CN203768202U - Sludge drying treatment system - Google Patents

Sludge drying treatment system Download PDF

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Publication number
CN203768202U
CN203768202U CN201420138484.1U CN201420138484U CN203768202U CN 203768202 U CN203768202 U CN 203768202U CN 201420138484 U CN201420138484 U CN 201420138484U CN 203768202 U CN203768202 U CN 203768202U
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CN
China
Prior art keywords
drying
sludge
treatment system
cooling unit
output terminal
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.)
Expired - Lifetime
Application number
CN201420138484.1U
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Chinese (zh)
Inventor
尹盛
冯秋兰
巩青松
黄志洋
王婷
卞德广
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.)
Jiangsu BOE Environmental Protection Technology Co Ltd
Original Assignee
Jiangsu BOE Environmental Protection Technology Co Ltd
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Filing date
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Priority to CN201420138484.1U priority Critical patent/CN203768202U/en
Application granted granted Critical
Publication of CN203768202U publication Critical patent/CN203768202U/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Abstract

The utility model discloses a sludge drying treatment system and belongs to the field of environment-friendly device. The sludge drying treatment system comprises a flocculation device and a stacked-spiral sludge dehydrater, wherein the output end of the flocculation device is connected with the input end of the stacked-spiral sludge dehydrater, the output end of the stacked-spiral sludge dehydrater is connected with a sludge drying device, wherein the sludge drying device comprises a drying unit and a cooling unit, the drying unit comprises layered conveyor mesh belts arranged in a drying box, circulating air ducts are arranged between the conveyor mesh belts, input ends of the circulating air ducts are connected to a heating box, a condenser section of a separation-type heat pipe heat exchanger and a circulating fan are arranged in the heating box, the output ends of the circulating air ducts are respectively communicated with air and the heating box, the output end located at the bottom of the drying box is communicated with the cooling unit, and the cooling unit comprises a plurality layers of inclined sieve plates arranged in the cooling box in interleaved manner. The sludge drying treatment system disclosed by the utility model has the advantages of simple structure, relatively low requirement on both tightness and machining accuracy, reduced application cost and high drying efficiency and can be used for drying sludge.

Description

A kind of drying sludge treatment system
Technical field
The utility model relates to a kind of sludge treatment device, particularly a kind of sludge treatment device.
Background technology
" mud " this concept refers to a kind of viscous mixt consisting of water and the solid matter that is derived from sewage being dispersed in water.The sludge problem that we face, refer to be exactly all kinds of sewage works thickened sludge after pretreatment, the mud of water ratio between 75-90%.High-moisture percentage be mud as a kind of topmost feature of solid waste pollutent, and just because of the existence of large quantity of moisture, being mud has the hazardness in eye more than other forms of solid waste thing.The high-moisture percentage of mud is the topmost technical barrier running in whole sludge stabilizing, minimizing, harmlessness disposing.
In order to carry out economy and the processing of environmental protection to this mud, must successively by dehydration and drying treatment, its water content be decreased to a clear and definite value.After processed, water content generally can be reduced to the degree that makes mud be semi-solid state or shot shape, and the target of drying sludge is still to residue in the moisture in mud after removing dehydration as far as possible completely.Dried mud can offer energy recovery equipment generating and/heating, or be separately used as him, for example, as fertilizer.
The integrated deep dehydration desiccation machine of a kind of mud is disclosed in prior art, its publication number is: CN203128381, it comprises flocculation plant, folded spiral shell formula sludge dewatering equipment, the output terminal of described flocculation plant is connected with folded spiral shell formula sludge dewatering equipment input terminus, and the output terminal of folded spiral shell formula sludge dewatering equipment is connected with gear type sludge dryer.Its weak point is, gear type sludge dryer heats mud by screw shaft, and this device drying efficiency is lower, and this structure is higher to sealing requirements, and this has just strengthened maintaining and has obtained cost.
Separate type heat pipe exchanger is a kind ofly to utilize the vaporization of working medium to realize heat transmission, separate type heat pipe exchanger is that the evaporator section of heat pipe and condensation segment is arranged apart, be not in an integral body together, with vapor uptake, be connected with condensate descending, can be applicable to cold and hot fluid apart from each other or cold and hot fluid and absolutely not allow the occasion of mixing.
Utility model content
The purpose of this utility model is to provide a kind of drying sludge treatment system, improves drying efficiency, reduces working accuracy, reduces maintenance cost.
The purpose of this utility model is achieved in that a kind of drying sludge treatment system, comprise flocculation plant, folded spiral shell formula sludge dewatering equipment, the output terminal of described flocculation plant is connected with folded spiral shell formula sludge dewatering equipment input terminus, the output terminal of described folded spiral shell formula sludge dewatering equipment is connected with sludge drying device, described sludge drying device comprises drying unit and cooling unit, described drying unit comprises the laminar foraminous conveyer being arranged in loft drier, between foraminous conveyer, be provided with circulation air path, the input terminus of circulation air path is connected with heating container, in described heating container, be provided with separate type heat pipe exchanger condensation segment and recirculation blower, the output terminal of circulation air path is communicated with respectively air and heating container, described loft drier bottom output terminal is connected with cooling unit, cooling unit comprises the multi-layer intercrossed slanted screen plate being arranged in cooling tank.
The utility model when work, mud through the folded spiral shell of former process out after, by transfer roller, after even distributor refining, send into drying unit, mud is advanced with foraminous conveyer; Cold wind enters centrifugal blower from heating container wind-supplying mouth, after separate type heat pipe exchanger heating, enters loft drier, and hot blast penetrates sludge blanket in loft drier, fully contact with wet mud, carry out caloic exchange, the moisture in mud is evaporated to water vapor, takes away together with warm air; Dried mud is sent into cooling unit, and mud slowly moves down in case, thereby makes mud obtain sufficient cooling drying.Compared with prior art, the beneficial effects of the utility model are: the utility model is simple in structure, drying process is carried out heat exchange realization by the hot blast of sending with separate type heat pipe exchanger, lower to sealing requirements, thereby requirement on machining accuracy is lower, this has just reduced use cost, simultaneously, by hot blast and mud, directly carry out heat exchange, its drying efficiency is high.The utility model can be used in being dried of mud.
In order further to improve drying efficiency, described foraminous conveyer comprises the transmission net that is arranged on conveying belt below, is provided with some flitch of taking off on described conveying belt.
Accompanying drawing explanation
Fig. 1 is the utility model structural representation.
Fig. 2 is drying unit structural representation in the utility model.
Fig. 3 is the utility model cooling unit structural representation.
Fig. 4 be in the utility model in loft drier sludge stream to schematic diagram.
Fig. 5 be in the utility model in loft drier hot air flow to schematic diagram.
Wherein, 1 flocculation plant, 2 folded spiral shell formula sludge dewatering equipments, 3 drying units, 3a recirculation blower, 3b heating container, 3c loft drier, 3d takes off flitch, 3e conveying belt, 3f transmission net, 3g circulation air path, 4 cooling units, 4a cooling tank, 4b slanted screen plate.
Embodiment
A kind of drying sludge treatment system as Figure 1-5, comprise flocculation plant 1, folded spiral shell formula sludge dewatering equipment 2, the output terminal of flocculation plant 1 is connected with folded spiral shell formula sludge dewatering equipment 2 input terminuss, the output terminal of folded spiral shell formula sludge dewatering equipment 2 is connected with sludge drying device, sludge drying device comprises drying unit 3 and cooling unit 4, drying unit 3 comprises the laminar foraminous conveyer being arranged in loft drier 3c, between foraminous conveyer, be provided with circulation air path 3g, the input terminus of circulation air path 3g is connected with heating container 3b, in heating container 3b, be provided with separate type heat pipe exchanger condensation segment and recirculation blower 3a, the output terminal of circulation air path 3g is communicated with respectively air and heating container 3b, loft drier 3c bottom output terminal is connected with cooling unit 4, cooling unit 4 comprises the multi-layer intercrossed slanted screen plate 4b being arranged in cooling tank 4a, foraminous conveyer comprises the transmission net 3f that is arranged on conveying belt 3e below, on conveying belt 3e, be provided with some flitch 3d that take off.
The utility model when work, mud through the folded spiral shell of former process out after, by transfer roller, after even distributor refining, send into drying unit 3, mud is advanced with foraminous conveyer; Cold wind enters centrifugal blower from heating container 3b wind-supplying mouth, after the heating of separate type heat pipe exchanger condensation segment, enters loft drier 3c, and hot blast penetrates sludge blanket in loft drier 3c, fully contact with wet mud, carry out caloic exchange, the moisture in mud is evaporated to water vapor, takes away together with warm air; Dried mud is sent into cooling unit 4, and mud slowly moves down in case, makes mud obtain sufficient cooling drying.
The utility model is not limited to above-described embodiment; on the basis of the disclosed technical scheme of the utility model; those skilled in the art is according to disclosed technology contents; do not need performing creative labour just can make some replacements and distortion to some technical characterictics wherein, these replacements and distortion are all in protection domain of the present utility model.

