CN208279324U - A kind of active carbon Preparation equipment - Google Patents
A kind of active carbon Preparation equipment Download PDFInfo
- Publication number
- CN208279324U CN208279324U CN201820556807.7U CN201820556807U CN208279324U CN 208279324 U CN208279324 U CN 208279324U CN 201820556807 U CN201820556807 U CN 201820556807U CN 208279324 U CN208279324 U CN 208279324U
- Authority
- CN
- China
- Prior art keywords
- active carbon
- preparation equipment
- carbon preparation
- gas
- carbonized
- 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
Abstract
The utility model provides a kind of active carbon Preparation equipment, which is characterized in that the active carbon Preparation equipment includes: heating device；It is arranged in the heating device and carries out to material multiple carbonizing apparatus of charing process；And centralized processor, wherein the heating device carries out concentration heating to the multiple carbonizing apparatus, and the centralized processor focuses on the substance generated after charing process.By the way that more external-heating revolving retorts are integrated in same heating furnace, more tail gas of carbonization stove share a set of processing system, can reach increase capacity usage ratio, reduce cost of investment, the purpose to reduce environmental pollution.
Description
Technical field
The utility model relates to a kind of active carbon Preparation equipment, the outer heat of especially a kind of Activated Carbon Production of multi-stove bodies parallel connection
Formula revolution charing furnace apparatus.
Background technique
In recent years, Environmental Protection in China situation is increasingly severe, and environmental emission standard is also more harsh therewith.It is promoting a conservation culture
Overall background under, the active carbon market demand that can be widely applied to air cleaning, sewage treatment etc. increases substantially.
Production process of activated carbon is divided into charing and two stages of activation, and rotary retort is most widely used charing side
One of formula.Currently, Activated Carbon Production enterprise of China belongs to medium-sized and small enterprises mostly, production scale of enterprise is little, every production line it
Between it is mutually indepedent, carbonization process generates a large amount of tail gas and tar brings serious problem of environmental pollution, what exhaust combustion generated
Energy still has residue that cannot but efficiently use in addition to supply drying and carbonization process itself.It is small to be limited to production scale, unit
Product cost is higher, therefore is equipped with complete tail gas and tar processing equipment and will increase dramatically entreprise cost.
It is turned round in Activated Carbon Production between retort production line at present independently of each other, vent gas treatment and energy utilization cannot be done
To centralized management, so that capacity usage ratio is low, high production cost, and cause certain environmental pollution.Meanwhile each charing revolution
Furnace body needs to carry out isothermal holding respectively, and overall occupied area is larger, causes certain wasting of resources.
It is, therefore, desirable to provide a kind of active carbon Preparation equipment, at least partly to solve the above problems.
Utility model content
In view of the deficiencies of the prior art, the utility model provides a kind of active carbon Preparation equipment, which is characterized in that the work
Property charcoal Preparation equipment includes:
Heating device；
It is arranged in the heating device and carries out to material multiple carbonizing apparatus of charing process；And
Centralized processor,
Wherein, the heating device carries out concentration heating to the multiple carbonizing apparatus, and the centralized processor is to charcoal
The substance generated after change processing is focused on.
In one example, the multiple carbonizing apparatus is disposed side by side in the heating device.
In one example, material carries out generating high-temperature flue gas after charing process in the multiple carbonizing apparatus, and one
The high-temperature flue gas is divided to be admitted in the heating device to heat the multiple carbonizing apparatus.
In one example, the multiple carbonizing apparatus includes multiple revolution retorts, and the heating device includes heating
Furnace.
In one example, it is provided with gas inlet and exhanst gas outlet on the heating furnace, it is described more after charing process
The high-temperature flue gas generated in a revolution retort enters in the heating furnace from gas inlet, and is arranged by the exhanst gas outlet
It is put into the outside of the heating furnace；
Close to the gas inlet, the other end is described close to the exhanst gas outlet for one end of the multiple revolution retort
Material enters in the multiple revolution retort and moves from one end close to the exhanst gas outlet of the multiple revolution retort
One end close to the gas inlet of the multiple revolution retort is moved,
Wherein, the flow direction of high-temperature flue gas and the flow direction of material are on the contrary, so that the material in the multiple revolution retort is first
Pre-heating drying processing and charing process are carried out afterwards.
In one example, the amount entered in the heating furnace by adjusting the high-temperature flue gas is come to the multiple charing
The carbonization temperature of device is controlled.
In one example, by the way that the tilt angle of the multiple revolution retort is arranged and/or adjusts the multiple time
Turn the revolving speed of retort to control the carbonization time of the charing process.
In one example, the material includes biological material, and the biological material is carbonized in the multiple revolution
Carbonization temperature in furnace is 500 DEG C -550 DEG C, carbonization time 30min-40min.
In one example, the centralized processor includes carbonized material centralized processor and carbonized gas centralized processing dress
It sets,
The carbonized material centralized processor carries out cooling treatment to the carbonized material generated after charing process；
The carbonized gas centralized processor carries out burning processing to the carbonized gas that charing process generates.
In one example, the carbonized material centralized processor includes water cooling heat exchanger, and material is in the multiple charing
It is transported in the water cooling heat exchanger and is cooled down after progress charing process in device；
The carbonized gas centralized processor includes dual firing chamber, and the carbonized gas that the charing process generates is transported to described
It burns in dual firing chamber.
The utility model provides a kind of active carbon Preparation equipment, and more charing rotary furnaces are integrated, and shares one and adds
Hot stove body carries out concentrated combustion, gas cleaning, UTILIZATION OF VESIDUAL HEAT IN to the tail gas that carbonization process generates, to be obviously improved system energy
Utilization rate is measured, reduces occupied area, and reduce environmental pollution.By the way that more external-heating revolving retorts are integrated in same heating
In furnace, more tail gas of carbonization stove share a set of processing system, can reach increase capacity usage ratio, reduce cost of investment, reduce ring
The purpose of border pollution.
Detailed description of the invention
The following drawings of the utility model is used to understand the utility model in this as a part of the utility model.Attached drawing
In show the embodiments of the present invention and its description, for explaining the principles of the present invention.
In attached drawing:
Fig. 1 is the structural schematic diagram of the active carbon Preparation equipment of one embodiment of the utility model.
Specific embodiment
In the following description, a large amount of concrete details are given more thoroughly to manage in order to provide to the utility model
Solution.It is, however, obvious to a person skilled in the art that the utility model may not need it is one or more of these thin
It saves and is carried out.In other examples, in order to avoid obscuring with the utility model, for more well known in the art
Technical characteristic is not described.
In order to thoroughly understand the utility model, detailed method and step and/or structure will be proposed in following description.It is aobvious
So, the execution of the utility model is not limited to specific details appreciated by those skilled in the art.The utility model compared with
Good embodiment is described in detail as follows, however other than these detailed descriptions, the utility model can also have other embodiments.
It should be understood that the utility model can be implemented in different forms, and should not be construed as being limited to mention here
Embodiment out.Disclosure will be made thoroughly and complete and the scope of the utility model is complete on the contrary, providing these embodiments
Ground passes to those skilled in the art.In the accompanying drawings, for clarity, the size and relative size in the area Ceng He may be exaggerated.
Same reference numerals indicate identical element from beginning to end.
It should be understood that when the term " comprising " and/or " including " is used in this specification, indicating described in presence
Feature, entirety, step, operation, element and/or component, but do not preclude the presence or addition of other one or more features, entirety,
Step, operation, element, component and/or their combination." one " of singular, "one" and " described/should " be also intended to
Plural form, unless the context clearly indicates other mode.
In existing Activated Carbon Production, turn round between retort production line independently of each other, vent gas treatment and energy utilization are not
It can accomplish to manage concentratedly, so that capacity usage ratio is low, high production cost, and cause certain environmental pollution.Meanwhile each charing
Revolution furnace body needs to carry out isothermal holding respectively, and overall occupied area is larger, causes certain wasting of resources.
The utility model provides a kind of active carbon Preparation equipment, and more charing rotary furnaces are integrated, and shares one and adds
Hot stove body carries out concentrated combustion, gas cleaning, UTILIZATION OF VESIDUAL HEAT IN to the tail gas that carbonization process generates, to be obviously improved system energy
Utilization rate is measured, reduces occupied area, and reduce environmental pollution.By the way that more external-heating revolving retorts are integrated in same heating
In furnace, more tail gas of carbonization stove share a set of processing system, can reach increase capacity usage ratio, reduce cost of investment, reduce ring
The purpose of border pollution.
As shown in Figure 1, the active carbon Preparation equipment 100 of the utility model includes heating furnace 110, is arranged in heating furnace 110
Interior multiple revolution retorts 120 and the centralized processor focused on to the substance generated after charing process are (in figure
It is not shown).Material carries out pre-heating drying and carbonization process in multiple revolution retorts 120.More charing rotary furnaces share one
A heating furnace body carries out concentrated combustion, gas cleaning, UTILIZATION OF VESIDUAL HEAT IN to the tail gas that carbonization process generates, to be obviously improved and be
System capacity usage ratio, reduces occupied area, and reduce environmental pollution.
In one example, multiple revolution retorts 120 are tubular and are arranged side by side, between multiple revolution retorts 120
It is not interfered mutually for parallel relationship that is, material carries out charing process in multiple revolution retorts 120 respectively.
Material generates high-temperature flue gas after being carbonized in multiple revolution retorts 120, and a part of high-temperature flue gas is admitted to
In heating furnace 110, to realize the heating to multiple revolution retorts 120.In this way, the heat utilization ratio of high-temperature flue gas also mentions significantly
Height avoids the waste of energy, while Economization on land, improves production capacity.
The control for being controlled to realize the carbonization temperature of charing process by adjusting the amount that high-temperature flue gas enters in heating furnace
System, by the way that the tilt angle of multiple revolution retorts is arranged and adjusts the revolving speed of multiple revolution retorts come the charcoal to charing process
The change time is controlled.Specifically, carbonization temperature is controlled by adjusting high-temperature flue gas charge flow rate, carbonization time is in furnace body
The inclination angle that adaptation is calculated is carried out when design, and is controlled to adjust in the process of running by adjusting rotary furnace revolving speed.One
In a example, material is biological material, and carbonization temperature of the material of biological material in multiple revolution retorts 120 is
500 DEG C -550 DEG C, carbonization time 30min-40min, in one example, carbonization temperature is 500 DEG C, and carbonization time is
30min。
In one example, gas inlet 111 and exhanst gas outlet 112 are provided on heating furnace 110, gas inlet 111 is set
It sets in one end of heating furnace 110, the other end of heating furnace 110 is arranged in exhanst gas outlet 112.After charing process, multiple revolutions
The high-temperature flue gas generated in retort 120 enters in heating furnace 110 from gas inlet 111, and is discharged by exhanst gas outlet 112
To outside heating furnace 110
Close to gas inlet 111, the other end of multiple revolution retorts 120 is close for one end of multiple revolution retorts 120
Exhanst gas outlet 112.Material enters multiple revolution retorts from one end of the close exhanst gas outlet 112 of multiple revolution retorts 120
In 120 and be moved to multiple revolution retorts 120 close gas inlets 111 one end, the flow direction of high-temperature flue gas and material
Flow direction is on the contrary, this makes the material in multiple revolution retorts 120 successively carry out pre-heating drying processing and charing process.
Centralized processor includes carbonized material centralized processor and carbonized gas centralized processor, carbonized material centralized processing
Device carries out cooling treatment to the carbonized material generated after charing process；The charcoal that carbonized gas centralized processor generates charing process
Change gas and carries out burning processing.
In one example, carbonized material centralized processor includes water cooling heat exchanger, and material is in multiple revolution retorts
It is transported in water cooling heat exchanger and is cooled down after being carbonized.Carbonized gas centralized processor includes dual firing chamber, carbonization process
The carbonized gas of generation, which is transported in dual firing chamber, to burn.It, can be by gained carbonized material after charing due to this intensive arrangement
It is delivered in a water cooling heat exchanger and is cooled down, saved equipment and occupied area, and be convenient for subsequent processing.Carbonized gas simultaneously
It is transported in the same dual firing chamber and burns, gained high-temperature flue gas a part gas inlet 111 from figure, which enters heating furnace, to be tieed up
It holds reaction to carry out, remainder is discharged after gas cleaning by waste heat boiler.Such intensive style arrangement makes to produce energy
Power improves, and equipment simplifies.
The advantages of the utility model:
1, the charing link in Activated Carbon Production is arranged in the utility model.The system not yet starts to walk at home, at present state
A plurality of production line is mostly mutually indepedent in interior Activated Carbon Production；
2, this system shares the structure of a heating furnace by multiple rotary retort parallel connections, makes entire fume treatment ring
Section, carbonized material cooling treatment link are simplified, while the heat utilization ratio of high-temperature flue gas also greatly improves, and avoids energy
Waste, while Economization on land improve production capacity.
The utility model provides a kind of active carbon Preparation equipment, and more charing rotary furnaces are integrated, and shares one and adds
Hot stove body carries out concentrated combustion, gas cleaning, UTILIZATION OF VESIDUAL HEAT IN to the tail gas that carbonization process generates, to be obviously improved system energy
Utilization rate is measured, reduces occupied area, and reduce environmental pollution.By the way that more external-heating revolving retorts are integrated in same heating
In furnace, more tail gas of carbonization stove share a set of processing system, can reach increase capacity usage ratio, reduce cost of investment, reduce ring
The purpose of border pollution.
The similar replacement or deformation of individual part or component in this practical active carbon Preparation equipment each fall within this reality
Within novel protection scope.
The utility model is illustrated through the foregoing embodiment, but it is to be understood that, above-described embodiment is
Purpose for illustrating and illustrating, and be not intended to limit the invention within the scope of described embodiment.Furthermore ability
Field technique personnel are it is understood that the utility model is not limited to above-described embodiment, and introduction according to the present utility model is also
More kinds of variants and modifications can be made, these variants and modifications all fall within the utility model range claimed with
It is interior.The protection scope of the utility model is defined by the appended claims and their equivalents.
Claims (10)
1. a kind of active carbon Preparation equipment, which is characterized in that the active carbon Preparation equipment includes:
Heating device；
It is arranged in the heating device and carries out to material multiple carbonizing apparatus of charing process；And
Centralized processor,
Wherein, the heating device carries out concentration heating to the multiple carbonizing apparatus, the centralized processor to charing at
The substance generated after reason is focused on.
2. active carbon Preparation equipment according to claim 1, which is characterized in that the multiple carbonizing apparatus is disposed side by side on
In the heating device.
3. active carbon Preparation equipment according to claim 2, which is characterized in that material in the multiple carbonizing apparatus into
High-temperature flue gas is generated after row charing process, a part of high-temperature flue gas is admitted to the multiple to heat in the heating device
Carbonizing apparatus.
4. active carbon Preparation equipment according to claim 3, which is characterized in that the multiple carbonizing apparatus includes multiple times
Turn retort, the heating device includes heating furnace.
5. active carbon Preparation equipment according to claim 4, which is characterized in that be provided with gas inlet on the heating furnace
And exhanst gas outlet, after charing process, the high-temperature flue gas generated in the multiple revolution retort enters institute from gas inlet
It states in heating furnace, and discharge the outside of the heating furnace by the exhanst gas outlet；
One end of the multiple revolution retort is close to the gas inlet, and the other end is close to the exhanst gas outlet, the material
Enter in the multiple revolution retort and be moved to from one end close to the exhanst gas outlet of the multiple revolution retort
One end close to the gas inlet of the multiple revolution retort,
Wherein, the flow direction of high-temperature flue gas and the flow direction of material are on the contrary, so that the material in the multiple revolution retort is first laggard
The processing of row pre-heating drying and charing process.
6. active carbon Preparation equipment according to claim 4, which is characterized in that enter institute by adjusting the high-temperature flue gas
The amount in heating furnace is stated to control the carbonization temperature of the multiple carbonizing apparatus.
7. active carbon Preparation equipment according to claim 4, which is characterized in that by the way that the multiple revolution retort is arranged
Tilt angle and/or the revolving speed of the multiple revolution retort of adjustment the carbonization time of the charing process controlled
System.
8. active carbon Preparation equipment according to claim 4, which is characterized in that the material includes biological material, institute
Stating carbonization temperature of the biological material in the multiple revolution retort is 500 DEG C -550 DEG C, carbonization time 30min-
40min。
9. active carbon Preparation equipment according to claim 1, which is characterized in that the centralized processor includes carbonized material
Centralized processor and carbonized gas centralized processor,
The carbonized material centralized processor carries out cooling treatment to the carbonized material generated after charing process；
The carbonized gas centralized processor carries out burning processing to the carbonized gas that charing process generates.
10. active carbon Preparation equipment according to claim 9, which is characterized in that the carbonized material centralized processor packet
Include water cooling heat exchanger, material carry out being transported in the water cooling heat exchanger after charing process in the multiple carbonizing apparatus into
Row cooling；
The carbonized gas centralized processor includes dual firing chamber, and the carbonized gas that the charing process generates is transported to two combustion
It burns in room.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820556807.7U CN208279324U (en) | 2018-04-18 | 2018-04-18 | A kind of active carbon Preparation equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820556807.7U CN208279324U (en) | 2018-04-18 | 2018-04-18 | A kind of active carbon Preparation equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN208279324U true CN208279324U (en) | 2018-12-25 |
Family
ID=64751405
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201820556807.7U Active CN208279324U (en) | 2018-04-18 | 2018-04-18 | A kind of active carbon Preparation equipment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN208279324U (en) |
-
2018
- 2018-04-18 CN CN201820556807.7U patent/CN208279324U/en active Active
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN103708452B (en) | A kind of autothermal continuously carbonizing activation working method of biomass and device thereof | |
| CN106044767B (en) | A kind of carbonization-activation integral processing unit (plant) and its processing method | |
| CN103409155B (en) | Multi-tube rotary furnace and method for performing low-temperature carbonization on materials by using multi-tube rotary furnace | |
| CN103224234B (en) | Process for producing active carbon by cyclic utilization of high temperature flue gas | |
| CN102226092A (en) | Continuous biomass low-temperature pyrolytic charring method and charring furnace thereof | |
| CN108217649B (en) | A kind of coal activated carbon furnace preparing active carbon method | |
| CN105621410B (en) | A kind of process for preparing activated carbon | |
| CN104121591B (en) | A kind of efficient energy-saving incinerator | |
| CN205528594U (en) | Continuous retort of multilayer | |
| CN110775975A (en) | Furnace tube fixed type active carbon drying and regenerating integrated furnace | |
| CN108559538A (en) | A kind of biomass pyrolysis furnace | |
| CN201892206U (en) | Continuous rotary device integrating biomass pyrolysis and carbonization and boiler heating | |
| CN107990741A (en) | A kind of retort UTILIZATION OF VESIDUAL HEAT IN temperature regulating device and its temperature control method | |
| CN103602340B (en) | Stirring-type biomass carbonizing furnace | |
| CN110295063A (en) | A kind of hot charcoal co-generation system of biomass external heating and method | |
| CN201737705U (en) | Device for batch and continuous preparation of activated charcoal by biomass | |
| CN204939394U (en) | Rotary type continuous pyrolysis stalk coke oven | |
| CN104031666A (en) | Bamboo charring kiln with flue gas residual heat recycling function | |
| CN102249225A (en) | System using biomass for heat supply for producing activated carbon by fly ash | |
| CN101749726A (en) | Air circulating system for combustion furnace | |
| CN208279324U (en) | A kind of active carbon Preparation equipment | |
| CN201309830Y (en) | Liner type rotary carbonization and activation furnace utilizing chemical method to manufacture activated carbon | |
| CN205933748U (en) | System for living beings preparation active carbon | |
| CN110257093A (en) | The control method of carbonization system in a kind of hot charcoal co-generation system of biomass external heating | |
| CN106679174A (en) | High-temperature hot blast stove |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant |