CN210313988U - Waste slurry dewatering equipment - Google Patents

Waste slurry dewatering equipment Download PDF

Info

Publication number
CN210313988U
CN210313988U CN201921022719.XU CN201921022719U CN210313988U CN 210313988 U CN210313988 U CN 210313988U CN 201921022719 U CN201921022719 U CN 201921022719U CN 210313988 U CN210313988 U CN 210313988U
Authority
CN
China
Prior art keywords
medicament
slurry
sedimentation tank
waste
filter press
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.)
Active
Application number
CN201921022719.XU
Other languages
Chinese (zh)
Inventor
张运达
殷俊
江建斌
何健
宋刚练
祝宏文
陈大勇
顾春杰
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.)
Shanghai Geological Construction Co ltd
Original Assignee
Shanghai Geological Construction 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 Shanghai Geological Construction Co ltd filed Critical Shanghai Geological Construction Co ltd
Priority to CN201921022719.XU priority Critical patent/CN210313988U/en
Application granted granted Critical
Publication of CN210313988U publication Critical patent/CN210313988U/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Landscapes

  • Separation Of Suspended Particles By Flocculating Agents (AREA)
  • Treatment Of Sludge (AREA)

Abstract

The utility model discloses an abandonment mud dewatering equipment belongs to abandonment mud processing technology field. The system comprises a waste slurry pool, a slurry pump, a medicament adding device, a medicament pump, a fluid mixer, a belt filter press and a three-stage sedimentation tank. The slurry flocculant and the waste slurry are mixed by adopting a fluid mixer, a flocculation reaction can be generated, solid and liquid generated by the flocculation reaction are separated by a belt filter press, filter press liquid is precipitated by a three-stage sedimentation tank, purified clear water is finally obtained, and the waste slurry is more fully treated by combining chemical flocculation and mechanical dehydration; set up two at least medicament agitator, open the corresponding medicament valve of one of them medicament agitator in turn, reserve medicament stirring curing time for another medicament agitator for waste mud treatment work is more efficient.

Description

Waste slurry dewatering equipment
Technical Field
The utility model relates to an abandonment mud dewatering equipment belongs to abandonment mud processing technology field.
Background
The cast-in-situ bored pile is a construction method adopted for construction in a stratum with shallow underground water level, and the main principle is to replace mud by using an underwater concrete pouring method to complete the construction of the cast-in-situ bored pile. But during the construction process of the bored pile foundation, a large amount of waste mud is generated. Typically, the amount of waste mud generated is 3-5 times the volume of the pore-forming volume. At present, the method for treating the waste slurry comprises the steps of directly burying or discharging the waste slurry into fields and river channels, seriously damaging the urban ecological environment and causing great threat to the survival and health of human beings. Therefore, comprehensive treatment of waste sludge has become an urgent problem to be solved.
In recent years, Polyacrylamide (PAM) has been widely used in the field of sludge preparation and dewatering due to its excellent flocculation property. At present, most of scholars at home and abroad make more researches on the resource utilization of river and lake sludge and activated sludge, while the treatment of the waste mud in building construction mainly takes solid-liquid separation as a main part, and still more problems exist in the processes of reduction and resource treatment and recycling of the waste mud.
Aiming at the problem that the treatment of the waste slurry of the cast-in-situ bored pile cannot be fully finished by adopting a single treatment mode in the prior art, a set of waste slurry treatment process integrating chemical flocculation and mechanical dehydration is designed. By enhancing the quality control of the site and optimizing the equipment, the waste slurry generated in the process of drilling the cast-in-situ pile is efficiently, economically and environmentally treated.
Disclosure of Invention
The utility model discloses the technical problem that will solve lies in: the utility model provides a waste slurry dewatering equipment, it has solved the problem that present waste slurry adopts single mode can't obtain the abundant processing.
The utility model discloses the technical problem that will solve takes following technical scheme to realize:
a waste slurry dehydration device comprises a waste slurry pool, a slurry pump, a medicament adding device, a medicament pump, a fluid mixer, a belt filter press and a three-stage sedimentation tank;
a slurry stirrer is arranged in the waste slurry tank, and the waste slurry tank is connected with a waste slurry feeding end of the fluid mixer through a slurry pump;
the device comprises a fluid mixer, a medicament adding device, a slurry flocculating agent, a plurality of medicament stirring barrels, a plurality of medicament valves and a plurality of medicament mixing tanks, wherein the medicament adding device comprises at least two parallel medicament stirring barrels and a corresponding number of medicament valves;
the discharge end of the fluid mixer is connected with the feed end of the belt filter press, solid slag is discharged from a solid slag port of the belt filter press, and a water outlet of the belt filter press is communicated with the three-stage sedimentation tank.
As a preferred example, the bottom of the waste slurry tank is provided with a slurry outlet.
As a preferable example, a control flow valve is arranged on a communication pipeline between the fluid mixer and the belt filter press.
As a preferred example, the medicament valve is an electrically controlled valve.
As a preferable example, the slurry flocculant in the agent stirring barrel is polyacrylamide polymer.
As a preferable example, the three-stage sedimentation tank is composed of a first-stage sedimentation tank, a second-stage sedimentation tank and a third-stage sedimentation tank which are arranged in sequence, and the first-stage sedimentation tank and the second-stage sedimentation tank and the third-stage sedimentation tank are communicated through overflow holes.
A waste slurry dehydration process comprises the following steps:
(1) uniformly stirring the waste slurry, and uniformly stirring the waste slurry in the waste slurry pool by a slurry stirrer;
(2) stirring and curing the medicaments, namely adding a slurry flocculant into the medicament stirring barrels by using at least two parallel medicament stirring barrels and medicament valves with corresponding quantity, fully stirring and curing the medicaments by using a medicament stirrer, wherein each medicament stirring barrel is connected with the feed end of a medicament pump by the corresponding medicament valve, the corresponding medicament valve of one medicament stirring barrel is alternately opened, the medicament stirring and curing time is reserved for the other medicament stirring barrel, and the cured medicaments are output by the medicament pump;
(3) waste mud and medicaments are mixed, the waste mud in the waste mud pool is pumped by a mud pump and is sent into a fluid mixer, the fully cured mud flocculant in a medicament stirring barrel is pumped by a medicament pump and is sent into the fluid mixer, and the waste mud and the medicaments are fully mixed by a stirring device in the fluid mixer;
(4) flocculating and dewatering the waste slurry, preliminarily flocculating the mixed fluid in the fluid mixer, then flowing into a belt filter press for dewatering, discharging solid slag from a solid slag port, and introducing the pressure filtrate into a three-stage sedimentation tank;
(5) the filter-pressing water is precipitated and purified, and tertiary sedimentation tank comprises first order sedimentation tank, second level sedimentation tank, the third level sedimentation tank of arranging in order, and tertiary sedimentation tank carries out tertiary sediment to filter-pressing water, and the clear water of third level sedimentation tank supernatant for after tertiary sediment is discharged from tertiary sedimentation tank outlet.
The utility model has the advantages that:
(1) the slurry flocculant and the waste slurry are mixed by adopting a fluid mixer, a flocculation reaction can be generated, solid and liquid generated by the flocculation reaction are separated by a belt filter press, filter press liquid is precipitated by a three-stage sedimentation tank, purified clear water is finally obtained, and the waste slurry is more fully treated by combining chemical flocculation and mechanical dehydration;
(2) arranging at least two medicament mixing barrels, alternately opening a medicament valve corresponding to one medicament mixing barrel, and reserving medicament mixing and curing time for the other medicament mixing barrel, so that the waste slurry treatment work is more efficient;
(3) the method has the advantages that the waste slurry is treated by adopting a flocculation-dehydration mode, the high-molecular polyacrylamide is used as a slurry flocculant, filtrate and muck generated after filter pressing and dehydration are both harmless substances, outward transportation of the waste slurry is obviously reduced, normal operation of site construction is ensured, damage to the ecological environment is reduced, meanwhile, the filtrate and muck generated by filter pressing and dehydration of the slurry can be recycled, the material cost is reduced, and the method has wide application prospect in the field of treatment of waste slurry generated in urban underground engineering construction.
Drawings
Fig. 1 is a schematic structural view of the present invention;
fig. 2 is a schematic structural view of the middle-level and third-level sedimentation tank of the present invention.
