CN208898735U - A kind of sludge compound thermal anhydration system - Google Patents
A kind of sludge compound thermal anhydration system Download PDFInfo
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- CN208898735U CN208898735U CN201821256608.0U CN201821256608U CN208898735U CN 208898735 U CN208898735 U CN 208898735U CN 201821256608 U CN201821256608 U CN 201821256608U CN 208898735 U CN208898735 U CN 208898735U
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Abstract
The utility model and a kind of sludge compound thermal anhydration system, desiccation greenhouse including top transparent, the desiccation greenhouse is provided with ventilating fan structure, turning machine for sludge is equipped in the desiccation greenhouse, it is characterized in that, be additionally provided in the desiccation greenhouse towards turning machine for sludge warm-air drier and be fixed on several pairs of ground fans of desiccation greenhouse top bay, the lower section of the turning machine for sludge is equipped with drying bed, floor heating pipe is equipped in the drying bed bottom, the floor heating pipe and warm-air drier are respectively communicated with the steam collection portion of the steam turbine of refuse-burning plant, the drying bed is additionally provided with aeration tank, the aeration tube that cross section is semicircle is fixed in the aeration tank, the plane side of the aeration tube is aeration face, the aeration is up and equipped with several solarization air caps, the aeration tube is connected to floor heating pipe；By the steam inlet amount for controlling solenoid valve control floor heating pipe and aeration tube.It is controllable to realize drying cycle, solves the problems, such as that small desiccation amount, low efficiency, at high cost, desiccation is slow-footed.
Description
Technical field
The utility model and sludge drying technique field more particularly to a kind of sludge compound thermal anhydration system.
Background technique
Existing sludge drying technique is as follows:
(1) solar energy desiccation: heating in such a way that the sun is radiable to wet stock, is thermal energy by material sorption enhanced, will
The process of moisture heating vaporization；Disadvantage and there are the problem of: influenced by area, sunshine-duration, radiations heat energy, weather, season
Larger desiccation speed is slow.
(2) rotary drum desiccation: indirect heating rotary drum sludge, dewatered sludge are delivered to the feed hopper of desiccation machine by spiral shell
Rotation conveyer is sent to desiccation machine, the quantitative conveying of auger conveyor variable ratio frequency changer control.Desiccation machine is made of rotary drum and fin screw rod,
For rotary drum by burning stove heating, rotary drum revolving speed is 1.5r min.Fin screw rod is conducted heat by circulating hot oil, o.5r revolving speed is
min.Rotary drum and fin screw rod in the same direction or reversely rotate, and sludge, which can continuously move forward, carries out desiccation, and the heating agent in fin screw rod can also
Think vapor or hot water.Rotary drum is controlled through exhausting, and internal is negative pressure, and steam and dust can not escape.Sludge through rotary drum and
Fin screw rod passage and heating gradually dried and wear into it is granular, rotary drum rear end low-temperature space by serpentine air back valve by
Dry mud screw conveyor is sent to storage warehouse.The steam that sludge evaporates is sent by system exhaust fan to condensation and washing absorption system
System.Disadvantage and there are the problem of: needing fossil fuel heats, stringent to arrangement place and process control needs, expends electricity
Greatly, maintenance is inconvenient,
(3) freeze desiccation: moisture is frozen into ice in material, and then material is placed in vacuum state, and ice is made directly to distil
Moisture is removed for aqueous vapor；Disadvantage and there are the problem of: inefficiency, vacuum system are complicated, and Operation and Maintenance is inconvenient.
(4) dielectric heating desiccation: dielectric heating desiccation is that the material of desiccation will be needed to be placed in high-frequency electric field, utilizes high frequency
Wet stock is heated in the alternation effect of electric field, and hygroscopic water vaporization, material is dried.Disadvantage and there are the problem of: electrisity consumption is big, efficiency
It is low, be not suitable for a large amount of desiccation of sludge.
(5) centrifugation, vacuum desiccation: being dehydrated sludge using vacuum or centrifugal force,
Disadvantage and there are the problem of: moisture cannot complete desiccation, power consumption is high, is not applied for a large amount of sludge dryings, efficiency
Lowly.
(6) it flashes desiccation: using steam contact heating sludge, improving the temperature of sludge, improve the evaporation rate of moisture.Problem
And disadvantage: inefficiency, drying time are long.
In consideration of it, being badly in need of a kind of sludge drying technique of comprehensive high-efficiency.
Summary of the invention
In order to solve the above-mentioned technical problem, the utility model provides a kind of sludge compound thermal anhydration system.
In order to achieve the above object, the utility model takes following technical scheme:
A kind of sludge compound thermal anhydration system, the desiccation greenhouse including top transparent, the desiccation greenhouse, which is provided with, changes wind
Mechanism, the desiccation greenhouse is interior to be equipped with turning machine for sludge, and the warm-air drier towards turning machine for sludge is additionally provided in the desiccation greenhouse
With several pairs of ground fans for being fixed on desiccation greenhouse top bay, the lower section of the turning machine for sludge is equipped with drying bed, described dry
To change and is equipped with floor heating pipe in bed bottom, the floor heating pipe and warm-air drier are respectively communicated with the steam collection portion of the steam turbine of refuse-burning plant,
The drying bed is additionally provided with aeration tank, and the aeration tube that cross section is semicircle is fixed in the aeration tank, and the aeration tube is put down
Face side is aeration face, and for the aeration up and equipped with several solarization air caps, the aeration tube is connected to floor heating pipe；The floor heating
Pipe, aeration tube are equipped with the solenoid valve of control air inflow, and the solenoid valve is electrically connected controller, by controlling solenoid valve control
The steam inlet amount of floor heating pipe and aeration tube.
Further, the drying bed is hollow double-layer structure, including contacting the top layer of sludge and the bottom on contact ground
Layer, top layer are the high metal of the coefficient of heat conduction, and bottom is the low rubber material of the coefficient of heat conduction, and the floor heating pipe is close to top layer and is set
It is placed between double-layer structure, the floor heating pipe is snakelike coil-shaped pipe.
Further, compatible planar metal is welded at the top of half slot of the aeration tube for the setting that is recessed on drying bed
Plate, the aeration face are planar metal plate；The pitch of holes that solarization air cap is arranged on the aeration face is 50~60mm, the aeration
The diameter in hole is 1~1.5mm.
Further, the ventilating fan structure includes that suction ventilator is provided in air passage, and desiccation greenhouse is provided with air hole, institute
State the incinerator of air passage connection refuse-burning plant.
Further, temperature and humidity sensing device is additionally provided in the desiccation greenhouse, the temperature and humidity sensing device is electrically connected
Controller is connect, controller detects the temperature and humidity in desiccation greenhouse by temperature and humidity sensing device.
Above-mentioned apparatus application method is arranged on desiccation greenhouse including being turned over throwing repeatedly in transparent desiccation greenhouse
Ventilating fan structure is aerated ventilation, and the exhaust steam generated using refuse-burning plant is carried out bottom-heated to sludge, is aerated, while to
Sludge in desiccation greenhouse is passed through warm wind；The foul smell that ventilating fan structure is extracted out is passed through in the incinerator of refuse-burning plant.
Further, the exhaust steam that refuse-burning plant generates is collected by steam collection portion, is set in sludge bottom
Drying bed is set, floor heating pipe is set in drying bed, aeration tank is set on drying bed, solarization air cap is arranged in aeration tank, by institute
State be passed through in floor heating pipe and aeration tank collection exhaust steam come to sludge carry out bottom-heated, aeration；Setting in desiccation greenhouse
Warm-air drier, the warm-air drier are connected to steam collection portion.
The utility model has the advantages that the steam waste heat using power plant is auxiliary thermal source using the greenhouse effects of transparent desiccation greenhouse,
Reduce discharge of the heat to atmosphere, while having saved fossil energy, effectively reduces the cost of specific resistance to filtration；It reduces
Solar energy sludge drying is influenced by the variation in sunshine, meteorology, season, and it is controllable to realize drying cycle, solve desiccation amount it is small,
Low efficiency, at high cost, the slow-footed problem of desiccation realize the efficient controllable of a large amount of desiccation of sludge.
Detailed description of the invention
Fig. 1 is the structural schematic diagram of sludge compound thermal anhydration system.
Fig. 2 is the structural schematic diagram of drying bed.
In figure, desiccation greenhouse 1, warm-air drier 2, turner 3, drying bed 4, top layer 41, bottom 42, aeration tank 43, aeration face
44, solarization air cap 45, floor heating pipe 5, steam collection portion 6, air passage 7, steam-driven generator 8, incinerator 9.
Specific embodiment
The utility model is described in further detail below with reference to embodiment.
Embodiment 1
As shown in Figure 1 to Figure 2, a kind of sludge compound thermal anhydration system, the desiccation greenhouse 1 including top transparent are described dry
Changing greenhouse 1 is to add tempered glass to be designed to that solar energy desiccation greenhouse 1, the desiccation greenhouse 1 are provided with ventilating fan using steel construction
Structure, the desiccation greenhouse 1 is interior to be equipped with turning machine for sludge 3, and the warm wind towards turning machine for sludge 3 is additionally provided in the desiccation greenhouse 1
The lower section of machine 2 and several pairs of ground fans for being fixed on 1 top bay of desiccation greenhouse, the turning machine for sludge 3 is equipped with drying bed 4,
Floor heating pipe 5 is equipped in 4 bottom of drying bed, the floor heating pipe 5 and warm-air drier 2 are respectively communicated with the steam-driven generator of refuse-burning plant
The steam collection portion 6 of the steam collection portion 6 of 8 steam turbine, steam turbine is adapted with the exhaust portion of steam turbine, is threadedly coupled or is welded
It connects and fixes, the drying bed 4 is additionally provided with aeration tank 43, and the aeration that cross section is semicircle is fixed in the aeration tank 43
Pipe, the plane side of the aeration tube are aeration face 44, and the aeration face 44 is upward and equipped with several solarization air caps 45, the aeration
Pipe is connected to floor heating pipe 5；The air inlet pipe of the floor heating pipe 5, aeration tube and warm-air drier 2 is equipped with the solenoid valve of control air inflow, institute
It states solenoid valve and is electrically connected controller, the controller is PLC, by control solenoid valve control floor heating pipe 5, aeration tube and is warmed up
The steam inlet amount of blower 2, to realize the automation control of the temperature of the heating of floor heating pipe 5 and aeration；Desiccation greenhouse 1 is by changing
The incinerator 9 of wind mechanism connection refuse-burning plant so can be achieved to handle the foul smell rationalization that sludge drying processing generates.
The drying bed is hollow double-layer structure, including contacting the top layer 41 of sludge and the bottom 42 on contact ground, top
The metal high for the coefficient of heat conduction of layer 41, bottom 42 are the low rubber material of the coefficient of heat conduction, and the floor heating pipe 5 is close to top layer 41
It is set between double-layer structure, slot can be equipped on bottom 41, top layer 42 so connects in the slot of bottom 41；Institute
Stating floor heating pipe 5 is snakelike coil-shaped pipe, and material usesStainless steel tube.The ventilating fan structure includes in air passage 7
Be provided with suction ventilator, desiccation greenhouse 1 is provided with air hole, and the air passage 7 is connected to the incinerator 9 of refuse-burning plant, by
A through-hole is opened on the side wall of incinerator 9, then by 7 sealing welding of air passage in through hole.
Preferably, the aeration tube is compatible flat for welding at the top of the half slot for the setting that is recessed on drying bed 4
Face metal plate, the aeration face 44 are planar metal plate；The pitch of holes that solarization air cap 45 is arranged on the aeration face 44 is 50mm,
The diameter of the solarization air cap 45 is 1mm.Temperature and humidity sensing device, the temperature in the present embodiment are additionally provided in the desiccation greenhouse 1
Humidity induction device is Temperature Humidity Sensor, and XW-TH-B cabinet Temperature Humidity Sensor, the temperature and humidity induction dress can be selected in model
Electrical connection PLC controller is set, controller detects the temperature and humidity in desiccation greenhouse 1 by temperature and humidity sensing device, is sludge
The automation and left unguarded intelligence of compound thermal anhydration system are laid a good foundation.
Compared with traditional sludge drying technique, traditional solar greenhouse desiccation is that upper surface one side is heated, desiccation
Time is long, and summer drying cycle is 10 days, and winter drying cycle is 15 days, and drying cycle is not easily controlled；The utility model
Sludge compound thermal anhydration system makes sludge upper and lower surface thermally equivalent, is effectively increased the evaporation rate of moisture, drying cycle
It is 5 days, effectively shortens the sludge drying time, drying efficiency is high, and drying cycle is short, and drying cycle is controllable.
It is main heating source that sludge compound thermal drying technique, which relies on clean solar energy, using the greenhouse of glass desiccation greenhouse 1
Effect reduces discharge of the heat to atmosphere, has saved fossil energy using the steam waste heat in power plant as auxiliary thermal source, will
Foul smell in canopy is passed through the incinerator 9 of refuse-burning plant, handles foul smell using garbage power plant smoke processing equipment, effective to drop
The low cost of specific resistance to filtration.
Moisture percentage in sewage sludge is down to 20% from about 80% up to 90% or more this technology by the sludge solid content after drying and other treatment
Hereinafter, sludge volume reduces 2/3 or more, the sludge calorific value after municipal sludge desiccation is 14000KJ/Kg, with general colm
Calorific value is close, is generated electricity after waste incinerator 9 burns surprise using the sludge after desiccation, realizes the minimizing, innoxious of sludge,
Resource Rationalization processing disposition.
In conclusion the obvious benefit of the utility model has: using the greenhouse effects of transparent desiccation greenhouse 1, benefit
It is auxiliary thermal source with the steam waste heat in power plant, reduces discharge of the heat to atmosphere, while having saved fossil energy, effectively
Reduce the cost of specific resistance to filtration；Reduce solar energy sludge drying is influenced by the variation in sunshine, meteorology, season, is realized
Drying cycle is controllable, solves the problems, such as that small desiccation amount, low efficiency, at high cost, desiccation is slow-footed, realizes sludge and largely does
That changes is efficient controllable.
Embodiment 2
Based on the compound heat drying method of sludge of sludge compound thermal anhydration system described in embodiment 1, by underground heat, two kinds of aeration
Sludge drying combines, and is specifically included in desiccation greenhouse 1 and is turned over throwing repeatedly, and ventilating fan structure is arranged on desiccation greenhouse 1
It is aerated ventilation, using sufficient solar energy resources, solar energy desiccation greenhouse 1 is designed to using steel construction plus tempered glass,
Electronic execution skylight mechanism is set on big ceiling, greenhouse area is pressed inside greenhouse, is arranged by a certain percentage to ground fan, this reality
It applies every four square meter in example and is arranged one to ground fan；
The exhaust steam generated simultaneously using refuse-burning plant carries out bottom-heated, aeration to sludge, specifically, at sludge bottom
Drying bed 4 is arranged in portion, and floor heating pipe 5 is arranged in drying bed 4, and aeration tank 43 is arranged on drying bed 4, on aeration tank 43 welding with
The aeration face 44 of 4 flush of drying bed, aeration face 44 are a metal plate, one end sealing welding of aeration tank 43, other end weldering
Lead to aeration tube in succession, be aerated on face 44 and solarization air cap 45 is set, the exhaust steam that refuse-burning plant generates is led to by steam collection portion 6
Enter floor heating pipe 5, floor heating pipe 5 is connected to aeration tube, by be passed through into the floor heating pipe 5 and aeration tube the exhaust steam of collection come pair
Sludge carries out bottom-heated, aeration, is respectively provided with solenoid valve in the inlet end of floor heating pipe 5 and the inlet end of aeration tube, so passes through
Control the air inflow of solenoid valve controllably heating coil 5 and aeration tube, so realize the heating temperature of sludge is automated it is controllable.
Further include being passed through warm wind into desiccation greenhouse 1, warm-air drier 2, the warm-air drier 2 are set in sludge drying greenhouse 1
It is connected to steam collection portion 6；While can so cooperating the air for accelerating Sludge Surface to ground fan to flow, make the air of flowing
Temperature is higher, accelerates the evaporation to sludge water content.
In addition, the foul smell that ventilating fan structure is extracted out is passed through in the incinerator 9 of refuse-burning plant, specifically, the ventilating fan
Structure includes that suction ventilator is provided in air passage 7, and desiccation greenhouse 1 is provided with air hole, is passed through enough dry airs, takes away sludge
Humid air in desiccation greenhouse 1 accelerates sludge drying；The air passage 7 is connected to the incinerator 9 of refuse-burning plant, by burning
It burns and opens a through-hole on the side wall of furnace 9, then 7 sealing welding of air passage is so realized in through hole and generates sludge drying
Foul smell rationally handle.
This technology by moisture percentage in sewage sludge from about 80% be down to 20% hereinafter, the sludge solid content after drying and other treatment up to 90%
More than, sludge volume reduces 2/3 or more, and the sludge calorific value after municipal sludge desiccation is 14000KJ/Kg, with general colm
Calorific value is close, is generated electricity after the burning of waste incinerator 9 using the sludge after desiccation, realizes the minimizing, innoxious of sludge, money
Rationalize processing disposition in source.
Principles and methods: sludge of the moisture content greater than 80% utilizes the sludge pump after repacking to be pumped into the dry canopy of sludge drying
Interior, turning machine for sludge 3 carries out turning over repeatedly to sludge, is evenly distributed on sludge on drying bed 4, is existed using solar radiation
Greenhouse effects are generated in desiccation greenhouse 1 increases the temperature of Sludge Surface, evaporates the moisture in sludge；By power plant exhaust steam
It is passed through floor heating pipe 5 and ground heating type heating in bottom is carried out to sludge, improve the temperature of sludge bottom, make sludge up and down while heated, mention
The evaporation rate of high sludge water content；Exhaust steam is passed through aeration tube, sludge is flashed using aeration, improves the temperature of sludge,
Make to be passed through enough dry airs in desiccation greenhouse 1 by ventilating fan structure, by the smelly humid air in sludge drying greenhouse 1,
Be passed through in the incinerator 9 of refuse-burning plant, accelerate sludge drying while by refuse-burning plant to the processing equipment of flue gas
The foul smell of sludge drying generation is rationally handled；The utility model finishes the steam of function using power plant, will be hot by warm-air drier 2
Gas is passed through in desiccation greenhouse 1, while accelerating flowing to the air of Sludge Surface, so that the temperature of moving air is higher, is accelerated
The evaporation rate of moisture in sludge.
Claims (5)
1. a kind of sludge compound thermal anhydration system, the desiccation greenhouse including top transparent, the desiccation greenhouse are provided with ventilating fan
Structure, the desiccation greenhouse is interior to be equipped with turning machine for sludge, which is characterized in that is additionally provided in the desiccation greenhouse towards turning machine for sludge
Warm-air drier and be fixed on several pairs of ground fans of desiccation greenhouse top bay, the lower section of the turning machine for sludge is equipped with desiccation
Bed, floor heating pipe is equipped in the drying bed bottom, the floor heating pipe and warm-air drier are respectively communicated with the steaming of the steam turbine of refuse-burning plant
Vapour collection portion, the drying bed are additionally provided with aeration tank, and the aeration tube that cross section is semicircle, the exposure are fixed in the aeration tank
The plane side of tracheae is aeration face, and for the aeration up and equipped with several solarization air caps, the aeration tube is connected to floor heating pipe；Institute
State floor heating pipe, aeration tube is equipped with the solenoid valve of control air inflow, the solenoid valve is electrically connected controller, passes through control electromagnetism
The steam inlet amount of valve control floor heating pipe and aeration tube.
2. sludge compound thermal anhydration system as described in claim 1, which is characterized in that the drying bed is the hollow double-deck knot
Structure, including contacting the top layer of sludge and the bottom on contact ground, top layer is the high metal of the coefficient of heat conduction, and bottom is heat transfer system
The low rubber material of number, the floor heating pipe are close to top layer and are set between double-layer structure, and the floor heating pipe is snakelike coil-shaped pipe.
3. sludge compound thermal anhydration system as described in claim 1, which is characterized in that the aeration tube is to be recessed on drying bed
Compatible planar metal plate is welded at the top of the half slot of setting, the aeration face is planar metal plate；It is set on the aeration face
The pitch of holes for setting solarization air cap is 50~60mm, and the diameter of the solarization air cap is 1~1.5mm.
4. sludge compound thermal anhydration system as described in claim 1, which is characterized in that the ventilating fan structure includes in air passage
It is provided with suction ventilator, desiccation greenhouse is provided with air hole, the incinerator of the air passage connection refuse-burning plant.
5. sludge compound thermal anhydration system as described in claim 1, which is characterized in that be additionally provided with temperature in the desiccation greenhouse
Humidity induction device, the temperature and humidity sensing device are electrically connected controller, and controller detects desiccation by temperature and humidity sensing device
Temperature and humidity in greenhouse.
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| Application Number | Priority Date | Filing Date | Title |
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| CN201821256608.0U CN208898735U (en) | 2018-08-06 | 2018-08-06 | A kind of sludge compound thermal anhydration system |
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| Application Number | Priority Date | Filing Date | Title |
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| CN201821256608.0U CN208898735U (en) | 2018-08-06 | 2018-08-06 | A kind of sludge compound thermal anhydration system |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108947202A (en) * | 2018-08-06 | 2018-12-07 | 宁夏中科国通新能源有限公司 | A kind of sludge compound thermal anhydration system and its method |
| CN110451765A (en) * | 2019-09-02 | 2019-11-15 | 安徽舜禹水务股份有限公司 | A kind of energy-saving sludge drying equipment |
| CN110918610A (en) * | 2019-12-09 | 2020-03-27 | 中城绿建科技有限公司 | Method for biological drying aeration by recycling power generation waste heat of pyrolysis combustible gas |
-
2018
- 2018-08-06 CN CN201821256608.0U patent/CN208898735U/en active Active
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108947202A (en) * | 2018-08-06 | 2018-12-07 | 宁夏中科国通新能源有限公司 | A kind of sludge compound thermal anhydration system and its method |
| CN110451765A (en) * | 2019-09-02 | 2019-11-15 | 安徽舜禹水务股份有限公司 | A kind of energy-saving sludge drying equipment |
| CN110918610A (en) * | 2019-12-09 | 2020-03-27 | 中城绿建科技有限公司 | Method for biological drying aeration by recycling power generation waste heat of pyrolysis combustible gas |
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