CN205164747U - Particle activated carbon regeneration facility - Google Patents
Particle activated carbon regeneration facility Download PDFInfo
- Publication number
- CN205164747U CN205164747U CN201520850560.6U CN201520850560U CN205164747U CN 205164747 U CN205164747 U CN 205164747U CN 201520850560 U CN201520850560 U CN 201520850560U CN 205164747 U CN205164747 U CN 205164747U
- Authority
- CN
- China
- Prior art keywords
- kiln body
- activated carbon
- kiln
- section
- granular activated
- 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
- Carbon And Carbon Compounds (AREA)
Abstract
The utility model discloses a particle activated carbon regeneration facility, including car pusher (1), high temperature air exhauster (3), chimney (4), kiln car (5), dress charcoal jar (6), heating system, cooling fan (10), the kiln body (11), the kiln body (11) be provided with preceding wicket (2), back wicket (12), the kiln body (11) around according to the wicket direction divide into in proper order, activation section and cooling zone, high temperature air exhauster (3) set up in the dry section of the kiln body (11), just high temperature air exhauster (3) are sent into the wind of taking out in chimney (4), heating system sets up in the activation section of the kiln body (11), and cooling fan (10) set up on the cooling zone of the kiln body (11), kiln car (5) enter into the kiln body (11) through the promotion of car pusher (1). The utility model discloses production simple process has, equipment simple structure, convenient operation, and the regeneration loss is low, small investment, low in labor strength.
Description
Technical field
The utility model relates to granular activated carbon manufacturing machine, particularly relates to a kind of granular activated carbon reclaim equiment.
Background technology
Granular activated carbon, with its excellent absorption property and chemical stability, is widely applied in water treatment field, especially in drinking water advanced treatment, serves important function.Along with its a large amount of uses, the key limiting its economic utilization is become to the disposal of saturated activity charcoal.If do not carry out regeneration process to the active carbon that those lose adsorption capacity, not only can cause the wasting of resources, also can cause the secondary pollution of environment.In recent years, the recycling utilization technology of active carbon is fast-developing, and granular activated carbon regeneration has become the focus in activated carbon application field.
The principle of the hot recycling of active carbon is by slowly dry for wet charcoal high-temperature gas, in heating process, by the organic matter that adsorbs by its different in kind, by these processes of steam distillation, desorb or thermal decomposition, eliminate with the matrix of the form of desorb, charing, oxidation from active carbon.Hot recycling developing history is longer, is to be employed maximum a kind of renovation process a few days ago.The mainly converter of existing hot recycling equipment, this equipment has the shortcomings such as efficiency of utilization is low, production efficiency is low, product quality fluctuation is larger usually.
Utility model content
The utility model, for the deficiency of the problems referred to above, proposes a kind of granular activated carbon reclaim equiment and renovation process thereof, has production technology simple, simple in equipment, easy to operate, and regeneration losses is low, small investment, and labour intensity is low.
The utility model is the technical scheme solving the problems of the technologies described above proposition:
A kind of granular activated carbon reclaim equiment, comprise car puller (1), high temperature air exhauster (3), chimney (4), kiln car (5), dress charcoal tank (6), heating system, cooling fan (10), kiln body (11), one end of described kiln body (11) is provided with front wicket (2), the other end is provided with rear wicket (12), and described kiln body (11) is divided into dryer section, activation section and cooling section successively by wicket direction, front and back; Described high temperature air exhauster (3) is arranged in the dryer section of kiln body (11), and the wind of extraction is sent in chimney (4) by described high temperature air exhauster (3); Described heating system is arranged on the activation section of kiln body (11), and cooling fan (10) is arranged on the cooling section of kiln body (11); Described kiln car (5) enters into kiln body (11) by the promotion of car puller (1).
