WO2021253504A1 - 一种通过动态进料通道进泥的污泥脱水方法及板框（厢式）脱水机 - Google Patents

一种通过动态进料通道进泥的污泥脱水方法及板框（厢式）脱水机 Download PDF

Info

Publication number
WO2021253504A1
WO2021253504A1 PCT/CN2020/099636 CN2020099636W WO2021253504A1 WO 2021253504 A1 WO2021253504 A1 WO 2021253504A1 CN 2020099636 W CN2020099636 W CN 2020099636W WO 2021253504 A1 WO2021253504 A1 WO 2021253504A1
Authority
WO
WIPO (PCT)
Prior art keywords
filter
filter cloth
dynamic
sludge
feed channel
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.)
Ceased
Application number
PCT/CN2020/099636
Other languages
English (en)
French (fr)
Inventor
石文政
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Publication of WO2021253504A1 publication Critical patent/WO2021253504A1/zh
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

Links

Images

Classifications

    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F11/00—Treatment of sludge; Devices therefor
    • C02F11/12—Treatment of sludge; Devices therefor by de-watering, drying or thickening
    • C02F11/121—Treatment of sludge; Devices therefor by de-watering, drying or thickening by mechanical de-watering
    • C02F11/122—Treatment of sludge; Devices therefor by de-watering, drying or thickening by mechanical de-watering using filter presses
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D25/00—Filters formed by clamping together several filtering elements or parts of such elements
    • B01D25/12—Filter presses, i.e. of the plate or plate and frame type
    • B01D25/21—Plate and frame presses
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D25/00—Filters formed by clamping together several filtering elements or parts of such elements
    • B01D25/30—Feeding devices ; Discharge devices
    • B01D25/302—Feeding devices ; Discharge devices specially adapted for chamber filter presses
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D25/00—Filters formed by clamping together several filtering elements or parts of such elements
    • B01D25/32—Removal of the filter cakes
    • B01D25/322—Removal of the filter cakes specially for chamber filter presses
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D25/00—Filters formed by clamping together several filtering elements or parts of such elements
    • B01D25/32—Removal of the filter cakes
    • B01D25/34—Removal of the filter cakes by moving, e.g. rotating, the filter elements

