CN206927781U - A kind of differential sludge drier - Google Patents
A kind of differential sludge drier Download PDFInfo
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- CN206927781U CN206927781U CN201720806733.3U CN201720806733U CN206927781U CN 206927781 U CN206927781 U CN 206927781U CN 201720806733 U CN201720806733 U CN 201720806733U CN 206927781 U CN206927781 U CN 206927781U
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- hothouse
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- conveyer belt
- compressed air
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Abstract
It the utility model is related to a kind of differential sludge drier, including homogenizing device, hothouse, drawing mechanism, drying system and condenser system；The utility model is in original tradition directly in the Equipment Foundations of dewatered sludge, compression hot-air is sprayed into hothouse by diffuser with mode of jet based on pressure difference design, airflow volume expands rapidly on quick stripping conveyer belt moisture in sludge, simultaneously under sludge layer resistance and air-heater effect, hot-air below hothouse conveyer belt is changed into negative pressure by malleation rapidly, forms vacuum chamber, because hot-air saturation degree reduces, the boiling point of water reduces under negative pressure simultaneously, and sludge reclaimed water gets rapid evaporation；Front and rear air-flow realization is dried in system of the present utility model to recycle, whole system closure designs, without exhaust-gas treatment, eliminate the demand to deduster, washer or exhaust chimney, and associated exhaust discharge permit, can efficiently, energy-saving and environmental protection, the processing sludge of safety, simple to operate, maintenance is few.
Description
Technical field
Sludge treatment device field is the utility model is related to, specifically discloses a kind of differential sludge drier.
Background technology
Growth and expanding economy and the constantly improve of sewage network and sewage disposal degree with population, in sewage
Sludge yield is also constantly rising while treating capacity is growing.However, there is serious " weight in the construction of wastewater treatment in China factory
The light mud of water " phenomenon, cause a large amount of sludge to overstock and do not obtain reasonable benefit/risk disposal, directly contribute " secondary pollution ", " sludge is asked
Topic " turns into national focal point.
At present in sewage sludge harmlessness processing application, the processing mode accounting of desiccation still ranks first, wherein main processing
Technique concentrates on mechanical deep dehydration and energy desiccation.Mainly fully melted with what medicament was nursed one's health by impressed pressure in mechanical desiccation
The process that sludge is carried out to pressure dehydration is closed, the handling process is high in the presence of final discharging moisture content, and added amount of chemical is big, to processing
The increase-volume of sludge is obvious, increases freight, and operating environment is poor, complex operation, can not meet efficient automaticity；
Energy desiccation is divided into indirectly drying and direct desiccation, and for indirectly drying in the higher sludge of processing moisture content, energy consumption cost is expensive,
And for traditional direct desiccation, it is maximum the characteristics of be that desiccation high water content sludge efficiency is higher, but simultaneously bring
Problem is that the discharge capacity of flue gas is very big, and processing cost is sufficiently expensive, or even risk of exceeding criterion be present.
Utility model content
In view of the shortcomings of the prior art, the technical problems to be solved in the utility model is that providing a kind of differential sludge does
Dry machine, realize efficient, energy-saving and environmental protection, the processing sludge of safety.
Designed for this utility model and use following scheme：
A kind of differential sludge drier, including homogenizing device, hothouse, drawing mechanism, drying system and condensed system
System；The homogenizing device, hothouse and drawing mechanism are sequentially communicated, and are laid with the conveyer belt inside three；It is described dry
Drying system includes heat exchanger, and the outlet of the heat exchanger is connected with heated compressed air pipeline, and the outlet of heat exchanger leads to
Cross air-heater and be connected with reflux cycle air duct；Length direction of the heated compressed air pipeline along conveyer belt is laid in dry
Above dry room, heated compressed air pipeline is evenly distributed on the heated compressed air pipe joint above hothouse by several
Connected with hothouse, be heated compressed air room above the conveyer belt in the hothouse, be vacuum chamber below conveyer belt, it is described
In heated compressed air room diffuser is laid with below each heated compressed air pipe joint；The condenser system is included by mistake
Filter component and condense the condensing unit of tube assembly composition, the inlet end of the condensing unit is connected by condensing air hose with vacuum chamber
Logical, the outlet side of condensing unit is connected with reflux cycle air duct.
Further, the conveyer belt is netted conveyer belt, and conveyer belt material is PPS plastics or stainless steel.
Further, the filter assemblies use stainless steel filter core.
