CN205360710U - But dehydration of high moisture clean coal is with superhigh pressure piston varactor pressure filter after coal slime flotation - Google Patents

But dehydration of high moisture clean coal is with superhigh pressure piston varactor pressure filter after coal slime flotation Download PDF

Info

Publication number
CN205360710U
CN205360710U CN201620119867.3U CN201620119867U CN205360710U CN 205360710 U CN205360710 U CN 205360710U CN 201620119867 U CN201620119867 U CN 201620119867U CN 205360710 U CN205360710 U CN 205360710U
Authority
CN
China
Prior art keywords
filter
plate
filter plate
pressure
piston
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Withdrawn - After Issue
Application number
CN201620119867.3U
Other languages
Chinese (zh)
Inventor
陈亦军
欧阳征国
汪家喜
刘道广
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.)
Shenzhen Ruicheng Shidai Industrial Co Ltd
SHANGHAI TECHASE ENVIRONMENT PROTECTION CO Ltd
Original Assignee
Shenzhen Ruicheng Shidai Industrial Co Ltd
SHANGHAI TECHASE ENVIRONMENT PROTECTION CO 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 Shenzhen Ruicheng Shidai Industrial Co Ltd, SHANGHAI TECHASE ENVIRONMENT PROTECTION CO Ltd filed Critical Shenzhen Ruicheng Shidai Industrial Co Ltd
Priority to CN201620119867.3U priority Critical patent/CN205360710U/en
Application granted granted Critical
Publication of CN205360710U publication Critical patent/CN205360710U/en
Anticipated expiration legal-status Critical
Withdrawn - After Issue legal-status Critical Current

Links

Landscapes

  • Filtration Of Liquid (AREA)

Abstract

The utility model discloses a but dehydration of high moisture clean coal is with superhigh pressure piston varactor pressure filter after coal slime flotation. It includes hydro -cylinder, hydro -cylinder seat, girder, pressure plate, thrust plate and a plurality of filter frame, the front end of filter frame, rear end are equipped with respectively and bulldoze board, bearing plate, it is equipped with a plurality of seal spring to bulldoze on same circumference between board and the bearing plate, bearing plate and filter plate mounting panel fixed connection, fixed filter plate and filter plate mounting panel fixed connection, fixed mounting has the piston axle on the fixed filter plate, ejecting filter plate and piston axle fixed connection, be equipped with ejecting spring between fixed filter plate and ejecting filter plate. The utility model discloses the improvement has been done on current superhigh pressure elasticity squeezer: through fixed mounting piston axle on fixed filter plate, the ejecting filter plate of the epaxial fixed mounting of piston again, but make original elasticity squeezer become piston varactor pressure filter, through set up ejecting spring between fixed filter plate and ejecting filter plate, realized that the filter cake unloads automatically.

Description

煤泥浮选后高含水精煤脱水用超高压活塞式可变容压滤机Ultra-high pressure piston type variable capacity filter press for dehydration of high water content clean coal after coal slime flotation

技术领域technical field

本实用新型属于过滤技术领域,涉及一种煤泥浮选后高含水精煤脱水用超高压活塞式可变容压滤机。The utility model belongs to the technical field of filtration, and relates to an ultra-high pressure piston-type variable-capacity filter press for dehydrating high-water clean coal after coal slime flotation.

背景技术Background technique

从废弃的煤泥中通过加药浮选提取低硫低灰分的清洁精煤,是一种节能环保新工艺,这种新工艺路线中需要用到一种可对煤泥浮选后的高含水精煤直接进行脱水的过滤分离设备。Extracting clean clean coal with low sulfur and low ash content from waste coal slime by dosing flotation is a new technology for energy saving and environmental protection. Clean coal is directly dehydrated by filtration and separation equipment.

申请人针对煤泥浮选后高含水精煤脱水用过滤分离设备的研发已整整三年,在这过程中,他们走访了国内主要的过滤分离设备制造、使用厂家,与这些厂家进行了不同形式的技术沟通和研讨,在转鼓真空过滤机、带式混溶压榨机、各种离心机、箱式压滤机、弹性板框压榨机等过滤分离设备上进行了无数次小试、中试试验,取得了大量的实验数据。但最后结果发现,没有一种现有设备可以直接应用在煤泥浮选后高含水精煤的脱水过滤分离上,只有弹性板框压榨机比较接近其要求。难点主要有四,一是要求精煤含水率低,过滤后精煤含水率≤9%;二是要求产量大,处理量大,精煤绝对处理量≥10吨/小时台;三是压榨压力大,≥5.5MPa;四是应能实现自动卸泥饼。The applicant has been researching and developing filtration and separation equipment for high water content clean coal dehydration after coal slime flotation for three years. During this process, they visited major domestic manufacturers and users of filtration and separation equipment, and conducted different forms of cooperation with these manufacturers. Numerous small tests and pilot tests have been carried out on filtration and separation equipment such as drum vacuum filters, belt miscible presses, various centrifuges, box filter presses, and elastic plate and frame presses. A large amount of experimental data has been obtained. However, it was finally found that there is no existing equipment that can be directly applied to the dehydration, filtration and separation of high-water clean coal after coal slime flotation, and only the elastic plate and frame press is relatively close to its requirements. There are four main difficulties. One is that the water content of clean coal is required to be low, and the water content of clean coal after filtration is ≤9%; Large, ≥5.5MPa; Fourth, it should be able to automatically unload the mud cake.

而现有的过滤分离设备均无法满足这些工艺要求,现有技术的缺点如下:However, existing filtration and separation equipment cannot meet these technological requirements, and the disadvantages of the prior art are as follows:

(1)压榨压力不够,国内的压榨压力≤5MPa。(1) The squeezing pressure is not enough, and the domestic squeezing pressure is ≤5MPa.

(2)处理量不够,国内生产的弹性板框压榨机处理量最大的是上海同臣环保有限公司生产的TCYZ200(1770)机型,其处理量为绝干泥4吨/小时·台。(2) The processing capacity is not enough. The largest processing capacity of the domestically produced elastic plate and frame press is the TCYZ200 (1770) model produced by Shanghai Tongchen Environmental Protection Co., Ltd., and its processing capacity is 4 tons/hour of dry mud.

(3)含水率达不到,现有压榨机滤饼的含水率≥20%。(3) The water content cannot reach, and the water content of the filter cake of the existing press is more than or equal to 20%.

(4)不能实现滤饼自动卸落,特别是精煤的含水率≤9%时,滤饼很干很硬,往往卡在滤板空隙中。(4) Automatic unloading of the filter cake cannot be realized, especially when the moisture content of the clean coal is ≤9%, the filter cake is very dry and hard, and is often stuck in the gap of the filter plate.

(5)现有过滤分离设备的滤室深度在10~30mm,处理量小,效率低。(5) The depth of the filter chamber of the existing filtration and separation equipment is 10-30mm, the processing capacity is small, and the efficiency is low.

实用新型内容Utility model content

本实用新型的目的在于克服现有技术的不足,提供一种在现有的超高压弹性压榨机基础上改进,能满足工艺要求的煤泥浮选后高含水精煤脱水用超高压活塞式可变容压滤机。The purpose of this utility model is to overcome the deficiencies of the prior art, and provide an ultra-high pressure piston-type dehydration machine for high-water clean coal dehydration after coal slime flotation, which is improved on the basis of the existing ultra-high pressure elastic press and can meet the process requirements. Variable capacity filter press.

本实用新型的技术方案如下:The technical scheme of the utility model is as follows:

一种煤泥浮选后高含水精煤脱水用超高压活塞式可变容压滤机,它包括油缸、油缸座、主梁、压力板、止推板,以及设在压力板和止推板之间的若干滤框;滤框的前后两侧分别设有推压板、承压板;推压板和承压板之间在同一圆周上设有若干密封弹簧;承压板与滤板安装板固定连接;固定滤板与滤板安装板固定连接;固定滤板上固定安装有活塞轴;顶出滤板与活塞轴固定连接;在固定滤板和顶出滤板之间设有顶出弹簧。An ultra-high-pressure piston-type variable-capacity filter press for dehydrating high-water clean coal after slime flotation, which includes an oil cylinder, an oil cylinder seat, a main beam, a pressure plate, a thrust plate, and a pressure plate and a thrust plate There are several filter frames in between; the front and rear sides of the filter frame are respectively provided with a push plate and a pressure plate; there are several sealing springs on the same circumference between the push plate and the pressure plate; the pressure plate is fixed to the filter plate mounting plate Connection; the fixed filter plate is fixedly connected with the filter plate mounting plate; the fixed filter plate is fixedly installed with a piston shaft; the ejector filter plate is fixedly connected with the piston shaft; an ejector spring is arranged between the fixed filter plate and the ejector filter plate.

