CN202569691U - Full-automatic sludge treatment membrane pressure filter - Google Patents

Full-automatic sludge treatment membrane pressure filter Download PDF

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Publication number
CN202569691U
CN202569691U CN 201220018275 CN201220018275U CN202569691U CN 202569691 U CN202569691 U CN 202569691U CN 201220018275 CN201220018275 CN 201220018275 CN 201220018275 U CN201220018275 U CN 201220018275U CN 202569691 U CN202569691 U CN 202569691U
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CN
China
Prior art keywords
filter
full
filtration
sludge
automatic treatment
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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
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CN 201220018275
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Chinese (zh)
Inventor
李文斌
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.)
Guangdong Lee and Man Paper Manufacturing Co Ltd
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Guangdong Lee and Man Paper Manufacturing 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.)
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Priority to CN 201220018275 priority Critical patent/CN202569691U/en
Application granted granted Critical
Publication of CN202569691U publication Critical patent/CN202569691U/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Abstract

The utility model discloses a full-automatic sludge treatment membrane pressure filter, which comprises a filtration chamber, and a water pressure device for conveying sludge into the filtration chamber, wherein the filtration chamber is internally provided with at least two mobile filtration plates and filtration cloth sleeved at two ends of adjacent filtration plates in a snake-shaped alternating manner and an extrusion device for extruding the filtration plates; the filtration plates are parallel to each other; and the filtration cloth is connected to the inner wall of the filtration chamber in a closed manner to separate the water pressure device from the water outlet of the filtration chamber. By adopting the technical scheme, the full-automatic sludge treatment membrane pressure filter realizes automation by adopting an automatic control device; the extrusion device is matched with a filtration device, and the structure is simple, so that an effect for separating sludge from water is good; the moisture content in the separated sludge is low; the sludge can be outwards conveyed and further treated and used; and damage of sewage to the environment is effectively reduced.

Description

Full-automatic Treatment of Sludge diaphragm filter press
Technical field
The utility model relates to technical field of sewage, specifically, relates to full-automatic Treatment of Sludge diaphragm filter press.
Background technology
Reduce the mud generation at present, reduce moisture content, become the target that each sewage treatment plant of the whole world lays siege to.
The filter plant majority that sludge dewatering is at present used is belt filter press and centrifuge, and its work principle of filter is: belt filter press forms mud cake by the beaming roller extruding that is installed on the body by the mud discharge water branch that feed pump injects on the strainer; Centrifuge makes mud and separated form water form mud cake by the centrifugal force of rotation generation at a high speed, reaches the purpose of filtering back mud cake outward transport.
But be to use these two kinds of equipment make mud, separated form water effect its tangible weak point is arranged; Be that the mud that the belt filter press beaming roller pushes on the strainer is in a flash; Moisture in the mud is difficult to discharge fast, makes mud, separated form water effect very undesirable, and the moisture percentage in sewage sludge after the processing is higher; The mud that centrifuge relies on centrifugal force to separate, moisture content is also higher, therefore is difficult to form mud cake, is not easy to outward transport and further handles.
Summary of the invention
The utility model has overcome defective of the prior art, and a kind of full-automatic Treatment of Sludge diaphragm filter press is provided, and reaches the generation that reduces mud, reduces the water for cleaning of dewaterer, reduces the purpose of polluting, reducing operating cost.
In order to solve the problems of the technologies described above, the utility model is realized through following technical scheme:
Full-automatic Treatment of Sludge diaphragm filter press; Comprise filter chamber and carry mud to get into the water pressure device of said filter chamber; Be provided with at least two movably filter plates and in the said filter chamber, also be provided with the pressurizing unit of the said filter plate of extruding with the snakelike filter cloth that alternately is enclosed within the two ends of adjacent said filter plate.
Further, filter plate is parallel to each other.
Further, filter cloth sealing is connected in said filter chamber inwall the delivery port of said water pressure device and said filter chamber is separated.
Further, the water pressure device is a compression pump.
Further, the changed course roller that is used to change the filter cloth direction of motion is installed on the filter plate.
Further, automaton is a programmable control unit.
Further, the below that is positioned at filter cloth between each adjacent filter plate is provided with delivery hose, and delivery hose is connected in same outfall sewer.
Further, pressurizing unit comprises pressing plate and promotes the pressing plate cylinder that pressing plate compresses said filter plate.
Compared with prior art, the beneficial effect of the utility model is:
Adopt above technical scheme, full-automatic Treatment of Sludge diaphragm filter press is a kind of intermittent pressure filtration equipment, is used for the Separation of Solid and Liquid of various suspension; It is to rely on hold down gag that filter plate is compressed, again with suspension with being pumped into filter chamber, reach the purpose that solid particle is separated with liquid material through filter cloth; Reach the generation that reduces mud, reduce the water for cleaning of dewaterer, reduce the purpose of polluting, reducing operating cost; Machine energy-saving is efficient, and good separating effect is easy to use.
Description of drawings
Accompanying drawing is used to provide the further understanding to the utility model, is used to explain the utility model with the embodiment of the utility model, does not constitute the restriction to the utility model, in the accompanying drawings:
Fig. 1 is the structural representation of an embodiment of the utility model.
The structural representation of the filter cloth of an embodiment of Fig. 2 the utility model, filter plate and changed course roller.
Include among Fig. 1, Fig. 2 with lower component:
1---filter chamber;
2---the water pressure device;
3---filter plate;
4---filter cloth;
5---delivery hose;
6---pressing plate;
7---the pressing plate cylinder;
8---outfall sewer;
9---connect pipeline;
10---the changed course roller.
The specific embodiment
Describe below in conjunction with the preferred embodiment of accompanying drawing, should be appreciated that preferred embodiment described herein only is used for explanation and explains the utility model, and be not used in qualification the utility model the utility model.
Embodiment 1:
As shown in Figure 1, the full-automatic Treatment of Sludge diaphragm filter press of present embodiment comprises automaton, filter chamber 1 and water pressure device 2, is provided with between filter chamber 1 and the water pressure device 2 to connect pipeline 9, is provided with filter and pressurizing unit in the filter chamber 1.
Concrete, water pressure device 2 is thrown suspension into filter chamber 1 through connecting pipeline 9, and pressurizing unit compresses filter, and water is through filter, and solid particles etc. are trapped on the filter, accomplish mud, separated form water.This technical scheme, simple in structure, mud, separated form water are effective, and the moisture percentage in sewage sludge after the separation is low, is convenient to the mud outward transport and further handles or utilize, and has reduced the generation of mud, reduces the water for cleaning of dewaterer, has reduced operating cost, and is easy to use.
Reduced the harm of sewage effectively to environment.
Filter comprises two movably filter plates 3 and with the snakelike filter cloth 4 that alternately is enclosed within the two ends of adjacent filter plate 3, and filter plate 3 is propped up filter cloth 4, plays support, the fixedly effect of filter cloth 4.
Filter cloth 4 sealings are connected in filter chamber 1 inwall the delivery port of water pressure device 2 with filter chamber 1 are separated.
Water pressure device 2 is a compression pump.Suspension is squeezed into filter chamber 1 through compression pump 2, and gives liquid in the filter chamber 1 with pressure, makes water flows, passes filter cloth 4.
Every filter plate 3 is equipped with delivery hose 5, and delivery hose 5 is connected in same outfall sewer 8.The water that filters out through filter cloth 4 is pooled to outfall sewer 8 discharges via delivery hose 5.
Pressurizing unit comprises pressing plate 6 and promotes the pressing plate cylinder 7 that pressing plate 6 compresses filter plate 3.Pressing plate cylinder 7 promotes the filter plate 3 and filter cloth 4 that pressing plate 6 extruding stack, and mud, separated form water are come out.
This equipment can be realized automatic feed, arm-tie discharging automatically, filter cloth washing automatically, connect liquid turnover panel, pressurize eardrum, draining automatically automatically automatically through PLC control.Automaton is a programmable control unit.Each parts of programmable control unit control are accomplished whole flow process, realize automation.
Embodiment 2:
The main technical schemes of present embodiment is identical with embodiment 1, and unaccounted characteristic adopts the explanation among the embodiment 1 in the present embodiment, no longer gives unnecessary details at this.The difference of present embodiment and embodiment 1 is:
As shown in Figure 2, filter plate 3 is at least two, and the winding of 4 one-tenth S shapes of filter cloth is on filter plate 3.Multilayer filter plate 3 makes filter effect better, and the sewage quantity that the unit interval handles is more, and filter efficiency is higher.
Embodiment 3:
The main technical schemes of present embodiment is identical with embodiment 1, and unaccounted characteristic adopts the explanation among the embodiment 1 in the present embodiment, no longer gives unnecessary details at this.The difference of present embodiment and embodiment 1 is:
As shown in Figure 2, the changed course roller 10 that is used to change filter cloth 4 directions of motion is installed on the filter plate 3, be used to change the direction of filter cloth 4.
What should explain at last is: more than be merely the preferred embodiment of the utility model; Be not limited to the utility model; Although the utility model has been carried out detailed explanation with reference to embodiment; For a person skilled in the art, it still can be stated scheme to the skill that aforementioned each embodiment put down in writing and make amendment, and perhaps part technical characterictic wherein is equal to replacement.All within the spirit and principle of the utility model, any modification of being done, be equal to replacement, improvement etc., all should be included within the protection domain of the utility model.