Claims (2)

1. a drying sludge treatment system, comprise flocculation plant, folded spiral shell formula sludge dewatering equipment, the output terminal of described flocculation plant is connected with folded spiral shell formula sludge dewatering equipment input terminus, it is characterized in that, the output terminal of described folded spiral shell formula sludge dewatering equipment is connected with sludge drying device, described sludge drying device comprises drying unit and cooling unit, described drying unit comprises the laminar foraminous conveyer being arranged in loft drier, between foraminous conveyer, be provided with circulation air path, the input terminus of circulation air path is connected with heating container, in described heating container, be provided with separate type heat pipe exchanger condensation segment and recirculation blower, the output terminal of circulation air path is communicated with respectively air and well heater, described loft drier bottom output terminal is connected with cooling unit, cooling unit comprises the multi-layer intercrossed slanted screen plate being arranged in cooling tank.
2. a kind of drying sludge treatment system according to claim 1, is characterized in that, described foraminous conveyer comprises the transmission net that is arranged on conveying belt below, is provided with some flitch of taking off on described conveying belt.
CN201420138484.1U 2014-03-26 2014-03-26 Sludge drying treatment system Expired - Lifetime CN203768202U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201420138484.1U CN203768202U (en) 2014-03-26 2014-03-26 Sludge drying treatment system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201420138484.1U CN203768202U (en) 2014-03-26 2014-03-26 Sludge drying treatment system

Publications (1)

Publication Number Publication Date
CN203768202U true CN203768202U (en) 2014-08-13

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Family Applications (1)

Application Number Title Priority Date Filing Date
CN201420138484.1U Expired - Lifetime CN203768202U (en) 2014-03-26 2014-03-26 Sludge drying treatment system

Country Status (1)

Country Link
CN (1) CN203768202U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106242237A (en) * 2016-10-20 2016-12-21 湖南野森环保科技有限责任公司 A kind of dual sludge dewatering environmental protection equipment with drying function

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106242237A (en) * 2016-10-20 2016-12-21 湖南野森环保科技有限责任公司 A kind of dual sludge dewatering environmental protection equipment with drying function

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CX01 Expiry of patent term

Granted publication date: 20140813

CX01 Expiry of patent term