固定滤板上固定安装有四根活塞轴;四根活塞轴在同一圆周上均匀分布。Four piston shafts are fixedly installed on the fixed filter plate; the four piston shafts are evenly distributed on the same circumference.

在固定滤板和顶出滤板之间在同一圆周上设有四个顶出弹簧;四个顶出弹簧均匀分布在同一圆周上。Four ejection springs are arranged on the same circumference between the fixed filter plate and the ejection filter plate; the four ejection springs are evenly distributed on the same circumference.

本实用新型的有益效果:The beneficial effects of the utility model:

本实用新型的煤泥浮选后高含水精煤脱水用超高压活塞式可变容压滤机,在现有的超高压弹性压榨机的基础上作了如下改进:1、通过在固定滤板上固定安装活塞轴,再活塞轴上固定安装顶出滤板,使原来的弹性压榨机变成了活塞式可变容压滤机,使其能够满足煤泥浮选后高含水精煤的脱水过滤分离工艺要求。2、通过在固定滤板和顶出滤板之间设置顶出弹簧,实现了滤饼自动卸落(弹簧卸泥)。The ultra-high-pressure piston-type variable-capacity filter press for dehydrating high-moisture clean coal after coal slime flotation of the utility model has been improved as follows on the basis of the existing ultra-high-pressure elastic press: 1. The piston shaft is fixedly installed on the top of the piston shaft, and the ejector filter plate is fixedly installed on the piston shaft, so that the original elastic press machine becomes a piston type variable capacity filter press, which can meet the dehydration of high water content clean coal after slime flotation. Filtration separation process requirements. 2. By setting the ejection spring between the fixed filter plate and the ejection filter plate, the automatic unloading of the filter cake (spring unloading) is realized.

本实用新型的煤泥浮选后高含水精煤脱水用超高压活塞式可变容压滤机,具有如下优点:The ultra-high pressure piston-type variable capacity filter press for dehydrating high-water clean coal after coal slime flotation of the utility model has the following advantages:

(1)该超高压活塞式可变容压榨机的压榨压力最高达6~9MPa;(1) The maximum pressing pressure of the ultra-high pressure piston type variable capacity press is 6-9 MPa;

(2)经该超高压活塞式可变容压榨机脱水后,精煤的含水率≤9%;(2) After being dehydrated by the ultra-high pressure piston type variable capacity press, the moisture content of the clean coal is ≤9%;

(3)该超高压活塞式可变容压榨机的精煤处理量达到了绝干泥11~13吨/小时·台;(4)该超高压活塞式可变容压榨机的压缩量可达15%~20%;(3) The clean coal processing capacity of the ultra-high-pressure piston variable-capacity press reaches 11-13 tons/hour of dry mud per unit; (4) The compression capacity of the ultra-high-pressure piston-type variable-capacity press can reach 15% to 20%;

(5)该超高压活塞式可变容压榨机板框专门设计了滤饼自动弹卸落装置,解决了煤饼难卸落问题。(5) The plate frame of the ultra-high pressure piston type variable capacity press is specially designed with an automatic ejection and unloading device for filter cakes, which solves the problem that coal cakes are difficult to unload.

附图说明Description of drawings

图1是本实用新型中的超高压活塞式可变容压滤机的整机结构示意图;Fig. 1 is the complete machine structure schematic diagram of ultra-high pressure piston type variable capacity filter press in the utility model;

图2是本实用新型中的滤框总成的正面结构示意图;Fig. 2 is a schematic view of the front structure of the filter frame assembly in the utility model;

图3是本实用新型中的滤框侧视图(进泥状态);Fig. 3 is a side view of the filter frame (into mud state) in the utility model;

图4是本实用新型中的滤框侧视图(卸料状态)。Fig. 4 is a side view of the filter frame (unloading state) in the utility model.

图中:1—进泥管,2—止推板,3—主梁,4—滤框,5—压力板,6—油缸座,7—油缸,8—液压站,9—耳肩,10—辊轮,11—承压板,12—固定滤板,13—密封弹簧,14—滤板安装板,15—活塞轴,16—顶出弹簧,17—推压板,18—顶出滤板,19—滤布In the figure: 1—mud inlet pipe, 2—thrust plate, 3—main beam, 4—filter frame, 5—pressure plate, 6—oil cylinder seat, 7—oil cylinder, 8—hydraulic station, 9—ear shoulder, 10 —roller, 11—pressure bearing plate, 12—fixed filter plate, 13—sealing spring, 14—filter plate mounting plate, 15—piston shaft, 16—ejection spring, 17—push plate, 18—ejection filter plate , 19—filter cloth

具体实施方式detailed description

以下结合附图和实施例对本实用新型作进一步的说明。Below in conjunction with accompanying drawing and embodiment the utility model is described further.