Claims (8)

1. full-automatic Treatment of Sludge diaphragm filter press; It is characterized in that: comprise filter chamber and carry mud to get into the water pressure device of said filter chamber; Be provided with at least two movably filter plates and alternately be enclosed within the filter cloth at the two ends of adjacent said filter plate in the said filter chamber, also be provided with the pressurizing unit of the said filter plate of extruding with S shape.
2. full-automatic Treatment of Sludge diaphragm filter press according to claim 1, it is characterized in that: said filter plate is parallel to each other.
3. full-automatic Treatment of Sludge diaphragm filter press according to claim 2 is characterized in that: the sealing of said filter cloth is connected in said filter chamber inwall the delivery port of said water pressure device and said filter chamber is separated.
4. full-automatic Treatment of Sludge diaphragm filter press according to claim 1 is characterized in that: said water pressure device is a compression pump.
5. according to each described full-automatic Treatment of Sludge diaphragm filter press of claim 1 to 4, it is characterized in that: the changed course roller that is used to change the filter cloth direction of motion is installed on the said filter plate.
6. full-automatic Treatment of Sludge diaphragm filter press according to claim 1 is characterized in that: said automaton is a programmable control unit.
7. full-automatic Treatment of Sludge diaphragm filter press according to claim 3 is characterized in that: the below that is positioned at said filter cloth between each adjacent said filter plate is provided with delivery hose, and said delivery hose is connected in same outfall sewer.
8. full-automatic Treatment of Sludge diaphragm filter press according to claim 1 is characterized in that: said pressurizing unit comprises pressing plate and promotes the pressing plate cylinder that pressing plate compresses said filter plate.
CN 201220018275 2012-01-16 2012-01-16 Full-automatic sludge treatment membrane pressure filter Expired - Lifetime CN202569691U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 201220018275 CN202569691U (en) 2012-01-16 2012-01-16 Full-automatic sludge treatment membrane pressure filter

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 201220018275 CN202569691U (en) 2012-01-16 2012-01-16 Full-automatic sludge treatment membrane pressure filter

Publications (1)

Publication Number Publication Date
CN202569691U true CN202569691U (en) 2012-12-05

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Family Applications (1)

Application Number Title Priority Date Filing Date
CN 201220018275 Expired - Lifetime CN202569691U (en) 2012-01-16 2012-01-16 Full-automatic sludge treatment membrane pressure filter

Country Status (1)

Country Link
CN (1) CN202569691U (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110330208A (en) * 2019-07-16 2019-10-15 广东恒鑫智能装备股份有限公司 Sludge filter press
CN112221217A (en) * 2018-06-29 2021-01-15 谢婷婷 Sludge filter pressing device

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112221217A (en) * 2018-06-29 2021-01-15 谢婷婷 Sludge filter pressing device
CN112221217B (en) * 2018-06-29 2021-10-26 山东菲特环保设备有限公司 Sludge filter pressing device
CN110330208A (en) * 2019-07-16 2019-10-15 广东恒鑫智能装备股份有限公司 Sludge filter press

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GR01 Patent grant
CX01 Expiry of patent term

Granted publication date: 20121205

CX01 Expiry of patent term