CN105000778A - Sludge reduction processing system - Google Patents

Sludge reduction processing system Download PDF

Info

Publication number
CN105000778A
CN105000778A CN201510400082.3A CN201510400082A CN105000778A CN 105000778 A CN105000778 A CN 105000778A CN 201510400082 A CN201510400082 A CN 201510400082A CN 105000778 A CN105000778 A CN 105000778A
Authority
CN
China
Prior art keywords
sludge
mud
conveying belt
tank body
stir shaft
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.)
Granted
Application number
CN201510400082.3A
Other languages
Chinese (zh)
Other versions
CN105000778B (en
Inventor
王科敏
吴金强
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.)
Yixing jinfulai environmental protection equipment Co.,Ltd.
Original Assignee
Jiangsu Nine Water Treatment Technology 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 Jiangsu Nine Water Treatment Technology Co Ltd filed Critical Jiangsu Nine Water Treatment Technology Co Ltd
Priority to CN201510400082.3A priority Critical patent/CN105000778B/en
Publication of CN105000778A publication Critical patent/CN105000778A/en
Application granted granted Critical
Publication of CN105000778B publication Critical patent/CN105000778B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Abstract

A sludge reduction processing system comprises a filter press, a sludge blender, a belt conveyor, and a drying machine. The filter press is arranged above the sludge blender. An outlet of the filter press is connected to an upper sludge-entering opening by arranging a sludge-collecting hopper. A bottom sludge-dumping opening of the sludge blender directly faces the belt conveyor below. A tail end of the belt conveyor is above a sludge-entering opening of the drying machine. Dehydration efficiency is greatly improved, a moisture content of dehydrated sludge is low to about 30%, and a device structure is simple, and industrialized application is facilitated.

Description

A kind of mud decrement treatment system
Technical field
The present invention relates to field of sludge treatment, particularly relate to device for dehydrating sladge waste.
Background technology
Along with the development in city and the continuous expansion of urban population, the quantity discharged of trade effluent and sanitary sewage is increasing, and in corresponding sewage treatment process, mud quantum of output also increases sharply.According to the firmly portion of building statistics, by by the end of March, 2014, national the planned city, county (not containing other organic town) is accumulative builds up sewage work 3622, sewage treatment capacity about 1.53 billion cubic meters/day, comparatively newly-increased about 430 ten thousand steres/day in the end of the year 2013.Activated sludge process is the most widely used biologic treating technique of current city domestic sewage process, a large amount of excess sludges can be produced in the process of Wastewater Treated by Activated Sludge Process sanitary sewage, in water ratio 80%, year mud total generation in the whole nation is more than 3,000 ten thousand tons, if do not carry out appropriate process to dispose, great harm will be caused to environment.The most frequently used process method of disposal of excess sludge is concentrated, anaerobic digestion, mechanical dehydration, mummification, compost, burning and landfill etc.Chinese patent 201220311040.4(application number) disclose a kind of residual sludge reduction pyrolysis installation, this device comprises pressure pump, heat exchanger and reactor, excess sludge is by pressure pump import access to plant, pressure pump outlet connects the import of the heat-absorbing chamber of heat exchanger, the outlet of the heat-absorbing chamber of heat exchanger connects the import of reactor, the outlet of reactor connects the import in heat exchanger heat release chamber, the mud after the outlet discharge minimizing pyrolysis in the heat release chamber of heat exchanger.This pyrolysis installation produces High Temperature High Pressure and requires high to reactor, and treating processes power consumption is higher.
Summary of the invention
The present invention is directed to the deficiencies in the prior art, provide a kind of dewatering efficiency high, after dehydration, water ratio can reach 30%, and structure is simple, a kind of mud decrement treatment system that cost of manufacture is low.
For realizing the object of the invention, provide following technical scheme: a kind of mud decrement treatment system, it is characterized in that comprising pressure filter, sludge stirring machine, rotary conveyor and drying machine, described pressure filter is arranged at above sludge stirring machine, pressure filter outlet connects sludge stirring machine upper end mud inlet by arranging sludge hopper, sludge agitation motor spindle mud discharging mouth is just to the rotary conveyor of below, rotary conveyor end is positioned at above drying machine mud inlet, described sludge stirring machine comprises tank body, tank body bottom is bucket, bucket end is provided with mud discharging mouth, tank body center is provided with stir shaft, stir shaft upper end connects drive-motor, stir shaft arranges the agitating vane that haves three layers, agitating vane is screw blade, stir shaft periphery is provided with central tube, center sleeve is on stir shaft, tank body is separated into inside and outside two chambers, central tube is evenly equipped with through hole, central tube inner tube wall is provided with some vertical raised lines around the center of circle, the most external diameter 100 ~ 150mm of raised line outer face distance agitating vane, described drying machine comprises casing, mud inlet is opened in top, casing side, mud inlet side is provided with blast inlet, the nearly bottom of casing is provided with mud mouth, the conveying belt of the 5 mutual levels in road is placed with from top to bottom successively in described casing, the end of the 2nd and the 4th conveying belt all exceeds the 1st, 3, the end of 5 conveying belt, the 3rd, 4, at least one shredder assembly is provided with between 5 conveying belt, described shredder assembly comprises the rotating shaft vertical with conveying belt, the drive-motor be connected with rotating shaft, and the broken blade in rotating shaft, described broken blade is cross, broken blade end is spination.
As preferably, pressure filter is belt filter press.
As preferably, raised line outer face offers saw-tooth grooves.
As preferably, downward-sloping 35 degree of through hole.
Beneficial effect of the present invention: the present invention substantially increases dewatering efficiency, after making sludge dewatering, water ratio is low to moderate about 30%, and device structure is simple, is convenient to commercial application.
Accompanying drawing explanation
Fig. 1 is native system structural representation.
Fig. 2 is sludge stirring machine structural representation in Fig. 1.
Fig. 3 is shredder assembly structural representation.
Embodiment
Embodiment 1: a kind of mud decrement treatment system, comprise pressure filter 1, sludge stirring machine 2, rotary conveyor 3 and drying machine 4, described pressure filter 1 is arranged at above sludge stirring machine 2, pressure filter 1 exports and connects sludge stirring machine 2 upper end mud inlet 2.1 by arranging sludge hopper 5, bottom sludge stirring machine 2, mud discharging mouth 2.2 is just to the rotary conveyor 3 of below, rotary conveyor 3 end is positioned at above drying machine 4 mud inlet 4.1, described sludge stirring machine 2 comprises tank body, tank body bottom is bucket, bucket end is provided with mud discharging mouth 2.2, tank body center is provided with stir shaft 2.3, stir shaft 2.3 upper end connects drive-motor 2.4, stir shaft 2.3 arranges the agitating vane 2.5 that haves three layers, agitating vane 2.5 is screw blade, stir shaft 2.3 periphery is provided with central tube 2.6, central tube 2.6 is placed on stir shaft 2.3, tank body is separated into inside and outside two chambers, central tube 2.6 is evenly equipped with through hole 2.6.1, central tube 2.6 inner tube wall is provided with some vertical raised line 2.6.2 around the center of circle, the most external diameter 100 ~ 150mm of raised line 2.6.2 outer face distance agitating vane 2.5, described drying machine 4 comprises casing, mud inlet 4.1 is opened in top, casing side, mud inlet side is provided with blast inlet 4.2, the nearly bottom of casing is provided with mud mouth 4.3, the conveying belt 4.4 of the 5 mutual levels in road is placed with from top to bottom successively in described casing, the end of the 2nd and the 4th conveying belt 4.4 all exceeds the 1st, 3, the end of 5 conveying belt 4.4, the 3rd, 4, four shredder assemblys 6 are provided with between 5 conveying belt 4.4, described shredder assembly 6 comprises the rotating shaft 6.1 vertical with conveying belt, the drive-motor be connected with rotating shaft 6.1, and the broken blade 6.2 in rotating shaft 6.1, described broken blade 6.2 is cross, broken blade 6.2 end is spination.Pressure filter 1 is belt filter press.Raised line 2.6.2 outer face offers saw-tooth grooves.Downward-sloping 35 degree of through hole 2.6.1.
Mud 1000Kg(water ratio about 80% after mechanical dehydration) enter sludge stirring machine 2, churning time 5-30min, add solidifying agent 5-30%, power of motor: 3-5.5KW, rotating speed: 5-30rpm, temperature: 0-50 degree, mud after stirring falls rotary conveyor 3(1.5KW) be transported to drying machine 4(and first enter the first layer conveying belt 4.4, enter the second layer successively, third layer, 4th layer, layer 5 conveying belt 4.4, wind is sent in drying machine 4, simultaneously at the 4th layer, layer 5 conveying belt 4.4 arranges shredder assembly 6, mud is helped to reduce particle diameter, dehydrated sludge (water ratio about 30%).