如图1所示,本实用新型一种煤泥浮选后高含水精煤脱水用超高压活塞式可变容压滤机,它包括油缸7、油缸座6、主梁3、压力板5、止推板2,以及设在压力板5和止推板2之间的若干滤框4等部件。As shown in Figure 1, the utility model is an ultra-high pressure piston-type variable-capacity filter press for dehydrating high-water clean coal after coal slime flotation, which includes an oil cylinder 7, an oil cylinder seat 6, a main beam 3, a pressure plate 5, Thrust plate 2, and several filter frames 4 and other components arranged between pressure plate 5 and thrust plate 2.

如图3所示,滤框4的前后两侧分别设有推压板17、承压板11;在推压板17和承压板11之间在同一圆周上设有若干密封弹簧13;承压板11与滤板安装板14固定连接;固定滤板12与滤板安装板14固定连接;固定滤板12上在同一圆周上均匀分布固定安装有四根活塞轴15;顶出滤板18与四根活塞轴15固定连接;在固定滤板12和顶出滤板18之间在同一圆周上设有四个顶出弹簧16(图3中画出了上下对称的两个顶出弹簧16)。As shown in Figure 3, the front and rear sides of the filter frame 4 are respectively provided with a pushing plate 17 and a pressure bearing plate 11; between the pushing plate 17 and the pressure bearing plate 11, several sealing springs 13 are arranged on the same circumference; the pressure bearing plate 11 is fixedly connected with the filter plate mounting plate 14; the fixed filter plate 12 is fixedly connected with the filter plate mounting plate 14; the fixed filter plate 12 is evenly distributed and fixedly installed with four piston shafts 15 on the same circumference; Root piston shaft 15 is fixedly connected; Between fixed filter plate 12 and ejection filter plate 18, be provided with four ejection springs 16 (two ejection springs 16 of upper and lower symmetry are drawn in Fig. 3) on the same circumference.

如图2所示,滤框总成上设有耳肩9、辊轮10,由此滤框可以安装在主梁3上。As shown in FIG. 2 , the filter frame assembly is provided with ear shoulders 9 and rollers 10 , so that the filter frame can be installed on the main beam 3 .

工作过程包括:预压阶段、进料阶段、压榨阶段、拉板卸料阶段四个主要过程。The working process includes four main processes: pre-pressing stage, feeding stage, pressing stage, and pulling plate unloading stage.

预压阶段:启动液压站8带动油缸7将滤框4推向止推板2一侧,使各滤框4紧密贴紧;如图3所示,滤框4外圈在承压板框和推压板框之间的密封弹簧13在油缸压力作用下会被挤压缩短;密封弹簧13的弹性范围设计值可控制在10~30mm。Preloading stage: start the hydraulic station 8 to drive the oil cylinder 7 to push the filter frame 4 to the side of the thrust plate 2, so that each filter frame 4 is tightly attached; as shown in Figure 3, the outer ring of the filter frame 4 is between the pressure plate frame and the The sealing spring 13 between the pushing plates and frames will be squeezed and shortened under the action of the oil cylinder pressure; the design value of the elastic range of the sealing spring 13 can be controlled at 10-30mm.

进料阶段:通过柱塞泵将煤浆经进泥管1打入滤框4中,水分透过滤布19渗走,煤浆逐渐充满滤框4,浓度逐渐升高,与此同时,高浓度的煤浆逐渐产生压力,推动顶出滤板18向内侧移动,顶出弹簧16被压缩,吸收部分势能;顶出弹簧16压缩部分行程后,与其连在一起的顶出滤板18背部与滤板安装板14贴合,不再后退。Feeding stage: the coal slurry is pumped into the filter frame 4 through the mud inlet pipe 1 through the plunger pump, the water seeps through the filter cloth 19, the coal slurry gradually fills the filter frame 4, and the concentration gradually increases. At the same time, the high concentration The coal slurry gradually generates pressure, pushing the ejection filter plate 18 to move inward, and the ejection spring 16 is compressed to absorb part of the potential energy; after the ejection spring 16 compresses part of the stroke, the back of the ejection filter plate 18 connected with it is connected to the filter plate. The board mounting board 14 fits together and does not retreat any more.

压榨阶段:再次启动油缸7,向止推板2方向推挤滤框4,在高压作用下,密封弹簧13进一步被挤压,如图3、图4所示,滤室深度从进料时的A=65~80mm被挤压到B=30~50mm左右,压力可升高到5~9MPa,煤浆被挤压为煤饼(滤饼);煤饼含水率降至10%~8%左右。Squeezing stage: Start the oil cylinder 7 again, push the filter frame 4 toward the thrust plate 2, under the action of high pressure, the sealing spring 13 is further squeezed, as shown in Figure 3 and Figure 4, the depth of the filter chamber changes from the A=65~80mm is extruded to about B=30~50mm, the pressure can be increased to 5~9MPa, and the coal slurry is extruded into coal cake (filter cake); the moisture content of coal cake is reduced to about 10%~8%. .

拉板卸料阶段:油缸7回位,密封弹簧13的力量释放,滤框4恢复至自由态,通过设备自带的拉板机构,将滤板依次拉开;拉开过程中因顶出弹簧16势能释放,推动顶出滤板18移位,这一力量可以克服煤饼与框体之间的结合力。这样煤饼自然与框体分离,脱出滤框,完成卸料。Pull plate unloading stage: the oil cylinder 7 returns to its position, the force of the sealing spring 13 is released, the filter frame 4 returns to the free state, and the filter plates are pulled apart sequentially through the pull plate mechanism that comes with the equipment; 16 releases the potential energy, pushes the ejection filter plate 18 to shift, and this force can overcome the binding force between the briquette and the frame. In this way, the briquettes are naturally separated from the frame and come out of the filter frame to complete the unloading.

本实用新型的超高压活塞式可变容压滤机的主要技术点如下:The main technical points of the ultra-high pressure piston type variable capacity filter press of the present invention are as follows:

1、大容积,压缩量可达15%~20%;1. Large volume, the compression amount can reach 15% to 20%;

2、高压力,压榨压力可达5~9MPa;2. High pressure, the pressing pressure can reach 5-9MPa;

3、新型辅助卸料方式(弹簧卸泥),能实现滤饼自动卸落。3. The new auxiliary unloading method (spring unloading mud) can realize automatic unloading of filter cake.

Claims (5)

1. High water cut cleaned coal dehydration ultra-high pressure piston type variable capacity pressure filter after a coal slime flotation, it is characterised in that it includes oil cylinder, oil cylinder seat, girder, pressure plare, thrust plate, and is located at the some filter frames between pressure plare and thrust plate;The front end of filter frame, rear end are respectively equipped with push plate, bearing plate;On same circumference, some Packing springs it are provided with between push plate and bearing plate;Bearing plate is fixing with filter plate installing plate to be connected;Fixing filter plate is fixing with filter plate installing plate to be connected;Fixing filter plate is installed with piston shaft;Eject that filter plate and piston shaft are fixing to be connected;At fixing filter plate with eject and be provided with ejector spring between filter plate.
2. High water cut cleaned coal dehydration ultra-high pressure piston type variable capacity pressure filter after coal slime flotation as claimed in claim 1, it is characterised in that be installed with four piston shaft on fixing filter plate.
3. High water cut cleaned coal dehydration ultra-high pressure piston type variable capacity pressure filter after coal slime flotation as claimed in claim 2, it is characterised in that four piston shaft are uniformly distributed on same circumference.
4. High water cut cleaned coal dehydration ultra-high pressure piston type variable capacity pressure filter after the coal slime flotation as described in claim 1,2 or 3, it is characterised in that at fixing filter plate with eject and be provided with four ejector springs between filter plate on same circumference.
5. High water cut cleaned coal dehydration ultra-high pressure piston type variable capacity pressure filter after coal slime flotation as claimed in claim 4, it is characterised in that four ejector springs are evenly distributed on same circumference.
CN201620119867.3U 2016-02-14 2016-02-14 But dehydration of high moisture clean coal is with superhigh pressure piston varactor pressure filter after coal slime flotation Withdrawn - After Issue CN205360710U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201620119867.3U CN205360710U (en) 2016-02-14 2016-02-14 But dehydration of high moisture clean coal is with superhigh pressure piston varactor pressure filter after coal slime flotation

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201620119867.3U CN205360710U (en) 2016-02-14 2016-02-14 But dehydration of high moisture clean coal is with superhigh pressure piston varactor pressure filter after coal slime flotation

Publications (1)

