するラメラ空間に
より分離を連続的に行う傾斜板型沈降分離装置の
適用を試みた。
Therefore, in order to continuously classify this titanium oxide slurry, we attempted to apply an inclined plate type sedimentation separator that performs continuous separation using a lamellar space having a large number of inclined plates.

ところが、この傾斜板型沈降分離装置は、下水
処理における砂と腐敗有機分との分離のように、
沈降物の粒子径や比重がそれ以外の物と大きく異
なる場合の沈降分離に適用されてきていたので、
従来の装置構造では、酸化チタンスラリから粗大
粒子を分級除去することは困難であつた。
However, this inclined plate type sedimentation separator is difficult to use, such as separating sand and decaying organic matter in sewage treatment.
It has been applied to sedimentation separation when the particle size and specific gravity of sediment are significantly different from other materials.
With conventional equipment structures, it has been difficult to classify and remove coarse particles from titanium oxide slurry.

そこで、本発明は、酸化チタンスラリからの粗
大粒子の分級除去を連続的に行うことが可能な傾
斜板型の分級装置の開発を目的に鋭意検討した結
果、本発明をなすに至つたものである。
Therefore, the present invention was developed as a result of intensive studies aimed at developing an inclined plate type classification device that can continuously classify and remove coarse particles from titanium oxide slurry. be.

[課題を解決するための手段] この目的を達成するため、本発明に係る酸化チ
タンスラリ用分級装置は、底面が円錘状または角
錘状をなしているホツパ1と、該ホツパの上方に
多数の平行な板8を略一定の間隔をおいてかつ一
定の角度で傾斜させて並べてなるラメラ空間2と
からなる分級槽3;前記ホツパ内の上部空間4に
開口を有する供給管5;前記ホツパ内の底部に下
を向いて開口している抜出管6;および前記ラメ
ラ空間の上方に開口を有する排出管7からなる。
[Means for Solving the Problems] In order to achieve this object, the titanium oxide slurry classification device according to the present invention includes a hopper 1 having a conical or pyramidal bottom surface, and a hopper 1 above the hopper. A classification tank 3 consisting of a lamellar space 2 in which a large number of parallel plates 8 are arranged at substantially constant intervals and inclined at a constant angle; a supply pipe 5 having an opening in the upper space 4 in the hopper; It consists of an extraction pipe 6 that opens downward at the bottom of the hopper; and a discharge pipe 7 that opens above the lamella space.

以下、本発明に係る装置の一例を示す第1図お
よび第2図に沿つて、装置の構造、その作用、効
果を説明する。なお、第1図は、分級装置の一部
分を破断して示す側面斜視図である。
Hereinafter, the structure of the device, its operation, and effects will be explained with reference to FIGS. 1 and 2 showing an example of the device according to the present invention. Note that FIG. 1 is a partially cutaway side perspective view of the classification device.

本発明に係る分級装置は、基本的には、ホツパ
1とその上に連設した状態で載つているラメラ空
間2とを有する分級槽3、ホツパ上部に取付けら
れている供給管5、ホツパ下部に取付けられてい
る抜出管6、および、ラメラ空間上方の排出管7
から成り立つている。
The classification device according to the present invention basically consists of a classification tank 3 having a hopper 1 and a lamella space 2 placed in a continuous manner on the hopper, a supply pipe 5 attached to the upper part of the hopper, and a lower part of the hopper. an extraction pipe 6 attached to the lamellar space, and a discharge pipe 7 above the lamella space.
It consists of

そして、微細粒子と粗大粒子とを共に含む酸化
チタンスラリ原液は、供給管5を通して供給さ
れ、ラメラ空間2により分級され、粗大粒子が除
去された微細粒子スラリは排出管7から取出さ
れ、また、酸化チタン粗大粒子を含む粗大粒子ス
ラリは抜出管6から取出される。
Then, the titanium oxide slurry stock solution containing both fine particles and coarse particles is supplied through the supply pipe 5, classified by the lamella space 2, and the fine particle slurry from which the coarse particles have been removed is taken out from the discharge pipe 7. A coarse particle slurry containing coarse titanium oxide particles is taken out from the extraction pipe 6.