Definitions

  • the present invention relates to the technical field of the field of sludge dewatering equipment, in particular to a sludge dewatering method and a plate-and-frame (chamber-type) dewatering machine for feeding sludge through a dynamic feed channel.
  • Chamber or plate and frame dewatering machine is a kind of equipment that realizes solid-liquid separation.
  • the existing common dewatering machine arranges filter plates with filtrate passages in parallel, and a filter cloth is sandwiched between the filter plate and the adjacent The plate is compressed to form a filter press chamber between the filter plate and the adjacent filter plate.
  • the suspension is continuously pumped into the filter chamber of the filter press.
  • the filter residue is trapped in the filter chamber to form a filter cake. Flow away in the drainage channel. After the pump reaches the set pressure, stop feeding. At this time, if the water content of the filter cake needs to be further reduced, the filter cake needs to be squeezed twice.
  • the filter plate After the second squeezing time is up, the filter plate will be opened to unload the filter cake, and the filter cake will be unloaded. After finishing washing the filter cloth, ply the board again and wait for the next mud entry. Due to the adhesiveness of the filter cake, the filter cake often does not fall off completely, and many of it will stick to the filter cloth. This requires workers to assist in shoveling off the filter cake.
  • the traditional chamber or plate and frame dehydrator uses high-pressure water or air to fill the filter cake through the diaphragm on the filter plate to perform secondary extrusion.
  • the secondary extrusion pressure is generally about 15kg/CM2, and the secondary compression pressure is insufficient. , Which will affect the subsequent dehydration process.
  • the purpose of the present invention is to solve the deficiencies of the prior art and provide a method for sludge dewatering through a dynamic feed channel of a dewatering machine without manual shoveling and having a higher secondary extrusion pressure.
  • a dehydrator with a dynamic feed channel is also designed.
  • a method for dewatering sludge through a dynamic feed channel of a dewatering machine includes the following steps:
  • the dynamic feed channel is composed of the elastic feed port, the filter cloth clamp and the unit mud cake injection hole on the filter cloth clamp;
  • Sludge is pumped into the dynamic feed channel by a feed pump, and the feed is stopped when the pressure in the dynamic feed channel reaches a certain value;
  • the main oil cylinder pushes the filter plates on both sides of the dynamic feed channel to further squeeze and remove the moisture in the mud cake between the two filter plates, further reducing the moisture content of the filter cake; when the filter plate approaches again, feed
  • the channel needs to be compressed synchronously, and the compression process is realized by the compression deformation of the elastic mud inlet of the dynamic feed channel.
  • step S2 when the pressure in the dynamic feeding channel is 6-10 kg/cm2 (the pressure received by the mud cake), the feeding is stopped.
  • the pressure to push the filter plates on both sides of the dynamic feed channel is greater than or equal to 30 kg/cm2 (the pressure of the second squeezing of the mud cake).
  • a dehydrator with a dynamic feed channel which includes an elastic feed port and a filter cloth.
  • the elastic feed port and the filter cloth clip form a dynamic feed channel.
  • the feed port is connected with the feed pump, the filter cloth is connected with the filter cloth traction drive device, the two sides of the dynamic feed channel are provided with filter plates, and the filter plate is connected with the main oil cylinder.
  • a filter cloth sealing device is provided above and below the filter plate.
  • the filter plate is close to the elastic feed port in the feed channel for synchronous compression.
  • the dehydrator may include a dynamic feed channel composed of several elastic feed ports and filter cloth clips.
  • the advantages of the sludge dewatering method provided by the present invention through the dynamic feed channel of the dewatering machine include, but are not limited to: not only can realize the ultra-high pressure secondary pressing technology of the variable filter chamber, but also can realize the up and down movement of the filter cloth, Automatic sludge removal, no artificial auxiliary sludge removal is required, and because the water content of sludge is greatly reduced, it provides favorable conditions for the subsequent treatment and disposal of sludge, which greatly saves the investment and operating costs of subsequent sludge treatment and disposal, and has huge social benefits. .
  • Fig. 1 exemplarily shows a structural schematic diagram of a dehydrator with a dynamic feed channel according to the present invention
  • Figure 2 exemplarily shows a schematic structural diagram of a dehydrator with a dynamic feed channel of the present invention during secondary extrusion
  • Fig. 3 exemplarily shows a schematic diagram of the structure of a dehydrator with a dynamic feed channel of the present invention when the filter plate is opened;
  • FIG. 1 to 3 it is an embodiment of a dehydrator with a dynamic feed channel of the present invention. With reference to Figures 1 to 3, the working principle of this embodiment will be further explained.
  • the elastic feed port is also compressed, and the compressed length is B1-B2.
  • the secondary pressurizing pressure can reach more than 30kg/cm2, which is nearly double the squeezing force compared to the way the diaphragm squeezes the filter cake twice.
  • the filter plate is kept under pressure for a period of time and then the main oil cylinder moves back again and pulls the filter plate to open synchronously one by one (as shown in Figure 3), and then the filter cloth 2 moves up and down through the filter cloth traction drive device , Driving the filter cake 6 to move down, all the filter cakes adhered to the filter cloth will automatically fall off under the influence of gravity, so that manual auxiliary shoveling is not required.
  • the filter cloth can automatically fall mud and the ultra-high pressure secondary extrusion with variable filter chamber thickness can be well realized.
  • the present invention also provides a sludge dewatering method through the dynamic feed channel of the dewatering machine, which is characterized in that it comprises the following steps:
  • a dynamic feed channel is composed of an elastic feed port and a filter cloth clip
  • Sludge is pumped into the dynamic feed channel by a feed pump, and the feed is stopped when the pressure in the dynamic feed channel reaches a certain value;
  • the main oil cylinder pushes the filter plates on both sides of the dynamic feed channel to squeeze the sludge between the filter cloths (between the filter plates) into a filter cake;
  • the present invention is beneficial in that it can not only realize the ultra-high pressure secondary squeezing of the variable filter chamber, but also realize the automatic mud dropping of the filter cloth up and down, without the need for manual auxiliary mud dropping.
  • This can promote the further upgrade of the box or plate and frame filter press, which not only solves the demand, but also provides favorable conditions for the subsequent treatment and disposal of sludge due to the greatly reduced water content of the sludge, which greatly saves the subsequent sludge treatment and disposal
  • the investment and operating costs of the company have huge social benefits.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Hydrology & Water Resources (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Organic Chemistry (AREA)
  • Treatment Of Sludge (AREA)
  • Filtration Of Liquid (AREA)