Preferred: described heating system comprises burner (7), thermal source, an air distribution blower fan (9) and burning feeding pipe (8), described burner (7) is evenly distributed in the dryer section of kiln body (11), and the heat that thermal source produces by a described air distribution blower fan (9) is provided and delivered to burner (7) by burning feeding pipe (8).
Preferred: described dress charcoal tank (6) is inverted cone-shaped structure, is uniform-distribution with hole at the bottom of its tank.
Preferred: dryer section and the activation section of described kiln body (11) are followed successively by common brick layer, adiabator layer, fire brick layer from outside to inside; Kiln body (11) cooling section is followed successively by common brick layer, fire brick layer from outside to inside.
Preferred: the activation section regeneration temperature of described kiln body (11) is 850-950 DEG C, and soak time is 4-8 hour.
Preferred: described granular activated carbon is ature of coal or shell material active carbon.
A kind of seed activity carbon regeneration method, comprises the following steps:
Step 1, need carry out removal of impurities by granular activated carbon to be processed, the granular activated carbon after removal of impurities is being carried out water absorption, until its absorption is saturated;
Step 2, loads active carbon saturated for absorption in dress charcoal tank (6);
Step 3, is transported to kiln body (11) by the dress charcoal tank (6) loading active carbon by kiln car (5), is sending in kiln body (11) through car puller (1) by front wicket (2);
Step 4, kiln car (5) first enters drying stage after entering kiln body (11); Temperature controls at 100-150 DEG C;
Step 5, then along with the propelling of kiln car enters in the middle part of kiln, enter activation stage, active carbon is heated to 150 ~ 1000 DEG C;
Step 6, kiln car (5) enters the cooling section of kiln, and at cooling section, the active carbon in refractory container is lowered the temperature gradually, and wait is come out of the stove.
Preferred: the loading volume of active carbon loading dress charcoal tank (6) that described absorption is saturated is the 1/2-2/3 of tank volume.
The utility model compared to existing technology, has following beneficial effect:
Have production technology simple, simple in equipment, easy to operate, regeneration losses low (about 5%), small investment, labour intensity is low.
Accompanying drawing explanation
Fig. 1 is a kind of structural representation of granular activated carbon reclaim equiment;
Detailed description of the invention
Accompanying drawing discloses the structural representation of the utility model preferred embodiment without limitation, explains the technical solution of the utility model below with reference to accompanying drawing.
Embodiment
The present embodiment,
A kind of granular activated carbon reclaim equiment, as shown in Figure 1, comprise car puller 1, high temperature air exhauster 3, chimney 4, kiln car 5, dress charcoal tank 6, heating system, cooling fan 10, kiln body 11, one end of described kiln body 11 is provided with front wicket 2, the other end is provided with rear wicket 12, and described kiln body 11 is divided into dryer section, activation section and cooling section successively by wicket direction, front and back; Described high temperature air exhauster 3 is arranged in the dryer section of kiln body 11, and the wind of extraction is sent in chimney 4 by described high temperature air exhauster 3; Described heating system is arranged on the activation section of kiln body 11, and cooling fan 10 is arranged on the cooling section of kiln body 11; Described kiln car 5 enters into kiln body 11 by the promotion of car puller 1.
Described heating system comprises burner 7, thermal source, an air distribution blower fan 9 and burning feeding pipe 8, and described burner 7 is evenly distributed in the dryer section of kiln body 11, and the heat that thermal source produces by a described air distribution blower fan 9 is provided and delivered to burner 7 by burning feeding pipe 8.
Described dress charcoal tank 6 is inverted cone-shaped structure, is uniform-distribution with hole at the bottom of its tank.
Dryer section and the activation section of described kiln body 11 are followed successively by common brick layer, adiabator layer, fire brick layer from outside to inside; Kiln body 11 cooling section is followed successively by common brick layer, fire brick layer from outside to inside.
The activation section regeneration temperature of described kiln body 11 is 850-950 DEG C, and soak time is 4-8 hour, and finished product activation recovery rate is 90-98%.
