CN108503185A - A kind of sludge removal moisture drying system - Google Patents
A kind of sludge removal moisture drying system Download PDFInfo
- Publication number
- CN108503185A CN108503185A CN201810588505.2A CN201810588505A CN108503185A CN 108503185 A CN108503185 A CN 108503185A CN 201810588505 A CN201810588505 A CN 201810588505A CN 108503185 A CN108503185 A CN 108503185A
- Authority
- CN
- China
- Prior art keywords
- baking oven
- heat exchange
- evaporator
- wind
- several
- 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.)
- Pending
Links
- 239000010802 sludge Substances 0.000 title claims abstract description 23
- 238000001035 drying Methods 0.000 title claims abstract description 21
- 238000010438 heat treatment Methods 0.000 claims abstract description 44
- 238000007791 dehumidification Methods 0.000 claims abstract description 32
- 238000005192 partition Methods 0.000 claims abstract description 4
- 238000007689 inspection Methods 0.000 claims description 4
- 238000004891 communication Methods 0.000 claims description 3
- 238000001704 evaporation Methods 0.000 claims description 2
- 230000008020 evaporation Effects 0.000 claims description 2
- 238000001816 cooling Methods 0.000 abstract description 13
- 238000000034 method Methods 0.000 abstract description 9
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 9
- 238000010010 raising Methods 0.000 abstract description 4
- 238000009833 condensation Methods 0.000 description 9
- 230000005494 condensation Effects 0.000 description 9
- 238000013461 design Methods 0.000 description 9
- 239000000463 material Substances 0.000 description 8
- 230000008901 benefit Effects 0.000 description 5
- 238000012545 processing Methods 0.000 description 5
- 238000005057 refrigeration Methods 0.000 description 5
- 230000005611 electricity Effects 0.000 description 3
- 230000007812 deficiency Effects 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000009826 distribution Methods 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 239000003507 refrigerant Substances 0.000 description 2
- 229910000831 Steel Inorganic materials 0.000 description 1
- 208000027418 Wounds and injury Diseases 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 230000000295 complement effect Effects 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 230000006378 damage Effects 0.000 description 1
- 230000006837 decompression Effects 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000003116 impacting effect Effects 0.000 description 1
- 230000008676 import Effects 0.000 description 1
- 208000014674 injury Diseases 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000005457 optimization Methods 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 238000003303 reheating Methods 0.000 description 1
- 239000000523 sample Substances 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
- 230000032258 transport Effects 0.000 description 1
- 238000010792 warming Methods 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F11/00—Treatment of sludge; Devices therefor
- C02F11/12—Treatment of sludge; Devices therefor by de-watering, drying or thickening
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Drying Of Solid Materials (AREA)
Abstract
The present invention relates to various sludge treatment device technical fields, and in particular to a kind of sludge removal moisture drying system, it includes box shell, which is separated into left chamber and right chamber by partition board, which is that refrigerated dehumidification heats case, which is baking oven；Refrigerated dehumidification heating component is provided in the refrigerated dehumidification heating case；Baking oven component is provided in the baking oven；The baking oven component includes several net formula conveyers being mutually parallel being mounted in baking oven；It uses the application of wind wind heat exchange, highest that can will will dry room hot blast temperature and set the best critical-temperature for being promoted to water and switching to steam, and auxiliary thermal source carries out 2 heat temperature raisings using the high-temperature hot-air of electromagnetism hot-air system generation to condenser outlet air one's intention as revealed in what one says；Being blown into wind wind heat exchanger by the cold wind of the dehumidifying of evaporator cooling, passively heating is re-fed into the condenser heating of compressor assembly, and internal system balance control method so in cycles ensure that the reliable and stable operation of compressor assembly.
Description
Technical field
The present invention relates to acid sludge processing equipment technical fields, and in particular to a kind of sludge removal moisture drying system.
Background technology
Tradition is for the drying equipment that the processing mode of sludge is using condensation method, after being dried sludge to reduce
Ton amount of the phase to Treatment of Sludge.Its operation principle is：Industry is similar using the drying equipment basic principle of condensation method, generally use
The refrigeration system principle for the drying machine that material is dried in dehumidifier method is all to make the humid air cooling dehumidification from hothouse, when
When humid air stream is through evaporator, the heat that internal low pressure refrigerant absorbs air becomes gaseous state from liquid, and air is due to cooling
Most of condensed water therein is discharged.Come flash-pot low voltage refrigeration steam boosted by compressor after send to condenser.When de-
When cold dry air after wet flows through condenser, internal high-pressure refrigerant releases heat because of condensation, and external air is then added
Heat is the product that hot wind is returned to that hothouse continues dry required drying.The expanded valve of high-pressure refrigeration liquid flowed out from condenser
Evaporator is flowed into after decompression continues next cycle.
There are the following problems when in use for associated processing equipment in the market：
Although first, these equipment and the refrigeration compressor set and cooling and warming feature that use, due to failing reasonably will
The application of refrigeration principle science well, ensures compressor nominal situation, takes the unreasonable not science of scheme again, although open a surname
It is closed loop to pass their systems, but is all to install additional to arrange outside external water cooling tower or additional condensation device carry out system in system in fact
Heat, additional heat loss are the inevitable root problems of its system.Its processing equipment international communication is existed using compressor set
Operation with closed ring, but because whole equipment air duct setting and material physical state variation can all break compressor set evaporator and
The cold and hot balance of condenser, the equipment of xx companies in order to solve the problems, such as system temperature imbalance this, in compressor and evaporation
External water cooling tower is concatenated on device pipeline, in system temperature over-limit condition, by extra heat by cooling tower from setting
Standby middle transfer is discharged into environment, and there are one an insufficient, benefits for the xxx Corporation systems which distinguishes and be described below
With three disadvantages.One deficiency is：Fail compressor assembly and equipment optimization into a good integrated system；One benefit
It is：It not give baking oven good heating temperature to meeting before limiting value in compressor assembly temperature when compressor assembly works.Disadvantage one is：
The operating mode of compressor is always in the variation of impact peak value in cycles, and by matching outside equipment when high pressure always impacts peak value
Heat is unloaded in the cooling tower startup set, and has both wasted thermal energy, frequent high pressure is unbalance and impacting with high pressure also results in working conditions of compressor very
Severe disadvantages second is that：Directly shorten the compressor service life and cause compressor fault rate high, maintenance cost is high.Disadvantage three is：Because unloading
Temperature causes thermal loss, causes grid electricity fee cost height.
For the processing equipment of xxx Corporation systems available on the market, there are the following problems when using：
The equipment dehumidification system of xxx Corporation systems be also use low temperature dehumidification, condenser generate thermal energy go give material heating, from
And realize the purpose of dry materials, the design of the system difference and above system is by compressor evaporator inlet air temperature by setting
Plate heat exchanger controls the temperature upper limit that can be born into evaporator constant built in standby external cooling tower bonding apparatus
Temperature, to ensure that compressor assembly is normally run, which is two weakness of a benefit.Benefit is：It ensure that pressure
The bearing temperature of contracting machine system evaporator avoids above system compressor because operating mode is constantly passively changed impact peak value, gives
Injury caused by system.But the weakness one of the system is：Although above design method has ensured that evaporator temperature is relatively steady,
But the higher temperature output of condenser is not realized, so will not be broken through by being sent into the temperature of baking room by 60 degree.Weakness second is that：Because external
Cooling tower endlessly unload temperature and cause heat heavy losses, cause grid electricity fee cost height.
Invention content
In view of the defects and deficiencies of the prior art, the present invention intends to provide a kind of sludge removal moisture drying systems.
A kind of sludge removal moisture drying system of the present invention, it includes box shell, which is separated into left case by partition board
Room and right chamber, the left chamber are that refrigerated dehumidification heats case, which is baking oven；It is provided in the refrigerated dehumidification heating case
Refrigerated dehumidification heats component；Baking oven component is provided in the baking oven；
The baking oven component includes several net formula conveyers being mutually parallel being mounted in baking oven；The baking oven inner top is longitudinal
Direction is provided with several return fans；It is provided with introduction member at the top of the baking oven；
If if the refrigerated dehumidification heating component include wind wind heat exchange component, several evaporators one, evaporator two, dry condenser,
Dry electromagnetic heating air hose；The refrigerated dehumidification heating case inner top is provided with wind wind heat exchange component, which heats in case
Top is provided with several evaporators one, evaporator two, and several evaporators one form evaporator group；In the refrigerated dehumidification heating case
If middle part is provided with dry condenser, if dry condenser forms condenser group；Several electromagnetic heating air hoses are pacified by longitudinal arrangement
The bottom in refrigerated dehumidification heating case；
The wind wind heat exchange component include heat exchange babinet, the heat exchange babinet be rectangle structure, the right side of the heat exchange babinet and
Bottom surface is openning shape, and several heat-exchange tubes are provided in the heat exchange box body；In the heat exchange babinet right side open end and baking oven
The air port of several return fans at top is opposite；The heat exchange babinet bottom opening end is arranged in the surface of evaporator group；It is described
Evaporator group is connected by air duct one with the rear end nozzle of the heat-exchange tube in heat exchange box body；Heat in the heat exchange box body is handed over
The front end nozzle for changing pipe is connected by air duct two with evaporator two, and evaporator two is connected by air duct three with condenser group；Institute
It states condenser group with suction ventilator to be connected, suction ventilator is connected by air duct four with several electromagnetic heating air hoses, electromagnetic heating air hose
Right side air-out mouth stretches to bottom in baking oven.
Further, several radiating fins, the front end nozzle of the heat-exchange tube are installed in the tube rod of the heat-exchange tube
It is respectively interposed to the front surface of heat exchange babinet and rear surface to outer with rear end nozzle.
Further, it is separately installed with temperature sensor on several electromagnetic heating air hoses, if dry temperature sensor passes through 485
Digital communication signal is connected with PLC controller.
Further, it is provided with inspection door on the right side of the bottom surface of the baking oven.
Further, several evaporators one, evaporator two bottom be provided with reception basin.
Further, it is respectively arranged with air quantity on the air duct one of the bottom of the evaporator one, evaporator two or air duct two
Balancer.
Further, secondary condenser is installed on the box shell top surface, which passes through air duct five and condenser group
Series connection.
The beneficial effects of the invention are as follows：A kind of sludge removal moisture drying system of the present invention, it is using the heat exchange of wind wind
Using being detected zone sensors from several distributions and equipment and be monitored and feed back to plc and instruct with each frequency converter and air-valve
It will not additionally unload, will be dried to can guarantee using the technological means of big internal system balance, heat after compressor assembly is integrated
Room hot blast temperature promotes the best critical-temperature for switching to steam to water, and auxiliary thermal source uses the high temperature that electromagnetism hot-air system generates
Hot wind carries out 2 heat temperature raisings to condenser outlet air one's intention as revealed in what one says；Wind wind heat exchanger quilt is blown by the cold wind that evaporator cools down and dehumidifies
Dynamic heat up is re-fed into the condenser heating of compressor assembly, and internal system balance control method so in cycles ensure that compression
The reliable stable operation of machine system.
【Description of the drawings】
Attached drawing described herein is to be used to provide further understanding of the present invention, and is constituted part of this application, but not
Inappropriate limitation of the present invention is constituted, in the accompanying drawings：
Fig. 1 is schematic structural view of the invention；
Fig. 2 is the topological structure schematic diagram of the present invention；
Fig. 3 is the right side structural representation of the wind wind heat exchange component of the present invention；
Fig. 4 is the forward sight structural schematic diagram of the wind wind heat exchange component of the present invention；
Reference sign：
1, wind wind heat exchange component；2, baking oven；3, net formula conveyer；4, evaporator one；5, evaporator two；6, condenser；7, electromagnetism
Heat air hose；8, temperature sensor；9, PLC controller；10, heat-exchange tube；101, tube rod；102, radiating fin；103, front end
Nozzle；104, rear end nozzle；11, refrigerated dehumidification heats case；12, return fan；13, inspection door；14, exchange heat babinet；15, secondary condensation
Device；16, reception basin；17, blast balance apparatus；18, suction ventilator.
【Specific implementation mode】
Below in conjunction with attached drawing and specific embodiment, the present invention will be described in detail, and illustrative examples therein and explanation are only
For explaining the present invention, but it is not as a limitation of the invention.
As Figure 1-Figure 2, a kind of sludge removal moisture drying system described in present embodiment, it includes box shell, should
Box shell is separated into left chamber and right chamber by partition board, which is that refrigerated dehumidification heats case 11, which is baking oven 2；
Refrigerated dehumidification heating component is provided in the refrigerated dehumidification heating case 11；Baking oven component is provided in the baking oven 2；
The baking oven component includes several net formula conveyers 3 being mutually parallel being mounted in baking oven 2；2 inner top of the baking oven
Longitudinal direction is provided with several return fans 12；The top of the baking oven 2 is provided with introduction member；
If the refrigerated dehumidification heating component includes wind wind heat exchange component 1, several evaporators 1, evaporator 25, dry condenser
6, several electromagnetic heating air hoses 7；Refrigerated dehumidification heating 11 inner top of case is provided with wind wind heat exchange component, the refrigerated dehumidification system
11 internal upper part of hot tank is provided with several evaporators 1, evaporator 25, one 4 evaporator group of several evaporators；The refrigerated dehumidification
If middle part is provided with dry condenser 6 in heating case 11, if 6 condenser group of dry condenser；Several electromagnetic heating air hoses 7 are by vertical
It is mounted on bottom in refrigerated dehumidification heating case 11 to arrangement；
Such as Fig. 3-Fig. 4, the wind wind heat exchange component 1 includes heat exchange babinet 14, which is rectangle structure, the heat exchange
The right side and bottom surface of babinet 14 are openning shape, and several heat-exchange tubes 10 are provided in the heat exchange babinet 14；The heat exchange babinet
14 right sides open end are opposite with the air port of several return fans 12 of 2 inner top of baking oven；The 14 bottom opening end of heat exchange babinet
It is arranged in the surface of evaporator group；The rear end that the evaporator group passes through air duct one and the heat-exchange tube 10 in heat exchange babinet 14
Nozzle 104 is connected；The front end nozzle 102 of heat-exchange tube 10 in the heat exchange babinet 14, passes through air duct two and evaporator 25
It is connected, evaporator 25 is connected by air duct three with condenser group；The condenser group is connected with suction ventilator 18, suction ventilator 18
It is connected with several electromagnetic heating air hoses 7 by air duct four, the right side air-out mouth of electromagnetic heating air hose 7 stretches to bottom in baking oven 2.
Further, several radiating fins 102 are installed in the tube rod 101 of the heat-exchange tube 10, the heat-exchange tube
Front end nozzle 103 and rear end nozzle 104 are respectively interposed to the front surface of heat exchange babinet 14 and rear surface to outer.
Further, it is separately installed with temperature sensor 8 on several electromagnetic heating air hoses 7, if dry temperature sensor 8 passes through
Wireless signal is connected with PLC controller 9.
Further, it is provided with inspection door 13 on the right side of the bottom surface of the baking oven 2.
Further, several evaporators 1, evaporator 25 bottom be provided with reception basin 16.
Further, it is respectively arranged with wind on the air duct one of the bottom of the evaporator 1, evaporator 25 or air duct two
Measure balancer 17.
Further, secondary condenser 15 is installed on the box shell top surface, which passes through air duct five and condensation
Device group is connected.
Working principle of the present invention is as follows：
In the design, left chamber is that refrigerated dehumidification heats case 11, and right chamber is baking oven 2.The design when in use, dirt to be processed
Mud enters to after being granulated from the import component numerical control at the top of right chamber in net formula conveyer 3；At this time from the electromagnetism of left chamber bottom
It heats in air hose 7 in blowout high-temperature hot-air to right chamber, right chamber is baking oven at this time；Several return fans of right chamber inner top are opened
Beginning work installs more horizontally arranged return fans 12 and forms return air unit, the moisture in sludge is inhaled upwards under normal circumstances
Go out, produces the damp and hot wind of the high temperature with moisture at this time；
Then, the damp and hot wind of the high temperature is directed in the heat exchange babinet in wind wind heat exchange component, the damp and hot wind of high temperature is blown by blower fan group
It is dissipated to the open end of 14 right side of heat exchange babinet into the heat-exchange tube 10 in heat exchange babinet 14 by radiating fin
Then heat is exported from the open end of 14 bottom surface of heat exchange babinet, again until the evaporator group immediately below it（By one 4 groups of several evaporators
At）, freeze to obtain 8-10 DEG C of cold wind by evaporator heat exchange, then heat exchange 14 subsequent heat-exchange tube of babinet is led to by wind guide channel
Rear end nozzle 104 is passed through to heat-exchange tube front end nozzle 103 from the tube rod 101 of heat-exchange tube and is exported, due to heat-exchange tube 10
Tube rod and radiating fin 102 thereon temperature so that by the tube rod 102 of heat-exchange tube 10 it is distinguished and admirable again plus
Temperature, it is to be raised, then pass through air duct two to evaporator 25 to export distinguished and admirable temperature.
Then, then by exchanging heat in air duct three to condenser group, a secondary condenser 15 of connecting in condenser group, side
This compressor group is helped to carry out reducing the upborne temperature that should exchange heat and carry out alleviating the set compressor because of the hot wind of crossing to outlet 103
Extra duty, suction ventilator 18 will carry out the distinguished and admirable quick export of primary heating by condenser group, then as by air duct four
On dry electromagnetic heating air hose 7, by electromagnetic heating air hose reheating by distinguished and admirable heating, high temperature drying hot wind is formed；Then again
It blows into right chamber（Baking oven）The interior sludge on net formula conveyer heats, and forms dehumidification work cycle in cycles.
This system is to be distributed to be monitored with the humiture probe in the detected area of equipment by several to feed back to plc instructions respectively
It will not additionally be unloaded using the technological means of big internal system balance, heat after frequency converter and air-valve cooperation compressor assembly are integrated
It carries, baking room hot blast temperature is promoted to water to the best critical-temperature for switching to steam to can guarantee, hot wind is blown on guipure and transports
Capable material, quickly moisture in material is formed after vapor state take out of with the wind hothouse cooled down in advance by the heat exchange of wind wind it is laggard
Enter evaporator condensation, moisture rapid condensation is the sink that dew instills outside collecting box remover apparatus.Auxiliary thermal source uses 9 Cr 2 steel using electromagnetic heating
The high-temperature hot-air that wind system generates carries out 2 heat temperature raisings to condenser outlet air one's intention as revealed in what one says.
In the design, evaporator one and evaporator two are the evaporator with model same specification.For example, by using 6 with model
Evaporator forms evaporator groups by its 5 as evaporators one, and another is used as evaporator two, in the design, one He of evaporator
Evaporator two is the evaporator with model same specification.For example, by using 6 evaporators with model, evaporator one is used as by its 5
Evaporator group is formed, it is after exchanging the heat exchange of wind wind from 103 outlet of wind wind heat exchange that another, which is used as evaporator two, its effect,
Hot wind is sent into condenser group and the temperature of heating is gone to be cooled down in advance, is caused to pressure by condenser to avoid the excessively high hot wind of temperature
Contracting machine operating mode it is unfavorable.
For the control of electromagnetic heating air hose 7 in the design, using the structure of PLC controller 9+ temperature sensors 8, temperature
Sensor 8 carrys out the temperature of the hot wind of the blowout of the real time measure electromagnetic heating air hose 7, and the temperature of hot wind is controlled by PLC controller 9
Degree, above-mentioned control belongs to the prior art, therefore the circuit the design being related to is not elaborated.
The operation principle of the compressor balance system of this system is：Material moisture quilt in material in hothouse motion process
The hot wind for the generating high temperature and humidity feeding evaporator rapid condensation after wind wind heat exchanger cools down for the first time that is evaporated converges at water droplet
Enter header tank discharge production line, being blown into wind wind heat exchanger by the cold wind of the dehumidifying of evaporator cooling, passively heating is re-fed into compressor
The condenser of system heats up, and internal system balance control method so in cycles ensure that the reliable and stable of compressor assembly
Operation.
The characteristics of this system is：
1, two unique design：（1）The application of wind wind heat exchange；（2）The application of electromagnetism auxiliary heating.
2, three advantages：
（1）Thermal loss caused by additional water cooling equipment expels the heat-evil is not needed；
（2）Because work load can be mitigated supplemented with heat to compressor assembly by applying electromagnetism hot wind, reach pre- in temperature
It of short duration can be shut down when definite value, gain time and save electric energy to compressor assembly quantum balancing.
（3）Because the balance and stability of big system ensure that the balance of compressor assembly and it is mutually coordinated complement one another,
It not only economizes on electricity but also dry room temperature can promote about 100 degree of accidental conditions without breaking compressor assembly.
A kind of sludge removal moisture drying system of the present invention, it use wind wind heat exchange application, by several distribution with
Equipment, which is detected area and is monitored, to be fed back to after plc instructs each frequency converter and air-valve cooperation compressor assembly integrated using big system
The technological means of internal balance, heat will not be unloaded additionally, switch to steam to water to can guarantee to dry room hot blast temperature and set to be promoted
The best critical-temperature of gas, auxiliary thermal source carry out condenser outlet air one's intention as revealed in what one says using the high-temperature hot-air that electromagnetism hot-air system generates
2 heat temperature raisings；Being blown into wind wind heat exchanger by the cold wind of the dehumidifying of evaporator cooling, passively heating is re-fed into compressor assembly
Condenser heats up, and internal system balance control method so in cycles ensure that the reliable and stable operation of compressor assembly.
The above is only the better embodiment of the present invention, therefore all constructions according to described in present patent application range,
The equivalent change or modification that feature and principle are done, is included within the scope of present patent application.
Claims (7)
1. a kind of sludge removal moisture drying system, it is characterised in that：It includes box shell, and box shell is separated into left chamber and the right side by partition board
Chamber, left chamber are that refrigerated dehumidification heats case（11）, right chamber is baking oven（2）；The refrigerated dehumidification heats case（11）Interior setting
There is refrigerated dehumidification to heat component；The baking oven（2）Inside it is provided with baking oven component；The baking oven component includes being mounted on baking oven（2）
The interior several net formula conveyers being mutually parallel（3）；The baking oven（2）Inner top longitudinal direction is provided with several return fans
（12）；The baking oven（2）Top be provided with introduction member；
The refrigerated dehumidification heating component includes wind wind heat exchange component（1）, several evaporators one（4）, evaporator two（5）, it is several
Condenser（6）, several electromagnetic heating air hoses（7）；The refrigerated dehumidification heats case（11）Inner top is provided with wind wind heat exchange component,
The refrigerated dehumidification heats case（11）Internal upper part is provided with several evaporators one（4）, evaporator two（5）, several evaporators one（4）It adopts
With horizontal Tile arrangement form evaporator group；The refrigerated dehumidification heats case（11）If interior middle part is provided with dry condenser（6）If
Dry condenser（6）Using horizontal Tile arrangement form condenser group；Several electromagnetic heating air hoses（7）It is installed by longitudinal arrangement
Case is heated in refrigerated dehumidification（11）Interior bottom；The wind wind heat exchange component（1）Including the babinet that exchanges heat（14）, the heat exchange babinet（14）
For rectangle structure, the heat exchange babinet（14）Right side and bottom surface be openning shape, the heat exchange babinet（14）It is inside provided with several
Heat-exchange tube（10）；The heat exchange babinet（14）Right side open end and baking oven（2）Several return fans of inner top（12）Wind
Mouth is opposite；The heat exchange babinet（14）Bottom opening end is arranged in the surface of evaporator group；The evaporator group passes through air duct
One with heat exchange babinet（14）Interior heat-exchange tube（10）Rear end nozzle（104）It is connected；The heat exchange babinet（14）Interior heat
Exchange pipe（10）Front end nozzle（102）, pass through air duct two and evaporator two（5）It is connected, evaporator two（5）By air duct three with
Condenser group is connected；The condenser group and suction ventilator（18）It is connected, suction ventilator（18）Added by air duct four and several electromagnetism
Hot blast pipe（7）It is connected, electromagnetic heating air hose（7）Right side air-out mouth stretch to baking oven（2）Interior bottom.
2. a kind of sludge removal moisture drying system according to claim 1, it is characterised in that：The heat-exchange tube（10）Pipe
Bar（101）On several radiating fins are installed（102）, the front end nozzle of the heat-exchange tube（103）With rear end nozzle（104）Respectively
Intert to heat exchange babinet（14）Front surface and rear surface to outer.
3. a kind of sludge removal moisture drying system according to claim 1, it is characterised in that：Several electromagnetic heating air hoses（7）
On be separately installed with temperature sensor（8）If dry temperature sensor（8）Pass through 485 digital communication signals and PLC controller（9）
It is connected.
4. a kind of sludge removal moisture drying system according to claim 1, it is characterised in that：The baking oven（2）Bottom surface it is right
Side is provided with inspection door（13）.
5. a kind of sludge removal moisture drying system according to claim 1, it is characterised in that：Several evaporators one（4）、
Evaporator two（5）Bottom be provided with reception basin（16）.
6. a kind of sludge removal moisture drying system according to claim 1, it is characterised in that：The evaporator one（4）, evaporation
Device two（5）Bottom air duct one or air duct two on be respectively arranged with blast balance apparatus（17）.
7. a kind of sludge removal moisture drying system according to claim 1, it is characterised in that：It is equipped on the box shell top surface
Secondary condenser（15）, the secondary condenser（15）It is connected with condenser group by air duct five.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810588505.2A CN108503185A (en) | 2018-06-08 | 2018-06-08 | A kind of sludge removal moisture drying system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810588505.2A CN108503185A (en) | 2018-06-08 | 2018-06-08 | A kind of sludge removal moisture drying system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN108503185A true CN108503185A (en) | 2018-09-07 |
Family
ID=63403075
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201810588505.2A Pending CN108503185A (en) | 2018-06-08 | 2018-06-08 | A kind of sludge removal moisture drying system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN108503185A (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109553270A (en) * | 2018-12-06 | 2019-04-02 | 江苏天舒电器有限公司 | A kind of pump type heat enclosed sludge drying system and its control method |
| CN110028219A (en) * | 2018-12-06 | 2019-07-19 | 江苏天舒电器有限公司 | A kind of pump type heat enclosed sludge drying system |
| CN110131987A (en) * | 2019-05-20 | 2019-08-16 | 江苏申炬环保科技有限公司 | A kind of system closed loop sludge dehumidifying drying system |
Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR101274819B1 (en) * | 2012-02-15 | 2013-06-17 | 엄태경 | Dryer of wet sludge and operating method thereof |
-
2018
- 2018-06-08 CN CN201810588505.2A patent/CN108503185A/en active Pending
Patent Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR101274819B1 (en) * | 2012-02-15 | 2013-06-17 | 엄태경 | Dryer of wet sludge and operating method thereof |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109553270A (en) * | 2018-12-06 | 2019-04-02 | 江苏天舒电器有限公司 | A kind of pump type heat enclosed sludge drying system and its control method |
| CN110028219A (en) * | 2018-12-06 | 2019-07-19 | 江苏天舒电器有限公司 | A kind of pump type heat enclosed sludge drying system |
| CN109553270B (en) * | 2018-12-06 | 2021-11-26 | 江苏天舒电器有限公司 | Heat pump type closed sludge drying system and control method thereof |
| CN110131987A (en) * | 2019-05-20 | 2019-08-16 | 江苏申炬环保科技有限公司 | A kind of system closed loop sludge dehumidifying drying system |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN107166902A (en) | A kind of multifunctional heat pump drying device | |
| CN207422789U (en) | A kind of high-efficiency energy-saving drying machine | |
| CN207738619U (en) | A kind of sludge drying system with total heat recovery case | |
| CN205536673U (en) | Dry heat pump system of constant temperature | |
| CN207456058U (en) | Multifunctional air energy dehumidifying drying system | |
| CN108503185A (en) | A kind of sludge removal moisture drying system | |
| CN102445066B (en) | Natural air dehydrating and preheating drying oven system adopting condensate water waste heat for two-effect flash evaporation | |
| CN207231092U (en) | A kind of multifunctional heat pump drying device | |
| CN208801728U (en) | A kind of drying device of printing machine | |
| CN102288016A (en) | Energy-saving and environment-friendly drying box | |
| CN201731730U (en) | Semiconductor condensing dryer | |
| CN204104803U (en) | Air energy high-temperature dehumidification heat pump leaf drier | |
| CN103398566A (en) | Spiral-flow type heat pump dryer | |
| CN107702498A (en) | A kind of canal drier | |
| KR101793638B1 (en) | Red pepper drier | |
| CN102653166B (en) | Photogravure press | |
| CN208545290U (en) | A kind of sludge removal moisture drying system | |
| CN105783472A (en) | Heat pump-type vermicelli drying equipment | |
| CN111912211A (en) | Sludge heat pump drying system based on air treatment unit | |
| CN106949716A (en) | A kind of medium, energy interior circulation drying means and drying machine | |
| CN214308095U (en) | Be used for disappearance mould stoving heat pump set | |
| CN209801956U (en) | energy-saving drying equipment | |
| CN207375936U (en) | A kind of tunnel sterilizing and drying machine | |
| CN109974411B (en) | Drying method and energy-saving drying equipment | |
| CN209605504U (en) | A kind of drying materials room heated using air energy heat pump |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20180907 |
|
| WD01 | Invention patent application deemed withdrawn after publication |