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JPH11128670A - Belt-filter - Google Patents

Belt-filter

Info

Publication number
JPH11128670A
JPH11128670A JP9301879A JP30187997A JPH11128670A JP H11128670 A JPH11128670 A JP H11128670A JP 9301879 A JP9301879 A JP 9301879A JP 30187997 A JP30187997 A JP 30187997A JP H11128670 A JPH11128670 A JP H11128670A
Authority
JP
Japan
Prior art keywords
gypsum
belt filter
fine particle
belt
cake
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
JP9301879A
Other languages
Japanese (ja)
Other versions
JP3600417B2 (en
Inventor
Haruo Kitamura
治男 北村
Eiji Ochi
英次 越智
Takeo Shinoda
岳男 篠田
Susumu Okino
沖野  進
Masao Hino
日野  正夫
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 JP30187997A priority Critical patent/JP3600417B2/en
Priority to TW087114751A priority patent/TW402518B/en
Priority to KR1019980041003A priority patent/KR100276126B1/en
Priority to CN98123621A priority patent/CN1073872C/en
Priority to CZ19983484A priority patent/CZ291668B6/en
Priority to TR1998/02224A priority patent/TR199802224A3/en
Publication of JPH11128670A publication Critical patent/JPH11128670A/en
Application granted granted Critical
Publication of JP3600417B2 publication Critical patent/JP3600417B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D39/00Filtering material for liquid or gaseous fluids
    • B01D39/14Other self-supporting filtering material ; Other filtering material
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D33/00Filters with filtering elements which move during the filtering operation
    • B01D33/056Construction of filtering bands or supporting belts, e.g. devices for centering, mounting or sealing the filtering bands or the supporting belts
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D33/00Filters with filtering elements which move during the filtering operation
    • B01D33/58Handling the filter cake in the filter for purposes other than for regenerating the filter cake remaining on the filtering element
    • B01D33/60Handling the filter cake in the filter for purposes other than for regenerating the filter cake remaining on the filtering element for washing
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D33/00Filters with filtering elements which move during the filtering operation
    • B01D33/70Filters with filtering elements which move during the filtering operation having feed or discharge devices
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D33/00Filters with filtering elements which move during the filtering operation
    • B01D33/80Accessories
    • B01D33/804Accessories integrally combined with devices for controlling the filtration
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/34Chemical or biological purification of waste gases
    • B01D53/46Removing components of defined structure
    • B01D53/48Sulfur compounds
    • B01D53/50Sulfur oxides
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/34Chemical or biological purification of waste gases
    • B01D53/92Chemical or biological purification of waste gases of engine exhaust gases

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Filtration Of Liquid (AREA)
  • Treating Waste Gases (AREA)
  • Treatment Of Sludge (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a belt-filter enabling to secure dehydration performance even when a fine particle layer of a gypsum cake is formed. SOLUTION: In a belt-filter 1 by which gypsum slurry 2 from a flue gas desulfurization device is sucked and dehydrated with vacuum dehydration devices 4, 5, plural stages of dams 10 whose lower ends extend to the upper layer of a gypsum cake 8, are provided in the longitudinal direction of the belt-filter 1 so that a fine particle layer formed on the surface of the gypsum cake 8 is stirred with them.

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、排煙脱硫装置で石
膏スラリの脱水に用いられるベルトフィルタに関する。
The present invention relates to a belt filter used for dewatering gypsum slurry in a flue gas desulfurization apparatus.

【0002】[0002]

【従来の技術】排煙脱硫装置に用いられる石膏スラリ用
脱水機は、設備費、運転費、保守費及び脱水性能等の観
点で、遠心分離機方式からベルトフィルタによるバスケ
ット形真空吸引脱水方式に移行しつつある。しかし、ス
ラリ中に含まれる微細な不純物、例えば未燃カーボン
や、フッ化カルシウム、シリカ、水酸化アルミニウム、
水酸化鉄からなる微粒子ダストが、図2に示すように脱
水ケーキ201の表面で微粒子層202を1〜数mm程
度形成し、これによって真空吸引する際の通気性を悪化
させ、脱水性能の低下を引き起こすこととなっていた。
2. Description of the Related Art A gypsum slurry dehydrator used in a flue gas desulfurization apparatus is changed from a centrifugal separator system to a basket type vacuum suction dehydrator system using a belt filter from the viewpoint of equipment costs, operation costs, maintenance costs and dewatering performance. Migrating. However, fine impurities contained in the slurry, such as unburned carbon, calcium fluoride, silica, aluminum hydroxide,
Fine particle dust made of iron hydroxide forms a fine particle layer 202 of about 1 to several mm on the surface of the dewatering cake 201 as shown in FIG. 2, thereby deteriorating air permeability during vacuum suction and deteriorating dewatering performance. Was to be caused.