Abstract

一种通过脱水机动态进料通道的污泥脱水方法及脱水机，包括：由弹性进料口（1）与滤布（2）共同组成动态进料通道；污泥由进料泵泵入动态进料通道，当动态进料通道内压力到达一定数值时停止进料；主油缸推动动态进料通道两侧的滤板（3），将动态进料通道内的污泥挤压为滤饼（6）；打开滤板（3），通过与滤布（2）连接的滤布牵引装置拉动滤布（2），使滤饼（6）从滤布（2）上脱落。其既能够实现可变滤室的超高压二次压榨技术，又能够实现滤布（2）的自动落泥，而且由于污泥含水率大大下降，为污泥后续处理处置提供了有利条件，大大节约了后续污泥处理处置的投资和运行成本，具有巨大的社会效益。

Description

一种通过动态进料通道进泥的污泥脱水方法及板框(厢式)脱水机 技术领域
本发明涉及污泥脱水设备领域技术领域，具体来说是一种通过动态进料通道进泥的污泥脱水方法及板框(厢式)脱水机。
背景技术
厢式或板框脱水机是一种实现固液分离的设备，现有常见的脱水机将带有滤液通路的滤板平行排列，滤板和相邻滤板之间夹有滤布，将滤板压紧，使滤板与相邻滤板之间构成一个压滤室，悬浮液不断泵入压滤机的滤室内，滤渣被截留在滤室内形成滤饼，滤液透过滤布从滤板的排液通道中流走。待泵达到设定压力之后停止进料，此时如需进一步降低滤饼含水率需对滤饼进行二次挤压，二次挤压时间到之后就开滤板卸滤饼，卸完滤饼后对滤布完成冲洗，后续再合板，等待下一次进泥。由于滤饼具有粘附性，滤饼往往不会全部脱落，很多会粘黏在滤布上。这就需要工人辅助铲落滤饼。另外传统的厢式或板框脱水机是通过滤板上的隔膜充入高压水或空气对滤饼进行二次挤压的，二次挤压压力一般在15kg/CM2左右，二次压榨压力不足，对后续的脱水流程造成影响。
发明内容
本发明的目的在于解决现有技术的不足，提供一种无需人工铲泥，并具有更高二次挤压压力的一种通过脱水机动态进料通道的污泥脱水方法。
同时，为了实现上述目的，还设计了一种具有动态进料通道的脱水机
本发明采用的技术方案如下：
一种通过脱水机动态进料通道的污泥脱水方法，包括以下步骤：
S1.由弹性进料口与滤布夹以及滤布夹上的单位泥饼注入孔共同组成动态进料通道；
S2.污泥由进料泵泵入所述动态进料通道，当动态进料通道内压力到达一定数值时停止进料；
S3.主油缸推动所述动态进料通道两侧的滤板，将两块滤板之间泥饼内的水分进一步挤压去除，进一步降低滤饼含水率；在滤板再次靠近时，进料通道需要同步被压缩，该压缩过程通过动态进料通道的弹性进泥口的压缩变形实现。
S4.打开滤板，通过与所述滤布连接的滤布牵引装置拉动滤布，使滤饼从所述滤布上脱落。由于进料通道的进料口和滤布夹在开板后是分开的，这时候滤布上下行走时滤布夹是可以同步移动的，有效结合了滤布上下行走和滤饼弹性二次挤压两种功能。
进一步的，所述步骤S2中，当所述动态进料通道内的压力为6-10kg/cm2时(泥饼收到的压强)，停止进料。
进一步的，所述步骤S3中，推动所述动态进料通道两侧滤板的压力大于等于30kg/cm2(泥饼受到的二次挤压压强)。
本发明的另一方面，提供了一种具有动态进料通道的脱水机，包括弹性进料口和滤布，所述弹性进料口与所述滤布夹组成动态进料通道，所述弹性进料 口与进料泵连接，所述滤布与滤布牵引驱动装置连接，所述动态进料通道两侧设有滤板，所述滤板与主油缸连接。
进一步的，所述滤板上方和下方均设有滤布密封装置。
进一步的，所述滤板靠近是同步压缩进料通道中的弹性进料口的。
进一步的，所述脱水机可以包括由若干弹性进料口与滤布夹组成的动态进料通道。
发明的有益效果
本发明所提供的一种通过脱水机动态进料通道的污泥脱水方法的优点包括但不限于：既能够实现可变滤室的超高压二次压榨技术，又能够实现滤布的上下移动，自动落泥，不需要人工辅助落泥，而且由于污泥含水率大大下降，为污泥后续处理处置提供了有利条件，大大节约了后续污泥处理处置的投资和运行成本，具有巨大的社会效益。
附图说明
图1示例性示出了本发明的一种具有动态进料通道的脱水机的结构示意图；
图2示例性示出了本发明的一种具有动态进料通道的脱水机进行二次挤压时的结构示意图；
图3示例性示出了本发明的一种具有动态进料通道的脱水机打开滤板时的结构示意图；
图中：1.弹性进料口 2.滤布 3.滤板 4.滤布密封装置 5.滤布夹 6.滤 饼
具体实施方式
下面结合附图，对本发明所采用的技术方案做进一步说明。
如图1～3所示，为本发明一种具有动态进料通道的脱水机的一种实施例，结合图1～3，对本实施例的工作原理作进一步的说明。
如图1所示，在进行二次挤压前的状态下，由弹性进料口1和滤布夹5交替压紧组成了进料通道，然后污泥由进料泵泵入进料通道1，当压力达到一定值后，一般是6-10kg/cm2时，停止进料，此时，主油缸进行二次动作，向内侧推动所有滤板靠紧，每两块滤板之间形成的滤室厚度不断变薄，滤布2内的滤饼6受到越来越大的挤压力，滤饼6中的水被再次挤压出来，滤饼厚度由图1中的B1减小到图2中的B2，同样弹性进料口也被压缩了，压缩的长度为B1-B2。此时二次加压压力可以达到30kg/cm2以上，相较于隔膜二次挤压滤饼的方式，其挤压力多了将近一倍。当主油缸到达预先设计的位置后，对滤板保压一段时间后主油缸再次动作后退，拉动滤板逐片同步打开(如图3所示)，然后滤布2通过滤布牵引驱动装置上下移动，带动滤饼6往下移动，所有粘连在滤布上的滤饼会受到重力影响自动脱落，这样可以不需要人工辅助铲泥了。通过以上的结构形式和工艺流程能够很好地实现滤布自动落泥和可变滤室厚度超高压二次挤压。
同时，本发明还提供一种通过脱水机动态进料通道的污泥脱水方法，其特征在于，包括以下步骤：
S1.由弹性进料口与滤布夹共同组成动态进料通道；
S2.污泥由进料泵泵入所述动态进料通道，当动态进料通道内压力到达一定数值时停止进料；
S3.主油缸推动所述动态进料通道两侧的滤板，将滤布之间(滤板之间)的污泥挤压为滤饼；
S4.打开滤板，通过与所述滤布连接的滤布牵引装置拉动滤布，使滤饼从所述滤布上脱落。
综上所述，本发明的有益之处在于，既能够实现可变滤室的超高压二次压榨，又能够实现滤布的上下自动落泥，不需要人工辅助落泥。这样就能够推动厢式或板框压滤机的进一步升级换代，不仅解决了需求，而且由于污泥含水率大大下降，为污泥后续处理处置提供了有利条件，大大节约了后续污泥处理处置的投资和运行成本，具有巨大的社会效益。
以上所述，仅为此发明的具体实施方式，但本发明的保护范围不局限于此，任何熟悉本技术领域的技术人员在本发明揭露的技术范围内，根据本发明的技术方案和新型的构思加于等同替换或改变，都应涵盖在本发明的保护范围之内。

Claims (7)

