CN208635532U - Activated carbon raw material drying equipment - Google Patents
Activated carbon raw material drying equipment Download PDFInfo
- Publication number
- CN208635532U CN208635532U CN201821283765.0U CN201821283765U CN208635532U CN 208635532 U CN208635532 U CN 208635532U CN 201821283765 U CN201821283765 U CN 201821283765U CN 208635532 U CN208635532 U CN 208635532U
- Authority
- CN
- China
- Prior art keywords
- raw material
- drier
- activated carbon
- cyclone separator
- hot gas
- 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.)
- Active
Links
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 title claims abstract description 267
- 239000002994 raw material Substances 0.000 title claims abstract description 152
- 238000001035 drying Methods 0.000 title claims abstract description 39
- 239000000463 material Substances 0.000 claims description 29
- 229910052799 carbon Inorganic materials 0.000 claims description 23
- 238000000926 separation method Methods 0.000 claims description 9
- 230000000694 effects Effects 0.000 claims description 7
- 238000004519 manufacturing process Methods 0.000 description 5
- 238000000034 method Methods 0.000 description 5
- 238000002156 mixing Methods 0.000 description 4
- 238000002360 preparation method Methods 0.000 description 3
- 238000010438 heat treatment Methods 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 230000004913 activation Effects 0.000 description 1
- 238000001994 activation Methods 0.000 description 1
- 239000003463 adsorbent Substances 0.000 description 1
- 239000003610 charcoal Substances 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 230000001627 detrimental effect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 238000005485 electric heating Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
Landscapes
- Carbon And Carbon Compounds (AREA)
Abstract
The utility model provides a kind of activated carbon raw material drying equipment, comprising: the first drier, the first cyclone separator, the second drier, the second cyclone separator, hot gas stream generating apparatus and feed device；First drier, the first cyclone separator, the second drier and the second cyclone separator pass sequentially through pipeline connection, first drier has hot gas inflow entrance and the first feed(raw material)inlet, hot gas stream generating apparatus is connected to the hot gas inflow entrance of the first drier, second cyclone separator has hot gas outflux, the hot gas for being fed from hot gas stream generating apparatus flows through the hot gas inflow entrance inflow of the first drier, followed by the first cyclone separator, the second drier and the second cyclone separator, and exports and flow out from the thermal current of the second cyclone separator；Activated carbon raw material drying equipment provided by the utility model can be improved the drying efficiency and dry mass of activated carbon raw material, while more energy saving.
Description
Technical field
The utility model relates to Activated Carbon Production fields, more particularly to a kind of activated carbon raw material drying equipment.
Background technique
Active carbon is a kind of adsorbent material of pore structure prosperity, it has, and adsorption capacity is strong, chemical stability is good, mechanics
The features such as intensity is high is widely used in production, in life.Activated carbon raw material is generally by charing, cooling, activation, washing
Etc. series of processes be made, start active carbon preparation process before, need that activated carbon raw material is dried.Whole
In a process for preparing active carbon, activated carbon raw material drying is a most basic feedstock processing process, while being also processing daily
Measure maximum process.Currently, the drying of activated carbon raw material is completed using rotary furnace, and rotary furnace is a powerful work
Property charcoal Preparation equipment, not only have a function of dried active carbon feedstock, while charing and living can also be completed in active carbon preparation
The production process of change.The dry work of a large amount of activated carbon raw material, which is carried out, using rotary furnace daily is highly detrimental to equipment use cost
Control, the production efficiency of active carbon will be directly affected.
Utility model content
The purpose of this utility model is the problem low for current activated carbon raw material drying efficiency, provides a kind of drying effect
More preferably, more efficient activated carbon raw material drying equipment.
