CN206051826U - Belt type sludge drying baker - Google Patents

Belt type sludge drying baker Download PDF

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Publication number
CN206051826U
CN206051826U CN201621051837.XU CN201621051837U CN206051826U CN 206051826 U CN206051826 U CN 206051826U CN 201621051837 U CN201621051837 U CN 201621051837U CN 206051826 U CN206051826 U CN 206051826U
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CN
China
Prior art keywords
foraminous conveyer
sludge
drying
upper strata
thermal
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 - Fee Related
Application number
CN201621051837.XU
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Chinese (zh)
Inventor
陈谦
周卫华
王小东
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.)
Jiaxing wattek Environmental Protection Technology Co., Ltd
Original Assignee
Shanghai Dongcheng Environmental Protection 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
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Priority to CN201621051837.XU priority Critical patent/CN206051826U/en
Application granted granted Critical
Publication of CN206051826U publication Critical patent/CN206051826U/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

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  • Treatment Of Sludge (AREA)

Abstract

The utility model discloses a kind of belt type sludge drying baker, it is related to sludge drying technique field.It includes sludge forming machine, upper strata foraminous conveyer, lower floor's foraminous conveyer, cyclic drying blower fan and thermal-insulating body, the top of thermal-insulating body is provided with pair roller type sludge forming machine, upper strata foraminous conveyer, lower floor's foraminous conveyer, cyclic drying blower fan are installed inside thermal-insulating body, upper strata foraminous conveyer is arranged on the lower section of sludge forming machine, lower floor's foraminous conveyer is arranged on the lower section of upper strata foraminous conveyer, in the fixed plate bottom of lower floor's foraminous conveyer sidepiece, thermal-insulating body has been internally formed sealing and circulating drying space to cyclic drying assembling.This utility model mesh energy consumption is low, and non-secondary pollution, drying temperature are low, safe, effectively improves cold drying air-flow dehumidification ability, and high degree of automation is practical, it is easy to promote the use of.