The beneficial effects of the utility model are：
The utility model directly in the Equipment Foundations of dewatered sludge, will compress hot-air in original tradition based on pressure difference design
Being sprayed into by diffuser with mode of jet in hothouse, airflow volume expands rapidly on quick stripping conveyer belt moisture in sludge,
Simultaneously under sludge layer resistance and air-heater effect, the hot-air below hothouse conveyer belt is changed into negative pressure by malleation rapidly,
Vacuum chamber is formed, because hot-air saturation degree reduces, while the boiling point of water reduces under negative pressure, and sludge reclaimed water gets rapid steaming
Hair；Meanwhile front and rear air-flow realization is dried in system of the present utility model and is recycled, whole system closure designs, without useless
Gas disposal, eliminate the demand to deduster, washer or exhaust chimney, and associated exhaust discharge permit, can efficiently, section
Energy, environmental protection, the processing sludge of safety, simple to operate, maintenance is few.The sludge handled by the utility model, moisture content can drop
To 30%, compared to traditional drying equipment, operating cost can reduce by 45%.
Brief description of the drawings
Specific embodiment of the present utility model is described further below in conjunction with the accompanying drawings, wherein：
Fig. 1 is vertical view part section structural representation of the present utility model；
Fig. 2 is the cross-sectional view of hothouse；
Wherein：1- homogenizing devices；2- hothouses；3- condenses escape pipe；4- air-heaters；5- heat exchangers；6- heating compressions
Air duct；7- heated compressed air pipe joints；8- condenses air hose；9- condensing units；10- filter assemblies；11- condenser pipes
Component；12- reflux cycle air ducts；13- drawing mechanisms；14- condenses air conduit interface；15- sludge blankets；16- heating pressures
Contracting air chamber；17- conveyer belts；19- diffusers；20- vacuum chambers.
Embodiment
Shown a kind of differential sludge drier referring to Figures 1 and 2, including homogenizing device 1, hothouse 2, drawing mechanism
13rd, drying system and condenser system.
Homogenizing device 1 is arranged on the front end of hothouse 2, and drawing mechanism 13 is arranged on the end of hothouse 2, and three connects successively
It is logical, carry out the conveying of sludge by the conveyer belt 17 inside three, the conveyer belt 17 is netted conveyer belt, conveyer belt 17
Material is PPS plastics or stainless steel.
The drying system includes heat exchanger 5, and the outlet of the heat exchanger 5 is connected with heated compressed air pipeline 6,
The outlet of heat exchanger 5 is connected with reflux cycle air duct 12 by air-heater 4.The exchange thermal source of heat exchanger 5 can be city
Political affairs afterheat steam or natural gas, methanol burning produce.
Length direction of the heated compressed air pipeline 6 along conveyer belt 17 is laid in the top of hothouse 2, and heating compression is empty
The heated compressed air pipe joint 7 that feed channel 6 is evenly distributed on the top of hothouse 2 by several connects with hothouse 2.
With conveyer belt 17 it is boundary in the hothouse 2, the top of conveyer belt 17 is heated compressed air room 16, conveyer belt 17
Lower section is vacuum chamber 20, and diffusion is laid with below each heated compressed air pipe joint 7 in the heated compressed air room 16
Device 19.
The condenser system includes the condensing unit 9 being made up of filter assemblies 10 and condensation tube assembly 11, the condensation dress
9 inlet end is put to be connected with each condensation air conduit interface 14 on vacuum chamber 20 by condensing air hose 8, condensing unit 9
Outlet side is connected by condensing escape pipe 3 with reflux cycle air duct 12.
Wherein condensation tube assembly 11 uses water condensation, and moisture caused by the damp-heat air condensation that sludge distributes is received by receipts water tank
Collection, and periodically empty；Filter assemblies 10 use stainless steel filter core, can be cleaned and be changed at any time during drier.
Operation principle of the present utility model is as follows：
Sludge from sewage plant moisture content 80%, initially enters homogenizing device 1, and homogenizing device 1 is uniform by sludge to be dried
It is distributed on conveyer belt 17, conveyer belt 17 takes wet mud and at the uniform velocity enter hothouse 2 in the presence of drive transmission device, dry
Heated compressed air room 16 in dry room 2, the compression heating air sprayed using diffuser 19 are dried to sludge blanket 15, produced
Raw damp-heat air is entered in the vacuum chamber 20 of lower section by sludge blanket 15 and conveyer belt 17, and by condensing air conduit interface
14, entered via condensation air hose 8 in condensing unit 9；And dried sludge enters the row of drawing mechanism 13 through conveyer belt 17
Go out, that is, complete the drying process of sludge.Pass through the air quantity in instrument real-time monitoring system, air themperature and conveying in whole process
Tape running speed, and at drawing mechanism 13 detect sludge aridity.
In drying process, the air stream of sludge is dried in the presence of the compression of air-heater 4 and the heat supply of heat exchanger 5, via
The top heated compressed air pipeline 6 of hothouse 2 and heated compressed air pipe joint 7 sequentially enter heated compressed air room 16,
Heated compressed air is spurted into by the surface of sludge blanket 15 by diffuser 19, with the at the uniform velocity operating of conveyer belt 17, in sludge
Moisture is able to rapid evaporation, is blown into through sludge blanket 15 and conveyer belt 17 in the vacuum chamber 20 of lower section.
Damp-heat air from the condensation air conduit interface 14 of vacuum chamber 20 enter condensing unit 9 when, air-flow first will be through
Cross filter assemblies 10 and carry out dedusting cleaning, then waste heat air carries out cool-down dehumidification by condensing tube assembly 11, after dedusting dehumidifying
Air condensed escape pipe 3 and reflux cycle air duct 12 are again introduced into whole system successively in the presence of air-heater 4,
Realize that system airflow circulates.
The sludge handled by the utility model, moisture content can be down to 30%, compared to traditional drying equipment, run into
Originally 45% can be reduced.
It is described above, the only preferable embodiment of the utility model, but scope of protection of the utility model is not limited to
In this, any one skilled in the art is in the technical scope that the utility model discloses, the change that can readily occur in
Change or replace, should all cover within the scope of protection of the utility model.Therefore scope of protection of the utility model is with claim
The protection domain of book is defined.
Claims (3)
- A kind of 1. differential sludge drier, it is characterised in that：Including homogenizing device, hothouse, drawing mechanism, drying system with And condenser system；The homogenizing device, hothouse and drawing mechanism are sequentially communicated, and are laid with the conveying inside three Band；The drying system includes heat exchanger, and the outlet of the heat exchanger is connected with heated compressed air pipeline, heat exchanger Outlet reflux cycle air duct is connected with by air-heater；Length direction of the heated compressed air pipeline along conveyer belt It is laid in above hothouse, heated compressed air pipeline is evenly distributed on the heated compressed air above hothouse by several Pipe joint connects with hothouse, is heated compressed air room above the conveyer belt in the hothouse, is true below conveyer belt Empty room, diffuser is laid with below each heated compressed air pipe joint in the heated compressed air room；The condensed system System includes the condensing unit being made up of filter assemblies and condensation tube assembly, and the inlet end of the condensing unit is by condensing air hose With vacuum chamber, the outlet side of condensing unit is connected with reflux cycle air duct.
- A kind of 2. differential sludge drier according to claim 1, it is characterised in that：The conveyer belt is netted conveying Band, conveyer belt material are PPS plastics or stainless steel.
- A kind of 3. differential sludge drier according to claim 1, it is characterised in that：The filter assemblies are using stainless Steel filter core.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720806733.3U CN206927781U (en) | 2017-07-05 | 2017-07-05 | A kind of differential sludge drier |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720806733.3U CN206927781U (en) | 2017-07-05 | 2017-07-05 | A kind of differential sludge drier |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206927781U true CN206927781U (en) | 2018-01-26 |
Family
ID=61353666
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720806733.3U Active CN206927781U (en) | 2017-07-05 | 2017-07-05 | A kind of differential sludge drier |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206927781U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109231764A (en) * | 2018-10-30 | 2019-01-18 | 饶宾期 | Microwave hot air jet stream cooperates with desiccation apparatus |
| CN109455897A (en) * | 2018-10-30 | 2019-03-12 | 饶宾期 | Microwave hot air jet stream cooperates with drying method |
| CN113955915A (en) * | 2021-09-26 | 2022-01-21 | 江苏久发环境科技有限公司 | Sludge low-temperature drying system and drying method |
-
2017
- 2017-07-05 CN CN201720806733.3U patent/CN206927781U/en active Active
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109231764A (en) * | 2018-10-30 | 2019-01-18 | 饶宾期 | Microwave hot air jet stream cooperates with desiccation apparatus |
| CN109455897A (en) * | 2018-10-30 | 2019-03-12 | 饶宾期 | Microwave hot air jet stream cooperates with drying method |
| CN109231764B (en) * | 2018-10-30 | 2023-11-14 | 明阳(宁波)环保科技有限公司 | Microwave hot air jet flow cooperative drying device |
| CN113955915A (en) * | 2021-09-26 | 2022-01-21 | 江苏久发环境科技有限公司 | Sludge low-temperature drying system and drying method |
| CN113955915B (en) * | 2021-09-26 | 2023-09-26 | 江苏久发环境科技有限公司 | Sludge low-temperature drying system and drying method |
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