To achieve the goals above, the utility model provides a kind of activated carbon raw material drying equipment, the drying equipment
Include: the first drier, the first cyclone separator, the second drier, the second cyclone separator, hot gas stream generating apparatus and send
Expect device；
The hot gas stream generating apparatus is used to generate the thermal current and the conveying thermal current of the first preset temperature；
First drier, first cyclone separator, second drier and second cyclone separator
Pipeline connection is passed sequentially through, first drier has hot gas inflow entrance and the first feed(raw material)inlet, and the thermal current generates dress
It sets and is connected to the hot gas inflow entrance of first drier, second cyclone separator has hot gas outflux, is fed from institute
The hot gas for stating hot gas stream generating apparatus flows through the hot gas inflow entrance inflow of first drier, followed by described first
Cyclone separator, second drier and second cyclone separator, and from the thermal current of second cyclone separator
Outlet outflow；
Second drier has the second feed(raw material)inlet, and the active carbon for will be entered by second feed(raw material)inlet is former
Expect to be mixed with the thermal current for flowing through second drier living to form the first dryer section up to the second preset time period
Property carbon feedstock is simultaneously blowed the first dryer section activated carbon raw material to second cyclone separator by the thermal current；
Second cyclone separator has the second material outlet, and second cyclone separator is used for from the thermal current
In isolate the first dryer section activated carbon raw material and the first dryer section activated carbon raw material isolated is former through described second
Material outlet discharge；
The feed device respectively with the first feed(raw material)inlet of first drier and second cyclone separator
Second material outlet connection, for passing through the first dryer section activated carbon raw material isolated being discharged from second material outlet
First feed(raw material)inlet is delivered in first drier；
First drier be used for by the first dryer section activated carbon raw material isolated from the feed device with
The thermal current flowed into through the hot gas inflow entrance is mixed up to the first preset time period to form the second dryer section activity
Carbon feedstock, and blowed the second dryer section activated carbon raw material to first cyclone separator by the thermal current；
First cyclone separator has the first material outlet, dry for isolating described second from the thermal current
Simultaneously the second dryer section activated carbon raw material isolated is discharged through first material outlet for dry section of activated carbon raw material.
Preferably, the drying equipment further includes feeding device, and the feeding device includes hopper and feeding conveyor, institute
The feeding inlet for stating feeding conveyor is connected to the hopper, and the of the discharge port of the feeding conveyor and second drier
The connection of two feed(raw material)inlets.
Preferably, the feeding conveyor includes rectangular housing and screw conveyor shaft, and the screw conveyor shaft is installed in institute
It states in rectangular housing and parallel with the bottom surface of near end in the rectangular housing.
Preferably, the feed device includes the first conveyer and second conveyor, first conveyer and second defeated
Machine is sent to be vertically arranged, the feeding inlet of first conveyer is connected to the second material outlet of second cyclone separator, institute
The discharge port for stating the first conveyer is connected with the feeding inlet of the second conveyor, the discharge port of the second conveyor with it is described
First feed(raw material)inlet of the first cyclone separator connects.
Preferably, first preset temperature is 180 DEG C -200 DEG C.
Preferably, first preset time period is 2-8 seconds, and second preset time period is 2-8 seconds.
Activated carbon raw material drying equipment provided by the utility model does activated carbon raw material using double dryer configurations
It is dry, specifically, the second drier and the second cyclone separator using flow through the thermal current of the second drier to activated carbon raw material into
The hot gas isolated in the step of row preliminarily dried, thermal current used in preliminarily dried is from final dried active carbon feedstock
Stream, activated carbon raw material form the first dryer section activated carbon raw material after preliminarily dried and by described in the separation of the second cyclone separator
Thermal current and the first dryer section activated carbon raw material convey the first dryer section activated carbon raw material isolated by feed device
To the first drier, the first dryer section activated carbon raw material flows into pre- with first in the first drier and by hot gas inflow entrance
If the thermal current of temperature carries out becoming the second dryer section activated carbon raw material after mixing reaches the first preset time period, described second is dry
Dry section of activated carbon raw material is blown into the first cyclone separator via thermal current, and described is separated in first cyclone separator
Two dryer section activated carbon raw materials and thermal current, the second dryer section activated carbon raw material isolated are discharged by the first material outlet, and
The hot gas isolated flows through pipeline to the second drier, provides thermal current for preliminarily dried, this double driers of use are dry
The mode of dry activated carbon raw material accelerates the drying efficiency and dry mass of activated carbon raw material, and final dried active carbon feedstock
Activated carbon raw material of the thermal current isolated again to be newly added carries out preliminarily dried and provides heat source, and entire drying process has saved energy
Source improves efficiency.Activated carbon raw material drying equipment provided by the utility model and the dry effect that can be improved activated carbon raw material
Rate and dry mass, at the same it is more energy saving.
Other features and advantages of the utility model will the following detailed description will be given in the detailed implementation section.
Detailed description of the invention
Attached drawing is and to constitute part of specification for providing further understanding of the present application, with following tool
Body embodiment is used to explain the application together, but does not constitute the limitation to the application.In the accompanying drawings:
Fig. 1 is the structural schematic diagram of activated carbon raw material drying equipment provided by the embodiment of the utility model.
Description of symbols
10 first drier, 20 first cyclone separator
30 second drier, 40 second cyclone separator
50 hot gas stream generating apparatus, 60 feed device
61 first conveyer, 62 second conveyor
70 feeding device, 71 hopper
72 feeding conveyors
Specific embodiment
It is described in detail below in conjunction with specific embodiment of the attached drawing to the utility model embodiment.It should be understood that
It is that specific embodiment described herein is merely to illustrate and explains the utility model embodiment is not limited to this reality
Use new embodiment.
As shown in Figure 1, the utility model embodiment provides a kind of activated carbon raw material drying equipment, the drying equipment packet
It includes: the first drier 10, the first cyclone separator 20, the second drier 30, the second cyclone separator 40, hot gas stream generating apparatus
50 and feed device 60；
The hot gas stream generating apparatus 50 is used to generate the thermal current and the conveying thermal current of the first preset temperature；
First drier 10, first cyclone separator 20, second drier 30 and second whirlwind
Separator 40 passes sequentially through pipeline connection, and first drier 10 has hot gas inflow entrance and the first feed(raw material)inlet, the heat
Gas flow generating device 50 is connected to the hot gas inflow entrance of first drier 10, and second cyclone separator 40 has hot gas
Outflux, the hot gas for being fed from the hot gas stream generating apparatus 50 flow through the hot gas inflow entrance stream of first drier 10
Enter, followed by first cyclone separator 20, second drier 30 and second cyclone separator 40, and from institute
State the thermal current outlet outflow of the second cyclone separator 40；
Second drier 30 has the second feed(raw material)inlet, the active carbon for will be entered by second feed(raw material)inlet
Raw material is mixed dry to form first up to the second preset time period with the thermal current for flowing through second drier 30
Section activated carbon raw material is simultaneously blowed the first dryer section activated carbon raw material to second cyclonic separation by the thermal current
Device 40；
Second cyclone separator 40 has the second material outlet, and second cyclone separator 40 is used for from the heat
The first dryer section activated carbon raw material is isolated in air-flow and by the first dryer section activated carbon raw material isolated through described
The discharge of two material outlets；
The feed device 60 respectively with the first feed(raw material)inlet of first drier 10 and second cyclonic separation
Second material outlet of device 40 is connected to, the first dryer section active carbon isolated for will be discharged from second material outlet
Raw material is delivered in first drier 10 through first feed(raw material)inlet；
First drier 10 is used for will be former from the first dryer section active carbon of the feed device 60 isolated
Material is mixed up to the first preset time period with the thermal current flowed into through the hot gas inflow entrance to form the second dryer section
Activated carbon raw material, and blowed the second dryer section activated carbon raw material to first cyclone separator by the thermal current
20；
First cyclone separator 20 has the first material outlet, for isolating described second from the thermal current
Simultaneously the second dryer section activated carbon raw material isolated is discharged through first material outlet for dryer section activated carbon raw material.
Activated carbon raw material drying equipment provided by the utility model carries out activated carbon raw material using the structure of double driers
It dries twice, specifically, hot gas inflow entrance is provided on the first drier 10, the second raw material is provided on the second drier 30 and enters
Mouthful, activated carbon raw material is dried in two times in entire activated carbon raw material drying process, thermal current is from the first drier 10
Hot gas inflow entrance enter, followed by the first drier 10, the first cyclone separator 20, the second drier 30 and the second whirlwind
Separator 40 is finally exported from the thermal current of the second cyclone separator 40 and is flowed out, when thermal current flows through the second drier 30, heat
The temperature of air-flow can be declined, using flowing through the thermal current of the second drier 30 to the active carbon entered from the second feed(raw material)inlet
Raw material carries out preliminarily dried, and activated carbon raw material becomes the first dryer section activated carbon raw material after the completion of preliminarily dried, and described first
Dryer section activated carbon raw material is blowed by the thermal current for flowing through the second drier 30 to the second cyclone separator 40, the second cyclonic separation
Device 40 isolates the first dryer section activated carbon raw material and by the first dryer section activated carbon raw material isolated from from thermal current
Second material outlet of two cyclone separators 40 is discharged, and the first dryer section activated carbon raw material isolated is conveyed through feed device 60
To the first drier 10, the thermal current isolated is discharged from the hot gas outflux of the second cyclone separator 40, is delivered to first
The the first dryer section activated carbon raw material isolated in drier 10 and the heat from the inflow of the hot gas inflow entrance of the first drier 10
Air-flow is sufficiently mixed, and the hot stream temperature flowed at this time from hot gas inflow entrance is the first preset temperature, in order to ensure activity
Carbon feedstock is sufficiently dry, it is preferable that first preset temperature is 180 DEG C -200 DEG C, the heat with first preset temperature
Air-flow is directly from the hot gas stream generating apparatus 50, the first dryer section activated carbon raw material isolated and the thermal current
Become the second dryer section activated carbon raw material after being sufficiently mixed the first preset time period under the first preset temperature, described second is dry
Section activated carbon raw material is blown into first cyclone separator 20 through the thermal current, and first cyclone separator 20 will flow into
Thermal current and the second dryer section activated carbon raw material separation, the second dryer section activated carbon raw material isolated is through the first raw material
Outlet discharge, the hot gas isolated flow through pipeline to the second drier 30, are delivered to the thermal current of the second drier 30 i.e.
It is isolated for the preliminarily dried of activated carbon raw material from the first cyclone separator 20 for the thermal current for flowing through the second drier 30
Thermal current be once used for dry the first dryer section activated carbon raw material isolated, the thermal current that heat can lose, therefore isolate
Temperature can be declined, and in order to further utilize the residual temperature for the thermal current isolated from the first cyclone separator 20, utilize tool
There is the thermal current of residual temperature first to carry out preliminarily dried to the activated carbon raw material being sent into the second drier 30, is more conducive to energy section in this way
About, while the drying efficiency and dry mass of activated carbon raw material can also be improved.
In one embodiment, the hot gas stream generating apparatus 50 includes liquefaction gas burning furnace and air-introduced machine, the liquid
Change gas burning furnace to be used to generate thermal current by burning liquid gas, when the hot stream temperature reaches the first preset temperature (first
Preset temperature is preferably 180 DEG C -200 DEG C) after, the thermal current of generation is blown into the heat of the first drier 10 using air-introduced machine
Air flow inlet；In another embodiment, the hot gas stream generating apparatus 50 includes electric heater and blower, the electric heating
Device heating flows through the air of electric heater and is introduced the air of heating in the first drier 10 with blower, and introduced adds
The air of heat is for the dry first segment dryer section activated carbon raw material isolated.
In one embodiment, second drier 30 includes the second column feed bin, in the second column feed bin
Side wall is provided with the second air intake vent, and the second air intake vent is connected to the first cyclone separator 20 by pipeline, and thermal current passes through pipeline
Into the second column feed bin, the second column feed bin top (distal end apart from ground) is provided with the second drier discharge port,
The second column feed bin inner cavity is formed with spiral volute passage, and the starting point of the spiral volute passage is described second
Air intake vent, the spiral volute passage form tubular structure, and the end of the spiral volute passage to inherent spiral center
End is connected to the tubular structure, and the spiral volute passage is the second swirl air-distribution band, is entered from the second air intake vent
Thermal current, which is blown, to be advanced by the activated carbon raw material of the second feed(raw material)inlet entrance of the second drier 30 along spiral channel, preceding