ホツパ1は、酸化チタンスラリを一定量蓄える
とともに、酸化チタンスラリ中の酸化チタン粗大
粒子を沈降させる作用を有する。そのため一定の
容積を有する。第1図に示されているように、底
面が角錘形をしていてもよいし、また他の形状、
例えば円錘形をしていてもよい。
The hopper 1 has the function of storing a certain amount of titanium oxide slurry and sedimenting the coarse titanium oxide particles in the titanium oxide slurry. Therefore, it has a certain volume. As shown in Figure 1, the bottom surface may be pyramid-shaped, or may have other shapes,
For example, it may have a conical shape.

ラメラ空間2は、多数の平行な、いわゆる層状
の板8がほぼ一定の間隔をおいて、しかも一定の
角度で傾斜させて並べられた空間をいう。その傾
斜角度は、30〜85度、好ましくは45〜75度であれ
ばよい。本発明では、ホツパ1とラメラ空間2と
を併せて分級槽3と称する。供給管5はホツパの
上部の空間4に開口を有する管である。開口は例
えば、第2図に示されているように、ホツパの下
方に向かつて(矢印)酸化チタンスラリ原液が分
散供給されていく形状であることが好ましい。開
口の位置は板8の下端より下であつてホツパ1の
できるだけ上部であることが好ましい。
The lamellar space 2 is a space in which a large number of parallel, so-called layered plates 8 are arranged at approximately constant intervals and tilted at a constant angle. The angle of inclination may be between 30 and 85 degrees, preferably between 45 and 75 degrees. In the present invention, the hopper 1 and the lamella space 2 are collectively referred to as a classification tank 3. The supply pipe 5 is a pipe having an opening in the space 4 above the hopper. For example, as shown in FIG. 2, the opening preferably has a shape in which the titanium oxide slurry stock solution is distributed and supplied toward the bottom of the hopper (arrow). The position of the opening is preferably below the lower end of the plate 8 and as high as possible above the hopper 1.

抜出管6はその開口がホツパの底部を向いて取
付けられている。これは沈降していく粗大粒子を
含む濃度の高い酸化チタンスラリを排出するため
である。従つて、ホツパの底面の形状と抜出管の
取付方法は粗大粒子を含む高濃度酸化チタンスラ
リの排出が可能なように決められる。
The extraction pipe 6 is attached with its opening facing the bottom of the hopper. This is to discharge highly concentrated titanium oxide slurry containing coarse particles that are settling. Therefore, the shape of the bottom surface of the hopper and the method of attaching the extraction pipe are determined so as to enable discharge of the highly concentrated titanium oxide slurry containing coarse particles.

酸化チタン微細粒子スラリ取出しのための排出
管7はラメラ空間2の上方に設けられている。こ
の排出管7は粗大粒子が沈降除去され、微細粒子
のみとなつた濃度の低い酸化チタンスラリをラメ
ラ空間2から排出するために設けられている。従
つて排出管の取付位置とその開口は低濃度の酸化
チタン微細粒子スラリの排出が可能であるように
決められている。
A discharge pipe 7 for taking out the titanium oxide fine particle slurry is provided above the lamella space 2. This discharge pipe 7 is provided to discharge from the lamella space 2 a low concentration titanium oxide slurry in which coarse particles have been sedimented and removed and only fine particles are left. Therefore, the mounting position of the discharge pipe and its opening are determined so that the low concentration titanium oxide fine particle slurry can be discharged.

[作用] 上記構造の装置は次のとおり作用する。[Effect] The device of the above structure operates as follows.

粗大粒子を含む酸化チタンスラリ原液を連続的
に供給管5からホツパに供給すると、まずホツパ
内に酸化チタンスラリがたまる。それでもなお連
続的にスラリの供給を続けると、やがて酸化チタ
ンスラリがホツパからあふれ、ラメラ空間2を上
昇する。
When a titanium oxide slurry stock solution containing coarse particles is continuously supplied to the hopper from the supply pipe 5, the titanium oxide slurry first accumulates in the hopper. If the slurry is still continuously supplied, the titanium oxide slurry will eventually overflow from the hopper and rise in the lamella space 2.

ところが、ラメラ空間には傾斜した板8が一定
の間隔をおいて並べられているので上昇してくる
酸化チタンスラリ中の粗大粒子が板8の傾斜下面
に衝突し下方に押し流され、沈降する。沈降の速
度と酸化チタンスラリの上昇の速度とがつりあつ
て粒子の分級が起きる。
However, since the inclined plates 8 are arranged at regular intervals in the lamella space, the coarse particles in the rising titanium oxide slurry collide with the inclined lower surface of the plates 8, are swept downward, and settle. The rate of sedimentation and the rate of rise of the titanium oxide slurry balance to cause particle classification.

