JPH1066895A - Classification device of particle in liquid - Google Patents

Classification device of particle in liquid

Info

Publication number
JPH1066895A
JPH1066895A JP22509196A JP22509196A JPH1066895A JP H1066895 A JPH1066895 A JP H1066895A JP 22509196 A JP22509196 A JP 22509196A JP 22509196 A JP22509196 A JP 22509196A JP H1066895 A JPH1066895 A JP H1066895A
Authority
JP
Japan
Prior art keywords
liquid
particles
sorting chamber
flow
horizontal flow
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.)
Withdrawn
Application number
JP22509196A
Other languages
Japanese (ja)
Inventor
Yoshinao Komatsu
由尚 小松
Hideo Nawata
秀夫 縄田
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.)
Mitsubishi Heavy Industries Ltd
Original Assignee
Mitsubishi Heavy 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 Mitsubishi Heavy Industries Ltd filed Critical Mitsubishi Heavy Industries Ltd
Priority to JP22509196A priority Critical patent/JPH1066895A/en
Publication of JPH1066895A publication Critical patent/JPH1066895A/en
Withdrawn legal-status Critical Current

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  • Separation Of Solids By Using Liquids Or Pneumatic Power (AREA)

Abstract

PROBLEM TO BE SOLVED: To efficiently separate and recover coarse particles and fine particles in liquid without supplying excess liquid. SOLUTION: A horizontal flow 14 is caused in the upper part by an inflow port 1 and an outflow port 2 of liquid. A first selection chamber 4 and a second selection chamber 5 are provided on the upstream side and the downstream side in the lower part of the horizontal flow 14. A classification leg 3 receiving particles is provided successively in the lower part of the first selection chamber 4. A flow path, which is extended from the upper part of the classification leg 3 to the top and joined to the horizontal flow 14, is provided. Liquid in the second selection chamber 5 is spouted upward from a conduit pipe 10 into the flow path 7.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、例えば排煙脱硫装
置の脱硫排水から再生したMg(OH)2 (以下水マグ
という)及び副産物であるCaSO4 ・2H2 O(以下
二水石膏という)を連続的に分離回収する場合等に用い
られる液中粒子の分級装置に関する。
The present invention relates to, for example, Mg (OH) 2 (hereinafter referred to as “water mug”) regenerated from desulfurization effluent of a flue gas desulfurization unit and CaSO 4 .2H 2 O (hereinafter referred to as “dihydrate gypsum”) as a by-product. The present invention relates to an apparatus for classifying particles in a liquid used for continuously separating and recovering particles.

【0002】[0002]

【従来の技術】図2に、従来の液中粒子の分級装置とし
ての水力分級器を示す。流入口01より原液を流入させ
水平流014 を発生させ流出口02より流出させる。原液
に含まれる粗粒及び微粒とも最初は選別室04に沈降す
るが、選別室04の底部の流入口015 より供給する液流
量を適当な量に調整すれば、選別室04内の上昇流011
の強さを微粒のみを持ち上げる強さにできるので、微粒
のみが再度水平流014 にのる。
2. Description of the Related Art FIG. 2 shows a hydraulic classifier as a conventional apparatus for classifying particles in liquid. The undiluted solution flows in from the inflow port 01, generates a horizontal flow 014, and flows out from the outflow port 02. Both coarse particles and fine particles contained in the undiluted liquid initially settle in the sorting chamber 04, but if the flow rate of the liquid supplied from the inlet 015 at the bottom of the sorting chamber 04 is adjusted to an appropriate amount, the upward flow 011 in the sorting chamber 04
Can be made to lift only the fine particles, so that only the fine particles again flow into the horizontal flow 014.

【0003】このようにすることで、微粒を流出口02
から、粗粒を下部の粒子抜出口09からそれぞれ独立に
抜出すことができる。
[0003] By doing so, the fine particles are discharged from the outlet 02
Thus, the coarse particles can be independently extracted from the lower particle extraction outlet 09.

【0004】[0004]

【発明が解決しようとする課題】図2に示す従来の分級
装置では、原液に含まれた粗粒及び微粒をともに選別室
04に沈降させており、微粒と粗粒を分級するために余
分な水の供給をしなくてはならず排水量が増加してしま
う。また、微粒のうちには粗粒表面への物理的吸着等に
よって粗粒に連行されることにより沈降するものもあ
り、それらを更に分離・回収することにより、粗粒の純
度及び微粒の回収率の向上を図る必要がある。
In the conventional classifier shown in FIG. 2, both coarse particles and fine particles contained in the stock solution are settled in the sorting chamber 04, and extra particles are required to classify the fine particles and coarse particles. Water must be supplied and the amount of drainage increases. In addition, some of the fine particles settle by being entrained by the coarse particles due to physical adsorption to the surface of the coarse particles. By separating and recovering them further, the purity of the coarse particles and the recovery rate of the fine particles Needs to be improved.

【0005】本発明は、以上の問題点を解決することが
できる液中粒子の分級装置を提供しようとするものであ
る。
An object of the present invention is to provide an apparatus for classifying submerged particles that can solve the above problems.

【0006】[0006]

【課題を解決するための手段】本発明の液中粒子の分級
装置は、分級装置内の上部に粒子を含む液の水平流を発
生させる液の流入口と流出口、分級装置内の前記水平流
の下方において水平流の上流側と下流側にそれぞれ設け
られた第1選別室と第2選別室、前記第1選別室の下方
に連設され同第1選別室に沈降した粒子を受入れる分級
脚、前記分級脚の上部より上方へ延び前記水平流に合流
する流路、及び前記第2選別室内の液を前記流路内へ上
方へ向って吹出す手段を備えたことを特徴とする。
According to the present invention, there is provided an apparatus for classifying particles in a liquid, comprising: an inlet and an outlet for a liquid for generating a horizontal flow of a liquid containing particles at an upper portion in the classifier; A first sorting chamber and a second sorting chamber provided on the upstream side and the downstream side of the horizontal flow below the flow, and a classifier provided below the first sorting chamber and receiving particles settled in the first sorting chamber. A leg extending upward from an upper portion of the classifying leg and joining the horizontal flow; and a means for blowing the liquid in the second sorting chamber upward into the flow channel.

【0007】本発明では、流入口から流出口へ向う水平
流をなす液中の粒子のうち、粒径の大きい粗粒は上流側
の第1選別室に沈降し、粒径の小さい微粒は下流側の第
2選別室に沈降する。残りの微粒は液と共に流出口より
流出する。
In the present invention, among the particles in the liquid forming a horizontal flow from the inlet to the outlet, coarse particles having a large particle diameter settle in the first sorting chamber on the upstream side, and fine particles having a small particle diameter are deposited on the downstream side. Settles in the second sorting room on the side. The remaining fine particles flow out of the outlet together with the liquid.

【0008】第1選別室に沈降した粗粒は分級脚内に受
入れられる。分級脚の上部より上方へ延びる流路には、
前記第2選別室内の微粒を含む液が吹出されており、分
級脚内の粗粒を含む液は前記第2選別室より吹出される
液によって流動化された上、その1部は前記流路内を上
昇して水平流に合流する。
[0008] The coarse particles settled in the first sorting chamber are received in a classification leg. In the channel extending above the upper part of the classification leg,
A liquid containing fine particles in the second sorting chamber is blown out, and a liquid containing coarse particles in the classification leg is fluidized by the liquid blown out from the second sorting chamber, and a part of the liquid is mixed with the flow path. It rises inside and joins a horizontal flow.

【0009】このように、分級脚内の粗粒を含む液を第
2選別室より流路内に吹出される液によって流動化する
ことによって、分級脚に受入れられた粗粒に連行された
微粒は流動化されて粗粒より分離し、その上で微粒は前
記流路内を上昇して水平流に合流し、前記と同様な水平
流による分離が行なわれる。
As described above, the liquid containing coarse particles in the classification leg is fluidized by the liquid blown out from the second sorting chamber into the flow path, so that the fine particles entrained in the coarse particles received in the classification leg. Is fluidized and separated from coarse particles, on which fine particles rise in the flow path and join a horizontal flow, and the same horizontal flow separation is performed as described above.

【0010】従って、本発明によれば、粗粒と微粒を回
収率よく分離回収することができる。
Therefore, according to the present invention, coarse particles and fine particles can be separated and recovered at a high recovery rate.

【0011】また、前記流路内には第2選別室内の液を
前記流路に吹出しているので、余分な液が分離装置に供
給されることがなく、従って、排液量が増加することは
ない。
Further, since the liquid in the second sorting chamber is blown into the flow path into the flow path, no extra liquid is supplied to the separation device, and therefore, the amount of drainage increases. There is no.

【0012】[0012]

【発明の実施の形態】本発明の実施の一形態を、図1に
よって説明する。本実施の形態は、水酸化マグネシウム
法による排煙脱硫を行った脱硫排水にCa(OH)2
加えることにより再生したMg(OH)2 (水マグ)と
副産物として発生したCaSO4 ・2H2 O(二水石
膏)の混和液を分級する装置に係る。
DESCRIPTION OF THE PREFERRED EMBODIMENTS One embodiment of the present invention will be described with reference to FIG. In the present embodiment, Mg (OH) 2 (water mug) regenerated by adding Ca (OH) 2 to desulfurization wastewater subjected to flue gas desulfurization by the magnesium hydroxide method and CaSO 4 .2H 2 generated as a by-product The present invention relates to an apparatus for classifying a mixed solution of O (gypsum).

【0013】分級装置には、その上部に水平流14を発
生させる水マグと二水石膏の混合スラリーである原液の
流入口1と流出口2が設けられている。分級装置内の水
平流14の下方の部分には、上流側の第1選別室4と下
流側の第2選別室5が設けられている。
The classifier is provided with an inlet 1 and an outlet 2 of a stock solution, which is a mixed slurry of a water mug and gypsum gypsum, for generating a horizontal flow 14 at the upper part thereof. A first sorting chamber 4 on the upstream side and a second sorting chamber 5 on the downstream side are provided below the horizontal flow 14 in the classification device.

【0014】第1選別室4の下方には同選別室4に沈降
した粒子を受入れる分級脚3が連設されている。同分級
脚3の上部からは仕切板6と分級装置の上流側の側壁に
よって構成される流路7が上方へ延び、同流路7の上端
は合流点13において前記水平流14に合流するように
なっている。
Below the first sorting chamber 4, a classifying leg 3 for receiving particles settled in the sorting chamber 4 is connected. A flow path 7 constituted by a partition plate 6 and an upstream side wall of the classification device extends upward from the upper part of the classifying leg 3, and the upper end of the flow path 7 joins the horizontal flow 14 at a junction 13. It has become.

【0015】前記第2選別室2の底部に接続されポンプ
8をもつ導水管10の下流端は前記流路7内に上方へ向
って開口しており、同流路7内に第2選別室2内の液を
上方へ向って吹出すようになっている。
A downstream end of a water guide pipe 10 connected to the bottom of the second sorting chamber 2 and having a pump 8 is open upward in the flow path 7, and is provided in the second sorting chamber 2. The liquid in 2 is blown upward.

【0016】なお、9は分級脚3の下部に設けられた粒
子抜出口であり、また、分級脚3内には、同分級脚3内
の液を流動化させるスクリュー又は振動膜(図示省略)
が設けられている。
Reference numeral 9 denotes a particle outlet provided below the classifying leg 3, and a screw or a vibrating membrane (not shown) for fluidizing the liquid in the classifying leg 3 is provided in the classifying leg 3.
Is provided.

【0017】本実施の形態では、流入口1から原液(水
マグと二水石膏の混合スラリー)を流入させ、水平流1
4を発生させる。水平流14が流出口2から流出するま
での間に粒径の大きい粗粒の二水石膏は第1選別室4
に、粒径の小さな微粒の水マグの1部は第2選別室5に
沈降し、残りの水マグは液と共に流出口2より流出す
る。
In this embodiment, the undiluted solution (mixed slurry of water mug and gypsum) is introduced from the inlet 1 into the horizontal flow 1
4 is generated. Before the horizontal flow 14 flows out of the outlet 2, the coarse gypsum gypsum having a large particle size is removed from the first sorting chamber 4
Then, a part of the water mug having a small particle diameter is settled in the second sorting chamber 5, and the remaining water mug flows out from the outlet 2 together with the liquid.

【0018】第1選別室4に沈降した粗粒の二水石膏は
第1選別室4の下部にある分級脚3に受入れられて堆積
する。この堆積した二水石膏の圧密を防ぐために分級脚
3内の液を図示しないスクリュー又は振動膜及び後記す
る導水管10より吹出される液によって流動させること
で二水石膏を流動化させ、粒子抜出口9より抜き出す。
二水石膏を流動させることにより表面に付着している水
マグが分離し、分級脚上部12付近に浮遊する。
The coarse gypsum gypsum that has settled in the first sorting chamber 4 is received by the classifying legs 3 at the bottom of the first sorting chamber 4 and is deposited. In order to prevent compaction of the deposited gypsum, the liquid in the classifying leg 3 is fluidized by a screw or a vibrating membrane (not shown) and a liquid blown out from a water pipe 10 described later to fluidize the gypsum and remove particles. Pull out from exit 9.
By flowing the gypsum dihydrate, the water mug adhering to the surface is separated and floats near the classifying leg upper portion 12.

【0019】第2選別室5に沈降した微粒の水マグはポ
ンプ8を用いて液と共に導水管10より流路7内に吹出
され、上昇流11を発生させると共に前記のようにこの
上昇流11によって分級脚3内の二水石膏を含む液を流
動化させる。この上昇流11により分級脚上部12付近
に浮遊している水マグ及び第2選別室5内の水マグを合
流点13まで運び、再度水平流14にのせ、流出口2か
ら抜き出す。
The fine water mug settled in the second sorting chamber 5 is blown out together with the liquid from the water pipe 10 into the flow channel 7 by using the pump 8 to generate the upward flow 11 and, as described above, the upward flow 11 The fluid containing gypsum in the classifying leg 3 is fluidized. With this ascending flow 11, the water mug floating near the classification leg upper part 12 and the water mug in the second sorting chamber 5 are conveyed to the confluence 13 and placed on the horizontal flow 14 again and extracted from the outlet 2.

【0020】このように、本実施の形態では、分級脚1
3内の二水石膏の粗粒に連行された水マグの微粒を粗粒
から分離させて再度水平流14にのせることによって、
二水石膏と水マグの分離を効率よく行なうことができ
る。
As described above, in the present embodiment, the classifying leg 1
By separating the fine particles of the water mug entrained in the coarse particles of gypsum in 3 from the coarse particles and placing the fine particles again on the horizontal stream 14,
Gypsum and water mug can be efficiently separated.

【0021】また、第2選別室5内の液を流路7に吹出
しているために、余分な液の供給は行なわれず、分級装
置からの排水量が増加することはない。
Further, since the liquid in the second sorting chamber 5 is blown out to the flow path 7, no extra liquid is supplied, and the amount of drainage from the classification device does not increase.

【0022】[0022]

【発明の効果】以上説明したように、本発明は、分級の
ための余分な液を供給することなく粗粒と微粒を効率よ
く分離し、回収される粗粒の純度を上げ、また、微粒の
回収率を向上させることができる。
As described above, according to the present invention, coarse particles and fine particles can be efficiently separated without supplying an extra liquid for classification, and the purity of the recovered coarse particles can be increased. Recovery rate can be improved.

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

【図1】本発明の実施の一形態の断面図である。FIG. 1 is a sectional view of an embodiment of the present invention.

【図2】従来の液中粒子の分級装置の断面図である。FIG. 2 is a cross-sectional view of a conventional apparatus for classifying particles in liquid.

【符号の説明】[Explanation of symbols]

1 流入口 2 流出口 3 分級脚 4 第1選別室 5 第2選別室 6 仕切板 7 流路 8 ポンプ 9 粒子抜出口 10 導水管 11 上昇流 12 分級脚上部 13 合流点 14 水平流 15 供給口 DESCRIPTION OF SYMBOLS 1 Inflow 2 Outflow 3 Classification leg 4 1st sorting room 5 2nd sorting room 6 Partition plate 7 Flow path 8 Pump 9 Particle extraction outlet 10 Water pipe 11 Upflow 12 Classification leg upper part 13 Confluence point 14 Horizontal flow 15 Supply port

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 分級装置内の上部に粒子を含む液の水平
流を発生させる液の流入口と流出口、分級装置内の前記
水平流の下方において水平流の上流側と下流側にそれぞ
れ設けられた第1選別室と第2選別室、前記第1選別室
の下方に連設され同第1選別室に沈降した粒子を受入れ
る分級脚、前記分級脚の上部より上方へ延び前記水平流
に合流する流路、及び前記第2選別室内の液を前記流路
内へ上方へ向って吹出す手段を備えたことを特徴とする
液中粒子の分級装置。
1. An inflow port and an outflow port for a liquid that generates a horizontal flow of a liquid containing particles at an upper portion in a classifier, and an upstream and a downstream of the horizontal flow below the horizontal flow in the classifier. A first sorting chamber and a second sorting chamber, a classifying leg that is provided below the first sorting room and receives particles settled in the first sorting room, and extends upward from an upper portion of the classifying leg to form the horizontal flow. An apparatus for classifying particles in a liquid, comprising: a flow path for merging; and means for blowing liquid in the second sorting chamber upward into the flow path.
JP22509196A 1996-08-27 1996-08-27 Classification device of particle in liquid Withdrawn JPH1066895A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP22509196A JPH1066895A (en) 1996-08-27 1996-08-27 Classification device of particle in liquid

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP22509196A JPH1066895A (en) 1996-08-27 1996-08-27 Classification device of particle in liquid

Publications (1)

Publication Number Publication Date
JPH1066895A true JPH1066895A (en) 1998-03-10

Family

ID=16823865

Family Applications (1)

Application Number Title Priority Date Filing Date
JP22509196A Withdrawn JPH1066895A (en) 1996-08-27 1996-08-27 Classification device of particle in liquid

Country Status (1)

Country Link
JP (1) JPH1066895A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPWO2012165560A1 (en) * 2011-06-02 2015-02-23 新東工業株式会社 Classification device and classification method, and blasting device and blasting method provided with the classification device

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPWO2012165560A1 (en) * 2011-06-02 2015-02-23 新東工業株式会社 Classification device and classification method, and blasting device and blasting method provided with the classification device

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