Description

Belt type sludge drying baker
Technical field
The utility model relates to sludge drying technique field, and in particular to belt type sludge drying baker.
Background technology
Sludge drying is burned after mummification is administered to from after mummification from directly burning is applied directly to, mummification up to date After gasify, substantially affirmed mummification as the importance of a necessary pilot process.Its reason mainly has two:It is economical Property, decrement, or energy resource consumption decrement are disposed in either transport;Wholesomeness, agricultural essential condition.Final disposal mode is state The selection of feelings, landfill are undoubtedly worthless, and this is not only in that land values are expensive, main still from the energy and bio-energy resource From the aspect of, national requirements is reduced and limits the landfill of sludge.Most of industry sludge dewatering is only with mechanical extruding type sludge Dehydration, such as belt filter press, plate and frame type filter-press, folded spiral shell machine and centrifugal drier, its dehydrated sludge moisture content exist 70%-90% or so;Select to burn as the means of disposal, the sludge shortage of heat of itself is maintaining its heat demand.So Such sludge for follow-up storage, transport and burn for it is less economical, this causes current sludge treatment high cost Major reason, to enterprise's sludge be dried loss of weight, the requirement of volume reduction increasingly increases severely.
At present, domestic sludge drying process, technology are evolving, and the energy mode of employing is mainly direct-heating type and occupies It is many, i.e., sludge is heated to into more than 100 DEG C using forms such as steam, flue tail gas, electrical heating, makes the moisture content of sludge be changed into water steaming Gas is discharged;There is problems with the form drying unit:
(1) high energy consumption:Energy requirement is every liter of 620 kilocalorie of evaporation capacity subsistence level, at direct-heating type drying equipment It is 800-850 kilocalories that reason trade mark claims the thermal demand of its system.
(2) bring secondary pollution:Drying sludge simultaneously brings the tail gas of contaminative, and needing to process device again can be up to standard Discharge.
(3) drying temperature height brings drying safety problem:The thing that sludge may be evaporated in high temperature drying sludge air-flow The problems such as matter blast, toxicity, is difficult to avoid that.
In order to solve the above problems, a kind of new belt type sludge drying baker or necessary is designed.
Utility model content
For deficiency present on prior art, it is to provide a kind of belt type sludge drying baker that this utility model purpose is, Simple structure, reasonable in design, energy consumption is low, and non-secondary pollution, drying temperature are low, safe, effectively improves cold drying air-flow Dehumidification ability, high degree of automation are practical, it is easy to promote the use of.
To achieve these goals, this utility model is by the following technical solutions realizing:Belt type sludge drying baker, Including sludge forming machine, upper strata foraminous conveyer, lower floor's foraminous conveyer, cyclic drying blower fan and thermal-insulating body, thermal-insulating body it is upper Portion is provided with the pair roller type sludge forming machine that broken molding is carried out to the sludge for luming, and upper strata conveying is provided with inside thermal-insulating body Guipure, lower floor's foraminous conveyer, cyclic drying blower fan, upper strata foraminous conveyer are arranged on the lower section of sludge forming machine, lower floor's transmission net Band is arranged on the lower section of upper strata foraminous conveyer, and cyclic drying assembling is protected in the fixed plate bottom of lower floor's foraminous conveyer sidepiece Warm box house is formed with sealing and circulating drying space.
Preferably, described upper strata foraminous conveyer, lower floor's foraminous conveyer are using outside small opening formula rustless steel foraminous conveyer Polyester square hole net.
Preferably, described cyclic drying blower fan is using without scroll casing type centrifugal blower.
Preferably, described thermal-insulating body is quick distachable formula PU plate.
The beneficial effects of the utility model:High degree of automation, energy consumption are low, will not bring secondary pollution, energy-conserving and environment-protective, and Drying temperature is low, effectively prevent the safety problems such as material blast, toxicity, and safety is higher, effectively increases cold drying gas Stream dehumidification ability, with wide market application foreground.
Description of the drawings
With reference to the accompanying drawings and detailed description describing this utility model in detail;
Fig. 1 is structural representation of the present utility model;
Fig. 2 is the flow chart that this utility model is used for sludge loss of weight dehumidification.
Specific embodiment
Technological means, creation characteristic, reached purpose and effect to realize this utility model is easy to understand, below With reference to specific embodiment, this utility model is expanded on further.
With reference to Fig. 1-2, this specific embodiment is employed the following technical solutions:Belt type sludge drying baker, including sludge molding Machine 1, upper strata foraminous conveyer 2, lower floor's foraminous conveyer 3, cyclic drying blower fan 4 and thermal-insulating body 5, the top of thermal-insulating body 5 are installed There is pair roller type sludge forming machine 1, upper strata foraminous conveyer 2, lower floor's foraminous conveyer 3, cyclic drying wind are installed inside thermal-insulating body 5 Machine 4, upper strata foraminous conveyer 2 are arranged on the lower section of sludge forming machine 1, and lower floor's foraminous conveyer 3 is arranged under upper strata foraminous conveyer 2 Side, cyclic drying blower fan 4 are arranged on the fixed plate bottom of 3 sidepiece of lower floor's foraminous conveyer, and cyclic drying blower fan 4 is using without scroll casing type Centrifugal blower, has been internally formed sealing and circulating drying space in thermal-insulating body 5.
It should be noted that described upper strata foraminous conveyer 2, lower floor's foraminous conveyer 3 are conveyed using small opening formula rustless steel The outer polyester square hole net of guipure.
Additionally, described thermal-insulating body 5 is quick distachable formula PU plate.
This specific embodiment provides adiabatic sludge drying environment by thermal-insulating body 5, and cyclic drying blower fan 4 provides drying Circulation wind-power, carries out forced heat-exchanging to wet mud, and the sludge of caking is carried out broken molding by sludge forming machine 1 first, with Profit increases heat exchange area, there is provided sludge after molding is delivered to lower floor's foraminous conveyer 3 by heat exchange efficiency, upper strata foraminous conveyer 2, while With allow sludge and circulated air to exchange heat, lower floor's foraminous conveyer 3 is delivered to dewatered sludge discharge bucket by sludge is dried, at the same with allow sludge with Circulated air exchanges heat.
This specific embodiment aims at drying sludge and provides sealing and circulating drying space, and the sludge drying baker form can be even It is continuous, automatically sludge is dried, while for provide sludge at low temperature drying heat pump efficiency provide effectively supply, return air temperature it is poor and Psychrometric difference:(1) supply back, wind temperature difference requirement 8-10 DEG C;(2) moisture is gone according to more than 30kg/h;Which is used for sludge loss of weight dehumidification Flow process is shown in Fig. 2.
This specific embodiment it is a technical advantage that:(1) theoretical energy consumption is low:Using hot pump in low temp drying plant, due to In heat pump, refrigerating capacity and heating capacity are all used for sludge drying, therefore theoretical energy consumption compared to direct-heating type high energy consumption more than 50%.
(2) non-secondary pollution:Sludge moisture content is emitted eventually through the form of condensed water, and wind is by recycling, nothing Exogenous QI discharges secondary pollution problem.
(3) drying temperature is low, reduces safety problem:As drying temperature is less than 70 DEG C, the thing that sludge may be evaporated The problems such as matter blast, toxicity, is few, and the sludge suitability is wide, requires little, stable equipment operation, mobility to equipment material energy problem It is high.
(4) improve cold drying air-flow dehumidification ability:The belt type sludge drying baker is by designing sludge shaped device, cloth mud Device and tissue air-flow forced heat exchange measure, improve the heat exchange dehumidification ability of cold drying air-flow, lift sludge drying heat with this The efficiency of pump, it is ensured that the lifting of system overall operation efficiency.
(5) automatic capability is high:Sludge drying is effectively realized that continuous and automatic runs by the equipment design form, and sludge is done Change process avoids the input of manpower.
Ultimate principle of the present utility model and principal character and advantage of the present utility model has been shown and described above.One's own profession The technical staff of industry it should be appreciated that this utility model is not restricted to the described embodiments, described in above-described embodiment and description Simply illustrate principle of the present utility model, on the premise of without departing from this utility model spirit and scope, this utility model is also Various changes and modifications are had, these changes and improvements are both fallen within the range of claimed this utility model.This utility model Claimed scope is by appending claims and its equivalent thereof.

Claims (4)

1. belt type sludge drying baker, it is characterised in that including sludge forming machine (1), upper strata foraminous conveyer (2), lower floor's transmission net Band (3), cyclic drying blower fan (4) and thermal-insulating body (5), the top of thermal-insulating body (5) is provided with breaks to the sludge for luming It is broken into inside pair roller type sludge forming machine (1) of type, thermal-insulating body (5) and upper strata foraminous conveyer (2), lower floor's foraminous conveyer is installed (3), cyclic drying blower fan (4), upper strata foraminous conveyer (2) are arranged on the lower section of sludge forming machine (1), lower floor's foraminous conveyer (3) It is arranged on the lower section of upper strata foraminous conveyer (2), fixed plate of the cyclic drying blower fan (4) installed in lower floor's foraminous conveyer (3) sidepiece Bottom, thermal-insulating body (5) have been internally formed sealing and circulating drying space.
2. belt type sludge drying baker according to claim 1, it is characterised in that described upper strata foraminous conveyer (2), lower floor Foraminous conveyer (3) is using the outer polyester square hole net of small opening formula rustless steel foraminous conveyer.
3. belt type sludge drying baker according to claim 1, it is characterised in that described cyclic drying blower fan (4) is adopted Without scroll casing type centrifugal blower.
4. belt type sludge drying baker according to claim 1, it is characterised in that described thermal-insulating body (5) is detachable Formula PU plate.
CN201621051837.XU 2016-08-30 2016-08-30 Belt type sludge drying baker Expired - Fee Related CN206051826U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201621051837.XU CN206051826U (en) 2016-08-30 2016-08-30 Belt type sludge drying baker

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201621051837.XU CN206051826U (en) 2016-08-30 2016-08-30 Belt type sludge drying baker

Publications (1)

Publication Number Publication Date
CN206051826U true CN206051826U (en) 2017-03-29

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Family Applications (1)

Application Number Title Priority Date Filing Date
CN201621051837.XU Expired - Fee Related CN206051826U (en) 2016-08-30 2016-08-30 Belt type sludge drying baker

Country Status (1)

Country Link
CN (1) CN206051826U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107459247A (en) * 2017-09-18 2017-12-12 郑州大学 A kind of new sludge treatment equipment in construction site

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107459247A (en) * 2017-09-18 2017-12-12 郑州大学 A kind of new sludge treatment equipment in construction site
CN107459247B (en) * 2017-09-18 2023-12-15 中建四局华南建设有限公司 Sludge treatment device for construction site

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GR01 Patent grant
GR01 Patent grant
TR01 Transfer of patent right

Effective date of registration: 20200330

Address after: No. 1569, Xingping Second Road, Zhongdai street, Pinghu City, Jiaxing City, Zhejiang Province

Patentee after: Jiaxing wattek Environmental Protection Technology Co., Ltd

Address before: 200540, A310, building 3, 421-425 West Ching Road, Shanghai, Jinshan District

Patentee before: SHANGHAI DONGCHENG ENVIRONMENTAL PROTECTION TECHNOLOGY Co.,Ltd.

TR01 Transfer of patent right
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20170329

Termination date: 20200830

CF01 Termination of patent right due to non-payment of annual fee