In the figure: the system comprises a waste slurry tank 1, a slurry pump 2, a medicament pump 3, a fluid mixer 4, a belt filter press 5, a three-stage sedimentation tank 6, a first-stage sedimentation tank 61, a second-stage sedimentation tank 62, a third-stage sedimentation tank 63, a slurry mixer 7, a medicament stirring barrel 8, a medicament valve 9, a medicament mixer 10, a slurry discharge port 11, a control flow valve 12, an overflow hole 13 and solid residues 14.
Detailed Description
In order to make the technical means, the creation features, the achievement purposes and the functions of the present invention easy to understand and understand, the present invention is further explained by combining the following specific drawings.
As shown in fig. 1 and 2, a waste slurry dewatering device comprises a waste slurry tank 1, a slurry pump 2, a chemical adding device, a chemical pump 3, a fluid mixer 4, a belt filter press 5 and a three-stage sedimentation tank 6;
a slurry stirrer 7 is arranged in the waste slurry pool 1, and the waste slurry pool 1 is connected with the waste slurry feeding end of the fluid mixer 5 through a slurry pump 2;
the medicament adding device is composed of at least two medicament stirring barrels 8 which are parallel to each other and medicament valves 9 with corresponding quantity, slurry flocculating agents are added into the medicament stirring barrels 8, a medicament stirring machine 10 is arranged in each medicament stirring barrel 8, each medicament stirring barrel 8 is connected with the feed end of the medicament pump 3 through the corresponding medicament valve 9, and the discharge end of the medicament pump 3 is connected with the medicament feed end of the fluid mixer 4;
the discharge end of the fluid mixer 4 is connected with the feed end of the belt filter press 5, the solid slag port of the belt filter press 5 discharges solid slag 14, and the water outlet of the belt filter press 5 is communicated with the third-stage sedimentation tank 6.
The waste pulp tank 1 is formed by reforming a container made of a steel plate material. The bottom of the waste pulp tank 1 is provided with a pulp outlet 11.
A control flow valve 12 is arranged on a communication pipeline between the fluid mixer 4 and the belt filter press 5.
The medicament valve 9 is an electrically controlled valve.
The slurry flocculant in the agent stirring barrel 8 is polyacrylamide polymer.
The tertiary sedimentation tank 6 comprises first order sedimentation tank 61, second level sedimentation tank 62, the tertiary sedimentation tank 63 of arranging in order, all communicates through overflow hole 13 between first order sedimentation tank 61 and the second level sedimentation tank 62, between second level sedimentation tank 62 and the tertiary sedimentation tank 63, and overflow hole 13 is established on the upper portion of tertiary sedimentation tank 6, and the supernatant flows into next level from overflow hole 13.
The slurry pump 2, the medicament pump 3, the fluid mixer 4 and the belt filter press 5 are all commercially available products, wherein the commercially available fluid mixer 4 generally comprises a tank body and an internal spiral stirring device (the spiral stirring device comprises two structures of static stirring and dynamic stirring), and the medicament and the waste slurry enter the fluid mixer 4 from two independent feeding ends and are fully stirred by the spiral stirring device to output mixed fluid; the belt filter press 5 adopts a belt sludge dehydrator of environmental protection machinery limited of green feng, guangzhou city, and can separate solid slag and liquid, and the belt filter press 5 has a double-layer 9-meter-long gravity concentration section, and can be used in parallel with a plurality of belt filter presses 5, thereby improving the treatment efficiency of on-site waste slurry.
A waste slurry dehydration process comprises the following steps:
(1) the waste slurry is uniformly stirred, and the waste slurry in the waste slurry pool 1 is uniformly stirred by a slurry stirrer 7;
(2) stirring and curing the medicaments, namely adding a slurry flocculant into the medicament stirring barrels 8 by using at least two parallel medicament stirring barrels 8 and medicament valves 9 with corresponding quantity, fully stirring and curing the mixture by using a medicament stirrer 10, wherein each medicament stirring barrel 8 is connected with the feed end of a medicament pump 3 through the corresponding medicament valve 9, alternately opening the medicament valve 9 corresponding to one medicament stirring barrel 8, reserving medicament stirring and curing time for the other medicament stirring barrel 8, the stirring and curing time is generally 0.5-1h, and outputting the cured medicaments by using the medicament pump 3;
(3) waste mud and a medicament are mixed, the waste mud in the waste mud pool 1 is pumped by a mud pump 2 and sent into a fluid mixer 4, a fully cured mud flocculant in a medicament stirring barrel 8 is pumped by a medicament pump 3 and sent into the fluid mixer 4, and the waste mud and the medicament are fully mixed by a stirring device in the fluid mixer 4;
(4) flocculating and dewatering the waste slurry, allowing the mixed fluid in the fluid mixer 4 to preliminarily flocculate and then flow into a belt filter press 5 for dewatering, discharging solid slag 14 from a solid slag port, and introducing the press filtrate into a three-stage sedimentation tank;
(5) the filter pressing water is precipitated and purified, the third-level sedimentation tank 6 is composed of a first-level sedimentation tank 61, a second-level sedimentation tank 62 and a third-level sedimentation tank 63 which are sequentially arranged, the third-level sedimentation tank 6 is used for carrying out third-level sedimentation on the filter pressing water, and supernatant of the third-level sedimentation tank 63 is clear water after the third-level sedimentation and is discharged from a water outlet of the third-level sedimentation tank 6.
The working principle is as follows: the slurry flocculant and the waste slurry are mixed by adopting a fluid mixer 4, flocculation reaction can be generated, solid and liquid generated by the flocculation reaction are separated by a belt filter press 5, filter pressing liquid is precipitated by a three-stage sedimentation tank 6, purified clear water is finally obtained, and the waste slurry is more fully treated by combining chemical flocculation and mechanical dehydration; arranging at least two medicament mixing barrels 8, alternately opening a medicament valve 9 corresponding to one medicament mixing barrel 8, and reserving medicament mixing and curing time for the other medicament mixing barrel 8, so that the waste slurry treatment work is more efficient; the waste slurry is treated by adopting a flocculation-dehydration mode, the high-molecular polyacrylamide is used as a slurry flocculant, filtrate and dregs generated after filter pressing and dehydration are all harmless substances, the outward transportation of the waste slurry is obviously reduced, the normal operation of field construction is ensured, the damage to the ecological environment is reduced, simultaneously the filtrate and dregs generated by filter pressing and dehydration of the slurry can be recycled, the effluent of the tertiary sedimentation tank 6 can be reused for preparing the flocculant and supplementing water for pile foundation construction, the material cost is reduced, and the method has wide application prospect in the field of treatment of waste slurry generated in urban underground engineering construction.
The basic principles and the main features of the invention and the advantages of the invention have been shown and described above. It should be understood by those skilled in the art that the present invention is not limited to the above embodiments, and that various changes and modifications may be made without departing from the spirit and scope of the invention, and such changes and modifications fall within the scope of the invention as claimed. The scope of the invention is defined by the appended claims and equivalents thereof.

Claims (6)

1. The waste slurry dewatering equipment is characterized by comprising a waste slurry pool, a slurry pump, a reagent adding device, a reagent pump, a fluid mixer, a belt filter press and a three-stage sedimentation tank;
a slurry stirrer is arranged in the waste slurry tank, and the waste slurry tank is connected with a waste slurry feeding end of the fluid mixer through a slurry pump;
the device comprises a fluid mixer, a medicament adding device, a slurry flocculating agent, a plurality of medicament stirring barrels, a plurality of medicament valves and a plurality of medicament mixing tanks, wherein the medicament adding device comprises at least two parallel medicament stirring barrels and a corresponding number of medicament valves;
the discharge end of the fluid mixer is connected with the feed end of the belt filter press, solid slag is discharged from a solid slag port of the belt filter press, and a water outlet of the belt filter press is communicated with the three-stage sedimentation tank.
2. The apparatus for dewatering waste sludge according to claim 1, wherein the bottom of the waste sludge tank is provided with a sludge discharge port.
3. The apparatus for dewatering waste sludge according to claim 1, wherein the fluid mixer is connected to the belt filter press through a control flow valve.
4. The waste sludge dewatering apparatus of claim 1, wherein the chemical valve is an electrically controlled valve.
5. The waste sludge dewatering apparatus of claim 1, wherein the sludge flocculant in the chemical mixing tank is polyacrylamide.
6. The waste sludge dewatering equipment as claimed in claim 1, wherein the tertiary sedimentation tank is composed of a first stage sedimentation tank, a second stage sedimentation tank and a third stage sedimentation tank which are arranged in sequence, and the first stage sedimentation tank and the second stage sedimentation tank and the third stage sedimentation tank are communicated through overflow holes.
CN201921022719.XU 2019-07-01 2019-07-01 Waste slurry dewatering equipment Active CN210313988U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201921022719.XU CN210313988U (en) 2019-07-01 2019-07-01 Waste slurry dewatering equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201921022719.XU CN210313988U (en) 2019-07-01 2019-07-01 Waste slurry dewatering equipment

Publications (1)

Publication Number Publication Date
CN210313988U true CN210313988U (en) 2020-04-14

Family

ID=70148073

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201921022719.XU Active CN210313988U (en) 2019-07-01 2019-07-01 Waste slurry dewatering equipment

Country Status (1)

Country Link
CN (1) CN210313988U (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112125496A (en) * 2020-08-12 2020-12-25 浙江维美环保工程科技有限公司 Production process for dehydrating and curing sludge
CN112250281A (en) * 2020-09-24 2021-01-22 徐州格雷安环保设备有限公司 Building engineering mud is handled with adding medicine mixing arrangement

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112125496A (en) * 2020-08-12 2020-12-25 浙江维美环保工程科技有限公司 Production process for dehydrating and curing sludge
CN112250281A (en) * 2020-09-24 2021-01-22 徐州格雷安环保设备有限公司 Building engineering mud is handled with adding medicine mixing arrangement

Similar Documents

Publication Publication Date Title
CN112174491A (en) Waste slurry dewatering equipment and process
CN111268875B (en) Sludge treatment method and integrated system
CN101318735B (en) Sewage water denitrification processing method of artificial rapid infiltration system and application thereof
CN101935140B (en) Dehydration treatment method for tail water sludge of water-work and special apparatus thereof
CN105600993A (en) Treatment method and device for high-concentration suspended matter waste water
CN210313988U (en) Waste slurry dewatering equipment
CN203513348U (en) Sludge water treatment and reuse system for settling pond
CN115849662A (en) Flocculation combined plate-and-frame filter pressing enhanced high-water-content dredged sludge rapid dehydration method
CN210237322U (en) Mine water recycling treatment system
CN105293822B (en) Coal chemical industry sewage disposal fundamental technology
CN102432098B (en) PAFR-B (pulse anaerobic fluidized bed reactor) and organic waste water processing method
CN105540803A (en) Full-automatic sewage treatment device
CN206051803U (en) For the biochemical materialization coupled processing system of mineral loading of sewage disposal
CN100443425C (en) Rapid treatment process for middle-small sewage source, and integrated rapid sewage treatment station thereof
CN112374684A (en) Oil and gas field drilling waste liquid recycling treatment device and method
CN201770592U (en) Device special for tail water sludge dewatering treatment of water plant
CN103304053B (en) Treatment system for converting mine waste-rock dredging drainage water into production water
CN102557214A (en) Method for treating high-concentration tailings wastewater
CN207142894U (en) System for coal mine water process
CN201151690Y (en) Apparatus for treating waste water using solid micro-electrolyzing filler
CN212406634U (en) Movable treatment system for marine drilling waste
CN211330688U (en) Harmless and recycling treatment system for electrolytic manganese slag
CN208949042U (en) A kind of shale gas waste water treatment system equipment for separating liquid from solid
CN210710932U (en) Reinforced internal and external double-circulation anaerobic reactor
CN106316068A (en) Two-stage magnetic separation apparatus for loading magnetic precipitation sludge disposal

Legal Events

Date Code Title Description
GR01 Patent grant
GR01 Patent grant
CB03 Change of inventor or designer information
CB03 Change of inventor or designer information

Inventor after: Yin Jun

Inventor after: Zhang Yunda

Inventor after: Jiang Jianbin

Inventor after: He Jian

Inventor after: Song Ganglian

Inventor after: Zhu Hongwen

Inventor after: Chen Dayong

Inventor after: Gu Chunjie

Inventor before: Zhang Yunda

Inventor before: Yin Jun

Inventor before: Jiang Jianbin

Inventor before: He Jian

Inventor before: Song Ganglian

Inventor before: Zhu Hongwen

Inventor before: Chen Dayong

Inventor before: Gu Chunjie