分級の程度はスラリの供給速度とラメラ空間の
断面積ならびに傾斜している板の角度に依存す
る。例えば酸化チタンスラリの場合、前記の角度
は30〜85度が好適である。
The degree of classification depends on the feed rate of the slurry and the cross-sectional area of the lamellar spaces as well as the angle of the inclined plates. For example, in the case of titanium oxide slurry, the angle is preferably 30 to 85 degrees.

このように本発明に係る分級装置は、傾斜した
ラメラ空間内における酸化チタン粗大粒子の沈降
流れと酸化チタン微細粒子スラリの上昇流れとを
つりあいを保つて生じさせることが重要である。
酸化チタンスラリの分級は、例えば、数μm以下
の酸化チタン粒子の中から1μm以上の粗大粒子を
分級除去するように、粒子径の幅が比較的狭く、
しかも、沈降除去する粒子とそれ以外の粒子との
差が極めて小さいスラリについて分級を行うので
あるから、上記した沈降流れと上昇流れとのつり
あいは、液の供給や抜出しに伴う液流の影響によ
つて乱され易い。
As described above, it is important for the classification device according to the present invention to maintain a balance between the descending flow of the titanium oxide coarse particles and the upward flow of the titanium oxide fine particle slurry in the inclined lamella space.
When classifying titanium oxide slurry, for example, coarse particles of 1 μm or more are classified and removed from titanium oxide particles of several μm or less, so the width of the particle size is relatively narrow.
Furthermore, since the classification is performed on slurry in which the difference between the particles to be settled and removed is extremely small, the balance between the above-mentioned settling flow and upward flow depends on the influence of the liquid flow accompanying the supply and withdrawal of the liquid. It is easily disturbed.

そこで、本発明に係る分級装置は、供給管5
を、ラメラ空間の下方に位置するホツパ上部空間
に開口させ、しかも、粗大粒子スラリの取出し
を、ホツパの底部に下を向けて開口させた抜出管
6により行うこととし、液の供給および取出しに
伴う悪影響を抑えることとしたものである。
Therefore, in the classification device according to the present invention, the supply pipe 5
is opened into the upper space of the hopper located below the lamella space, and the coarse particle slurry is taken out through an extraction pipe 6 which is opened facing downward at the bottom of the hopper, and the liquid is supplied and taken out. The aim was to suppress the negative effects associated with this.

[発明の効果] この装置構造により、ラメラ空間における酸化
チタン粗大粒子の沈降流れと酸化チタン微細粒子
スラリの上昇流れとをつりあいを保つて有効に生
じさせることが可能となり、従つて、酸化チタン
スラリから粗大粒子を連続的に精度よく分級除去
することができることとなり、高い生産性でもつ
て酸化チタンの分級を行うことが可能になつたの
である。
[Effects of the Invention] With this device structure, it is possible to maintain a balance between the sedimentation flow of coarse titanium oxide particles and the upward flow of titanium oxide fine particle slurry in the lamellar space, and to effectively generate the flow. It became possible to classify and remove coarse particles continuously and with high precision, and it became possible to classify titanium oxide with high productivity.

[実施例] 以下、実施例によつて本発明の装置の効果を説
明する。
[Example] Hereinafter, the effects of the apparatus of the present invention will be explained with reference to Examples.

実施例 分級装置として、第1図に示す装置構造を有
し、かつ、ホツパ部1は1000mmの四角錘形(底部
傾斜角60度)をなし、ラメラ空間部2は60度に傾
斜した1000mmの四角柱で、その内部には60度に傾
斜した板8を100mm間隔で9枚挿入されている装
置を用いた。そして、1μm以上の粗大粒子を2.4
重量%含む酸化チタン水スラリを270Kg/HR連
続的に6ケ月問供給した。
Example The classification device has the structure shown in Fig. 1, and the hopper part 1 has a 1000 mm square pyramid shape (bottom inclination angle 60 degrees), and the lamella space 2 has a 1000 mm square pyramid shape with a 60 degree inclination. The device used was a square prism, in which nine plates 8 tilted at 60 degrees were inserted at 100 mm intervals. Then, coarse particles of 1 μm or more were
Aqueous slurry of titanium oxide containing 270 kg/HR was continuously supplied for 6 months.