  1. 一种通过动态进料通道进泥的污泥脱水方法，其特征在于，包括以下步骤：
    S1.由弹性进料口与滤布交替共同组成动态进料通道；
    S2.污泥由进料泵泵入所述动态进料通道，当动态进料通道内压力到达一定数值时停止进料；
    S3.主油缸推动所述动态进料通道两侧的滤板，将动态进料通道内的污泥挤压为滤饼；
    S4.打开滤板，通过与所述滤布连接的滤布牵引装置拉动滤布，使滤饼从所述滤布上脱落。
  2. 如权利要求1所述的脱水方法，其特征在于，所述步骤S2中，当所述动态进料通道内所述滤饼受到的压强为6-10kg/cm2时，停止进料。
  3. 如权利要求1所述的脱水方法，其特征在于，所述步骤S3中，所述动态进料通道内滤饼受到的挤压压强大于等于30kg/cm2。
  4. 一种具有动态进料通道的脱水机，其特征在于，包括弹性进料口和滤布，所述弹性进料口与所述滤布夹组成动态进料通道，所述弹性进料口与进料泵连接，所述滤布与滤布牵引驱动装置连接，所述动态进料通道两侧设有滤板，所述滤板与主油缸连接。
  5. 根据权利要求4所述的一种具有动态进料通道的脱水机，其特征在于，所述滤板上方和下方均设有滤布密封装置。
  6. 根据权利要求4所述的一种具有动态进料通道的脱水机，其特征在于，所述滤布靠近所述弹性进料口处设有滤布夹。
  7. 根据权利要求4所述的一种具有动态进料通道的脱水机，其特征在于，所述脱水机可以包括由若干弹性进料口与滤布夹组成的多个动态进料通道。
PCT/CN2020/099636 2020-06-17 2020-07-01 一种通过动态进料通道进泥的污泥脱水方法及板框（厢式）脱水机 Ceased WO2021253504A1 (zh)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
CN202010553531.9 2020-06-17
CN202010553531.9A CN111875215A (zh) 2020-06-17 2020-06-17 一种通过动态进料通道进泥的污泥脱水方法及板框（厢式）脱水机

Publications (1)

Publication Number Publication Date
WO2021253504A1 true WO2021253504A1 (zh) 2021-12-23

Family

ID=73157919

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/CN2020/099636 Ceased WO2021253504A1 (zh) 2020-06-17 2020-07-01 一种通过动态进料通道进泥的污泥脱水方法及板框（厢式）脱水机

Country Status (2)

Country Link
CN (1) CN111875215A (zh)
WO (1) WO2021253504A1 (zh)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN114470895A (zh) * 2022-02-15 2022-05-13 集美大学 一种多工位污泥自动脱水压榨设备及方法
CN119661051A (zh) * 2024-12-30 2025-03-21 山东永正产业技术研究院有限公司 一种工业固体废弃物回收用固液分离设备
CN119774843A (zh) * 2025-02-19 2025-04-08 东莞市圣茵生物有机肥有限公司 一种污泥脱水处理系统及处理方法

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN114425188A (zh) * 2020-10-29 2022-05-03 陶辉全 一种压滤器、含有该压滤器的脱水机及一种压滤脱水机组
CN121517085B (zh) * 2026-01-13 2026-04-03 天津锐创环保工程有限公司 基于自动化运行的污泥压滤系统

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB1106388A (en) * 1963-11-14 1968-03-13 English Clays Lovering Pochin Improvements in or relating to filter-presses and method of using the same
US4317724A (en) * 1980-05-23 1982-03-02 Ingersoll-Rand Company Feeding device for use in filter presses
US6280638B1 (en) * 1996-12-12 2001-08-28 Belcho Alexandrov Belchev Apparatus for continuous purification of liquids, dewatering and drying of the separated solids
CN102100982A (zh) * 2011-01-18 2011-06-22 上海洁地环境治理有限公司 一种弹性可压缩压滤板框装置
CN102974140A (zh) * 2012-11-16 2013-03-20 浙江金鸟压滤机有限公司 一种压滤机
CN108339300A (zh) * 2017-12-28 2018-07-31 上海仁创环境科技有限公司 弹性体密封变滤室板框压滤机
CN209885317U (zh) * 2019-01-25 2020-01-03 安徽金宏橡塑科技有限公司 一种隔膜压滤机

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5092558A (zh) * 1973-12-21 1975-07-24
CN101890256B (zh) * 2010-07-21 2011-12-28 山东景津环保设备有限公司 一种悬挂式滤布和夹布器
JP6032559B2 (ja) * 2013-10-01 2016-11-30 株式会社石垣 フィルタープレスにおける原液の供給装置
CN108553959B (zh) * 2018-04-17 2021-05-14 上海仁创环境科技有限公司 一种多块滤布同时清洗的厢式板框机及其清洗方法

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB1106388A (en) * 1963-11-14 1968-03-13 English Clays Lovering Pochin Improvements in or relating to filter-presses and method of using the same
US4317724A (en) * 1980-05-23 1982-03-02 Ingersoll-Rand Company Feeding device for use in filter presses
US6280638B1 (en) * 1996-12-12 2001-08-28 Belcho Alexandrov Belchev Apparatus for continuous purification of liquids, dewatering and drying of the separated solids
CN102100982A (zh) * 2011-01-18 2011-06-22 上海洁地环境治理有限公司 一种弹性可压缩压滤板框装置
CN102974140A (zh) * 2012-11-16 2013-03-20 浙江金鸟压滤机有限公司 一种压滤机
CN108339300A (zh) * 2017-12-28 2018-07-31 上海仁创环境科技有限公司 弹性体密封变滤室板框压滤机
CN209885317U (zh) * 2019-01-25 2020-01-03 安徽金宏橡塑科技有限公司 一种隔膜压滤机

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN114470895A (zh) * 2022-02-15 2022-05-13 集美大学 一种多工位污泥自动脱水压榨设备及方法
CN119661051A (zh) * 2024-12-30 2025-03-21 山东永正产业技术研究院有限公司 一种工业固体废弃物回收用固液分离设备
CN119774843A (zh) * 2025-02-19 2025-04-08 东莞市圣茵生物有机肥有限公司 一种污泥脱水处理系统及处理方法

Also Published As

Publication number Publication date
CN111875215A (zh) 2020-11-03

Similar Documents

Publication Publication Date Title
CN111875215A (zh) 一种通过动态进料通道进泥的污泥脱水方法及板框（厢式）脱水机
CN109432841B (zh) 一种带真空抽滤式压滤机
CN104225985B (zh) 一种高压压滤装置
WO2019128618A1 (zh) 弹性体密封变滤室板框压滤机
CN207237401U (zh) 有移动滤板的压滤装置
CN107382009A (zh) 超高压污泥高干度脱水方法
CN106946435B (zh) 大处理量污水污泥深度减量化方法
CN202822909U (zh) 新型立式全自动自锁式高效隔膜压滤机
CN218686677U (zh) 一种用于滤浆的板框压滤机
CN110812904A (zh) 陶瓷泥浆脱水设备及其操作方法
CN105561645B (zh) 一种齿状式保压压滤方法
CN103223269B (zh) 节能型隔膜式压滤机
CN106943779B (zh) 大处理量污水污泥深度减量化装置
CN103803773A (zh) 一种无滤布垂直压缩污泥高压脱水机
CN107434345B (zh) 污泥压榨板
CN211896608U (zh) 一种高压高效污泥压滤机
CN220976791U (zh) 一种超高压单向推进压缩式淤泥深度压缩脱水设备
CN210419682U (zh) 一种便于卸泥的板框压滤机
CN203183762U (zh) 节能型隔膜式压滤机
CN209848415U (zh) 一种高效板框压滤机
CN202020958U (zh) 滑套式双活塞压滤装置
CN111957084A (zh) 一种高效节能型压滤机及基于该压滤机的压榨过滤方法
CN207062125U (zh) 一种超高压污泥高干度脱水装置
CN212440204U (zh) 压滤机压榨气体再利用装置及节能型隔膜压滤机
CN202700167U (zh) 柱塞预压紧压榨过滤单元及压榨机

Legal Events

Date Code Title Description
121 Ep: the epo has been informed by wipo that ep was designated in this application

Ref document number: 20940980

Country of ref document: EP

Kind code of ref document: A1

NENP Non-entry into the national phase

Ref country code: DE

122 Ep: pct application non-entry in european phase

Ref document number: 20940980

Country of ref document: EP

Kind code of ref document: A1