CN205833182U - A kind of industrial waste Al2o3bead micropore activation system - Google Patents
A kind of industrial waste Al2o3bead micropore activation system Download PDFInfo
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- CN205833182U CN205833182U CN201620704437.8U CN201620704437U CN205833182U CN 205833182 U CN205833182 U CN 205833182U CN 201620704437 U CN201620704437 U CN 201620704437U CN 205833182 U CN205833182 U CN 205833182U
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Abstract
This utility model provides a kind of industrial waste Al2O3Bead micropore activation system, described system includes activating device and waste liquid circulation utilizes system；Wherein, activation device includes soot blowing dust collect plant, impregnating active module and transmitting device, and transmitting device connects soot blowing dust collect plant and impregnating active module；Soot blowing dust collect plant is positioned at activation device body material inlet side, and impregnating active module is placed in material outlet side in activation device body；Impregnating active module includes heat ray filter, sets gradually activating tank and drying device along transmitting device traffic direction, arrange lowering or hoisting gear bottom activating tank in heat ray filter；The waste liquid outlet of activating tank utilizes system to be connected with waste liquid circulation.Al through this utility model micropore activation processing2O3Bead, can improve the efficiency that subsequent regeneration processes, and then prepare the regeneration Al with superperformance2O3Bead.
Description
Technical field
This utility model belongs to resource recycling field, relates to a kind of industrial waste Al2O3Bead micropore activation system.
Background technology
Hydrogen peroxide also known as hydrogen peroxide, drift at chemical industry, pharmaceuticals industry, printing and dyeing industry, intermetallic composite coating, textile,
All many-sides such as military project fuel and civilian disinfectant all have extensive and irreplaceable purposes.The Hydrogen Peroxide Production of China at present
Enterprise is still using in addition to electrolysis and isopropanol method except only a few, most 2-ethyl-anthraquinone methods all using comparative maturity
(the most anthraquinone) produces.
Anthraquinone technique is that 2-ethyl-anthraquinone and organic solvent are configured to working solution, in 3atm, 55～65 DEG C and catalysis
Agent is hydrogenated with hydrogenation under participating in, then carries out counter flow oxidation at 40～44 DEG C with air, through extracting, regenerating, refines and was concentrated to give
Hydrogen oxide aqueous products.In last handling process, need to utilize activated alumina bead working solution is carried out absorption except alkali and
Regeneration degradation product, thus obtain the working solution that can be recycled, the adsorption process of activated alumina bead is then not effectively reversible
Regeneration.Alumina globule adsorbent must be changed after using a period of time, to ensure the needs that working solution regenerates.
Hydrogen peroxide also known as hydrogen peroxide, drift at chemical industry, pharmaceuticals industry, printing and dyeing industry, intermetallic composite coating, textile,
All many-sides such as military project fuel and civilian disinfectant all have extensive and irreplaceable purposes.The Hydrogen Peroxide Production of China at present
Enterprise is still using in addition to electrolysis and isopropanol method except only a few, most 2-ethyl-anthraquinone methods all using comparative maturity
(the most anthraquinone) produces.
Anthraquinone technique is that 2-ethyl-anthraquinone and organic solvent are configured to working solution, in 3atm, 55～65 DEG C and catalysis
Agent is hydrogenated with hydrogenation under participating in, then carries out counter flow oxidation at 40～44 DEG C with air, through extracting, regenerating, refines and was concentrated to give
Hydrogen oxide aqueous products.In last handling process, need to utilize activated alumina bead working solution is carried out absorption except alkali and
Regeneration degradation product, thus obtain the working solution that can be recycled, the adsorption process of activated alumina bead is then not effectively reversible
Regeneration.Alumina globule adsorbent must be changed after using a period of time, to ensure the needs that working solution regenerates.
CN 101376100A discloses the activated alumina Regeneration Treatment side of a kind of hydrogen peroxide working liquid regenerative process
Method, concrete is: the inefficacy aluminium oxide that will draw off in working solution Regenerative beds in hydrogen peroxide manufacture and the inert aluminium oxide that burns
Entering tower reactor together from top, rely on gravity to move down, oxygen-containing gas enters reaction from the bottom of tower reactor
Device, moves upward, reacted regenerative aluminium oxide and the inert aluminium oxide that burns, and discharges from the bottom discharge device of reactor,
The reacted tail gas exhaust port from reactor top discharges reactor；Reaction temperature is 360～800 DEG C, solid material
The time of staying in the reactor is 3～15 hours.Although said method avoids in conventional regeneration technique because of more than 1000 DEG C
The Al that hot conditions causes2O3The problem of bead hydraulic performance decline, but it can not effectively remove Al2O3Metal in bead from
Son and anthraquinones, and regeneration efficiency is low.
To this end, how to find regeneration efficiency high, and the high suitable renovation process of impurity removal efficacy is to discard such
Thing realizes the key of high added value recycling.
Utility model content
For problems of the prior art, this utility model provides a kind of industrial waste Al2O3Bead micropore activates
System.Described method is by activating device to discarded Al2O3Bead leach activation processing, by within bead metal ion (as
Potassium, sodium, aluminum and magnesium etc.) bag connects separation, the activation bag such as anthraquinones in 2-ethyl-anthraquinone and DMF connect simultaneously.Through micropore
The Al of activation processing2O3Bead, can improve the efficiency that subsequent regeneration processes, and then prepare the regeneration Al with superperformance2O3
Bead.
For reaching this purpose, this utility model by the following technical solutions:
This utility model provides a kind of industrial waste Al2O3Bead micropore activation system, described system includes activating device
System is utilized with waste liquid circulation；Wherein, activation device includes soot blowing dust collect plant, impregnating active module and transmitting device, transmission
Device connects soot blowing dust collect plant and impregnating active module；Soot blowing dust collect plant is positioned at activation device body material inlet one
Side, impregnating active module is placed in material outlet side in activation device body；Impregnating active module includes heat ray filter, heat insulation dress
Put and interior set gradually activating tank and drying device along transmitting device traffic direction, lowering or hoisting gear is set bottom activating tank；Activating tank
Waste liquid outlet utilize system to be connected with waste liquid circulation；
Described waste liquid circulation utilizes collecting tank, sedimentation and filtration ditch, dosing pond and the sump assemblies that system includes being sequentially connected with；
Wherein, collecting tank is positioned in activation device bottom drying device, and the waste liquid outlet of activating tank enters with the liquid of sedimentation and filtration ditch
Mouth is connected, and the liquid outlet of sump assemblies is connected with the liquid inlet of activating tank.
In this utility model, equipped with activating solution in described activating tank, described activating solution is that nanometer hydrolyzes solution of silane；Described
Nanometer hydrolysis solution of silane includes aqueous silane coupling agent, nonionic surfactant and pH adjusting agent；Described nanometer hydrolyzes
In solution of silane, the concentration of aqueous silane coupling agent is 1～20wt%；The concentration of described nonionic surfactant be 0.1～
1wt%；Described pH adjusting agent is organic acid, and its consumption is 3～6.5 for making pH value of solution.
In this utility model, the lowering or hoisting gear arranged bottom activating tank is used for making activating tank be freely lifted, when material is delivered to
During activating tank top, activating tank is risen by lowering or hoisting gear, makes material immerse in activating tank, carries out priming reaction.Described activating tank
With the function of water bath with thermostatic control, activation can be made to carry out at a constant temperature；The effect of described heat ray filter is to make at activation system
Under a heat insulation environment, activation is kept to carry out at a certain temperature.
In this utility model, described industrial waste Al2O3Bead is adsorbed with 2-ethyl-anthraquinone, trioctyl phosphate and partially
The working solutions such as trimethylbenzene and Partial digestion product, its a diameter of 3～5mm, bulk density is 0.95～1.15g/cm3。
Following as the preferred technical scheme of this utility model, but the limit of the technical scheme provided not as this utility model
System, by the following technical programs, can preferably reach and realize technical purpose of the present utility model and beneficial effect.
As the preferred technical scheme of this utility model, described activation device includes preheating device, and preheating device is along transmission
Device is arranged.Described preheating device, to the discarded Al of transport on transporter2O3Bead material preheats, to reach
Need temperature.
As the preferred technical scheme of this utility model, described transmitting device is transmission chain, and it connects soot blowing dust dress
Put and impregnating active module；Described drying device includes jet-propelled exsiccator.
As the preferred technical scheme of this utility model, described sedimentation and filtration ditch is provided with filter clean barrier film, described filter only every
Sedimentation and filtration ditch is divided into sedimentation tank and filtering ponds two parts by film, and sedimentation tank is connected with the liquid inlet of sedimentation and filtration ditch, filters
Pond is connected with the liquid outlet of sedimentation and filtration ditch.
As the preferred technical scheme of this utility model, the clean barrier film of described filter arranges ion exchange membrane.
As the preferred technical scheme of this utility model, dosing pond is provided with stirring paddle and chemicals dosing plant.
As the preferred technical scheme of this utility model, described activation device includes vacuum extractor, described vacuum means
Put and be connected with activating tank.In this utility model, described priming reaction need to be carried out under vacuum, thus need to arrange vacuum means
Put.
As the preferred technical scheme of this utility model, described activation device arranges on-line monitoring device.Described regeneration
Monitoring system is for monitoring the process conditions in micropore activation system, and then regulates each technological parameter in real time, obtains one
Individual stable activation environment.
As the preferred technical scheme of this utility model, described activation device is provided with flue gas discharge opening, and it will activate
The flue gas produced in journey is sent into waste gas purification apparatus and is purified.
This utility model is described industrial waste Al2O3The processing method of bead micropore activation system is:
Industrial waste Al2O3Little ball warp soot blowing dust collect plant dedusting and preheating device send activating tank to live after preheating
Change processes the Al after being activated2O3Bead, the waste liquid produced in activation process is sent into waste liquid circulation and is utilized system, successively through heavy
The precipitation that carries out shallow lake filtering ponds filters and dosing pond carries out feeding sump assemblies after dosing, returns again to activating tank and recycles, activation
During produce waste gas carry out purified treatment.
Compared with prior art, this utility model has the advantages that
This utility model hydrolyzes solution of silane to discarded Al by nanometer2O3Bead leaches activation processing, within bead
Metal ion (such as potassium, sodium, aluminum and magnesium etc.) bag connects separation, simultaneously by material activation bags such as Anthraquinones in 2-ethyl-anthraquinone and DMF
Connect, and then the effect that beneficially subsequent regeneration processes, prepare the regeneration Al with superperformance2O3Bead.Meanwhile, this practicality is new
The waste liquid produced in activation process and dry run is recycled by type, it is achieved that Zero discharge, is more beneficial for money
The recycling in source.
Al in this utility model, after activated process2O3The bulk density of bead is 0.94～0.98g/cm3, have suitableeer
In moisture content, bag connects reaction fully, and bead surface cleaning is smooth；Al after activated process2O3Bead is again at calcination and regeneration
After reason, preferably saving pore structure and the specific surface of material, aperture is maintained at 0.4 at the duct accumulation pore volume of 1.5～200nm
～0.50mL/g；Its bulk density is 0.75～0.85g/cm3, specific surface area is 200～300m2The metal ion of/g, its remnants
Content is less than 10 μ g/g, and remaining carbon content is less than 3 μ g/g.
Accompanying drawing explanation
Fig. 1 is industrial waste Al described in embodiment 12O3The structural representation of bead micropore activation system；
Fig. 2 is industrial waste Al described in embodiment 12O3The side-looking structural representation of bead micropore activation system；
Fig. 3 is industrial waste Al described in embodiment 12O3Bead micropore activation system circulates the structural representation of liquid mixing system
Figure；
Wherein, 1-soot blowing dust collect plant, 2-heat ray filter, 3-activating tank, 4-drying device, 5-lowering or hoisting gear, 6-preheats
Device, 7-transmission chain, 8-collecting tank, 9-sedimentation and filtration ditch, 10-dosing pond, 11-sump assemblies, 12-filters clean barrier film, and 13-sinks
Pond, shallow lake, 14-filtering ponds, 15-on-line monitoring device, 16-flue gas discharge opening.
Detailed description of the invention
For this utility model is better described, it is simple to understand the technical solution of the utility model, below to this utility model
Further describe.But following embodiment is only simple example of the present utility model, does not represent or limits this practicality
Novel rights protection scope, this utility model protection domain is as the criterion with claims.
Embodiment 1:
Present embodiments provide a kind of industrial waste Al2O3Bead micropore activation system, described system include activate device and
Waste liquid circulation utilizes system.
As depicted in figs. 1 and 2, activation device includes soot blowing dust collect plant 1, impregnating active module and transmitting device, transmission
Device connects soot blowing dust collect plant 1 and impregnating active module；Soot blowing dust collect plant 1 is positioned at activation device body material inlet one
Side, impregnating active module is placed in material outlet side in activation device body；Impregnating active module includes heat ray filter 2, heat insulation
Set gradually activating tank 3 and drying device 4 along transmitting device traffic direction in device 2, lowering or hoisting gear 5 is set bottom activating tank 3；
The waste liquid outlet of activating tank 3 utilizes system to be connected with waste liquid circulation.
Described activation device includes preheating device 6, and preheating device 6 is arranged along transmitting device；Described transmitting device is for transmitting
Chain 7, it connects soot blowing dust collect plant 1 and impregnating active module；Described drying device 4 includes jet-propelled exsiccator.Described work
Changing in pond 3 equipped with activating solution, described activating solution is that nanometer hydrolyzes solution of silane.
Described activation device includes that vacuum extractor, described vacuum extractor are connected with activating tank 3；Arrange on activation device
On-line monitoring device 15 and flue gas discharge opening 16.
As it is shown on figure 3, described waste liquid circulation utilizes collecting tank 8 that system includes being sequentially connected with, sedimentation and filtration ditch 9, dosing
Pond 10 and sump assemblies 11；Wherein, collecting tank 8 is positioned in activation device bottom drying device 4, the waste liquid outlet of activating tank 3
Being connected with the liquid inlet of sedimentation and filtration ditch 9, the liquid outlet of sump assemblies 11 is connected with the liquid inlet of activating tank 3.
Being provided with the clean barrier film 12 of filter in described sedimentation and filtration ditch 9, sedimentation and filtration ditch 9 is divided into sedimentation tank by the clean barrier film of described filter 12
13 and filtering ponds 14 two parts, sedimentation tank 13 is connected with the liquid inlet of sedimentation and filtration ditch 9, filtering ponds 14 and sedimentation and filtration ditch 9
Liquid outlet be connected.
The clean barrier film of described filter 12 arranges ion exchange membrane.
Described dosing pond 10 is provided with stirring paddle and chemicals dosing plant.
Embodiment 2:
The present embodiment uses the industrial waste Al described in embodiment 12O3Bead micropore activation system is to industrial waste
Al2O3Bead carries out activation processing, described discarded Al2O3Bead is adsorbed with 2-ethyl-anthraquinone, trioctyl phosphate, pseudocumene etc.
Working solution and Partial digestion product, diameter 3～5mm, discarded Al2O3The bulk density 0.95～1.15g/cm of bead3。
Said method comprising the steps of:
By industrial waste Al2O3Bead send into micropore activation system, its activation device in through soot blowing dust collect plant 1 dedusting
Preheating with preheating device 6, bead after pretreatment enters in heat ray filter 2 by transmission chain 7, and lowering or hoisting gear 5 will
Activating tank 3 rises, and makes Al2O3Bead immerses in activating tank 3, and activating tank 3 is the most airtight, Al2O3Bead in activating tank 3 in 60
15s, Al after activation is activated at DEG C2O3Bead is dried 35min with drying device 4 at 70 DEG C, keeps vacuum, live in activation process
Change pressure be-0.07MPa, activated process activated after Al2O3Bead.
Wherein, the activating solution in activating tank 3 is that nanometer hydrolyzes solution of silane, even including the aqueous silane that concentration is 10wt%
Connection agent, the nonionic surfactant of 0.5wt% and pH adjusting agent acetic acid, the consumption of acetic acid is 4 for making pH value of solution.
The waste liquid produced in activation process is sent into waste liquid circulation and is utilized system, carries out precipitation at sedimentation and filtration ditch 9 and filters,
After addition aqueous silane coupling agent and pH adjusting agent are configured to nanometer hydrolysis solution of silane in dosing pond 10, send into sump assemblies
11, return again to activating tank 3 and recycle, the waste gas produced in activation process carries out purified treatment.
The Al obtained is processed by method described in the present embodiment2O3The bulk density of bead is 0.97g/cm3, have suitableeer
In moisture content, bag connects reaction fully, and bead surface cleaning is smooth.
Al after activated process2O3Bead is again after calcination and regeneration processes, and its bulk density is 0.85g/cm3, specific surface area
For 208m2/ g, regeneration efficiency is 99.8%.
Embodiment 3:
The present embodiment uses the industrial waste Al described in embodiment 12O3Bead micropore activation system is to industrial waste
Al2O3Bead carries out activation processing, described industrial waste Al2O3Bead is as described in Example 2.
Said method comprising the steps of:
By industrial waste Al2O3Bead send into micropore activation system, its activation device in through soot blowing dust collect plant 1 dedusting
Preheating with preheating device 6, bead after pretreatment enters in heat ray filter 2 by transmission chain 7, and lowering or hoisting gear 5 will
Activating tank 3 rises, and makes Al2O3Bead immerses in activating tank 3, and activating tank 3 is the most airtight, Al2O3Bead in activating tank 3 in 50
30s, Al after activation is activated at DEG C2O3Bead is dried 50min with drying device 4 at 60 DEG C, keeps vacuum, live in activation process
Change pressure be-0.05MPa, activated process activated after Al2O3Bead.
Wherein, the activating solution in activating tank 3 is that nanometer hydrolyzes solution of silane, even including the aqueous silane that concentration is 20wt%
Connection agent, the nonionic surfactant of 0.6wt% and pH adjusting agent acetic acid, the consumption of acetic acid is 6.5 for making pH value of solution.
The waste liquid produced in activation process is sent into waste liquid circulation and is utilized system, carries out precipitation at sedimentation and filtration ditch 9 and filters,
After addition aqueous silane coupling agent and pH adjusting agent are configured to nanometer hydrolysis solution of silane in dosing pond 10, send into sump assemblies
11, return again to activating tank 3 and recycle, the waste gas produced in activation process carries out purified treatment.
The Al obtained is processed by method described in the present embodiment2O3The bulk density of bead is 0.94g/cm3, have more moderate
Moisture content, bag connects reaction fully, and bead surface cleaning is smooth.
Al after activated process2O3Bead is again after calcination and regeneration processes, and its bulk density is 0.75g/cm3, specific surface area
For 293m2/ g, regeneration efficiency is 99.4%.
Embodiment 4:
The present embodiment uses the industrial waste Al described in embodiment 12O3Bead micropore activation system is to industrial waste
Al2O3Bead carries out activation processing, described industrial waste Al2O3Bead is as described in Example 2.
Said method comprising the steps of:
By industrial waste Al2O3Bead send into micropore activation system, its activation device in through soot blowing dust collect plant 1 dedusting
Preheating with preheating device 6, bead after pretreatment enters in heat ray filter 2 by transmission chain 7, and lowering or hoisting gear 5 will
Activating tank 3 rises, and makes Al2O3Bead immerses in activating tank 3, and activating tank 3 is the most airtight, Al2O3Bead in activating tank 3 in 70
20s, Al after activation is activated at DEG C2O3Bead is dried 40min with drying device 4 at 80 DEG C, keeps vacuum, live in activation process
Change pressure be-0.09MPa, activated process activated after Al2O3Bead.
Wherein, the activating solution in activating tank 3 is that nanometer hydrolyzes solution of silane, even including the aqueous silane that concentration is 1wt%
Connection agent, the nonionic surfactant of 0.1wt% and pH adjusting agent acetic acid, the consumption of acetic acid is 3 for making pH value of solution.
The waste liquid produced in activation process is sent into waste liquid circulation and is utilized system, carries out precipitation at sedimentation and filtration ditch 9 and filters,
After addition aqueous silane coupling agent and pH adjusting agent are configured to nanometer hydrolysis solution of silane in dosing pond 10, send into sump assemblies
11, return again to activating tank 3 and recycle, the waste gas produced in activation process carries out purified treatment.
The Al obtained is processed by method described in the present embodiment2O3The bulk density of bead is 0.98g/cm3, have more moderate
Moisture content, bag connects reaction fully, and bead surface cleaning is smooth.
Al after activated process2O3Bead is again after calcination and regeneration processes, and bulk density is 0.83g/cm3, specific surface area is
247m2/ g, regeneration efficiency is 99.6%.
Embodiment 5:
The present embodiment uses the industrial waste Al described in embodiment 12O3Bead micropore activation system is to industrial waste
Al2O3Bead carries out activation processing, described industrial waste Al2O3Bead is as described in Example 2.
Said method comprising the steps of:
Being 60 DEG C except activation temperature in described method, soak time is 10s, and baking temperature is 90 DEG C, and drying time is
30min, activation pressure is that in-0.1MPa activating solution, the concentration of nonionic surfactant is outside 1wt%, unclassified stores consumption with
Method is the most in the same manner as in Example 2.
The Al obtained is processed by method described in the present embodiment2O3The bulk density of bead is 0.96g/cm3, have more moderate
Moisture content, bag connects reaction fully, and bead surface cleaning is smooth.
Al after activated process2O3Bead is again after calcination and regeneration processes, and its bulk density is 0.81g/cm3, specific surface area
For 253m2/ g, regeneration efficiency is 99.5%.
Comparative example 1:
In this comparative example, in addition to activation process is carried out the most under vacuum, unclassified stores consumption is equal with renovation process
In the same manner as in Example 2.
The Al obtained is processed by method described in this comparative example2O3Bead, bag connects insufficient, and activation is not thorough, and bulk density is
0.89g/cm3。
Al after activated process2O3Bead is again after calcination and regeneration processes, and its bulk density is 0.86g/cm3, specific surface area
For 198m2/ g, regeneration efficiency is 78.7%.
The result of integrated embodiment 1-5 and comparative example 1 is it can be seen that this utility model hydrolyzes solution of silane pair by nanometer
Discarded Al2O3Bead leaches activation processing, is wrapped by the metal ion (such as potassium, sodium, aluminum and magnesium etc.) within bead and connects separation, simultaneously
The material activation bags such as Anthraquinones in 2-ethyl-anthraquinone and DMF are connect, and then the effect that beneficially subsequent regeneration processes, prepare and have
The regeneration Al of superperformance2O3Bead.Meanwhile, the waste liquid produced in activation process and dry run is carried out by this utility model
Recycle, it is achieved that Zero discharge, be more beneficial for the recycling of resource.
Al in this utility model, after activated process2O3The bulk density of bead is 0.94～0.98g/cm3, have relatively
Moderate moisture content, bag connects reaction fully, and bead surface cleaning is smooth；Al after activated process2O3Bead is again through calcination and regeneration
After process, its bulk density is 0.75～0.85g/cm3, specific surface area is 200～300m2The content of the metal ion of/g, its remnants
Less than 10 μ g/g, remaining carbon content is less than 3 μ g/g.
Applicant states, this utility model illustrates method detailed of the present utility model by above-described embodiment, but this reality
It is not limited to above-mentioned method detailed with novel, does not i.e. mean that this utility model has to rely on above-mentioned method detailed ability real
Execute.Person of ordinary skill in the field is it will be clearly understood that to any improvement of the present utility model, each former to this utility model product
The equivalence of material is replaced and the interpolation of auxiliary element, concrete way choice etc., all falls within protection domain of the present utility model and public affairs
Within the scope of opening.
Claims (9)
1. an industrial waste Al2O3Bead micropore activation system, it is characterised in that described system includes activating device and waste liquid
Cyclic utilization system；Wherein, activation device includes soot blowing dust collect plant (1), impregnating active module and transmitting device, transmitting device
Connect soot blowing dust collect plant (1) and impregnating active module；Soot blowing dust collect plant (1) is positioned at activation device body material inlet one
Side, impregnating active module is placed in material outlet side in activation device body；Impregnating active module includes heat ray filter (2), every
Setting gradually activating tank (3) and drying device (4) along transmitting device traffic direction in thermal (2), activating tank (3) bottom is arranged
Lowering or hoisting gear (5)；The waste liquid outlet of activating tank (3) utilizes system to be connected with waste liquid circulation；
Described waste liquid circulation utilizes collecting tank (8), sedimentation and filtration ditch (9), dosing pond (10) and the storage that system includes being sequentially connected with
Liquid device (11)；Wherein, collecting tank (8) is positioned at drying device (4) bottom, the waste liquid outlet of activating tank (3) in activation device
It is connected with the liquid inlet of sedimentation and filtration ditch (9), the liquid inlet phase of the liquid outlet of sump assemblies (11) and activating tank (3)
Even.
Micropore activation system the most according to claim 1, it is characterised in that described activation device includes preheating device (6),
Preheating device (6) is arranged along transmitting device.
Micropore activation system the most according to claim 1, it is characterised in that described transmitting device is transmission chain (7), its
Connect soot blowing dust collect plant (1) and impregnating active module；Described drying device (4) includes jet-propelled exsiccator.
Micropore activation system the most according to claim 1, it is characterised in that be provided with filter in described sedimentation and filtration ditch (9) clean
Barrier film (12), sedimentation and filtration ditch (9) is divided into sedimentation tank (13) and filtering ponds (14) two parts by the clean barrier film of described filter (12), precipitation
Pond (13) is connected with the liquid inlet of sedimentation and filtration ditch (9), and filtering ponds (14) are connected with the liquid outlet of sedimentation and filtration ditch (9).
Micropore activation system the most according to claim 4, it is characterised in that be provided with ion in the clean barrier film of described filter (12) and hand over
Change film.
Micropore activation system the most according to claim 1, it is characterised in that described dosing pond (10) is provided with stirring paddle and
Chemicals dosing plant.
Micropore activation system the most according to claim 1, it is characterised in that described activation device includes vacuum extractor,
Described vacuum extractor is connected with activating tank (3).
Micropore activation system the most according to claim 1, it is characterised in that on-line monitoring dress is set on described activation device
Put (15).
Micropore activation system the most according to claim 1, it is characterised in that described activation device is provided with flue gas discharge opening
(16)。
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107572567A (en) * | 2016-07-05 | 2018-01-12 | 江苏中科睿赛污染控制工程有限公司 | A kind of industrial waste Al2O3Bead micropore activation system and its processing method |
| CN107597084A (en) * | 2017-09-27 | 2018-01-19 | 江苏中科睿赛污染控制工程有限公司 | Industrial waste alumina globule micropore activation equipment |
| CN107737587A (en) * | 2017-10-17 | 2018-02-27 | 江苏中科睿赛污染控制工程有限公司 | For the circulation liquid mixing system in alumina globule micropore activation system |
| CN110523367A (en) * | 2019-07-25 | 2019-12-03 | 江苏中海华核环保有限公司 | A kind of processing of alumina globule generating apparatus and technique again |
-
2016
- 2016-07-05 CN CN201620704437.8U patent/CN205833182U/en active Active
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107572567A (en) * | 2016-07-05 | 2018-01-12 | 江苏中科睿赛污染控制工程有限公司 | A kind of industrial waste Al2O3Bead micropore activation system and its processing method |
| CN107572567B (en) * | 2016-07-05 | 2019-10-01 | 江苏中科睿赛污染控制工程有限公司 | A kind of industrial waste Al2O3Bead micropore activation system and its processing method |
| CN107597084A (en) * | 2017-09-27 | 2018-01-19 | 江苏中科睿赛污染控制工程有限公司 | Industrial waste alumina globule micropore activation equipment |
| CN107737587A (en) * | 2017-10-17 | 2018-02-27 | 江苏中科睿赛污染控制工程有限公司 | For the circulation liquid mixing system in alumina globule micropore activation system |
| CN110523367A (en) * | 2019-07-25 | 2019-12-03 | 江苏中海华核环保有限公司 | A kind of processing of alumina globule generating apparatus and technique again |
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