CN206046045U - A kind of Powdered Activated Carbon regenerating furnace - Google Patents
A kind of Powdered Activated Carbon regenerating furnace Download PDFInfo
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- CN206046045U CN206046045U CN201620924464.6U CN201620924464U CN206046045U CN 206046045 U CN206046045 U CN 206046045U CN 201620924464 U CN201620924464 U CN 201620924464U CN 206046045 U CN206046045 U CN 206046045U
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Abstract
The utility model discloses a kind of Powdered Activated Carbon regenerating furnace, including body of heater, base, charging aperture, conveying worm, gas burner, pyrolysis air burner, discharging opening, insulation material, refractory material, soot processing device；If Heavenly Stems and Earthly Branches gas burner and pyrolysis air burner have been evenly arranged in body of heater；Some conveying worms it have been evenly arranged in body of heater from top to bottom, the hopper of conveying worm constitutes bow-shaped structural chute feeder by connecting pipe；Sprocket wheel is provided with conveying worm, and is connected in turn by chain, then driven by motor and rotated, so that the two conveying worm feed directions for closing on up and down are conversely, make activated carbon that fluidised form is formed in body of heater；This utility model be it is a kind of operation is simple, regeneration energy consumption is low, activated carbon loss it is little, regeneration after high adsorption capacity and non-secondary pollution regenerating active carbon converter.
Description
Technical field
This utility model belongs to industrial equipment and Technology field, and in particular to it is a kind of for Powdered Activated Carbon regeneration
Converter.
Background technology
Powdered Activated Carbon（Activated Carbon, AC）It is that a kind of pore structure is very flourishing, specific surface area is very big, nothing
The tasteless adsorbing material of poison, it is very capable to Molecular Adsorption, as adsorption decolouriser be widely used in medicine, chemical industry, light industry,
The various fields such as food, environmental protection.In terms of environmental protection, activated carbon adsorption is widely used in Purification of Polluted Sources of Water and municipal sewage, work
The advanced treating of industry waste water, is to process one of important means of organic wastewater.
Powdered Activated Carbon manufacturing cost is higher, and discarded saturated activity charcoal not only causes the wasting of resources, can also cause two secondary rings
Border is polluted, therefore, from from the point of view of economical and environmentally friendly, make activated carbon effective regeneration, activated carbon utilization ratio improved with weight
Want meaning.
Regenerating active carbon is referred on the premise of activated carbon original structure is not destroyed, is adsorbed with either physically or chemically removing
In the adsorbate of activated carbon capillary, recover the process of its absorption property.Regeneration method of active carbon can be divided into two classes, and one is to introduce thing
Matter or energy make the reaction force attenuation between adsorption molecule and activated carbon or disappearance be desorbed adsorbate；Two is by thermal decomposition
Or redox reaction destroys adsorbate structure and reaches the purpose of removing adsorbate.Regeneration method of active carbon mainly has heat again
Life, chemical drugss regeneration, electrochemical regeneration, Photocatalytic Regeneration, CWO regeneration, supercritical fluid regeneration, biology are again
Life, microwave heating regeneration etc., wherein hot recycling method best results, can almost decompose the Organic substance of all absorption.It is domestic at present
There are outward various thermal regeneration methods and device, but still in place of Shortcomings：Charcoal loss rate is larger, between 5% ~ 16%；Inhale after regeneration
Attached ability has and is decreased obviously；The tail gas produced during regeneration can cause secondary pollution to environment；Energy consumption is higher, overall operation cost
Higher, economic benefit is low.
At present, the electric converter device of Powdered Activated Carbon regeneration is favorably carried out with electric-heating-wire-heating, gas fired radiant tubes is utilized
Heating carries out the converter device of Powdered Activated Carbon regeneration.
The device of existing Powdered Activated Carbon regeneration has the following disadvantages：
（1）Electrical heating activated carbon regeneration furnace uses electric energy, and energy cost is high；
（2）Gas fired radiant tubes heated active carbon regenerating furnace uses natural gas, and energy cost is relatively low, but gas fired radiant tubes adds
Heat is a kind of indirect heating manner, and the heat heating radiation pipe first of combustion of natural gas release, radial canal temperature are raised, then spoke
Penetrate pipe and heat radiation is delivered to materail tube, materail tube temperature is also raised, then the Powdered Activated Carbon of heated material in-pipe.
