CN104291550A - Sludge concentration system of gravity concentration tank - Google Patents

Sludge concentration system of gravity concentration tank Download PDF

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Publication number
CN104291550A
CN104291550A CN201410567611.4A CN201410567611A CN104291550A CN 104291550 A CN104291550 A CN 104291550A CN 201410567611 A CN201410567611 A CN 201410567611A CN 104291550 A CN104291550 A CN 104291550A
Authority
CN
China
Prior art keywords
sludge
mud
tank
agitation tank
dynamic agitation
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.)
Pending
Application number
CN201410567611.4A
Other languages
Chinese (zh)
Inventor
顾红兵
庄乐鸣
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.)
WUXI GENERAL MACHINERY WORKS CO Ltd
Original Assignee
WUXI GENERAL MACHINERY WORKS 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 WUXI GENERAL MACHINERY WORKS CO Ltd filed Critical WUXI GENERAL MACHINERY WORKS CO Ltd
Priority to CN201410567611.4A priority Critical patent/CN104291550A/en
Publication of CN104291550A publication Critical patent/CN104291550A/en
Pending legal-status Critical Current

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Classifications

    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F11/00Treatment of sludge; Devices therefor
    • C02F11/12Treatment of sludge; Devices therefor by de-watering, drying or thickening
    • C02F11/14Treatment of sludge; Devices therefor by de-watering, drying or thickening with addition of chemical agents
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2303/00Specific treatment goals
    • C02F2303/06Sludge reduction, e.g. by lysis

Abstract

The invention relates to a sludge concentration system of a gravity concentration tank. The sludge concentration system comprises sludge lifting pumps and a concentrator, and further comprises flow rate meters, a dynamic stirring tank and a medicament adding device, wherein the dynamic stirring tank is provided with a plurality of sludge inlets which are independent to each other; the dynamic stirring tank is provided with a sludge outlet and a medicament inlet; one sludge lifting pump is connected on each sludge inlet of the dynamic stirring tank by virtue of a sludge inlet pipeline; one flow rate meter is arranged on the sludge inlet pipeline between each sludge lifting pump and the dynamic stirring tank; the sludge outlet of the dynamic stirring tank is connected to the inlet of the concentrator; and the outlet of the medicament adding device is connected to the medicament inlet of the dynamic stirring tank. According to the sludge concentration system of the gravity concentration tank disclosed by the invention, the sludge and the medicaments are stirred and coagulated in the dynamic stirring tank, so that the defects in the using process of the conventional system are overcome, and beneficial conditions are provided for follow-up treatment of the sludge at the same time; and meanwhile, the added medicaments are low in cost and wide in range of application.

Description

Gravity concentration tank sludge condensation system
Technical field
The present invention relates to a kind of sludge condensation system, the present invention especially relates to a kind of gravity concentration tank sludge condensation system.
Background technology
At present, gravity concentration cell system is mainly used in the concentrated further of mud, is that sewage work carries out one of Major Systems of mud-water separation, as Fig. 1.It is mainly made up of following machine: sludge lifting pump 1 and thickner 2 two portions; Sludge lifting pump 1 by mud by Cemented filling to thickner 2 import, after concentrated, mud waits for that next step process, and filtrate is then directly discharged and entered plant area's pipe network; Due to the certain physical characteristics of mud itself, more or less there is mud extraction water ratio high, the residence time is long, and sludge anaerobic releases the problems such as phosphorus.
Summary of the invention
The object of the invention is to overcome the deficiencies in the prior art, provide a kind of can improve lignin-sludge diversity, reduce mud extraction water ratio and sludge anaerobic can be prevented to release the gravity concentration tank sludge condensation system of phosphorus.
According to technical scheme provided by the invention, described gravity concentration tank sludge condensation system, it comprises sludge lifting pump and thickner, also comprises under meter, dynamic agitation tank and medicament addition device; Described dynamic agitation tank has several separate mud inlets, and dynamic agitation tank has a mud mouth, and dynamic agitation tank has a medicament entrance; Each mud inlet of dynamic agitation tank enters mud pipeline by mud and is connected with a sludge lifting pump, mud between every platform sludge lifting pump and dynamic agitation tank enters on mud pipeline to be provided with a under meter, the described mud mouth of dynamic agitation tank is connected with the entrance of thickner, and the outlet of medicament addition device is connected with the medicament entrance of dynamic agitation tank.
Described sludge lifting pump is that hydraulic fitting submersible sewage pump or dry type install impeller pump.
Driven type thickner centered by described thickner.
Described flow counts magnetic flow meter.
The present invention stirs coagulation by carrying out mud medicine in dynamic agitation tank, overcomes in legacy system use procedure all drawbacks existed, simultaneously for the subsequent disposal of mud provides favourable condition; Add medicament expense low simultaneously; Use range is wide.
Accompanying drawing explanation
Fig. 1 is the structural representation of prior art.
Fig. 2 is structural representation of the present invention.
Embodiment
Below in conjunction with specific embodiment, the invention will be further described.
This gravity concentration tank sludge condensation system, it comprises sludge lifting pump 1 and thickner 2, also comprises under meter 3, dynamic agitation tank 4 and medicament addition device 5; Described dynamic agitation tank 4 has several separate mud inlets, and dynamic agitation tank 4 has a mud mouth, and dynamic agitation tank 4 has a medicament entrance; Each mud inlet of dynamic agitation tank 4 enters mud pipeline by mud and is connected with a sludge lifting pump 1, mud between every platform sludge lifting pump 1 and dynamic agitation tank 4 enters on mud pipeline to be provided with a under meter 3, the mud mouth of described dynamic agitation tank 4 is connected with the entrance of thickner 2, and the outlet of medicament addition device 5 is connected with the medicament entrance of dynamic agitation tank 4.
Described sludge lifting pump 1 is that hydraulic fitting submersible sewage pump or dry type install impeller pump.
Driven type thickner centered by described thickner 2.
Described under meter 3 is magnetic flow meter.
Described dynamic agitation tank 4 is mud medicine mixing device, and the mud inlet that it is arranged is multiple, can connect different sorts mud simultaneously and mix simultaneously, arrange stirrer in tank; Mud inlet arranges flow deflector simultaneously, prevents the short stream of mud; In tank, dosing mouth is set simultaneously, realizes the mixing of mud medicine.
Described medicament addition device 5 is can three slot type chemicals dosing plant and dosing pumps of continuous production liquid.
During work, mud is delivered to dynamic agitation tank 4 by pipeline through under meter 3 by sludge lifting pump 1, meanwhile, in the medicine outlet access dynamic agitation tank 4 of medicament addition device 5, with mud carry out mud medicine stir flocculate twist, the mud flocculated enters in thickner 2 and concentrates, and waits for that next step processes after concentrated after mud discharging, and the filtrate of discharge is then directly discharged and entered plant area's pipe network.By the analog quantity interface adding pump that under meter 3 will enter in the analog signals input medicament addition device 5 of mud amount, thus by the flow that frequency transformer regulates dosing pump to export, finally reach the object of saving medicament.

Claims (4)

1. a gravity concentration tank sludge condensation system, it comprises sludge lifting pump (1) and thickner (2), it is characterized in that: also comprise under meter (3), dynamic agitation tank (4) and medicament addition device (5); Described dynamic agitation tank (4) has several separate mud inlets, and dynamic agitation tank (4) has a mud mouth, and dynamic agitation tank (4) has a medicament entrance; Each mud inlet of dynamic agitation tank (4) enters mud pipeline by mud and is connected with a sludge lifting pump (1), mud between every platform sludge lifting pump (1) and dynamic agitation tank (4) enters on mud pipeline to be provided with a under meter (3), the mud mouth of described dynamic agitation tank (4) is connected with the entrance of thickner (2), and the outlet of medicament addition device (5) is connected with the medicament entrance of dynamic agitation tank (4).
2. gravity concentration tank sludge condensation system as claimed in claim 1, is characterized in that: described sludge lifting pump (1) is hydraulic fitting submersible sewage pump or dry type installation impeller pump.
3. gravity concentration tank sludge condensation system as claimed in claim 1, is characterized in that: driven type thickner centered by described thickner (2).
4. gravity concentration tank sludge condensation system as claimed in claim 1, is characterized in that: described under meter (3) is magnetic flow meter.
CN201410567611.4A 2014-10-22 2014-10-22 Sludge concentration system of gravity concentration tank Pending CN104291550A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201410567611.4A CN104291550A (en) 2014-10-22 2014-10-22 Sludge concentration system of gravity concentration tank

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201410567611.4A CN104291550A (en) 2014-10-22 2014-10-22 Sludge concentration system of gravity concentration tank

Publications (1)

Publication Number Publication Date
CN104291550A true CN104291550A (en) 2015-01-21

Family

ID=52311543

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201410567611.4A Pending CN104291550A (en) 2014-10-22 2014-10-22 Sludge concentration system of gravity concentration tank

Country Status (1)

Country Link
CN (1) CN104291550A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106746480A (en) * 2016-12-28 2017-05-31 江苏道科环境科技有限公司 A kind of sludge dewatering conditioning system and method

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1774404A (en) * 2003-04-11 2006-05-17 洪尚宪 Sludge concentration system and process which have functions for automatically charging a coagulant and for automatically controlling the concentration of sludge
CN101234841A (en) * 2008-01-02 2008-08-06 广州普得环保设备有限公司 Sludge concentration dehydration method
CN201321420Y (en) * 2009-03-18 2009-10-07 丹东东方机电工程有限公司 Multifunctional integrated spiral sludge processing unit
CN101880078A (en) * 2010-02-03 2010-11-10 王鹤立 High-efficiency low-consumption complete equipment for coagulation clarification sludge concentration
CN203568962U (en) * 2013-11-12 2014-04-30 福建省源顺环保工程有限公司 Sludge concentration system
CN204198571U (en) * 2014-10-22 2015-03-11 无锡市通用机械厂有限公司 Gravity concentration tank sludge condensation system

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1774404A (en) * 2003-04-11 2006-05-17 洪尚宪 Sludge concentration system and process which have functions for automatically charging a coagulant and for automatically controlling the concentration of sludge
CN101234841A (en) * 2008-01-02 2008-08-06 广州普得环保设备有限公司 Sludge concentration dehydration method
CN201321420Y (en) * 2009-03-18 2009-10-07 丹东东方机电工程有限公司 Multifunctional integrated spiral sludge processing unit
CN101880078A (en) * 2010-02-03 2010-11-10 王鹤立 High-efficiency low-consumption complete equipment for coagulation clarification sludge concentration
CN203568962U (en) * 2013-11-12 2014-04-30 福建省源顺环保工程有限公司 Sludge concentration system
CN204198571U (en) * 2014-10-22 2015-03-11 无锡市通用机械厂有限公司 Gravity concentration tank sludge condensation system

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106746480A (en) * 2016-12-28 2017-05-31 江苏道科环境科技有限公司 A kind of sludge dewatering conditioning system and method

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PB01 Publication
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RJ01 Rejection of invention patent application after publication

Application publication date: 20150121

RJ01 Rejection of invention patent application after publication