供給した酸化チタン水スラリの濃度は24.8重量
%、下部抜出管6から取出した粗大粒子スラリの
濃度は25.5重量%、上部排出管7から取出した微
細粒子スラリの濃度は17.0重量%であつた。
The concentration of the supplied titanium oxide water slurry was 24.8% by weight, the concentration of the coarse particle slurry taken out from the lower discharge pipe 6 was 25.5% by weight, and the concentration of the fine particle slurry taken out from the upper discharge pipe 7 was 17.0% by weight. .

上部排出管から排出されたスラリ中の酸化チタ
ン粒子は0.9μm以下であり、その酸化チタン微細
粒子スラリが22.5Kg/HRで連続的に得られた。
The titanium oxide particles in the slurry discharged from the upper discharge pipe were 0.9 μm or less, and the titanium oxide fine particle slurry was continuously obtained at 22.5 kg/HR.

6ケ月後に装置内部を点検したが、酸化チタン
の堆積物は無く、良好な運転が継続された。
Six months later, the inside of the equipment was inspected, but no titanium oxide deposits were found, and good operation continued.

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

第1図は本発明に係る分級装置の一例を示すも
のであつて一部分を破断した側面斜視図である。
第2図はそのスラリ供給管形状の一例を示す側面
斜視図である。 符号の説明、1……ホツパ、2……ラメラ空
間、3……分級槽、4……ホツパの上部空間、5
……スラリの供給管、6……スラリの抜出管、7
……スラリの排出管、8……層状の板。
FIG. 1 is a partially cutaway side perspective view showing an example of a classification device according to the present invention.
FIG. 2 is a side perspective view showing an example of the shape of the slurry supply pipe. Explanation of symbols, 1... hopper, 2... lamella space, 3... classification tank, 4... upper space of hopper, 5
... Slurry supply pipe, 6 ... Slurry extraction pipe, 7
...Slurry discharge pipe, 8...Layered plate.

Claims (1)

【特許請求の範囲】[Claims] 1 底面が円錘状または角錘状をなしているホツ
パ1と、該ホツパの上方に多数の平行な板8を略
一定の間隔をおいてかつ一定の角度で傾斜させて
並べてなるラメラ空間2とからなる分級槽3;前
記ホツパ内の上部空間4に開口を有する供給管
5;前記ホツパ内の底部に下を向いて開口してい
る抜出管6;および前記ラメラ空間の上方に開口
を有する排出管7からなる酸化チタンスラリ用分
級装置。
1 A hopper 1 whose bottom surface is conical or pyramid-shaped, and a lamellar space 2 formed by arranging a number of parallel plates 8 above the hopper at approximately constant intervals and tilted at a constant angle. A classification tank 3 consisting of; a supply pipe 5 having an opening in the upper space 4 in the hopper; a withdrawal pipe 6 opening downward at the bottom of the hopper; and an opening above the lamella space. A titanium oxide slurry classification device comprising a discharge pipe 7.
JP6822784A 1984-04-05 1984-04-05 Classifier of titanium slurry Granted JPS60212252A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP6822784A JPS60212252A (en) 1984-04-05 1984-04-05 Classifier of titanium slurry

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP6822784A JPS60212252A (en) 1984-04-05 1984-04-05 Classifier of titanium slurry

Publications (2)

Publication Number Publication Date
JPS60212252A JPS60212252A (en) 1985-10-24
JPS6365379B2 true JPS6365379B2 (en) 1988-12-15

Family

ID=13367705

Family Applications (1)

Application Number Title Priority Date Filing Date
JP6822784A Granted JPS60212252A (en) 1984-04-05 1984-04-05 Classifier of titanium slurry

Country Status (1)

Country Link
JP (1) JPS60212252A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105013600B (en) * 2015-07-03 2018-11-13 攀钢集团钛业有限责任公司 For continuously detaching coarse grained device before titanium dioxide coating process

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5355568A (en) * 1976-10-29 1978-05-20 Hitachi Metals Ltd Sewage precipitate sand cleaner
JPS5355654A (en) * 1976-10-29 1978-05-20 Hitachi Metals Ltd Sewage precipitate sand cleaner

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5355568A (en) * 1976-10-29 1978-05-20 Hitachi Metals Ltd Sewage precipitate sand cleaner
JPS5355654A (en) * 1976-10-29 1978-05-20 Hitachi Metals Ltd Sewage precipitate sand cleaner

Also Published As

Publication number Publication date
JPS60212252A (en) 1985-10-24

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