CN205650209U - Be used for palingenetic converter of powder activity charcoal - Google Patents
Be used for palingenetic converter of powder activity charcoal Download PDFInfo
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- CN205650209U CN205650209U CN201620365264.1U CN201620365264U CN205650209U CN 205650209 U CN205650209 U CN 205650209U CN 201620365264 U CN201620365264 U CN 201620365264U CN 205650209 U CN205650209 U CN 205650209U
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Abstract
The utility model discloses a be used for palingenetic converter of powder activity charcoal, including furnace body, base, feed inlet, screw conveyer, gas heating radiant tube, discharge gate, insulation material, refractory material and smoke and dust processing apparatus, a plurality of gass heating radiant tube has evenly been arranged in the furnace body, furnace inner wall all is provided with refractory material layer and insulation material layer outward by the lining, perpendicular parallel arrangement has a plurality of conveying mechanism of group in the furnace body, and conveying mechanism comprises a plurality of the screw conveyer that top -down arranged, through the pipe connection, constitutes bow -shaped conveying mechanism between every screw conveyer, need during palingenetic active carbon passes through feed inlet input furnace body, top -down discharges through the discharge gate behind the screw conveyer of process in proper order, and the gas that produces among the regenerative process gets into smoke and dust processing apparatus through the blast pipe, after the system of burning, discharged by the chimney. The utility model discloses do that the regeneration energy consumption is low, the active carbon loss is little, regeneration back adsorption energy reinforce and do not have secondary pollution.
Description
Technical field
This utility model belongs to industrial equipment and Technology field, is specifically related to a kind of converter for Powdered Activated Carbon regeneration.
Background technology
Powdered Activated Carbon (Activated Carbon, AC) it is the adsorbing material that a kind of pore structure is the most flourishing, specific surface area is very big, nonpoisonous and tasteless, very capable to Molecular Adsorption, the various fields such as medicine, chemical industry, light industry, food, environmental protection it have been widely used in as adsorption decolouriser.In terms of environmental protection, activated carbon adsorption is widely used in Purification of Polluted Sources of Water and municipal sewage, the advanced treating of industrial wastewater, is one of important means processing organic wastewater.
Powdered Activated Carbon manufacturing cost is higher, and discarded saturated activity charcoal not only causes the wasting of resources, also can cause secondary environmental pollution, therefore, from the point of view of economical and environmentally friendly, makes activated carbon effective regeneration, raising activated carbon utilization ratio significant.
Regenerating active carbon refers on the premise of not destroying activated carbon original structure, with either physically or chemically removing the adsorbate being adsorbed in activated carbon capillary, recovers the process of its absorption property.Regeneration method of active carbon can be divided into two classes, and one is introduced into material or energy makes the reaction force attenuation between adsorption molecule and activated carbon or disappearance make adsorbate be desorbed；Two are dependent on thermal decomposition or redox reaction destruction adsorbate structure and reach to remove the purpose of adsorbate.Regeneration method of active carbon mainly has the regeneration of hot recycling, chemical drugs, electrochemical regeneration, Photocatalytic Regeneration, CWO regeneration, supercritical fluid regeneration, bio-regeneration, microwave heating regeneration etc., wherein hot recycling method best results, almost can decompose the Organic substance of all absorption.There are multiple thermal regeneration method and device both at home and abroad at present, but still in place of Shortcomings: charcoal loss rate is relatively big, between 5% ~ 16%；After regeneration, absorbability has and is decreased obviously；Environment can be caused secondary pollution by the tail gas produced during regeneration；Energy consumption is higher, and overall operation is relatively costly, and economic benefit is low.
The electric converter device of existing Powdered Activated Carbon regeneration has the disadvantage that
(1) energy consumption cost is high；
(2) being dried, regenerate, activate each stage, the time of staying of Powdered Activated Carbon is identical, it is impossible to individually adjust；
(3) arch chute feeder supporting way is defective, yielding cracking, and device availability is the highest；
Utility model content
For not enough present in existing apparatus, this utility model provides that a kind of energy consumption cost time of staying low, Powdered Activated Carbon is controlled, high adsorption capacity and non-secondary pollution after regeneration, realization disposable high-volume cyclic regeneration, converter that regenerating unit availability is high.