Claims (4)

1. a mud decrement treatment system, it is characterized in that comprising pressure filter, sludge stirring machine, rotary conveyor and drying machine, described pressure filter is arranged at above sludge stirring machine, pressure filter outlet connects sludge stirring machine upper end mud inlet by arranging sludge hopper, sludge agitation motor spindle mud discharging mouth is just to the rotary conveyor of below, rotary conveyor end is positioned at above drying machine mud inlet, described sludge stirring machine comprises tank body, tank body bottom is bucket, bucket end is provided with mud discharging mouth, tank body center is provided with stir shaft, stir shaft upper end connects drive-motor, stir shaft arranges the agitating vane that haves three layers, agitating vane is screw blade, stir shaft periphery is provided with central tube, center sleeve is on stir shaft, tank body is separated into inside and outside two chambers, central tube is evenly equipped with through hole, central tube inner tube wall is provided with some vertical raised lines around the center of circle, the most external diameter 100 ~ 150mm of raised line outer face distance agitating vane, described drying machine comprises casing, mud inlet is opened in top, casing side, mud inlet side is provided with blast inlet, the nearly bottom of casing is provided with mud mouth, the conveying belt of the 5 mutual levels in road is placed with from top to bottom successively in described casing, the end of the 2nd and the 4th conveying belt all exceeds the 1st, 3, the end of 5 conveying belt, the 3rd, 4, at least one shredder assembly is provided with between 5 conveying belt, described shredder assembly comprises the rotating shaft vertical with conveying belt, the drive-motor be connected with rotating shaft, and the broken blade in rotating shaft, described broken blade is cross, broken blade end is spination.
2. a kind of mud decrement treatment system according to claim 1, is characterized in that pressure filter is belt filter press.
3. a kind of mud decrement treatment system according to claim 1, is characterized in that raised line outer face offers saw-tooth grooves.
4. a kind of mud decrement treatment system according to claim 1, is characterized in that downward-sloping 35 degree of through hole.
CN201510400082.3A 2015-07-10 2015-07-10 A kind of mud decrement processing system Active CN105000778B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201510400082.3A CN105000778B (en) 2015-07-10 2015-07-10 A kind of mud decrement processing system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201510400082.3A CN105000778B (en) 2015-07-10 2015-07-10 A kind of mud decrement processing system

Publications (2)

Publication Number Publication Date
CN105000778A true CN105000778A (en) 2015-10-28
CN105000778B CN105000778B (en) 2017-05-31

Family

ID=54373699

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201510400082.3A Active CN105000778B (en) 2015-07-10 2015-07-10 A kind of mud decrement processing system

Country Status (1)

Country Link
CN (1) CN105000778B (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105645731A (en) * 2016-01-19 2016-06-08 杭州国泰环保科技股份有限公司 Secondary concentration kettle for concentrating sludge and sludge treatment method thereof
CN105948451A (en) * 2016-06-27 2016-09-21 江苏巨博智能装备科技有限公司 Low-temperature energy-saving sludge treatment system
CN111018294A (en) * 2019-12-11 2020-04-17 苏州向达环境净化科技有限公司 Circulating sludge drying system based on TSP host machine crushing treatment

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE202007019055U1 (en) * 2007-11-06 2010-05-27 Spaleck Oberflächentechnik GmbH & Co. KG Drying plant for drying a solid fraction from the solid-liquid separation of a dispersion containing biological material
CN102267792A (en) * 2011-07-18 2011-12-07 庄维健 Method for drying bagged wet solid wastes stored in silo
CN202390301U (en) * 2011-11-14 2012-08-22 靖江市中大环境工程有限公司 Mechanical sludge rapid dewatering system
CN202532844U (en) * 2012-03-16 2012-11-14 常州市宇通干燥设备有限公司 Filtering washing vacuum boiling dryer
CN204824568U (en) * 2015-07-10 2015-12-02 江苏玖盛水处理科技有限公司 Mud decrement processing system