Self preheating burner and high-temperature alloy radial canal that gas fired radiant tubes heated active carbon regenerating furnace is adopted, its cost are higher,
Additionally, the combustible pyrolysis' tail gas produced in Powdered Activated Carbon regenerative process, its purified treatment also separately needs a waste gas combustion furnace；
（3）Former arch feeding slot structure, its part replacement are difficult, and maintainability is bad.
Utility model content
For deficiency present in existing apparatus, this utility model is low there is provided a kind of energy consumption cost, and an equipment is realized
Regeneration Powdered Activated Carbon and incineration of combustible pyrolysis two kinds of functions of tail gas, system cost are low, absorbability after Powdered Activated Carbon regeneration
Strong and non-secondary pollution, realizes disposable high-volume cyclic regeneration, the good novel converter of maintainability.
The technical scheme adopted by this utility model is：A kind of Powdered Activated Carbon regenerating furnace, it is characterised in that：Including stove
Body, charging aperture, conveying worm, gas burner, pyrolysis air burner, discharging opening, soot processing device；In described body of heater
If being evenly arranged Heavenly Stems and Earthly Branches gas burner and pyrolysis air burner；It has been evenly arranged some in described body of heater from top to bottom
Conveying worm, the hopper of conveying worm constitute bow-shaped structural chute feeder by connecting pipe；On the conveying worm
Sprocket wheel is provided with, and is connected in turn by chain, then driven by motor and rotated, so that close on up and down two
Platform conveying worm feed direction is conversely, make activated carbon that fluidised form is formed in body of heater；Described upper of furnace body is provided with flue gas and goes out
Mouth, charging aperture, bottom are provided with discharging opening, and are connected with soot processing device by exhaustor；The activated carbon of regeneration is needed to lead to
Cross in charging aperture input body of heater, discharged by discharging opening after sequentially passing through described conveying worm from top to bottom；Regenerative process
The pyrolysis gas of middle generation enter soot processing device by exhaustor, and purifying and dedusting rear portion pyrolysis gas return stream dust treatment
Device, when fluidized wind is used, another part pyrolysis gas Jing pyrolysis air burners burn in body of heater, and then heat smoke Jing flue gases go out
Mouth is discharged.
Preferably, the hopper of the conveying worm is made up of inner sleeve, socket trocar sheath and bellmouth trocar sheath, it is described
Inner sleeve the right and left is arranged with socket trocar sheath and bellmouth trocar sheath, the hopper of two for closing on up and down conveying worm respectively
Connected using upper and lower bell and spigot frame, i.e., the socket trocar sheath and a following conveying worm of a spiral conveyer trough above
The bellmouth trocar sheath socket joint connection of hopper.
Preferably, the inner sleeve and socket trocar sheath, bellmouth trocar sheath axial direction socket joint junction, socket trocar sheath and
The gap of the upper and lower socket joint junction of bellmouth trocar sheath is filled with refractory fibre.
Preferably, the soot processing device include one-level spray thrower, fluid bed three-phase cleaner unit, spray water inlet pipe,
Spray escape pipe, water tank；The conveying worm is connected with one-level spray thrower by exhaustor；The one-level spray thrower top
Connected with the fluid bed three-phase cleaner unit bottom by conduit；The fluid bed three-phase cleaner unit top be provided with demister,
Spray escape pipe；A pyrolysis gas part after purifying and dedusting is sent into the fluidisation by pyrolysis gas blower fan by the spray escape pipe
Bed three-phase cleaner unit, when fluidized wind is used, another part sends into the pyrolysis air burner, burns in body of heater；The one-level spray
Drench device, fluid bed three-phase cleaner unit upper end to be connected with the spray water inlet pipe by conduit respectively, described water is stretched in lower end
Under case internal liquid level, it is ensured that the effective dedusting of soot processing device.
Preferably, the body of heater side is evenly arranged installs several temperature probes, for the reality to stove body temperature
When monitor.
Preferably, the inboard wall of furnace body is by inner and be mounted on outward refractory material, insulation material.
Preferably, the body of heater is also configured with base.
Preferably, the charging aperture, discharging opening are each configured with feed arrangement and drawing mechanism.
The electricity that Powdered Activated Carbon regeneration is carried out with traditional general Powdered Activated Carbon regenerating furnace, using electric-heating-wire-heating is turned
Stove and the converter for carrying out Powdered Activated Carbon regeneration using gas fired radiant tubes heating are compared, and useful achievement of the present utility model is：
Energy consumption cost is low, and an equipment realizes regeneration Powdered Activated Carbon and incineration of combustible pyrolysis two kinds of functions of tail gas, and system cost is low, powder
High adsorption capacity and non-secondary pollution after last regenerating active carbon, realize disposable high-volume cyclic regeneration, and plant maintenance is good, show
Work improves economic benefit.
Description of the drawings
Fig. 1：The external structure of this utility model embodiment.
Fig. 2：The cut-away view of this utility model embodiment.
Fig. 3：The sectional view of this utility model embodiment.
Fig. 4：The top view of this utility model embodiment.
Fig. 5：The schematic diagram that is connected of this utility model embodiment.
Fig. 6：The bow-shaped structural chute feeder structure chart of this utility model embodiment.
Specific embodiment
With reference to the technical program is further described with reference to the drawings, the example of the embodiment is shown in the drawings, its
In from start to finish same or similar label represent same or similar element or the element with same or like function, but should
Description is only used for explanation this utility model, and it is not intended that to restriction of the present utility model.
Ask for an interview Fig. 1, Fig. 2, Fig. 3, Fig. 4, Fig. 5 and Fig. 6, it is a kind of for Powdered Activated Carbon regeneration that this utility model is provided
Novel converter, including body of heater 1, base 2, charging aperture 3, conveying worm 4, gas burner 5, pyrolysis air burner 6, discharging opening
7th, insulation material 8, refractory material 9, exhaustor 10, one-level spray thrower 11, fluid bed three-phase cleaner unit 12, spray water inlet pipe 13,
Spray escape pipe 14, water tank 15, pyrolysis gas blower fan 16, temperature probe 17, feed arrangement 18 and drawing mechanism 19；In body of heater 1
It is even to arrange 5 flat flame gas burners 5 and 6 long flames pyrolysis air burners 6；Body of heater 1 be arranged on base 2 on, its inwall by
In and be mounted on outward refractory material 9, insulation material 8；In body of heater 1, uniform parallel arranges 5 conveying worms from top to bottom
4, the hopper of conveying worm 4 constitutes bow-shaped structural chute feeder by connecting pipe；The hopper of conveying worm 4 is by inner sleeve
23rd, socket trocar sheath 24 and bellmouth trocar sheath 25 are constituted, and 23 the right and left of inner sleeve is arranged with socket trocar sheath 24 respectively and holds
Mouth trocar sheath 25, the hopper of two for closing on up and down conveying worm 4 are connected using upper and lower bell and spigot frame, i.e., a spiral above
The socket trocar sheath 24 of 4 hopper of conveyer is connected with 25 socket joint of bellmouth trocar sheath of 4 hopper of a following conveying worm；Inner sleeve
Pipe 23 and socket trocar sheath 24,25 axial socket joint junction of bellmouth trocar sheath, socket trocar sheath 24 and bellmouth trocar sheath are about 25
The gap of socket joint junction is filled with refractory fibre；Be provided with sprocket wheel 21 on every conveying worm 4, and by chain according to
It is secondary to link together, then driven by the motor 20 below base 2 and rotated, so that two spiral shells for closing on up and down
Rotation 4 feed direction of conveyer is conversely, make activated carbon form fluidised form in body of heater 1；1 side of body of heater be evenly arranged be mounted with four groups,
Totally 8 temperature probes 17, for the monitor in real time to temperature in body of heater 1；1 top of body of heater is provided with an exhanst gas outlet 22,
Individual charging aperture 3, bottom is provided with a discharging opening 7, and is connected with soot processing device by exhaustor 10；Soot processing device
Including exhaustor 10, one-level spray thrower 11, fluid bed three-phase cleaner unit 12, spray water inlet pipe 13, spray escape pipe 14, water tank 15
With pyrolysis gas blower fan 16；5 conveying worms 4 are connected with one-level spray thrower 11 by exhaustor 10；On one-level spray thrower 11
Portion is connected with 12 bottom of fluid bed three-phase cleaner unit by conduit；12 top of fluid bed three-phase cleaner unit is provided with demister, spray
Drench escape pipe 14；The spray connection pyrolysis gas of escape pipe 14 blower fan 16 and pyrolysis air burner 6；One-level spray thrower 11, fluid bed three
12 upper end of phase cleaner unit is connected with spray water inlet pipe 13 by conduit respectively, and lower end is stretched under 15 internal liquid level of water tank, it is ensured that
The effective dedusting of soot processing device；The activated carbon of regeneration is needed to be input in body of heater 1 by feed arrangement 18, charging aperture 3, from upper
Under sequentially pass through conveying worm 4 after discharged by discharging opening 7, drawing mechanism 19；The pyrolysis gas produced in regenerative process by
Exhaustor 10 enters soot processing device, and purifying and dedusting rear portion pyrolysis gas return fluid bed three-phase cleaner unit 12, work as fluidisation
Wind use, another part pyrolysis gas Jing pyrolysis air burner 6, in body of heater 1 burn, then heat smoke Jing exhanst gas outlets 22 discharge into
Enter lower one technological process.
Although this specification more used body of heater 1, base 2, charging aperture 3, conveying worm 4, gas burner 5,
Pyrolysis air burner 6, discharging opening 7, insulation material 8, refractory material 9, exhaustor 10, one-level spray thrower 11, fluid bed three are divided by
Dirt device 12, spray water inlet pipe 13, spray escape pipe 14, water tank 15, pyrolysis gas blower fan 16, temperature probe 17, feed arrangement 18, go out
The terms such as material device 19, motor 20, sprocket wheel 21, exhanst gas outlet 22, inner sleeve 23, socket trocar sheath 24 and bellmouth trocar sheath 25,
But it is not precluded from the probability using other terms.It is used for the purpose of more easily describing of the present utility model using these terms
Essence, it is all contrary with this utility model spirit to be construed as any additional restriction.
It should be appreciated that the part that this specification is not elaborated belongs to prior art.
It should be appreciated that the above-mentioned description for preferred embodiment is more detailed, therefore can not be considered to this
The restriction of utility model patent protection domain, one of ordinary skill in the art under enlightenment of the present utility model, without departing from
In the case of this utility model scope of the claimed protection, replacement can also be made or deformed, be each fallen within of the present utility model
Within protection domain, the scope that is claimed of the present utility model should be defined by claims.
Claims (8)
1. a kind of Powdered Activated Carbon regenerating furnace, it is characterised in that：Including body of heater（1）, charging aperture（3）, conveying worm（4）, combustion
Air burner（5）, pyrolysis air burner（6）, discharging opening（7）, soot processing device；
The body of heater（1）If in be evenly arranged Heavenly Stems and Earthly Branches gas burner（5）With pyrolysis air burner（6）；The body of heater（1）In
Some conveying worms have been evenly arranged from top to bottom（4）, conveying worm（4）Hopper arch is constituted by connecting pipe
Structure chute feeder；The conveying worm（4）On be provided with sprocket wheel（21）, and be connected in turn by chain, then
By motor（20）Drive and rotate, so that two conveying worms for closing on up and down（4）Feed direction is conversely, make activated carbon
In body of heater（1）Middle formation fluidised form；
The body of heater（1）Top is provided with exhanst gas outlet（22）, charging aperture（3）, bottom be provided with discharging opening（7）, and by row
Trachea（10）It is connected with soot processing device；The activated carbon of regeneration is needed to pass through charging aperture（3）Input body of heater（1）In, from upper and
Under sequentially pass through the conveying worm（4）Pass through discharging opening afterwards（7）Discharge；The pyrolysis gas produced in regenerative process are by aerofluxuss
Pipe（10）Into soot processing device, purifying and dedusting rear portion pyrolysis gas return stream soot processing device, when fluidized wind is used, separately
A part of pyrolysis gas Jing is pyrolyzed air burner（6）, in body of heater（1）Middle burning, then heat smoke Jing exhanst gas outlets（22）Discharge.
2. Powdered Activated Carbon regenerating furnace according to claim 1, it is characterised in that：The conveying worm（4）Hopper
By inner sleeve（23）, socket trocar sheath（24）With bellmouth trocar sheath（25）Composition, the inner sleeve（23）The right and left covers respectively
It is provided with socket trocar sheath（24）With bellmouth trocar sheath（25）, two conveying worms for closing on up and down（4）Hopper using upper and lower
Bell and spigot frame connects, i.e., a conveying worm above（4）The socket trocar sheath of hopper（24）With a following conveying worm
（4）The bellmouth trocar sheath of hopper（25）Socket joint connects.
3. Powdered Activated Carbon regenerating furnace according to claim 2, it is characterised in that：The inner sleeve（23）With socket overcoat
Pipe（24）, bellmouth trocar sheath（25）Axial socket joint junction, socket trocar sheath（24）With bellmouth trocar sheath（25）Socket joint connects up and down
The gap for meeting place is filled with refractory fibre.
4. Powdered Activated Carbon regenerating furnace according to claim 1, it is characterised in that：The soot processing device includes one-level
Spray thrower（11）, fluid bed three-phase cleaner unit（12）, spray water inlet pipe（13）, spray escape pipe（14）, water tank（15）；The spiral shell
Rotation conveyer（4）Pass through exhaustor（10）With one-level spray thrower（11）Connection；The one-level spray thrower（11）Top is by leading
Pipe and the fluid bed three-phase cleaner unit（12）Bottom connects；The fluid bed three-phase cleaner unit（12）Top is provided with demisting
Device, spray escape pipe（14）；The spray escape pipe（14）By pyrolysis gas blower fan（16）By the pyrolysis gas one after purifying and dedusting
Send into the fluid bed three-phase cleaner unit in part（12）, when fluidized wind is used, another part sends into the pyrolysis air burner（6）,
In body of heater（1）Middle burning；The one-level spray thrower（11）, fluid bed three-phase cleaner unit（12）Upper end respectively by conduit with it is described
Spray water inlet pipe（13）Described water tank is stretched in connection, lower end（15）Under internal liquid level, it is ensured that soot processing device is effectively removed
Dirt.
5. Powdered Activated Carbon regenerating furnace according to claim 1, it is characterised in that：The body of heater（1）Side is evenly arranged
Several temperature probes are installed（17）, for body of heater（1）The monitor in real time of interior temperature.
6. the Powdered Activated Carbon regenerating furnace according to claim 1-5 any one, it is characterised in that：The body of heater（1）It is interior
Wall is by inner and be mounted on outward refractory material（9）, insulation material（8）.
7. the Powdered Activated Carbon regenerating furnace according to claim 1-5 any one, it is characterised in that：The body of heater（1）Also
It is configured with base（2）.
8. the Powdered Activated Carbon regenerating furnace according to claim 1-5 any one, it is characterised in that：The charging aperture（3）、
Discharging opening（7）It is each configured with feed arrangement（18）And drawing mechanism（19）.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620924464.6U CN206046045U (en) | 2016-08-23 | 2016-08-23 | A kind of Powdered Activated Carbon regenerating furnace |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620924464.6U CN206046045U (en) | 2016-08-23 | 2016-08-23 | A kind of Powdered Activated Carbon regenerating furnace |
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| Publication Number | Publication Date |
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| CN206046045U true CN206046045U (en) | 2017-03-29 |
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ID=58385143
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| Application Number | Title | Priority Date | Filing Date |
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| CN201620924464.6U Active CN206046045U (en) | 2016-08-23 | 2016-08-23 | A kind of Powdered Activated Carbon regenerating furnace |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106111099A (en) * | 2016-08-23 | 2016-11-16 | 湖北君集水处理有限公司 | A kind of Powdered Activated Carbon regenerating furnace |
| CN111250070A (en) * | 2020-03-17 | 2020-06-09 | 沈阳鑫迪环境技术有限公司 | Regeneration device and recovery method for waste mercury adsorption material |
-
2016
- 2016-08-23 CN CN201620924464.6U patent/CN206046045U/en active Active
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106111099A (en) * | 2016-08-23 | 2016-11-16 | 湖北君集水处理有限公司 | A kind of Powdered Activated Carbon regenerating furnace |
| CN111250070A (en) * | 2020-03-17 | 2020-06-09 | 沈阳鑫迪环境技术有限公司 | Regeneration device and recovery method for waste mercury adsorption material |
| CN111250070B (en) * | 2020-03-17 | 2024-02-06 | 沈阳鑫迪环境技术有限公司 | Regeneration device and recovery method for waste mercury adsorption material |
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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. |