Described granular activated carbon is sizing or the indefinite form active carbon of ature of coal or shell material.
A kind of seed activity carbon regeneration method, comprises the following steps:
Step 1, need carry out removal of impurities by granular activated carbon to be processed, the granular activated carbon after removal of impurities is being carried out water absorption, until its absorption is saturated;
Step 2, loads in dress charcoal tank 6 by active carbon saturated for absorption;
Step 3, is transported to kiln body 11 by the dress charcoal tank 6 loading active carbon by kiln car 5, is sending in kiln body 11 through car puller 1 by front wicket 2;
Step 4, first kiln car 5 enters drying stage after entering kiln body 11; Temperature controls at 100-150 DEG C;
Step 5, then along with the propelling of kiln car enters in the middle part of kiln, enter activation stage, active carbon is heated to 150 ~ 1000 DEG C;
Step 6, kiln car 5 enters the cooling section of kiln, and at cooling section, the active carbon in refractory container is lowered the temperature gradually, and wait is come out of the stove.
The loading volume of the active carbon loading dress charcoal tank 6 that described absorption is saturated is the 1/2-2/3 of tank volume.
Concrete, as shown in Figure 1, the saturated active carbon that adsorbs through pretreatment (removal of impurities etc.) loads in pretreatment workshop, load in dress charcoal tank 6, loading volume is the 1/2-2/3 of tank volume, be transported to kiln workshop by kiln car 5 after filling, send in kiln body 11 through car puller 1 by front wicket 2, first kiln car carries out drying stage after entering kiln.Temperature controls at 100-150 DEG C, by moisture content 50% ~ 86% the heating of wet charcoal, make adsorbed water evaporation in carbon granule, part low-boiling-point organic compound also volatilizees thereupon simultaneously.Then along with the propelling of kiln car enters in the middle part of kiln, carry out activation stage, grain charcoal is heated to 150 ~ 1000 DEG C.Different organic matters raises with temperature, respectively with the form of volatilization, decomposition, carbonization, oxidation, eliminates from the matrix of active carbon.Active carbon after activation stage enters middle the contact with the hot blast that heating system provides of kiln and activates, last kiln car enters the cooling section of kiln, and at cooling section, the active carbon in refractory container is lowered the temperature gradually, arrive kiln outlet gradually in order, wait is come out of the stove.Whole roasting process is approximately 24-48 hour.The waste gas produced in activation process is then sent in chimney 4 emptying after treatment by high temperature air exhauster 3.
The preferred specific embodiment of the utility model described by reference to the accompanying drawings is above only for illustration of embodiment of the present utility model; instead of as the restriction to aforementioned utility model object and claims content and scope; every according to technical spirit of the present utility model to any simple modification made for any of the above embodiments, equivalent variations and modification, all still belong to the utility model technology and rights protection category.
Claims (6)
1. a granular activated carbon reclaim equiment, it is characterized in that: comprise car puller (1), high temperature air exhauster (3), chimney (4), kiln car (5), dress charcoal tank (6), heating system, cooling fan (10), kiln body (11), one end of described kiln body (11) is provided with front wicket (2), the other end is provided with rear wicket (12), and described kiln body (11) is divided into dryer section, activation section and cooling section successively by wicket direction, front and back; Described high temperature air exhauster (3) is arranged in the dryer section of kiln body (11), and the wind of extraction is sent in chimney (4) by described high temperature air exhauster (3); Described heating system is arranged on the activation section of kiln body (11), and cooling fan (10) is arranged on the cooling section of kiln body (11); Described kiln car (5) enters into kiln body (11) by the promotion of car puller (1).
2. granular activated carbon reclaim equiment according to claim 1; it is characterized in that: described heating system comprises burner (7), thermal source, an air distribution blower fan (9) and burning feeding pipe (8); described burner (7) is evenly distributed in the dryer section of kiln body (11), and the heat that thermal source produces by a described air distribution blower fan (9) is provided and delivered to burner (7) by burning feeding pipe (8).