【0003】[0003]

【発明が解決しようとする課題】本発明はこのような現
状に鑑み、石膏ケーキの微粒子層が形成されても、脱水
性能を確保するようにしたベルトフィルタを提供するこ
とを目的とする。
SUMMARY OF THE INVENTION In view of such circumstances, an object of the present invention is to provide a belt filter capable of ensuring dewatering performance even when a fine particle layer of a gypsum cake is formed.

【0004】[0004]

【課題を解決するための手段】上記目的を達成するた
め、請求項1に記載された発明は、真空脱水装置によっ
て排煙脱硫装置からの石膏スラリを吸引脱水するように
したベルトフィルタにおいて、下端が石膏ケーキの上層
に延長するせきをベルトフィルタの長手方向に複数段設
け、石膏ケーキの表面に形成される微粒子層をかき乱す
ようにしたことを特徴とする。請求項2に記載された発
明は、請求項1のベルトフィルタにおいて、温水、蒸
気、又は温水及び蒸気をベルトフィルタ上の石膏スラリ
又は石膏ケーキに供給する洗浄水供給装置を設けたこと
を特徴とする。
SUMMARY OF THE INVENTION In order to achieve the above object, an invention according to claim 1 is a belt filter in which gypsum slurry from a flue gas desulfurization unit is suction-dehydrated by a vacuum dehydration unit. Is characterized in that a plurality of weirs extending from the top of the gypsum cake are provided in the longitudinal direction of the belt filter so as to disturb the fine particle layer formed on the surface of the gypsum cake. According to a second aspect of the present invention, in the belt filter of the first aspect, a washing water supply device that supplies hot water, steam, or hot water and steam to a gypsum slurry or a gypsum cake on the belt filter is provided. I do.

【0005】[0005]

【発明の実施の形態】以下に添付図面に示した実施の形
態を参照して、本発明にかかるベルトフィルタを説明す
る。図1に示すように、本実施の形態にかかるベルトフ
ィルタ1は、石膏スラリ2を供給ヘッダ3より供給する
こととし、真空脱水装置を構成する要素として、第1真
空ボックス部4と第2真空ボックス部5とを備える。真
空ボックス部4、5の上面には、これに接して移動巡回
する搬送用のゴムベルト6が設けられている。このゴム
ベルト6は、移動巡回するベルトフィルタ(ろ布)本体
7を支持している。ベルトフィルタ本体7は、通気性を
有し、石膏スラリ2及び石膏ケーキ8を保持する適度の
強度を備えている。さらに、本実施の形態は、洗浄水供
給装置9を備える。この装置9は高品位(純度)の石膏
を得るために石膏スラリ2に含まれる高濃度の塩素イオ
ン等の塩類を洗い流すためのものである。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS A belt filter according to the present invention will be described below with reference to an embodiment shown in the accompanying drawings. As shown in FIG. 1, a belt filter 1 according to the present embodiment supplies a gypsum slurry 2 from a supply header 3, and includes a first vacuum box 4 and a second vacuum And a box unit 5. On the upper surfaces of the vacuum boxes 4 and 5, there is provided a transfer rubber belt 6 which moves and circulates in contact with the vacuum boxes. The rubber belt 6 supports a belt filter (filter cloth) main body 7 that moves and circulates. The belt filter body 7 has air permeability, and has an appropriate strength to hold the gypsum slurry 2 and the gypsum cake 8. Further, the present embodiment includes a cleaning water supply device 9. This device 9 is for washing out high-concentration chloride ions and other salts contained in the gypsum slurry 2 in order to obtain high-grade (purity) gypsum.

【0006】さらに、本実施の形態にかかるベルトフィ
ルタ1は、せき10を有する。このせき10は、石膏ケ
ーキ8の表面に形成される微粒子層をかき乱すための手
段である。せき10は、下端が石膏ケーキ8の上層に延
長しており、ベルトフィルタ1の長手方向に3箇所に設
けられている。なおここで、「下端が石膏ケーキ8の上
層に延長する。」とは、せき10が上下方向に十分な長
さを持っており、その下端が石膏ケーキ8の微粒子層を
かき乱し、脱水性能を確保できるに足りることを意味す
る。せき10はラバー、プラスチック、竹、木材、金属
等によって構成することができるが、好ましくはラバー
すなわち合成ゴム製である。せき10は矩形状の形状で
あり、図示しない支持手段によってベルトフィルタ1の
幅方向に亘って懸架されている。
Further, the belt filter 1 according to the present embodiment has a weir 10. The weir 10 is a means for disturbing the fine particle layer formed on the surface of the gypsum cake 8. The weir 10 has a lower end extending to the upper layer of the gypsum cake 8 and is provided at three places in the longitudinal direction of the belt filter 1. Here, "the lower end extends to the upper layer of the gypsum cake 8" means that the crest 10 has a sufficient length in the vertical direction, and the lower end thereof disturbs the fine particle layer of the gypsum cake 8, and the dewatering performance is reduced. It means that it can be secured. The weir 10 can be made of rubber, plastic, bamboo, wood, metal, or the like, but is preferably made of rubber, that is, synthetic rubber. The weir 10 has a rectangular shape and is suspended in the width direction of the belt filter 1 by supporting means (not shown).

【0007】上記構成の図1の実施の形態において、石
膏スラリ2は、供給ヘッダ3からベルトフィルタ本体7
上に供給され、第1真空ボックス部4で真空吸引ろ過さ
れる。真空吸引ろ過して得られたベルトフィルタ本体7
上の石膏ケーキ8はゴムベルト6により第2真空ボック
ス部5へ送られる。この時、洗浄水供給装置9より石膏
ケーキ8上に洗浄液が供給される。第2真空ボックス部
5で洗浄水を真空吸引ろ過した後、さらに所定時間真空
吸引して石膏ケーキ8中の水分を脱水する。脱水された
石膏ケーキ8はゴムベルト6の動きにより回収コンベア
11側へ送られて、ベルトフィルタ本体7から剥離して
この回収コンベア11に回収される。石膏ケーキ8を剥
離したベルトフィルタ本体7はベルトフィルタ洗浄装置
12で洗浄された後再度スラリ供給部へ送られる。上記
洗浄水供給装置9より石膏ケーキ8上に供給される洗浄
水は、石膏スラリと同温又は好ましくはスラリ温度+1
0℃とする。これによって石膏ケーキ8内の間隙水を昇
温させ、間隙水の粘度及び表面張力を小さくして粒子間
移動抵抗を下げ通気性を良くするためである。
In the embodiment shown in FIG. 1, the gypsum slurry 2 is supplied from the supply header 3 to the belt filter body 7.
It is supplied to the upper part and is subjected to vacuum suction filtration in the first vacuum box section 4. Belt filter body 7 obtained by vacuum suction filtration
The upper gypsum cake 8 is sent to the second vacuum box section 5 by the rubber belt 6. At this time, the cleaning liquid is supplied onto the gypsum cake 8 from the cleaning water supply device 9. After the washing water is vacuum-suction-filtered in the second vacuum box section 5, the water in the gypsum cake 8 is dehydrated by vacuum suction for a further predetermined time. The dehydrated gypsum cake 8 is sent to the collection conveyor 11 side by the movement of the rubber belt 6, is separated from the belt filter body 7, and is collected by the collection conveyor 11. The belt filter body 7 from which the gypsum cake 8 has been peeled off is washed by the belt filter washing device 12 and then sent to the slurry supply unit again. The washing water supplied onto the gypsum cake 8 from the washing water supply device 9 is at the same temperature as the gypsum slurry or preferably at the slurry temperature +1.
0 ° C. Thereby, the temperature of the pore water in the gypsum cake 8 is raised, the viscosity and surface tension of the pore water are reduced, the resistance between particles is reduced, and the air permeability is improved.

【0008】一方、上記せき10の下端は石膏ケーキ8
の上層に延長しており、形成される微粒子層を含めて石
膏ケーキ8の上層をかき乱す。これによって、石膏ケー
キ8の通気性を保ち、効率的に脱水を行うことができ
る。また、このせき10は、水相を保持する役割も果た
す。すなわち、微粒子層が形成されるに到った位置にお
いて、表層に浮いてくる水をせき止め、同時に微粒子層
をかき乱して真空吸引によって水を吸い出させることが
でき、水相がケーキ8表面に排出されることを防ぐこと
ができる。本実施の形態では、せき10を複数設けてい
るので、かき乱し効果が大きく、かつ石膏スラリ2の性
状が変化し、微粒子層の形成される位置(水切れ位置)
が変化しても、いずれかのせき10で対応することがで
き、確実にこれをかき乱し、脱水性能を確保することが
できる。
On the other hand, the lower end of the weir 10 is a gypsum cake 8
And disturbs the upper layer of the gypsum cake 8 including the formed fine particle layer. Thereby, the air permeability of the gypsum cake 8 can be maintained and dehydration can be performed efficiently. The weir 10 also plays a role in retaining the aqueous phase. That is, at the position where the fine particle layer is formed, the water floating on the surface layer can be dammed, and at the same time, the fine particle layer can be disturbed and the water can be sucked out by vacuum suction. Can be prevented. In the present embodiment, since a plurality of weirs 10 are provided, the turbulence effect is large, the properties of the gypsum slurry 2 change, and the position where the fine particle layer is formed (water drainage position).
Can be dealt with by any of the weirs 10, which can be reliably disturbed and the dewatering performance can be ensured.

【0009】他の実施の形態 上記実施の形態では、第1の真空部及び第2の真空部を
設けたが、第1の真空部を省略し、この部分では、自然
沈降のみを行うようにすることもできる。上記図1の実
施の形態では、せき10を3箇所設けている。しかし、
本発明の目的を達成するためには、微粒子層が形成され
る位置に複数段あれば良い。また、図1の実施の形態よ
りも数を増加させることもできる。さらに、微粒子層の
形成される位置の相違に応じて設定される位置を可変に
構成することもできる。なお、より厳密に言うと、せき
10の効果は、脱水により水が切れる直前(微粒子層が
形成される直前)がもっとも効果的である。このため、
固定式のせきの場合には複数段設ける。これは、図1の
実施の形態について述べたごとく、石膏の組成により水
切れ位置が変化するためである。また、上記図1の実施
の形態ような固定式のものでなく、可動式のせきとする
こともできる。この場合、厚みセンサー等で水切れ位置
を検知して位置を自動的に変える機能を持たせる。もち
ろん、微粒子層202が形成された後の位置にせき10
を設けても効果は期待できるが、せき10の材質を比較
的硬い材質であることが必要となる。これによって石膏
が付着したり、せき10がろ布(ベルトフィルタ本体)
にあたってこれを破るといった等の問題を生じる可能性
がある。
Other Embodiments In the above embodiment, the first vacuum section and the second vacuum section are provided. However, the first vacuum section is omitted, and only natural settling is performed in this section. You can also. In the embodiment of FIG. 1, three weirs 10 are provided. But,
In order to achieve the object of the present invention, it is sufficient that a plurality of steps are provided at the position where the fine particle layer is formed. Further, the number can be increased as compared with the embodiment of FIG. Further, the position set according to the difference in the position where the fine particle layer is formed can be variably configured. Strictly speaking, the effect of the cough 10 is most effective immediately before water is drained by dehydration (immediately before the fine particle layer is formed). For this reason,
In the case of a fixed type weir, a plurality of stages are provided. This is because the drainage position changes depending on the composition of the gypsum, as described in the embodiment of FIG. Further, instead of the fixed type as in the embodiment of FIG. 1, a movable type weir can be used. In this case, a function to automatically change the position by detecting the drainage position with a thickness sensor or the like is provided. Of course, at the position after the fine particle layer 202 is formed,
Although the effect can be expected even if it is provided, it is necessary that the material of the weir 10 is a relatively hard material. As a result, gypsum adheres or cough 10 becomes filter cloth (belt filter body).
There is a possibility that problems such as breaking this may occur.

【0010】洗浄水供給装置より供給される洗浄水は、
蒸気としても良い。要するに、間隙水の粘度及び表面張
力を低下させる程度に高温であれば良い。温水と蒸気を
併用することもできる。上記実施の形態では、石膏スラ
リをかき乱すために、ラバー等のせき10を採用した。
しかし、金属製の熊手等であって、微粒子層をかき乱す
ことのできる手段であれば本発明に採用することができ
る。また、複数の種類の手段を併用することもできる。
The washing water supplied from the washing water supply device is
Good as steam. In short, it is sufficient that the temperature is high enough to reduce the viscosity and surface tension of the pore water. Hot water and steam can be used together. In the above-described embodiment, the weir 10 such as rubber is used to disturb the gypsum slurry.
However, any means such as a metal rake which can disturb the fine particle layer can be employed in the present invention. Further, a plurality of types of means can be used in combination.

【0011】[0011]

【発明の効果】以上説明したところから明かなように、
本発明によれば、石膏ケーキの微粒子層が形成されて
も、脱水性能を確保するようにしたベルトフィルタが提
供される。また、せきを採用する実施の形態では、微粒
子層が形成されるに到った位置において、表層に浮いて
くる水をせき止め、同時に微粒子層をかき乱して真空吸
引によって水を吸い出させることができ、水相がケーキ
表面に排出されることを防ぐことができる。またさら
に、せきを複数段設けているので、かき乱し効果が大き
く、かつ石膏スラリの性状が変化し、微粒子層の形成さ
れる位置が変化しても、いずれかのせきで対応すること
ができ、確実にこれをかき乱し、脱水性能を確保するこ
とができる。
As is clear from the above description,
ADVANTAGE OF THE INVENTION According to this invention, even if the fine particle layer of a gypsum cake is formed, the belt filter which ensured the dehydration performance is provided. Further, in the embodiment employing a weir, at the position where the fine particle layer is formed, the water floating on the surface layer can be dammed, and at the same time, the fine particle layer can be disturbed and the water can be sucked out by vacuum suction. In addition, the water phase can be prevented from being discharged to the cake surface. Further, since a plurality of weirs are provided, the turbulence effect is large, and the properties of the gypsum slurry change, and even if the position where the fine particle layer is formed changes, it is possible to cope with any of the weirs, This can be reliably disturbed, and the dewatering performance can be ensured.

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

【図1】本発明にかかるベルトフィルタの一実施の形態
を説明する断面図である。
FIG. 1 is a cross-sectional view illustrating an embodiment of a belt filter according to the present invention.

【図2】石膏ケーキに形成される微粒子層を説明する断
面図である。
FIG. 2 is a cross-sectional view illustrating a fine particle layer formed on a gypsum cake.

【符号の説明】[Explanation of symbols]

1 ベルトフィルタ 2 石膏スラリ 3 供給ヘッダ 4 第1真空ボックス部 5 第2真空ボックス部 6 ゴムベルト 7 ベルトフィルタ本体 8 石膏ケーキ 9 洗浄水供給装置 10 せき 11 回収コンベア 12 ベルトフィルタ洗浄装置 DESCRIPTION OF SYMBOLS 1 Belt filter 2 Gypsum slurry 3 Supply header 4 First vacuum box part 5 Second vacuum box part 6 Rubber belt 7 Belt filter body 8 Gypsum cake 9 Washing water supply device 10 Cough 11 Recovery conveyor 12 Belt filter cleaning device

───────────────────────────────────────────────────── フロントページの続き (72)発明者 沖野 進 広島県広島市西区観音新町四丁目6番22号 三菱重工業株式会社広島研究所内 (72)発明者 日野 正夫 広島県広島市西区観音新町四丁目6番22号 三菱重工業株式会社広島研究所内 ──────────────────────────────────────────────────続 き Continuing on the front page (72) Inventor Susumu Okino 4-22, Kannonshinmachi, Nishi-ku, Hiroshima City, Hiroshima Prefecture Mitsubishi Heavy Industries, Ltd. Hiroshima Research Laboratory (72) Inventor Masao Hino 4-chome Kannonshinmachi, Nishi-ku, Hiroshima City, Hiroshima Prefecture No. 6-22 Mitsubishi Heavy Industries, Ltd. Hiroshima Laboratory

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 真空脱水装置によって排煙脱硫装置から
の石膏スラリを吸引脱水するようにしたベルトフィルタ
において、下端が石膏ケーキの上層に延長するせきをベ
ルトフィルタの長手方向に複数段設け、石膏ケーキの表
面に形成される微粒子層をかき乱すようにしたことを特
徴とするベルトフィルタ。
1. A belt filter in which gypsum slurry from a flue gas desulfurization unit is suctioned and dewatered by a vacuum dewatering device, wherein a plurality of weirs whose lower end extends to the upper layer of the gypsum cake are provided in the longitudinal direction of the belt filter. A belt filter characterized by disturbing a fine particle layer formed on the cake surface.
【請求項2】 請求項1のベルトフィルタにおいて、温
水、蒸気、又は温水及び蒸気をベルトフィルタ上の石膏
スラリ又は石膏ケーキに供給する洗浄水供給装置を設け
たことを特徴とするベルトフィルタ。
2. The belt filter according to claim 1, further comprising a washing water supply device for supplying hot water, steam, or hot water and steam to a gypsum slurry or a gypsum cake on the belt filter.
JP30187997A 1997-11-04 1997-11-04 Belt filter Expired - Lifetime JP3600417B2 (en)

Priority Applications (6)

Application Number Priority Date Filing Date Title
JP30187997A JP3600417B2 (en) 1997-11-04 1997-11-04 Belt filter
TW087114751A TW402518B (en) 1997-11-04 1998-09-05 Belt filter
KR1019980041003A KR100276126B1 (en) 1997-11-04 1998-09-30 Belt filter
CN98123621A CN1073872C (en) 1997-11-04 1998-10-29 belt filter
CZ19983484A CZ291668B6 (en) 1997-11-04 1998-10-30 Filtration method of gypsum slurry and belt filter for making the same
TR1998/02224A TR199802224A3 (en) 1997-11-04 1998-11-03 Filet filter.

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP30187997A JP3600417B2 (en) 1997-11-04 1997-11-04 Belt filter

Publications (2)

Publication Number Publication Date
JPH11128670A true JPH11128670A (en) 1999-05-18
JP3600417B2 JP3600417B2 (en) 2004-12-15

Family

ID=17902250

Family Applications (1)

Application Number Title Priority Date Filing Date
JP30187997A Expired - Lifetime JP3600417B2 (en) 1997-11-04 1997-11-04 Belt filter

Country Status (6)

Country Link
JP (1) JP3600417B2 (en)
KR (1) KR100276126B1 (en)
CN (1) CN1073872C (en)
CZ (1) CZ291668B6 (en)
TR (1) TR199802224A3 (en)
TW (1) TW402518B (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006110426A (en) * 2004-10-13 2006-04-27 Ishikawajima Harima Heavy Ind Co Ltd Gypsum dewatering equipment
WO2011104919A1 (en) 2010-02-26 2011-09-01 三菱重工業株式会社 Gypsum dewatering device for desulfurization facility
WO2025138583A1 (en) * 2023-12-28 2025-07-03 华能(福建)能源开发有限公司福州分公司 Wet flue gas desulfurization gypsum treatment method

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Family Cites Families (1)

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Publication number Priority date Publication date Assignee Title
SE402717B (en) * 1976-11-26 1978-07-17 Nordengren Patenter PROCEDURE FOR WASHING OUT FILTER CAKES AND SPREADER NOZZLE FOR PERFORMING THE PROCEDURE

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006110426A (en) * 2004-10-13 2006-04-27 Ishikawajima Harima Heavy Ind Co Ltd Gypsum dewatering equipment
WO2011104919A1 (en) 2010-02-26 2011-09-01 三菱重工業株式会社 Gypsum dewatering device for desulfurization facility
US8795516B2 (en) 2010-02-26 2014-08-05 Mitsubishi Heavy Industries, Ltd. Gypsum dewatering device for desulfurization facility
WO2025138583A1 (en) * 2023-12-28 2025-07-03 华能(福建)能源开发有限公司福州分公司 Wet flue gas desulfurization gypsum treatment method

Also Published As

Publication number Publication date
KR19990044832A (en) 1999-06-25
KR100276126B1 (en) 2000-12-15
JP3600417B2 (en) 2004-12-15
CN1073872C (en) 2001-10-31
CZ291668B6 (en) 2003-04-16
CZ348498A3 (en) 1999-07-14
TW402518B (en) 2000-08-21
TR199802224A2 (en) 1999-10-21
TR199802224A3 (en) 1999-10-21
CN1219440A (en) 1999-06-16

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