JPH0224568B2 - - Google Patents

Info

Publication number
JPH0224568B2
JPH0224568B2 JP61297954A JP29795486A JPH0224568B2 JP H0224568 B2 JPH0224568 B2 JP H0224568B2 JP 61297954 A JP61297954 A JP 61297954A JP 29795486 A JP29795486 A JP 29795486A JP H0224568 B2 JPH0224568 B2 JP H0224568B2
Authority
JP
Japan
Prior art keywords
filter
slurry
air
compressed air
supplied
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
Application number
JP61297954A
Other languages
Japanese (ja)
Other versions
JPS63151314A (en
Inventor
Masazumi Ito
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)

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
とができるフイ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、それによつ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イルタ
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。
Conventionally, 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 (special patent application). (Gan Sho 58-199763).

その概要は、フイ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. do,
This is to dehydrate slurry.

〔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
連通する圧縮空気供給管に設けられたエアブロー
弁を時間設定により開閉し、エアブローを行つて
いた。しかし、スラリーの脱水に必要なエアブロ
ー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つて、
圧縮空気の有効利用が図れず、効率が悪かつた。
また濾室ごとにケーキの固形分濃度が異なるた
め、脱水能力が低かつた。
By the way, in the conventional dehydration method, air blowing is performed by opening and closing an air blow valve provided in a compressed air supply pipe communicating with each filter chamber according to a set time. However, since the air blowing time required to dehydrate the slurry differs in each filter chamber, the time may be insufficient in one filter chamber and excessive in the other.
Compressed air could not be used effectively, resulting in poor efficiency.
Furthermore, since the solid content concentration of the cake differs 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イルタプレスの脱
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する貫通孔が形成された
フイ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
イ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。
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 with 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, alternately provided on the sides of each of the filter plates. A compressed air supply pipe and a filtrate discharge pipe having a filtrate flow rate measuring means are provided at opposite positions, and compressed air is supplied to one of the two supply pipes of the adjacent filter plates until the flow rate of the filtrate becomes almost 0. 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はエアブロー用およびバツクブロー用の空気圧
縮機、2は主ON−OFF弁、3はエアレシーバタ
ンク、4はフイルタプレスである。フイルタプレ
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
連通する貫通孔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
通するバツクブロー管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との間にはバツクブロースラリー
排出管16が配設されていて、該排出管16には
バツクブロースラリー排出弁13が取付けられて
いる。またバツクブロー管11にはバツクブロー
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 denotes an air compressor for air blowing and back blowing, 2 a main ON-OFF valve, 3 an air receiver tank, and 4 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 of the through hole 4c. A pressure gauge 14 and a slurry supply valve 10 are attached to the slurry supply pipe 9, and a back blow slurry discharge pipe 16 is disposed between the through hole 4c and the slurry supply valve 10. A back blow slurry discharge valve 13 is attached to the back blow slurry discharge valve 13. Further, a back 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
置にエアブロー管18,18′とドレン管19,
19′が設けられており、これらの管18,1
8′,19,19′は濾室4bに通じている。エア
ブロー管18,18′は、各濾過板4a側に取付
けられたエアブロー弁5,6、エア供給側に取付
けられたエアブロー元弁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19,1
9′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 sides of each filter plate 4a, air blow pipes 18, 18' and drain pipes 19 are arranged alternately on opposite sides.
19' are provided and these tubes 18,1
8', 19, 19' communicate with the filter chamber 4b. The air blow pipes 18, 18' communicate with the air receiver tank 3 via air blow valves 5, 6 attached to each filter plate 4a side and an air blow source valve 15 attached to the air supply side. Drain pipe 19,1
Drain valves 7, 8 and interstitial water flow rate detectors 17, 17' are attached to each filter plate 4a side of 9'.

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1
4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4cよりフイルタプレス4の各濾
室4b内にスラリーを供給する。このときエア
ブロー弁5,6は閉状態とし、ドレン弁7,8
は開状態としておく。
With the slurry supply valve 10 open, the pressure gauge 1
4 detects a predetermined pressure.
The slurry is supplied into each filter chamber 4b of the filter press 4 through the through hole 4c. At this time, the air blow valves 5 and 6 are closed, and the drain valves 7 and 8 are closed.
Leave it 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、エアブロー弁5、エ
アブロー元弁15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
ー管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(濾液)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, the air blow valve 5, the air blow source valve 15, and the drain valve 8 are opened, and the compressed air in the air receiver 3 is supplied from the air blow pipe 18 into the slurry in each filter chamber 4b to remove the slurry. The interstitial water (filtrate) and air that pass between the solid particles and remain between the particles 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1
7′が流量を検知しなくなつたら、ドレン弁8
およびエアブロー弁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
ロー弁6およびドレン弁7を開状態として、エ
アブロー管18より各濾室4bのスラリー内に
圧縮空気を供給する。
The flow rate of pore water becomes almost 0 and the flow rate detector 1
When 7' no longer detects the flow rate, drain valve 8
Then, the air blow valves 5 are closed, and the air blow valves 6 and drain valves 7 of the adjacent filter plates 4a opposite to these are opened, and compressed air is supplied from the air blow pipes 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つたら、エアブロー弁
6、ドレン弁7およびエアブロー元弁15を閉
状態とする。
The flow rate of pore water becomes almost 0 and the flow rate detector 17
When the flow rate is no longer detected, the air blow valve 6, drain valve 7, and air blow source valve 15 are closed.

バツクブロースラリー排出弁13およびバツ
クブロー弁12を開状態とし、バツクブロー管
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ツクブ
ロースラリー排出管16より系外へ排出させ
る。
Back blow slurry discharge valve 13 and back blow valve 12 are opened, compressed air is supplied from back blow pipe 11, and undehydrated slurry remaining in through hole 4c is discharged from the system through back blow slurry discharge pipe 16. let

なお以上述べた〜の各工程はシーケンサー
により制御されており、フイ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 above-mentioned steps ~ is controlled by a sequencer, and the slurry supply to the filter press, the compressed air supply to each filter chamber, the opening and closing of each valve, etc. are automatically performed.

〔発明の効果〕 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。
[Effects of the Invention] A filtrate flow rate measuring means is provided 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, and air blowing is performed, so that the dehydration of each filter chamber is uniform. and can be performed well. 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 inlet pipe, 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 drawings]

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ON−OFF弁、3
……エアレシーバタンク、4……フイルタプレ
ス、4a……濾過板、4b……濾室、4c……貫
通孔、5,6……エアブロー弁、7,8……ドレ
ン弁、9……スラリー供給管、10……スラリー
供給弁、11……バツクブロー管、12……バツ
クブロー弁、13……バツクブロースラリー排出
弁、14……圧力計、15……エアブロー元弁、
16……バツクブロースラリー排出管、17,1
7′……間隙水流量検知計、18,18′……エア
ブロー管、19,19′……ドレン管。
FIG. 1 is a conceptual diagram showing an embodiment of the present invention. 1...Air compressor, 2...Main ON-OFF 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 pipe, 12... Back blow valve, 13... Back blow slurry discharge valve, 14... Pressure gauge, 15... Air blow source valve,
16...Back blow slurry discharge pipe, 17,1
7'... Pore water flow rate detector, 18, 18'... Air blow pipe, 19, 19'... Drain pipe.

Claims (1)

【特許請求の範囲】 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イルタプ
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イルタプレ
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イル
タプレスによる脱水方法。 2 スラリーの脱水を行つた後、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項記載のフイルタプレスによる脱水方法。
[Scope of Claims] 1. A filter press having a plurality of filter plates overlapping each other, a filter chamber being formed between each filter plate, and a through hole passing through the filter plate and communicating the filter chambers. In a dehydration 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, on the side of each filter plate. A compressed air supply pipe and a filtrate discharge pipe having a filtrate flow rate measuring means are provided at positions that alternately meet and face each other, and air is compressed into one of the two supply pipes of adjacent filter plates until the flow rate of the filtrate becomes almost 0. A dewatering method using a filter press, which is characterized in that after supplying air, compressed air is then supplied to the other supply pipe on the opposite side, and these processes are repeated in sequence. 2. A dewatering method using a filter press according to claim 1, characterized in that after dewatering the slurry, compressed air is supplied to the through holes to discharge undehydrated slurry in the through holes to the outside of the filter chamber. .
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 JPS63151314A (en) 1988-06-23
JPH0224568B2 true 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)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN201059845Y (en) * 2007-06-08 2008-05-14 广州普得环保设备有限公司 Air-blowing type and plate and frame filter-pressing sludge dewatering machine
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
JP7245985B2 (en) * 2020-07-31 2023-03-27 株式会社石垣 Air blow method for filter press

Also Published As

Publication number Publication date
JPS63151314A (en) 1988-06-23

Similar Documents

Publication Publication Date Title
JPS6430615A (en) Filter composed of material obtained by freeze drying and control especially for pharmacuitical field and use method
JP2000266000A (en) Automatic pneumatic pump
KR102258655B1 (en) Filter press dehydrator equipped with a function to collect odor gas generated in the dehydration process
JPH0224568B2 (en)
JP5636040B2 (en) Solid-liquid separation method
JPH0224567B2 (en)
GB1256159A (en) Method for heating pressing plates of an automatic flat press
JP5985984B2 (en) Solid-liquid separator
US2016163A (en) Filter
JP3326784B2 (en) Dewatering method of slurry in filter press
JPS57150410A (en) Pressurized dehydrating method
CN110025996A (en) A kind of plate and frame type filter-press that filters pressing effect is good
US4029584A (en) Pneumatic sludge discharging system
GB488280A (en) Improvements in or relating to filter presses
JP2000153103A (en) Filter press apparatus and sludge dewatering
JPS54129571A (en) Filter press attached with vacuum process
CN107321028A (en) A kind of ceramic filter press membrane of pulse
JPS6354906A (en) Method for operating filter press
SU885756A1 (en) Unit for dewatering and drying finely distpersed pulp materials
JPH0472600B2 (en)
CN206566560U (en) A kind of full-automatic sand filter
CN2101783U (en) Heatless regenerating drier for vehicle
JPH0377609A (en) Method for cleaning filter cloth of dehydrating filter press
CN2306054Y (en) Plate frame filtering concentrator
JPS5928650Y2 (en) Combustion slag dehydration equipment