Publication Number Publication Date
CN205360710U true CN205360710U (en) 2016-07-06

Family

ID=56270538

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201620119867.3U Withdrawn - After Issue CN205360710U (en) 2016-02-14 2016-02-14 But dehydration of high moisture clean coal is with superhigh pressure piston varactor pressure filter after coal slime flotation

Country Status (1)

Country Link
CN (1) CN205360710U (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106267936A (en) * 2016-02-14 2017-01-04 上海同臣环保有限公司 High water cut cleaned coal dehydration ultra-high pressure piston type variable capacity pressure filter after a kind of coal slime flotation
CN109925771A (en) * 2019-04-22 2019-06-25 重庆长能环境科技有限公司 A kind of compressible oil cylinder sheet frame filter plate of super-pressure
CN109987748A (en) * 2019-04-22 2019-07-09 重庆长能环境科技有限公司 A kind of black water intelligent processing method and its equipment
CN110078341A (en) * 2019-04-28 2019-08-02 中铁四局集团有限公司 A kind of mud solid-liquid separator and process

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106267936A (en) * 2016-02-14 2017-01-04 上海同臣环保有限公司 High water cut cleaned coal dehydration ultra-high pressure piston type variable capacity pressure filter after a kind of coal slime flotation
CN106267936B (en) * 2016-02-14 2018-05-25 上海同臣环保有限公司 High water cut cleaned coal dehydration ultra-high pressure piston type variable capacity filter press after a kind of coal slime flotation
CN109925771A (en) * 2019-04-22 2019-06-25 重庆长能环境科技有限公司 A kind of compressible oil cylinder sheet frame filter plate of super-pressure
CN109987748A (en) * 2019-04-22 2019-07-09 重庆长能环境科技有限公司 A kind of black water intelligent processing method and its equipment
CN110078341A (en) * 2019-04-28 2019-08-02 中铁四局集团有限公司 A kind of mud solid-liquid separator and process
CN110078341B (en) * 2019-04-28 2022-04-12 中铁四局集团有限公司 Slurry solid-liquid separator and process

Similar Documents

Publication Publication Date Title
CN205360710U (en) But dehydration of high moisture clean coal is with superhigh pressure piston varactor pressure filter after coal slime flotation
CN101254368B (en) Sludge squeezing filtering method and sludge strong press-pate machine used for the method
CN104138675B (en) A kind of elasticity Filter pressing board of electro-osmosis high pressure mud, press filtration assembly and filter press
CN107008042B (en) Sewage sludge reduction dewatering device based on electromagnetic force
CN103550966B (en) A kind of method of operating of diaphragm filter press
CN104225985B (en) High-pressure filter pressing device
CN107382009A (en) Super-pressure sludge high-drying degree dewatering
CN108392867A (en) A kind of plate and frame filter press feed system and plate and frame filter press and charging filter-pressing method
CN104649561B (en) A kind of pressing method of variable displacement type pressure filter
CN105561645B (en) A kind of dentation formula pressurize filter-pressing method
CN110550840B (en) Sludge wall breaking device and wall breaking method for deep squeezing of sludge
CN106267936B (en) High water cut cleaned coal dehydration ultra-high pressure piston type variable capacity filter press after a kind of coal slime flotation
CN204734997U (en) Take horizontal spring pressure filter of dry and hard structure of anti -blow
CN107082550B (en) Sewage sludge dewatering device based on electromagnetic force
CN107151089A (en) Sludge pressing system
CN209392804U (en) A kind of energy-efficient filter press
CN107008041B (en) Sewage sludge reduction dehydration method based on electromagnetic force
CN207062125U (en) A kind of super-pressure sludge high-drying degree dehydration device
CN202020958U (en) Sliding sleeve type double-piston filter pressing device
CN205216311U (en) Alkali formula nickelous carbonate filters to press uses membrane filter press futilely
CN206642448U (en) Coal slime preparation belt filter press
CN201735221U (en) High-pressure variable volume filtering unit for presser
CN203971497U (en) A kind of squeezer automatic discharging system of smoothness run
CN107434345B (en) Sludge press plate
CN204502505U (en) Hydraulic pressure closes chamber filter press plate

Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
AV01 Patent right actively abandoned

Granted publication date: 20160706

Effective date of abandoning: 20180525

AV01 Patent right actively abandoned

Granted publication date: 20160706

Effective date of abandoning: 20180525

AV01 Patent right actively abandoned
AV01 Patent right actively abandoned