Heat exchange is completed to which the dry activated carbon raw material obtains by constantly mixing with activated carbon raw material into thermal current in the process
First dryer section activated carbon raw material, thermal current drives the first dryer section activated carbon raw material to enter the second cyclone separator 40, described
Second cyclone separator 40 is tubular, and outer wall tangential direction is provided with second entrance in second cyclone separator 40,
The first dryer section activated carbon raw material of thermal current carrying, which is tangentially entered inside the second cyclone separator 40 by second entrance, forms rotation
Movement, the first dryer section activated carbon raw material has biggish centrifugal inertial force under the drive of thermal current, in the effect of centrifugal force
Lower to separate the first dryer section activated carbon raw material from thermal current, the first dryer section activated carbon raw material isolated is from second
Second material outlet of cyclone separator 40 is discharged, and the hot gas isolated flows through thermal current outlet discharge, and first isolated is dry
Dry section of activated carbon raw material is transported to the first drier 10 through feed device 60, and first drier 10 includes the first column material
Storehouse is provided with hot gas inflow entrance in the side wall of the first column feed bin, and the first column feed bin top is (apart from the remote of ground
End) it is provided with the first drier discharge port, the first column feed bin inner cavity is formed with spiral volute passage, described spiral
The starting point of volute passage is the hot gas inflow entrance, and the spiral volute passage forms tubular knot to inherent spiral center
Structure, and the end of the spiral volute passage is connected to the tubular structure, the spiral volute passage is the first rotation
Wind band is spread, the thermal current entered from hot gas inflow entrance is blown to be isolated by what the first feed(raw material)inlet of the first drier 10 entered
The first dryer section activated carbon raw material and advance along spiral channel, during advance with the first preset temperature hot gas
Stream completes heat exchange by constantly mixing with the first dryer section activated carbon raw material isolated to isolate described in drying
First dryer section activated carbon raw material obtains the second dryer section activated carbon raw material, thermal current drive the second dryer section activated carbon raw material into
Enter the first cyclone separator 10, first cyclone separator 20 is tubular, in first cyclone separator 20 along outer wall
Tangential direction is provided with first entrance, and thermal current carries the second dryer section activated carbon raw material and tangentially enters the first rotation by first entrance
Rotary motion is formed inside wind separator 20, the second dryer section activated carbon raw material has biggish inertia under the drive of thermal current
Centrifugal force is under the influence of centrifugal force separated the second dryer section activated carbon raw material, second isolated from thermal current
Dryer section activated carbon raw material is discharged from the first material outlet of the first cyclone separator 20, and the hot gas isolated flows through pipeline
The preliminarily dried of activated carbon raw material is used for the second drier 30.
In order to control the feeding speed of activated carbon raw material, it is preferable that the drying equipment further includes feeding device 70, described
Feeding device 70 includes hopper 71 and feeding conveyor 72, and the feeding inlet of the feeding conveyor 72 is connected to the hopper 71,
The discharge port of the feeding conveyor 72 is connected to the second feed(raw material)inlet of second drier 30.
In one embodiment, the hopper 71 be the shell with big opening end and small open end, the small beginning with
The feeding inlet of the feeding conveyor 72 is connected to, and activated carbon raw material pours into hopper 71 from the big opening end, this up big and down small
Structure can control from the feeding inlet of feeding conveyor 72 enter activated carbon raw material speed.Activated carbon raw material enters charging
Conveyer 72, it is dry that activated carbon raw material is transported to second by second feed(raw material)inlet of the feeding conveyor 72 through the second drier 30
In dry device 30, for the ease of the conveying of activated carbon raw material, it is preferable that the feeding conveyor 72 includes rectangular housing and spiral transferring
Axis is sent, the screw conveyor shaft is installed in the rectangular housing and parallel with the bottom surface of near end in the rectangular housing.
Preferably, the feed device 60 includes the first conveyer 61 and second conveyor 62, first conveyer 61
It is vertically arranged with second conveyor 62, the second original of the feeding inlet of first conveyer 61 and second cyclone separator 40
Expect that outlet, the discharge port of first conveyer 61 are connected with the feeding inlet of the second conveyor 62, described second is defeated
The discharge port of machine 62 and the first feed(raw material)inlet of first cyclone separator 20 is sent to connect.
In one embodiment, first conveyer 61 and the second conveyor 62 include feeding shell and at least
A piece screw conveyor shaft.
In order to ensure the activated carbon raw material is sufficiently dried, it is preferable that first preset time period is 2-8 seconds,
Second preset time period is 2-8 seconds.
Activated carbon raw material drying equipment provided by the utility model does activated carbon raw material using double dryer configurations
It is dry, specifically, the second drier and the second cyclone separator using flow through the thermal current of the second drier to activated carbon raw material into
In the step of row preliminarily dried, thermal current used in preliminarily dried is from the final dried active carbon feedstock of activated carbon raw material point
The thermal current separated out, activated carbon raw material form the first dryer section activated carbon raw material after preliminarily dried and by the second cyclonic separations
Device separates the thermal current and the first dryer section activated carbon raw material, conveys the first dryer section isolated by feed device
To the first drier, the first dryer section activated carbon raw material isolated flows into the first drier with by hot gas activated carbon raw material
The thermal current with the first preset temperature that mouth flows into live after mixing reaches the first preset time period as the second dryer section
Property carbon feedstock, the second dryer section activated carbon raw material is blown into the first cyclone separator via thermal current, in first rotation
Separation the second dryer section activated carbon raw material and thermal current in wind separator, the second dryer section activated carbon raw material isolated by
The discharge of first material outlet, and the hot gas isolated flows through pipeline to the second drier, provides thermal current for preliminarily dried,
It is this to accelerate the drying efficiency and dry mass of activated carbon raw material by the way of double drier dried active carbon feedstocks, and
Activated carbon raw material of the thermal current that final dried active carbon feedstock is isolated again to be newly added carries out preliminarily dried and provides heat source, whole
A drying process has saved the energy and has improved efficiency.Activated carbon raw material drying equipment provided by the utility model can be improved activity
The drying efficiency and dry mass of carbon feedstock, at the same it is more energy saving.
Preferred embodiments of the present invention, still, the utility model and unlimited are described in detail in conjunction with attached drawing above
Detail in above embodiment can be to the skill of the utility model in the range of the technology design of the utility model
Art scheme carries out a variety of simple variants, these simple variants belong to the protection scope of the utility model.
It is further to note that specific technical features described in the above specific embodiments, in not lance
In the case where shield, it can be combined in any appropriate way.In order to avoid unnecessary repetition, the utility model is to each
No further explanation will be given for the possible combination of kind.
In addition, any combination can also be carried out between a variety of different embodiments of the application, as long as it is without prejudice to originally
The thought of application equally should be considered as content disclosed in the present application.
Claims (6)
1. a kind of activated carbon raw material drying equipment, which is characterized in that the drying equipment includes: the first drier (10), first
Cyclone separator (20), the second drier (30), the second cyclone separator (40), hot gas stream generating apparatus (50) and feeding dress
Set (60)；
The hot gas stream generating apparatus (50) is used to generate the thermal current and the conveying thermal current of the first preset temperature；
First drier (10), first cyclone separator (20), second drier (30) and second rotation
Wind separator (40) passes sequentially through pipeline connection, and first drier (10) has hot gas inflow entrance and the first feed(raw material)inlet,
The hot gas stream generating apparatus (50) is connected to the hot gas inflow entrance of first drier (10), second cyclone separator
(40) there is hot gas outflux, the hot gas for being fed from the hot gas stream generating apparatus (50) flows through first drier
(10) hot gas inflow entrance flows into, followed by first cyclone separator (20), second drier (30) and described
Second cyclone separator (40), and export and flow out from the thermal current of second cyclone separator (40)；
Second drier (30) has the second feed(raw material)inlet, and the active carbon for will be entered by second feed(raw material)inlet is former
Expect to be mixed with the thermal current for flowing through second drier (30) dry to form first up to the second preset time period
Section activated carbon raw material is simultaneously blowed the first dryer section activated carbon raw material to second cyclonic separation by the thermal current
Device (40)；
Second cyclone separator (40) has the second material outlet, and second cyclone separator (40) is used for from the heat
The first dryer section activated carbon raw material is isolated in air-flow and by the first dryer section activated carbon raw material isolated through described
The discharge of two material outlets；
The feed device (60) respectively with the first feed(raw material)inlet of first drier (10) and second cyclonic separation
Second material outlet of device (40) is connected to, the first dryer section activity isolated for will be discharged from second material outlet
Carbon feedstock is delivered in first drier (10) through first feed(raw material)inlet；
The first dryer section active carbon isolated of first drier (10) for that will come from the feed device (60) is former
Material is mixed up to the first preset time period with the thermal current flowed into through the hot gas inflow entrance to form the second dryer section
Activated carbon raw material, and blowed the second dryer section activated carbon raw material to first cyclone separator by the thermal current
(20)；
First cyclone separator (20) has the first material outlet, dry for isolating described second from the thermal current
Simultaneously the second dryer section activated carbon raw material isolated is discharged through first material outlet for dry section of activated carbon raw material.
2. drying equipment according to claim 1, which is characterized in that the drying equipment further includes feeding device (70),
The feeding device (70) includes hopper (71) and feeding conveyor (72), the feeding inlet of the feeding conveyor (72) with it is described
Second feed(raw material)inlet of hopper (71) connection, the discharge port of the feeding conveyor (72) and second drier (30) connects
It is logical.
3. drying equipment according to claim 2, which is characterized in that the feeding conveyor (72) include rectangular housing and
Screw conveyor shaft, the screw conveyor shaft are installed in the rectangular housing and put down with the bottom surface of near end in the rectangular housing
Row.
4. drying equipment according to claim 1, which is characterized in that the feed device (60) includes the first conveyer
(61) it is vertically arranged with second conveyor (62), first conveyer (61) with second conveyor (62), first conveying
The feeding inlet of machine (61) is connected to the second material outlet of second cyclone separator (40), first conveyer (61)
Discharge port is connected with the feeding inlet of the second conveyor (62), the discharge port of the second conveyor (62) and first rotation
First feed(raw material)inlet of wind separator (20) connects.
5. drying equipment according to claim 1, which is characterized in that first preset temperature is 180 DEG C -200 DEG C.
6. drying equipment according to claim 1, which is characterized in that first preset time period is 2-8 seconds, described the
Two preset time periods are 2-8 seconds.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821283765.0U CN208635532U (en) | 2018-08-09 | 2018-08-09 | Activated carbon raw material drying equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821283765.0U CN208635532U (en) | 2018-08-09 | 2018-08-09 | Activated carbon raw material drying equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN208635532U true CN208635532U (en) | 2019-03-22 |
Family
ID=65740036
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201821283765.0U Active CN208635532U (en) | 2018-08-09 | 2018-08-09 | Activated carbon raw material drying equipment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN208635532U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108775805A (en) * | 2018-08-09 | 2018-11-09 | 衢州市蓝天环保节能设备厂 | Activated carbon raw material drying equipment and drying means |
-
2018
- 2018-08-09 CN CN201821283765.0U patent/CN208635532U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108775805A (en) * | 2018-08-09 | 2018-11-09 | 衢州市蓝天环保节能设备厂 | Activated carbon raw material drying equipment and drying means |
| CN108775805B (en) * | 2018-08-09 | 2023-12-15 | 衢州市蓝天环保节能设备厂 | Active carbon raw material drying equipment and method |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN205156509U (en) | Rotatory flash drying system of combined thermal transmission formula | |
| CN204787600U (en) | Fluidized bed dryer | |
| CN203598502U (en) | Spray drying tower for preparing lithium iron phosphate positive electrode material | |
| CN203687563U (en) | Pneumatic drying device for material breaking | |
| CN205403417U (en) | Calcium hypochlorite flash drying equipment | |
| CN102997619A (en) | Nitrogen closed cycle drying method and device for drying polyacrylonitrile | |
| CN102788488A (en) | A high-speed centrifugal drying method and a drying system for implementing the method | |
| CN109780845A (en) | A kind of environment-friendly feed particle drying equipment | |
| CN205627126U (en) | Centrifugal spray drier is used in processing of blood cell albumen powder | |
| CN208635532U (en) | Activated carbon raw material drying equipment | |
| CN110411171A (en) | A kind of stagewise roller biomass dryer | |
| CN204648882U (en) | A kind of pulse type pneumatic drier | |
| CN204373318U (en) | A kind of Novel rotary flash dryer | |
| CN204594163U (en) | A kind of infrared drier for mine tailing flotation material | |
| CN204438701U (en) | A kind of granule materials drying unit | |
| CN206755752U (en) | Glutinous rice flour drying waste heat recovery system | |
| CN108775805A (en) | Activated carbon raw material drying equipment and drying means | |
| CN209302204U (en) | Drying machine with centrifugal spray | |
| CN202709675U (en) | Pneumatic drying system | |
| CN207585306U (en) | Regenerated carbon drying equipment | |
| CN205425621U (en) | Fluidized bed dryer automatic feed device | |
| CN203704551U (en) | Flake graphite drying device | |
| CN2775579Y (en) | High wet material drying unit | |
| CN207694277U (en) | For food, the small-sized centrifugal spray testing machine of Chinese medicine | |
| CN201819529U (en) | Material rotating dryer |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant |