[go: up one dir, main page]

JPS63151314A - Dehydration method by filter press - Google Patents

Dehydration method by filter press

Info

Publication number
JPS63151314A
JPS63151314A JP61297954A JP29795486A JPS63151314A JP S63151314 A JPS63151314 A JP S63151314A JP 61297954 A JP61297954 A JP 61297954A JP 29795486 A JP29795486 A JP 29795486A JP S63151314 A JPS63151314 A JP S63151314A
Authority
JP
Japan
Prior art keywords
slurry
valve
air
compressed air
filter
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
Application number
JP61297954A
Other languages
Japanese (ja)
Other versions
JPH0224568B2 (en
Inventor
Masazumi Ito
正澄 伊藤
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.)
Sumitomo Heavy Industries Ltd
Original Assignee
Sumitomo 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 Sumitomo Heavy Industries Ltd filed Critical Sumitomo Heavy Industries Ltd
Priority to JP61297954A priority Critical patent/JPS63151314A/en
Publication of JPS63151314A publication Critical patent/JPS63151314A/en
Publication of JPH0224568B2 publication Critical patent/JPH0224568B2/ja
Granted legal-status Critical Current

Links

Landscapes

  • Treatment Of Sludge (AREA)
  • Filtration Of Liquid (AREA)

Abstract

PURPOSE:To effectively utilize compressed air and to enhance dehydration capacity, by providing a compressed air feed-in pipe and a filtrate discharge pipe having a filtrate flow rate measuring means at positions opposed to each other on the lateral side of a filter plate to alternately perform air blow. CONSTITUTION:A slurry is supplied into each filter chamber 4b of a filter press 4 from a slurry supply pipe 9 and, when a pressure gauge 14 detects predetermined pressure, a drain valve 7 is closed and an air blow valve 5, an air blow original valve 15 and a drain valve 8 are opened to supply compressed air received in an air receiver 3 and the slurry is dehydrated to the discharged from a drain pipe 19'. When a flow rate detector 17' does not detect a flow rate, the drain valve 8 and the air blow valve 5 are closed and an air blow valve 6 and the drain valve 7 are opened to supply compressed air from an air blow pipe 18'. Finally, a back slurry discharge valve 13 and a back blow valve 12 are opened and compressed air is supplied from a back blow pipe 11 to be discharged from a discharge pipe 16.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 この発明は、石炭・水スラリ等の固形分粒子と水とが混
合したスラリーの脱水を効率良く行うことができるフィ
ルタプレスによる脱水方法に関する。
DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a dewatering method using a filter press that can efficiently dewater a slurry in which solid particles such as coal/water slurry are mixed with water.

〔従来の技術〕[Conventional technology]

従来、出願人は固形分粒子と水とが混合したスラリーを
脱水し、それによって形成されるケーキの固形分濃度を
さらに向上させるためのフィルタプレスによる脱水方法
を発明し、すでに出願済み(特願昭58−199763
号)である。
Previously, the applicant has invented a dewatering method using a filter press to further improve the solid content concentration of a cake formed by dewatering a slurry in which solid particles and water are mixed, and has already filed a patent application (patent application). Showa 58-199763
No.).

その概要は、フィルタプレスの各濾室内に供給したスラ
リー内に圧縮空気を供給してスラリーの固形分粒子間を
通過させ、この粒子間に滞留する間隙水(濾液)および
空気を濾室外に排出して、スラリーの脱水を行うもので
ある。
The outline of this process is to supply compressed air into the slurry supplied to each filter chamber of the filter press, pass it between the solid particles of the slurry, and discharge the interstitial water (filtrate) and air that remains between the particles to the outside of the filter chamber. The slurry is then dehydrated.

〔発明が解決しようとする問題点〕[Problem that the invention seeks to solve]

ところで、前記従来の脱水方法では、各濾室に連通ずる
圧縮空気供給管に設けられたエアブロ−弁を時間設定に
より開閉し、エアブローを行っていた。しかし、スラリ
ーの脱水に必要なエアブロ一時間は各濾室内で異なるた
め、一方濾室では時間が不足となり、他方の濾室では過
剰となって、圧縮空気の有効利用が図れず、効率が悪か
った。また濾室ごとにケーキの固形分濃度が異なるため
、脱水能力が低かった。
By the way, in the conventional dehydration method, air blowing is performed by opening and closing an air blow valve provided on a compressed air supply pipe communicating with each filter chamber at a set time. However, since the air blow time required to dehydrate the slurry differs in each filter chamber, there is insufficient time in one filter chamber and excess time in the other, making it impossible to use compressed air effectively and resulting in poor efficiency. Ta. Furthermore, since the solid content concentration of the cake differed depending on the filter chamber, the dehydration ability was low.

この発明は以上の問題点を解決するために創案されたも
ので、圧縮空気の有効利用を図ると共に、圧縮空気供給
源の各設備のコストダウンを達成でき、脱水能力を向上
するフィルタプレスの脱水方法を提供することを目的と
する。
This invention was devised to solve the above problems, and it makes effective use of compressed air, reduces the cost of each equipment of the compressed air supply source, and improves the dewatering capacity of a filter press. The purpose is to provide a method.

〔問題点を解決するための手段〕[Means for solving problems]

この発明は、互いに重なり合う複数の濾過板を有し、各
濾過板間に濾室が形成され、前記濾過板を貫通して各濾
室を連通ずる貫通孔が形成されたフィルタプレスを使用
し、前記貫通孔を経て各濾室内にスラリーを供給した後
、各濾室のスラリー内に圧縮空気を供給してスラリーの
脱水を行うフィルタプレスによる脱水方法において、 前記各濾過板側方には交互に合対向する位置に圧縮空気
給入管および濾液流量測定手段を有する濾液排出管を設
け、濾液の流量がほぼOになるまで相隣り合う濾過板の
2つの給入管のうちの一方に圧縮空気を供給した後、次
にこれと対向側の他方の給入管に圧縮空気を供給し、さ
らにこれらの過程を順次くり返し行うことを特徴とする
This invention uses a filter press that has a plurality of filter plates that overlap each other, a filter chamber is formed between each filter plate, and a through hole is formed that passes through the filter plate and communicates each filter chamber, In a dewatering method using a filter press in which the slurry is supplied into each filter chamber through the through hole and then compressed air is supplied into the slurry in each filter chamber to dehydrate the slurry, the following steps are provided on the sides of each of the filter plates alternately. A compressed air supply pipe and a filtrate discharge pipe having a filtrate flow rate measuring means are provided at opposing positions, and compressed air is supplied to one of the two supply pipes of adjacent filter plates until the flow rate of the filtrate reaches approximately O. After that, compressed air is then supplied to the other supply pipe on the opposite side, and these processes are repeated in sequence.

〔実 施 例〕〔Example〕

第1図はこの発明の実施例を示すもので、符号1はエア
ブロ−用およびバンクプロー用の空気圧縮機、2は主O
N−〇FF弁、3はエアレシーバタンク、4はフィルタ
プレスである。フィルタプレス4は、互いに重なり合う
複数の濾過板4aを有しており、各濾過板4a、4a間
に濾室4bが形成され、前記濾過板4aを貫通して各濾
室4bを連通ずる貫通孔4Cが形成されている。この貫
通孔4cの一端には図示しないスラリー貯蔵タンクに連
通するスラリー供給管9が連結されており、貫通孔4C
の他端にはエアレシーバタンク3に連通するバックブロ
ー管11が連結されている。スラリー供給管9には圧力
計14およびスラリー供給弁10が取付けられており、
貫通孔4Cとスラリー供給弁10との間にはバックプロ
ースラリー排出管16が配設されていて、該排出管16
にはバンクプロースラリー排出弁13が取付けられてい
る。またバックブロー管11にはバンクブロー弁12が
取付けられている。
FIG. 1 shows an embodiment of the present invention, in which reference numeral 1 is an air compressor for air blowers and bank blowers, and 2 is a main air compressor for air blowers and bank blowers.
N-〇FF valve, 3 is an air receiver tank, and 4 is a filter press. The filter press 4 has a plurality of filter plates 4a that overlap each other, a filter chamber 4b is formed between each filter plate 4a, and a through hole passes through the filter plate 4a and communicates each filter chamber 4b. 4C is formed. A slurry supply pipe 9 communicating with a slurry storage tank (not shown) is connected to one end of the through hole 4c.
A back blow pipe 11 communicating with the air receiver tank 3 is connected to the other end. A pressure gauge 14 and a slurry supply valve 10 are attached to the slurry supply pipe 9.
A backflow slurry discharge pipe 16 is disposed between the through hole 4C and the slurry supply valve 10, and the discharge pipe 16
A bank prose slurry discharge valve 13 is attached to the pump. Further, a bank blow valve 12 is attached to the back blow pipe 11.

各濾過板4a側方には、交互に対向側となる位置にエア
ブロ−管18.18′とドレン管19゜19′が設けら
れており、これらの管18.18’19.19’は濾室
4bに通じている。エアブロ−管18.18′は、各濾
過板4a側に取付けられたエアブロ−弁5,6、エア供
給側に取付けられたエアブロ−元弁15を介してエアレ
シーバタンク3に連通している。ドレン管19.19′
の各濾過板4a側にはドレン弁7,8および間隙水流量
検知計17.17′が取付けれている。
On the side of each filter plate 4a, air blow pipes 18.18' and drain pipes 19.19' are provided at alternately opposing positions, and these pipes 18.18'19.19' It leads to room 4b. The air blow pipes 18, 18' communicate with the air receiver tank 3 via air blow valves 5 and 6 attached to each filter plate 4a side and an air blow source valve 15 attached to the air supply side. Drain pipe 19.19'
Drain valves 7 and 8 and interstitial water flow rate detectors 17 and 17' are attached to each filter plate 4a side.

次にこの発明の脱水方法を図面に示す実施例に基づいて
説明する。
Next, the dewatering method of the present invention will be explained based on embodiments shown in the drawings.

■ スラリー供給弁10を開状態とし、圧力計14が所
定圧力を検知するまでスラリー供給管9を経て貫通孔4
Cよりフィルタプレス4の各濾室4b内にスラリーを供
給する。このときエアブロ−弁5,6は閉状態とし、ド
レン弁7.8は開状態としておく。
■ The slurry supply valve 10 is opened and the slurry is passed through the through hole 4 through the slurry supply pipe 9 until the pressure gauge 14 detects a predetermined pressure.
Slurry is supplied into each filter chamber 4b of the filter press 4 from C. At this time, the air blow valves 5 and 6 are kept closed, and the drain valve 7.8 is kept open.

■ 圧力計14が所定圧力を検知すると同時に、ドレン
弁7を閉状態とし、エアブロ−弁5、エアブロ−元弁1
5およびドレン弁8を開状態として、エアレシーバ3内
の圧縮空気をエアブロ−管18より各濾室4bのスラリ
ー内に供給してスラリーの固形分粒子間を通過させ、粒
子間に滞留する間隙水(濾りおよび空気を系外のドレン
管19′より排出させる。
■ At the same time as the pressure gauge 14 detects a predetermined pressure, the drain valve 7 is closed, and the air blow valve 5 and air blow main valve 1 are closed.
5 and drain valve 8 are opened, the compressed air in the air receiver 3 is supplied from the air blow pipe 18 into the slurry in each filter chamber 4b, and is passed between the solid particles of the slurry, thereby filling the gaps between the particles. Water (filtered air) and air are discharged from the drain pipe 19' outside the system.

■ 間隙水の流量がほぼ0となり流量検知計17′が流
量を検知しなくなったら、ドレン弁8およびエアブロ−
弁5を閉状態とし、これらと対向する位置の相隣り合う
濾過板4aのエアブロ−弁6およびドレン弁7を開状態
として、エアブロ−管18より各濾室4bのスラリー内
に圧縮空気を供給する。
■ When the flow rate of pore water reaches almost 0 and the flow rate detector 17' no longer detects the flow rate, close the drain valve 8 and the air blower.
The valve 5 is closed, the air blow valve 6 and the drain valve 7 of the adjacent filter plates 4a located opposite to these are opened, and compressed air is supplied from the air blow pipe 18 into the slurry in each filter chamber 4b. do.

■ 間隙水の流量がほぼ0となり流量検知計17が流量
を検知しなくなったら、エアブロ−弁6、ドレン弁7お
よびエアブロ−元弁15を閉状態とする。
(2) When the flow rate of the interstitial water reaches approximately 0 and the flow rate detector 17 no longer detects the flow rate, the air blow valve 6, drain valve 7, and air blow source valve 15 are closed.

■ バンクプロースラリー排出弁13およびバックブロ
ー弁12を開状態とし、バックブロー管11より圧縮空
気を供給して、貫通孔4c内に残留している脱水されな
いスラリーをバックプロースラリー排出管16より糸外
へ排出させる。
■ Open the bank plow slurry discharge valve 13 and back blow valve 12, supply compressed air from the back blow pipe 11, and remove undehydrated slurry remaining in the through hole 4c from the back plow slurry discharge pipe 16. discharge to.

なお以上述べた■〜■の各工程はシーケンサ−により制
御されており、フィルタプレスへのスラリー供給、各濾
室への圧縮空気供給、各弁の開閉等は自動的に行われる
Each of the steps (1) to (4) described above is controlled by a sequencer, and the supply of slurry to the filter press, the supply of compressed air to each filter chamber, the opening and closing of each valve, etc. are automatically performed.

〔発明の効果〕〔Effect of the invention〕

■ 各濾過板の排出管には濾液流量測定手段を設け、濾
液の流量がほぼ0となるまで各濾室に圧縮空気を供給し
てエアブローするので、各濾室の脱水を均一かつ良好に
行うことができる。また圧縮空気の有効利用が図れ、圧
縮空気供給源の各設備のコストダウンを達成できる。
■ A filtrate flow rate measuring means is installed in the discharge pipe of each filter plate, and compressed air is supplied to each filter chamber until the flow rate of the filtrate reaches almost 0 to perform air blowing, thereby ensuring uniform and good dewatering of each filter chamber. be able to. In addition, compressed air can be used effectively, and the cost of each equipment for the compressed air supply source can be reduced.

■ 各濾過板には交互に対向側となる位置に圧縮空気給
入管および濾液排出管を設け、相隣り合う濾過板の2つ
の給入管のうちの一方に圧縮空気を供給した後、これと
対向側の他方の給入管に圧縮空気を供給して脱水を行う
ので、濾室内のケーキ内には均等に圧力が加わり、脱水
能力が向上する。
■ Each filter plate is provided with a compressed air supply pipe and a filtrate discharge pipe at alternate positions on opposite sides, and after supplying compressed air to one of the two supply pipes of the adjacent filter plate, the compressed air is supplied to the opposite side. Since dehydration is performed by supplying compressed air to the other supply pipe on the side, pressure is evenly applied to the inside of the cake in the filter chamber, improving dehydration ability.

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

第1図はこの発明の一実施例を示す概念図である。 1・・・・・・空気圧縮機、2・・・・・・主○N−0
FF弁、3・・・・・・エアレシーバタンク、4・・・
・・・フィルタプレス、4a・・・・・・濾過板、4b
・・・・・・濾室、4C・・・・・・貫通孔、5,6・
・・・・・エアブロ−弁、7,8・・・・・・ドレン弁
、9・・・・・・スラリー供給管、10・・・・・・ス
ラリー供給弁、11・・・・・・バックブロー管、12
・・・・・・バックブロー弁、13・・・・・・バック
プロースラリー排出弁、14・・・・・・圧力計、15
・・・・・・エアブロ−元弁、16・・・・・・バック
プロースラリー排出管、17.17′・・・・・・間隙
水流量検知計、18.18’・・・・・・エアブロ−管
、19.19’・・・・・・ドレン管
FIG. 1 is a conceptual diagram showing an embodiment of the present invention. 1... Air compressor, 2... Main ○N-0
FF valve, 3...Air receiver tank, 4...
...Filter press, 4a...Filter plate, 4b
...Filter chamber, 4C...Through hole, 5,6.
...Air blow valve, 7,8...Drain valve, 9...Slurry supply pipe, 10...Slurry supply valve, 11... Back blow tube, 12
...Back blow valve, 13... Back blow slurry discharge valve, 14... Pressure gauge, 15
... Air blow main valve, 16... Backpros slurry discharge pipe, 17.17'... Pore water flow rate detector, 18.18'... Air blow pipe, 19.19'...Drain pipe

Claims (2)

【特許請求の範囲】[Claims] (1)互いに重なり合う複数の濾過板を有し、各濾過板
間に濾室が形成され、前記濾過板を貫通して各濾室を連
通する貫通孔が形成されたフィルタプレスを使用し、前
記貫通孔を経て各濾室内にスラリーを供給した後、各濾
室のスラリー内に圧縮空気を供給してスラリーの脱水を
行うフィルタプレスによる脱水方法において、 前記各濾過板側方には交互に合対向する位置に圧縮空気
給入管および濾液流量測定手段を有する濾液排出管を設
け、濾液の流量がほぼ0になるまで相隣り合う濾過板の
2つの給入管のうちの一方に圧縮空気を供給した後、次
にこれと対向側の他方の給入管に圧縮空気を供給し、さ
らにこれらの過程を順次くり返し行うことを特徴とする
フィルタプレスによる脱水方法。
(1) Using a filter press that has a plurality of filter plates that overlap each other, a filter chamber is formed between each filter plate, and a through hole is formed that penetrates the filter plate and communicates each filter chamber, In a dewatering method using a filter press in which slurry is supplied into each filter chamber through a through hole and then compressed air is supplied into the slurry in each filter chamber to dehydrate the slurry, a filter plate is provided on the side of each filter plate alternately. A compressed air supply pipe and a filtrate discharge pipe having a filtrate flow rate measuring means were provided at opposing positions, and compressed air was supplied to one of the two supply pipes of the adjacent filter plates until the flow rate of the filtrate reached almost 0. After that, compressed air is supplied to the other supply pipe on the opposite side, and these processes are repeated in sequence.
(2)スラリーの脱水を行った後、貫通孔に圧縮空気を
供給して貫通孔内の脱水されないスラリーを濾室外へ排
出することを特徴とする特許請求の範囲第1項記載のフ
ィルタプレスによる脱水方法。
(2) The filter press according to claim 1, characterized in that after dewatering the slurry, compressed air is supplied to the through holes to discharge the undehydrated slurry in the through holes to the outside of the filter chamber. Dehydration method.
JP61297954A 1986-12-15 1986-12-15 Dehydration method by filter press Granted JPS63151314A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP61297954A JPS63151314A (en) 1986-12-15 1986-12-15 Dehydration method by filter press

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP61297954A JPS63151314A (en) 1986-12-15 1986-12-15 Dehydration method by filter press

Publications (2)

Publication Number Publication Date
JPS63151314A true JPS63151314A (en) 1988-06-23
JPH0224568B2 JPH0224568B2 (en) 1990-05-30

Family

ID=17853235

Family Applications (1)

Application Number Title Priority Date Filing Date
JP61297954A Granted JPS63151314A (en) 1986-12-15 1986-12-15 Dehydration method by filter press

Country Status (1)

Country Link
JP (1) JPS63151314A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2008151531A1 (en) * 2007-06-08 2008-12-18 Guangzhou Pude Environmental Protection Equipment Co., Ltd. Plate and frame fliter press with air-blowing for dehydrating sludge
CN102580373A (en) * 2012-01-12 2012-07-18 杭州兴源过滤科技股份有限公司 Testing system and testing method for pumping pressure coal slime filter press
JP2022026674A (en) * 2020-07-31 2022-02-10 株式会社石垣 Air blow method of filter press

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2008151531A1 (en) * 2007-06-08 2008-12-18 Guangzhou Pude Environmental Protection Equipment Co., Ltd. Plate and frame fliter press with air-blowing for dehydrating sludge
CN102580373A (en) * 2012-01-12 2012-07-18 杭州兴源过滤科技股份有限公司 Testing system and testing method for pumping pressure coal slime filter press
JP2022026674A (en) * 2020-07-31 2022-02-10 株式会社石垣 Air blow method of filter press

Also Published As

Publication number Publication date
JPH0224568B2 (en) 1990-05-30

Similar Documents

Publication Publication Date Title
CN102225259A (en) A horizontal automatic filter press dehydration equipment and its working method
US4913771A (en) Method for dewatering sludge or slurry
JP2000354900A (en) Wastewater sludge dehydrating and drying system
US7815808B2 (en) Hot-gas pressure-filter apparatus
JPS63151314A (en) Dehydration method by filter press
JPH0224567B2 (en)
CN211486680U (en) Novel energy-saving efficient fine material dewatering unit
JP2001232109A (en) Device and method for dehydrating and drying sludge
US4029584A (en) Pneumatic sludge discharging system
WO2011118283A1 (en) Solid-liquid separation method
GB1256159A (en) Method for heating pressing plates of an automatic flat press
JP3326784B2 (en) Dewatering method of slurry in filter press
CN110368723B (en) Energy-saving efficient fine material dewatering unit
EA038051B1 (en) Method for operating a filter press and filter press
CN208839112U (en) A high-pressure plate and frame filter press with retractable filter plates
JPH0472600B2 (en)
JP3773193B2 (en) Filter press apparatus and sludge dewatering method
JP7617360B2 (en) Air blowing method for filter press
CN213623386U (en) Coal washing water treatment professional equipment
CN107837577A (en) A kind of apparatus and method for reducing carbide slag water content
SU885756A1 (en) Unit for dewatering and drying finely distpersed pulp materials
JP2000176496A (en) Filter cloth regenerating method for sludge concentration/dehydration device
JPS6236491Y2 (en)
SU875109A1 (en) Chamber-type dewatering and loading unit
JPH01203008A (en) Treatment process and device for sludge or the like