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE202007019055U1 (en) * 2007-11-06 2010-05-27 Spaleck Oberflächentechnik GmbH & Co. KG Drying plant for drying a solid fraction from the solid-liquid separation of a dispersion containing biological material
CN102267792A (en) * 2011-07-18 2011-12-07 庄维健 Method for drying bagged wet solid wastes stored in silo
CN202390301U (en) * 2011-11-14 2012-08-22 靖江市中大环境工程有限公司 Mechanical sludge rapid dewatering system
CN202532844U (en) * 2012-03-16 2012-11-14 常州市宇通干燥设备有限公司 Filtering washing vacuum boiling dryer
CN204824568U (en) * 2015-07-10 2015-12-02 江苏玖盛水处理科技有限公司 Mud decrement processing system

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105645731A (en) * 2016-01-19 2016-06-08 杭州国泰环保科技股份有限公司 Secondary concentration kettle for concentrating sludge and sludge treatment method thereof
CN105645731B (en) * 2016-01-19 2018-09-07 杭州国泰环保科技股份有限公司 The secondary concentration kettle and its method for sludge treatment of thickened sludge
CN105948451A (en) * 2016-06-27 2016-09-21 江苏巨博智能装备科技有限公司 Low-temperature energy-saving sludge treatment system
CN111018294A (en) * 2019-12-11 2020-04-17 苏州向达环境净化科技有限公司 Circulating sludge drying system based on TSP host machine crushing treatment

Also Published As

Publication number Publication date
CN105000778B (en) 2017-05-31

Similar Documents

Publication Publication Date Title
CN101691273B (en) Method for integration of thickening, dehydration and aerobic air drying of sewage sludge
CN102079615B (en) Method for harmlessly recycling sludge
CN103253842A (en) Sludge deep dewatering treatment system and process
CN106430809A (en) Sewage and sludge treatment system and environmental-friendly recycling method thereof
CN110217957A (en) A kind of inactivated sludge degradation equipment of Hydrodynamic Cavitation
CN106434296B (en) Integrated dry-wet anaerobic digestion device
CN202705209U (en) Screw extrusion type sludge deep dewatering granulator
CN105000778A (en) Sludge reduction processing system
CN204824568U (en) Mud decrement processing system
CN102815847B (en) Method for producing organic fertilizer by processing biological sludge, and sludge dewatering granulator
CN101857347B (en) Sludge ultrasonic roller drier
CN102432147A (en) Wet-type anaerobic digestion degritting device for sludge
CN203187511U (en) Deep sludge dewatering treatment system
CN204607815U (en) A kind of Sludge Chemical Conditioning concentration systems
CN105439403A (en) Sludge high-frequency vibration disintegrating and concentration system
CN108178483B (en) Device for dehydrating sladge waste
CN203904178U (en) Rotary type sludge drying system
CN204550363U (en) Miniature City septic tank ight soil recycling sludge is dissolved station
CN204185360U (en) A kind of activated sludge dehydration treatment unit
CN104418481A (en) Mass-energy transformation treatment process for production wastewater
CN204022633U (en) A kind of residual sludge reduction treatment unit
CN107900088B (en) System and process for preparing feed additive from kitchen waste
CN204607819U (en) A kind of horizontal sludge disintegration spiral bead grinding machine
CN201031177Y (en) Anaerobic reactor for processing high solid slag organic wastewater
CN204607818U (en) A kind of vertical sludge broken wall ball mill

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant
CP03 Change of name, title or address
CP03 Change of name, title or address

Address after: 214200 West Development Zone, HeQiao Town, Yixing City, Wuxi City, Jiangsu Province

Patentee after: Yixing jinfulai environmental protection equipment Co.,Ltd.

Address before: 214215 industrial concentration zone, Xushe Town, Yixing City, Wuxi City, Jiangsu Province

Patentee before: JIANGSU NINE WATER TREATMENT TECHNOLOGY Co.,Ltd.