This utility model be the technical scheme is that a kind of converter for Powdered Activated Carbon regeneration, it is characterized in that: include body of heater, base, charging aperture, conveying worm, gas heating radial canal, discharging opening, adiabator layer, refractory masses and soot processing device；
Described body of heater has been evenly arranged some gas heating radial canals；Described body of heater is arranged on base, and its inwall is by inner and be provided with outward refractory masses and adiabator layer；Vertical parallel in described body of heater being disposed with some groups of conveying mechanisms, described conveying mechanism is made up of some the conveying worms arranged from top to bottom, is connected by pipeline between every conveying worm, constitutes arch conveying mechanism；The described equal separate configurations of every conveying worm has motor, and two the conveying worm feed directions closed on up and down are contrary, make activated carbon form fluidised form in body of heater；
Described conveying mechanism top is provided with charging aperture, bottom is provided with discharging opening and is connected with soot processing device by exhaustor, need the activated carbon of regeneration by charging aperture input body of heater, discharged by discharging opening after sequentially passing through described conveying worm from top to bottom, the gas produced in regenerative process enters soot processing device through exhaustor, after through CIU, discharged by chimney.
As preferably, described soot processing device includes one-level spray, two grades of sprays, sprays water inlet pipe, water tank, spray escape pipe, tornado evaporator and blower fan；Described conveying worm is all connected with one-level spray by exhaustor；Described one-level spray top is connected with described two grades of spray bottoms by conduit；Described two grades of spray tops are provided with spray escape pipe；Described spray escape pipe connects tornado evaporator, blower fan and CIU, chimney；Described one-level spray, two grades of spray upper ends are connected with described spray water inlet pipe by conduit respectively, and bottom is all stretched under described water tank internal liquid level, it is ensured that the effective dedusting of soot processing device.
Described gas heating radial canal has totally 16, and points 4 groups vertical parallel is uniformly arranged in described body of heater.
As preferably, described conveying mechanism has 3 groups, and often group conveying mechanism is formed by 6 conveying worms.
As preferably, on described charging aperture, equal separate configurations has feed arrangement, the equal separate configurations of described drawing mechanism to have drawing mechanism, described feed arrangement and drawing mechanism to be conveying worm.
As preferably, described body of heater side is evenly arranged and is provided with several temperature probes, for the real-time monitoring to stove body temperature.
The Powdered Activated Carbon regenerating furnace general with tradition, and the electric converter utilizing electric-heating-wire-heating to carry out Powdered Activated Carbon regeneration compares, useful achievement of the present utility model is:
1, using gas heating, energy consumption cost is low；
2, every equal separate configurations of conveying worm has motor, can individually regulate and control the Powdered Activated Carbon time of staying in dry regeneration activating each stage；
3, high adsorption capacity and non-secondary pollution after regeneration；
4, realizing the cyclic regeneration of disposable high-volume, regenerating unit availability is high, significantly improves economic benefit；
5, this utility model can use electrical heating instead, reequips very convenient, and quantities is the least.
Accompanying drawing explanation
The converter structure figure of Fig. 1: this utility model embodiment.
The soot processing device structure chart of Fig. 2: this utility model embodiment.
Detailed description of the invention
Below in conjunction with the technical program is further described with reference to the drawings, the example of described embodiment is shown in the drawings, the most same or similar label represents same or similar element or has the element of same or like function, but this description is only used for explaining this utility model, and it is not intended that to restriction of the present utility model.
Ask for an interview Fig. 1 and Fig. 2, a kind of converter for Powdered Activated Carbon regeneration that this utility model provides, sprays 10, two grades of sprays 11, spray water inlet pipe 12, water tank 13, spray escape pipe 14, adiabator layer 15, refractory masses 16, temperature probe 17, feed arrangement 18 and drawing mechanism 19 including body of heater 1, base 2, charging aperture 3, conveying worm 4, exhaustor 5, gas heating radial canal 6, tornado evaporator 7, blower fan 8, discharging opening 9, one-level；In body of heater 1, parallel vertical has been evenly arranged four groups, totally 16 gas heating radial canals 6；Body of heater 1 is arranged on base 2, and its inwall is by inner and be sequentially installed with outward refractory masses 16 and adiabator layer 15；Vertical parallel in body of heater 1 being disposed with three groups of conveying mechanisms, often group conveying mechanism is made up of 6 conveying worms 4 arranged from top to bottom, connects by pipeline between every conveying worm 4, composition arch conveying mechanism；Every equal separate configurations of conveying worm 4 has motor, and two conveying worm 4 feed directions closed on up and down are contrary, make activated carbon form fluidised form in body of heater 1；Body of heater 1 side is evenly arranged and is mounted with four groups, totally 8 temperature probes 17, for the real-time monitoring of temperature in body of heater 1；Body of heater 1 top is provided with three charging apertures 3, bottom is provided with three discharging openings 9 and is connected with soot processing device by exhaustor 5；Soot processing device includes that one-level sprays 10, two grades of sprays 11, spray water inlet pipe 12, water tank 13, spray escape pipe 14, tornado evaporator 7 and blower fan 8；18 conveying worms 4 are all connected with one-level spray 10 by exhaustor 5；One-level is sprayed 10 tops and is connected by conduit and two grades of spray 11 bottoms；Two grades of spray 11 tops are provided with spray escape pipe 14；Spray escape pipe 14 connects tornado evaporator 7, blower fan 8 and CIU, chimney；One-level is sprayed 10, two grades of spray 11 upper ends and is connected with spray water inlet pipe 12 by conduit respectively, and bottom is all stretched under water tank 13 internal liquid level, it is ensured that the effective dedusting of soot processing device；The activated carbon needing regeneration inputs in body of heater 1 by feed arrangement 18, charging aperture 3, is discharged by discharging opening 9, drawing mechanism 19 after sequentially passing through conveying worm 4 from top to bottom；Feed arrangement 18 includes that three conveying worms, every conveying worm and a charging aperture 3 are individually connected；Drawing mechanism 19 includes that three conveying worms, every conveying worm and a discharging opening 9 are individually connected；The gas produced in regenerative process enters soot processing device through exhaustor 5, after through CIU, discharged by chimney.
Although this specification more employs the terms such as body of heater 1, base 2, charging aperture 3, conveying worm 4, exhaustor 5, gas heating radial canal 6, tornado evaporator 7, blower fan 8, discharging opening 9,10, two grades of sprays 11 of one-level spray, spray water inlet pipe 12, water tank 13, spray escape pipe 14, adiabator layer 15, refractory masses 16, temperature probe 17, feed arrangement 18 and drawing mechanism 19, but is not precluded from using the probability of other terms.Using these terms to be only used to more easily and describe essence of the present utility model, it is all contrary with this utility model spirit for being construed as any additional restriction.
It should be appreciated that the part that this specification does not elaborates belongs to prior art.
Should be understood that; the above-mentioned description for preferred embodiment is the most detailed; therefore the restriction to this utility model scope of patent protection can not be considered; those of ordinary skill in the art is under enlightenment of the present utility model; in the case of without departing from this utility model scope of the claimed protection; can also make replacement or deformation, within each falling within protection domain of the present utility model, the scope that is claimed of the present utility model should be as the criterion with claims.
Claims (6)
1. the converter for Powdered Activated Carbon regeneration, it is characterized in that: include body of heater (1), base (2), charging aperture (3), conveying worm (4), gas heating radial canal (6), discharging opening (9), adiabator layer (15), refractory masses (16) and soot processing device；
Described body of heater (1) has been evenly arranged some gas heating radial canals (6)；Described body of heater (1) is arranged on base (2), and its inwall is by inner and be provided with outward refractory masses (16) and adiabator layer (15)；Vertical parallel in described body of heater (1) being evenly arranged some groups of conveying mechanisms, described conveying mechanism is made up of some the conveying worms (4) arranged from top to bottom, is connected by pipeline between every conveying worm (4), constitutes arch conveying mechanism；Described every conveying worm (4) all separate configurations have motor, and two conveying worm (4) feed directions closed on up and down are contrary, make activated carbon form fluidised form in body of heater (1)；
Described conveying mechanism top is provided with charging aperture (3), bottom is provided with discharging opening (9) and is connected with soot processing device by exhaustor (5), need the activated carbon of regeneration by charging aperture (3) input body of heater (1), sequentially pass through described conveying worm (4) from top to bottom to be discharged by discharging opening (9) afterwards, the gas produced in regenerative process enters soot processing device through exhaustor (5), after through CIU, discharged by chimney.
Converter for Powdered Activated Carbon regeneration the most according to claim 1, it is characterised in that: described soot processing device includes one-level spray (10), two grades of sprays (11), spray water inlet pipe (12), water tank (13), sprays escape pipe (14), tornado evaporator (7) and blower fan (8)；Described conveying worm (4) is all connected with one-level spray (10) by exhaustor (5)；Described one-level spray (10) top is connected with described two grades of spray (11) bottoms by conduit；Described two grades of spray (11) tops are provided with spray escape pipe (14)；Described spray escape pipe (14) connects tornado evaporator (7), blower fan (8) and CIU, chimney；Described one-level spray (10), two grades of spray (11) upper ends are connected with described spray water inlet pipe (12) by conduit respectively, and bottom is all stretched under described water tank (13) internal liquid level, it is ensured that the effective dedusting of soot processing device.
Converter for Powdered Activated Carbon regeneration the most according to claim 1, it is characterised in that: described gas heating radial canal (6) has totally 16, and points 4 groups vertical parallel is uniformly arranged in described body of heater (1).
Converter for Powdered Activated Carbon regeneration the most according to claim 1, it is characterised in that: described conveying mechanism has 3 groups, and often group conveying mechanism is formed by 6 conveying worms (4).
Converter for Powdered Activated Carbon regeneration the most according to claim 1, it is characterized in that: the upper equal separate configurations of described charging aperture (3) has feed arrangement (18), described drawing mechanism (19) all separate configurations have drawing mechanism (19), described feed arrangement (18) and drawing mechanism (19) to be conveying worm.
6. according to the converter for Powdered Activated Carbon regeneration described in claim 1-5 any one, it is characterised in that: described body of heater (1) side is evenly arranged and is provided with several temperature probes (17), for the real-time monitoring to body of heater (1) interior temperature.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620365264.1U CN205650209U (en) | 2016-04-27 | 2016-04-27 | Be used for palingenetic converter of powder activity charcoal |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620365264.1U CN205650209U (en) | 2016-04-27 | 2016-04-27 | Be used for palingenetic converter of powder activity charcoal |
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| CN205650209U true CN205650209U (en) | 2016-10-19 |
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| CN201620365264.1U Active CN205650209U (en) | 2016-04-27 | 2016-04-27 | Be used for palingenetic converter of powder activity charcoal |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105727914A (en) * | 2016-04-27 | 2016-07-06 | 湖北君集水处理有限公司 | Converter for regenerating powdered activvated carbon |
| CN117069108A (en) * | 2023-09-04 | 2023-11-17 | 广东谷风三维科技有限公司 | Powder activating machine and use method |
-
2016
- 2016-04-27 CN CN201620365264.1U patent/CN205650209U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105727914A (en) * | 2016-04-27 | 2016-07-06 | 湖北君集水处理有限公司 | Converter for regenerating powdered activvated carbon |
| CN117069108A (en) * | 2023-09-04 | 2023-11-17 | 广东谷风三维科技有限公司 | Powder activating machine and use method |
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Address after: 430000, No.3, Huangjiahu University Town, Hongshan District, Wuhan City, Hubei Province Patentee after: Junji Environmental Technology Co.,Ltd. Address before: 430000, No.3, Huangjiahu University Town, Hongshan District, Wuhan City, Hubei Province Patentee before: HUBEI JUNJI WATER TREATMENT Co.,Ltd. |