3. granular activated carbon reclaim equiment according to claim 1, is characterized in that: described dress charcoal tank (6) is inverted cone-shaped structure, is uniform-distribution with hole at the bottom of its tank.
4. granular activated carbon reclaim equiment according to claim 1, is characterized in that: dryer section and the activation section of described kiln body (11) are followed successively by common brick layer, adiabator layer, fire brick layer from outside to inside; Kiln body (11) cooling section is followed successively by common brick layer, fire brick layer from outside to inside.
5. granular activated carbon reclaim equiment according to claim 1, is characterized in that: the activation section regeneration temperature of described kiln body (11) is 850-950 DEG C, and soak time is 4-8 hour.
6. granular activated carbon reclaim equiment according to claim 1, is characterized in that: described granular activated carbon is ature of coal or shell material active carbon.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520850560.6U CN205164747U (en) | 2015-10-29 | 2015-10-29 | Particle activated carbon regeneration facility |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520850560.6U CN205164747U (en) | 2015-10-29 | 2015-10-29 | Particle activated carbon regeneration facility |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205164747U true CN205164747U (en) | 2016-04-20 |
Family
ID=55728786
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520850560.6U Expired - Fee Related CN205164747U (en) | 2015-10-29 | 2015-10-29 | Particle activated carbon regeneration facility |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205164747U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105195117A (en) * | 2015-10-29 | 2015-12-30 | 徐州天正活性炭厂 | Granular active carbon regenerating device and regenerating method |
-
2015
- 2015-10-29 CN CN201520850560.6U patent/CN205164747U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105195117A (en) * | 2015-10-29 | 2015-12-30 | 徐州天正活性炭厂 | Granular active carbon regenerating device and regenerating method |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN104772114B (en) | A kind of organic adsorption saturated activity charcoal regenerating unit | |
| CN103115478B (en) | Drying equipment | |
| CN105148886B (en) | A kind of automatic production line of powdered active carbon regenerating | |
| CN102161484B (en) | Zero-coal-consumption activated carbon production process and production device used in same | |
| CN103242876A (en) | Drying or low-temperature dry distillation method and device of brown coal or low-metamorphic candle coal | |
| CN103333703B (en) | Drying or low-temperature destructive distillation method and device of brown coal or low-deterioration long flame coal | |
| CN205164747U (en) | Particle activated carbon regeneration facility | |
| CN203999502U (en) | A kind of organic solid castoff mummification charing integrated system | |
| CN204824570U (en) | Industrial sludge drying system | |
| CN103100548A (en) | Rapid fermentation technology of organic garbage | |
| CN204738001U (en) | System for mercury in useless mercury catalyst of high -efficient environmental protection recovery | |
| CN204079746U (en) | A kind of heat drying system | |
| CN205556106U (en) | Active carbon apparatus for producing | |
| CN105195117A (en) | Granular active carbon regenerating device and regenerating method | |
| CN104197692A (en) | Drying system and method for mercury catalyst production tail gas recycling | |
| CN104907317A (en) | Integrated harmless dead livestock treatment system and process thereof | |
| CN202080897U (en) | Active carbon production device with zero coal consumption | |
| CN202933935U (en) | Quick organic waste fermentation equipment | |
| CN204769831U (en) | Birds that dies of illness poultry innocent treatment integrated system | |
| CN203148165U (en) | Drying device | |
| CN204495081U (en) | A kind of reduction furnace head tail gas recycling device | |
| CN107353910A (en) | A kind of two-part fine coal distillation system | |
| CN203229489U (en) | Drying or smouldering device for lignite or low metamorphic long-flame coal | |
| CN106016276A (en) | System and method for drying garbage by recycling waste heat of pyrolytic carbon through steam in rotary hearth furnace | |
| CN205933593U (en) | Mud high -efficiency processing device |
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: 20160420 Termination date: 20161029 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |