CN205607033U - Material dewatering device - Google Patents
Material dewatering device Download PDFInfo
- Publication number
- CN205607033U CN205607033U CN201620387013.3U CN201620387013U CN205607033U CN 205607033 U CN205607033 U CN 205607033U CN 201620387013 U CN201620387013 U CN 201620387013U CN 205607033 U CN205607033 U CN 205607033U
- Authority
- CN
- China
- Prior art keywords
- dimethyl ether
- import
- tank
- outlet
- condenser
- 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
Links
Landscapes
- Drying Of Solid Materials (AREA)
Abstract
The utility model relates to a material dewatering device has material drain sump, dimethyl ether storage tank, one -level flash tank, second grade flash tank, filter, compressor, condenser. The dimethyl ether exit linkage material drain sump's of dimethyl ether storage tank dimethyl ether import. The import of material drain sump's moisture dimethyl ether exit linkage one -level flash tank, the import of the dimethyl ether exit linkage second grade flash tank of one -level flash tank. Be provided with the filter between the dimethyl ether export of second grade flash tank and the import of condenser, the dimethyl ether after the filtration gets into the dimethyl ether import of condenser, the dimethyl ether exit linkage dimethyl ether storage tank of condenser. The utility model discloses a method that the material need not to heat up removes water, the circulated use of dimethyl ether after the dehydration, not only energy -conservation but also environmental protection. The utility model discloses energy -conserving nearly 50%, area is little for the dehydration of more traditional fuel -heating, no fume emission, and the tradition adds the clean environmental protection of hot drying dehydration, accords with the strategy of national energy saving and emission reduction and environmental protection.
Description
Technical field
This utility model relates to material dewatering technical field.
Background technology
Material dewatering especially being dried after the sludge press filtration that coal drying and dewatering or sewage disposal produce at present
The fields such as dehydration, the fuel heating evaporation dried that use, water, material heats up, and consumes substantial amounts of more
Heat, discharge flue gas affects environment.
Utility model content
The technical problems to be solved in the utility model is: overcome deficiency of the prior art, it is provided that one
Planting material dehydrating device, material is without intensification, environmental protection and energy saving.
This utility model solves its technical problem and be the technical scheme is that a kind of material dehydrating device,
It is characterized in that: have material dewatering tank, have the dimethyl ether storage tank of dimethyl ether, primary flash tank, two grades
Flash tank, compressor, condenser.
Described material dewatering tank has material inlet, dimethyl ether import, dehydrated material outlet, aqueous dimethyl ether
Outlet, the dimethyl ether outlet of described dimethyl ether storage tank connects the dimethyl ether import of material drain sump.
The aqueous dimethyl ether outlet of described material dewatering tank connects the import of primary flash tank, described primary flash
The moisture outlet of tank connects the import of compressor, and the dimethyl ether outlet of described primary flash tank connects two-stage flash
The import of tank.
The moisture outlet of described two-stage flash tank connects the import of compressor, the dimethyl ether of described two-stage flash tank
Outlet connects the import of condenser.
The outlet of described compressor connects the steam import of condenser, and the moisture outlet of described condenser connects pressure
The import of contracting machine.
Described condenser has dimethyl ether outlet and outlet；The dimethyl ether outlet of described condenser connects diformazan
The dimethyl ether import of ether storage tank.
Further, between dimethyl ether outlet and the dimethyl ether import of material dewatering tank of described dimethyl ether storage tank
It is provided with the first pump.
Further, arrange between dimethyl ether outlet and the dimethyl ether import of dimethyl ether storage tank of described condenser
There is the second pump.
Further, it is provided with filtration between dimethyl ether outlet and the import of condenser of described two-stage flash tank
Device.
The beneficial effects of the utility model are: this utility model can be down to less than 10% by aqueous for coal, can be by
80% water-containing sludge is aqueous is down to less than 30%.Dimethyl ether after dehydration can be recycled.This utility model uses
Water is removed by material without the method heated up, energy-saving and environment-friendly.The heating of this utility model relatively traditional fuel is de-
Water energy-conservation nearly 50%, floor space is little, smokeless, relatively traditional heating drying and dehydrating clean environment firendly, symbol
Close national energy-saving to reduce discharging and the strategy of environmental protection.
Accompanying drawing explanation
Below in conjunction with the accompanying drawings this utility model is further illustrated.
Fig. 1 is structural representation of the present utility model；
Wherein: 1, material dewatering tank, 2, dimethyl ether storage tank, 3, primary flash tank, 4, two grades of sudden strains of a muscle
Steaming pot, 5, compressor, 6, condenser, the 7, first pump, the 8, second pump, 9, filter.
Detailed description of the invention
Presently in connection with accompanying drawing, this utility model is further described.These accompanying drawings are the schematic diagram of simplification
Basic structure of the present utility model is described the most in a schematic way, and therefore it only shows relevant with this utility model
Constitute.
As it is shown in figure 1, a kind of material dehydrating device, there is material dewatering tank 1, have the dimethyl ether of dimethyl ether
Storage tank 2, primary flash tank 3, two-stage flash tank 4, compressor 5, condenser 6.
Described material dewatering tank 1 has material inlet, dimethyl ether import, dehydrated material outlet, aqueous diformazan
Ether exports, and the dimethyl ether outlet of described dimethyl ether storage tank 2 connects the dimethyl ether import of material drain sump 1.
The aqueous dimethyl ether outlet of described material dewatering tank 1 connects the import of primary flash tank 3, described one-level
The moisture outlet of flash tank 3 connects the import of compressor 5, and the dimethyl ether outlet of described primary flash tank 3 is even
Connect the import of two-stage flash tank 4.
The moisture outlet of described two-stage flash tank 4 connects the import of compressor 5, described two-stage flash tank 4
Dimethyl ether outlet connects the import of condenser 6.
The outlet of described compressor 5 connects the steam import of condenser 6, the moisture outlet of described condenser 6
Connect the import of compressor 5.
Described condenser 6 has dimethyl ether outlet and outlet；The dimethyl ether outlet of described condenser 6 connects
The dimethyl ether import of dimethyl ether storage tank 2.
It is provided with between dimethyl ether outlet and the dimethyl ether import of material dewatering tank 1 of described dimethyl ether storage tank 2
First pump 7.
It is provided with second between dimethyl ether outlet and the dimethyl ether import of dimethyl ether storage tank 2 of described condenser 6
Pump 8.
It is provided with filter 9 between dimethyl ether outlet and the import of condenser 6 of described two-stage flash tank 4.Two
Methyl ether is filtered by filter 9, and the dimethyl ether after filtration enters condenser 6.
Water-containing materials enters from the material inlet of material dewatering tank 1, and dimethyl ether enters material from dimethyl ether storage tank
Drain sump, is mixed with material by dimethyl ether, is extracted by the outer water of material and is dissolved in dimethyl ether, after dehydration
Material export away from the dehydrated material of material dewatering tank 1, aqueous dimethyl ether contains from material dewatering tank 1
The outlet of water dimethyl ether enters primary flash tank 3, through primary flash tank 3 and two-stage flash tank 4, relends pressing aid
Contracting machine 5 and condenser 6 condense, and the dimethyl ether of dehydration exports from the dimethyl ether of condenser 6 and is back to dimethyl ether storage
Tank 2 so that dimethyl ether reusable edible.
This utility model can be down to less than 10% by aqueous for coal, can be down to 30% by aqueous for 80% water-containing sludge
Below.Dimethyl ether after dehydration can be recycled.This utility model uses material without the method for intensification by water
Remove, energy-saving and environment-friendly.This utility model energy-conservation compared with traditional fuel thermal dehydration nearly 50%, floor space
Little, smokeless, relatively traditional heating drying and dehydrating clean environment firendly, meet national energy-saving and reduce discharging and environmental protection
Strategy.
With above-mentioned according to desirable embodiment of the present utility model for enlightenment, by above-mentioned description, relevant
Staff can carry out various change completely in the range of without departing from this utility model technological thought
And amendment.The content that the technical scope of this utility model is not limited in description, it is necessary to root
Its technical scope is determined according to right.
Claims (4)
1. a material dehydrating device, it is characterised in that: there is material dewatering tank (1), have dimethyl ether
Dimethyl ether storage tank (2), primary flash tank (3), two-stage flash tank (4), compressor (5), condenser (6),
Described material dewatering tank (1) have material inlet, dimethyl ether import, dehydrated material outlet, aqueous two
Methyl ether exports, and the dimethyl ether outlet of described dimethyl ether storage tank (2) connects the dimethyl ether of material drain sump (1)
Import；
The aqueous dimethyl ether outlet of described material dewatering tank (1) connects the import of primary flash tank (3), institute
The moisture outlet stating primary flash tank (3) connects the import of compressor (5), described primary flash tank (3)
Dimethyl ether outlet connect two-stage flash tank (4) import；
The moisture outlet of described two-stage flash tank (4) connects the import of compressor (5), described two-stage flash
The dimethyl ether outlet of tank (4) connects the import of condenser (6)；
The outlet of described compressor (5) connects the steam import of condenser (6), described condenser (6)
Moisture outlet connects the import of compressor (5)；
Described condenser (6) has dimethyl ether outlet and outlet；The dimethyl ether of described condenser (6) goes out
Mouth connects the dimethyl ether import of dimethyl ether storage tank (2).
A kind of material dehydrating device the most according to claim 1, it is characterised in that: described dimethyl ether stores up
It is provided with the first pump (7) between dimethyl ether outlet and the dimethyl ether import of material dewatering tank (1) of tank (2).
A kind of material dehydrating device the most according to claim 1, it is characterised in that: described condenser (6)
Dimethyl ether outlet with the dimethyl ether import of dimethyl ether storage tank (2) between be provided with the second pump (8).
A kind of material dehydrating device the most according to claim 1, it is characterised in that: described two-stage flash
It is provided with filter (9) between dimethyl ether outlet and the import of condenser (6) of tank (4).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620387013.3U CN205607033U (en) | 2016-05-03 | 2016-05-03 | Material dewatering device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620387013.3U CN205607033U (en) | 2016-05-03 | 2016-05-03 | Material dewatering device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205607033U true CN205607033U (en) | 2016-09-28 |
Family
ID=56968948
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620387013.3U Expired - Fee Related CN205607033U (en) | 2016-05-03 | 2016-05-03 | Material dewatering device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205607033U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105972939A (en) * | 2016-05-03 | 2016-09-28 | 韩志学 | Material dehydration device |
-
2016
- 2016-05-03 CN CN201620387013.3U patent/CN205607033U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105972939A (en) * | 2016-05-03 | 2016-09-28 | 韩志学 | Material dehydration device |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN104230136A (en) | Sludge pyrohydrolysis joint vacuum flashing dehydration treatment method | |
| CN101824767A (en) | The recuperation of heat of waste cooking liquid in the chemical pulp mills boil house | |
| CN104832938B (en) | High-temperature flue gas recovery and heat energy utilization device and method for bamboo charcoal pyrolysis process | |
| CN1945181A (en) | Process and device for recovering and utilizing waste hot and wet air energy of drier | |
| CN108249733A (en) | A kind of low energy consumption municipal sludge heat treatment dehydration device and method | |
| CN205607033U (en) | Material dewatering device | |
| CN205627130U (en) | High -efficient chemical industry distiller | |
| CN105972939A (en) | Material dehydration device | |
| FI127386B (en) | A process for steam generation at a pulp mill digester | |
| CN203653407U (en) | Energy-saving sludge drying device using solar energy and afterheat | |
| CN205869055U (en) | Energy device is practiced thrift to reutilization steam | |
| CN204662174U (en) | A kind of drying cylinder high-efficiency steam cyclic utilization system | |
| CN207159697U (en) | A kind of paper machine steam and condensate system for ultrathin release raw paper | |
| CN205402666U (en) | Can be with room that evaporates of steam waste heat recovery utilization | |
| CN206276399U (en) | A kind of preparation system of giantreed biomass carbon adsorbent | |
| CN204569884U (en) | A kind of Wort boiling system of reusable edible secondary steam | |
| CN211170400U (en) | Solid waste drying device | |
| CN102492555B (en) | Method and device for high-efficiency energy-saving desolvation of fossilized animal/plant wax-containing solution | |
| CN207850110U (en) | A kind of steam condensate recovering device | |
| CN209145665U (en) | A kind of steam feed pump system of combination biomass combustion heat source | |
| CN205077315U (en) | Evaporation passivation flash steam recycling system | |
| CN205613066U (en) | A MVR vapor recompression equipment that is used for 6 polymerization monomers of nylon to retrieve | |
| CN206199300U (en) | A kind of system for preparing giantreed biomass adsorbent | |
| CN110526543A (en) | A kind of system and method coupling coal-fired incineration disposal suitable for sludge | |
| CN203741204U (en) | Indirect drum sludge dryer |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160928 Termination date: 20200503 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |