CN110523367A - A kind of processing of alumina globule generating apparatus and technique again - Google Patents
A kind of processing of alumina globule generating apparatus and technique again Download PDFInfo
- Publication number
- CN110523367A CN110523367A CN201910676931.6A CN201910676931A CN110523367A CN 110523367 A CN110523367 A CN 110523367A CN 201910676931 A CN201910676931 A CN 201910676931A CN 110523367 A CN110523367 A CN 110523367A
- Authority
- CN
- China
- Prior art keywords
- roll
- over
- alumina globule
- elevating conveyor
- vibration material
- 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.)
- Pending
Links
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 title claims abstract description 101
- 238000012545 processing Methods 0.000 title claims abstract description 21
- 238000000034 method Methods 0.000 title claims description 31
- 230000003028 elevating effect Effects 0.000 claims abstract description 52
- 239000000463 material Substances 0.000 claims abstract description 51
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 48
- 230000007246 mechanism Effects 0.000 claims abstract description 38
- 230000004913 activation Effects 0.000 claims abstract description 30
- 239000002245 particle Substances 0.000 claims abstract description 24
- 239000002912 waste gas Substances 0.000 claims abstract description 22
- 239000012855 volatile organic compound Substances 0.000 claims description 31
- 238000007689 inspection Methods 0.000 claims description 18
- 238000004062 sedimentation Methods 0.000 claims description 18
- 239000011324 bead Substances 0.000 claims description 15
- 239000003292 glue Substances 0.000 claims description 15
- 238000001816 cooling Methods 0.000 claims description 14
- 239000007789 gas Substances 0.000 claims description 13
- 230000008569 process Effects 0.000 claims description 12
- 238000006243 chemical reaction Methods 0.000 claims description 10
- 238000007654 immersion Methods 0.000 claims description 10
- 230000037452 priming Effects 0.000 claims description 10
- 239000010813 municipal solid waste Substances 0.000 claims description 6
- 238000003860 storage Methods 0.000 claims description 6
- 238000004140 cleaning Methods 0.000 claims description 3
- 239000002893 slag Substances 0.000 claims description 3
- 239000013589 supplement Substances 0.000 claims description 3
- 238000012384 transportation and delivery Methods 0.000 claims description 3
- 238000012856 packing Methods 0.000 claims 1
- 238000004519 manufacturing process Methods 0.000 abstract description 8
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 description 14
- 239000012224 working solution Substances 0.000 description 8
- 230000006872 improvement Effects 0.000 description 7
- 230000035611 feeding Effects 0.000 description 6
- 239000000428 dust Substances 0.000 description 5
- 238000012546 transfer Methods 0.000 description 5
- KFZMGEQAYNKOFK-UHFFFAOYSA-N Isopropanol Chemical compound CC(C)O KFZMGEQAYNKOFK-UHFFFAOYSA-N 0.000 description 4
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 4
- 229910052782 aluminium Inorganic materials 0.000 description 4
- 239000004411 aluminium Substances 0.000 description 4
- PYKYMHQGRFAEBM-UHFFFAOYSA-N anthraquinone Natural products CCC(=O)c1c(O)c2C(=O)C3C(C=CC=C3O)C(=O)c2cc1CC(=O)OC PYKYMHQGRFAEBM-UHFFFAOYSA-N 0.000 description 4
- 150000004056 anthraquinones Chemical class 0.000 description 4
- 238000007599 discharging Methods 0.000 description 4
- WHRIKZCFRVTHJH-UHFFFAOYSA-N ethylhydrazine Chemical compound CCNN WHRIKZCFRVTHJH-UHFFFAOYSA-N 0.000 description 4
- 238000004064 recycling Methods 0.000 description 4
- 231100000331 toxic Toxicity 0.000 description 4
- 230000002588 toxic effect Effects 0.000 description 4
- 230000008859 change Effects 0.000 description 3
- 230000013011 mating Effects 0.000 description 3
- 230000008929 regeneration Effects 0.000 description 3
- 238000011069 regeneration method Methods 0.000 description 3
- 238000010521 absorption reaction Methods 0.000 description 2
- 239000003463 adsorbent Substances 0.000 description 2
- 239000003513 alkali Substances 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 238000006555 catalytic reaction Methods 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 2
- 239000011248 coating agent Substances 0.000 description 2
- 238000000576 coating method Methods 0.000 description 2
- 230000000052 comparative effect Effects 0.000 description 2
- 239000002131 composite material Substances 0.000 description 2
- 239000007857 degradation product Substances 0.000 description 2
- 239000000645 desinfectant Substances 0.000 description 2
- 238000001514 detection method Methods 0.000 description 2
- 239000003814 drug Substances 0.000 description 2
- 238000004043 dyeing Methods 0.000 description 2
- 238000005868 electrolysis reaction Methods 0.000 description 2
- 238000000605 extraction Methods 0.000 description 2
- 239000000446 fuel Substances 0.000 description 2
- 239000001257 hydrogen Substances 0.000 description 2
- 229910052739 hydrogen Inorganic materials 0.000 description 2
- 125000004435 hydrogen atom Chemical class [H]* 0.000 description 2
- 238000005984 hydrogenation reaction Methods 0.000 description 2
- 239000003960 organic solvent Substances 0.000 description 2
- 230000003647 oxidation Effects 0.000 description 2
- 238000007254 oxidation reaction Methods 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 239000000047 product Substances 0.000 description 2
- 230000002441 reversible effect Effects 0.000 description 2
- 239000010865 sewage Substances 0.000 description 2
- 238000001179 sorption measurement Methods 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 239000004753 textile Substances 0.000 description 2
- 238000010586 diagram Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 238000004806 packaging method and process Methods 0.000 description 1
- 238000007670 refining Methods 0.000 description 1
- 231100000004 severe toxicity Toxicity 0.000 description 1
- 239000002341 toxic gas Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/02—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
- B01J20/06—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising oxides or hydroxides of metals not provided for in group B01J20/04
- B01J20/08—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising oxides or hydroxides of metals not provided for in group B01J20/04 comprising aluminium oxide or hydroxide; comprising bauxite
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/30—Processes for preparing, regenerating, or reactivating
- B01J20/34—Regenerating or reactivating
- B01J20/3433—Regenerating or reactivating of sorbents or filter aids other than those covered by B01J20/3408 - B01J20/3425
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01F—COMPOUNDS OF THE METALS BERYLLIUM, MAGNESIUM, ALUMINIUM, CALCIUM, STRONTIUM, BARIUM, RADIUM, THORIUM, OR OF THE RARE-EARTH METALS
- C01F7/00—Compounds of aluminium
- C01F7/02—Aluminium oxide; Aluminium hydroxide; Aluminates
- C01F7/021—After-treatment of oxides or hydroxides
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Analytical Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Life Sciences & Earth Sciences (AREA)
- Geology (AREA)
- Catalysts (AREA)
Abstract
A kind of alumina globule processing generating apparatus again, elevating conveyor lower end is impregnated in circulating water pool, roll-over setting is on impregnating elevating conveyor in No. 1, there is vibration material grain machine 1 in No. 1 under roll-over, vibration material grain machine 1 connects activation equipment furnace, there is waste gas treatment mechanism 1 on activation equipment furnace, roll-over is under activation equipment furnace in No. 2, under elevating conveyor 1 in No. 2 under roll-over, roll-over is on elevating conveyor 1 in No. 3, there is vibration material grain machine 2 in No. 3 under roll-over, there is roll-over in No. 4 under vibration material grain machine 2, roll-over is arranged in meshbeltfurnace one end in No. 4, there are waste gas treatment mechanism 2 on meshbeltfurnace, there is coolconveyer in meshbeltfurnace side, there is roll-over in No. 5 under coolconveyer one end, roll-over is in the upper of No. 2 lower ends of elevating conveyor in No. 5, elevating conveyor has roll-over in No. 6 under No. 2 upper ends, No. 6 There is particle jumbo bag to fill chartered plane under middle roll-over discharge gate.The utilization rate that alumina globule can be improved in the present invention reduces production cost.
Description
Technical field
The present invention relates to industrial resources recycling field, more particularly to a kind of processing of alumina globule again generating apparatus and
Technique.
Background technique
Hydrogen peroxide is also known as hydrogen peroxide, drift in chemical industry, pharmaceuticals industry, printing and dyeing industry, intermetallic composite coating, textile,
Military project fuel and civilian disinfectant etc. are all many-sided all with extensive and irreplaceable purposes.The Hydrogen Peroxide Production in China at present
In addition to only a few is still other than using electrolysis method and isopropanol method, the overwhelming majority uses the 2- ethyl hydrazine methods of comparative maturity for enterprise
(also referred to as anthraquinone) production.
Anthraquinone technique is that 2- ethyl hydrazine and organic solvent are configured to working solution, in 3atm, 55~65 DEG C and catalysis
Agent participates in lower plus hydrogen hydrogenation, then carries out counter flow oxidation with air at 40~44 DEG C, through extraction, regeneration, refines and was concentrated to get
Hydrogen oxide aqueous products.In last handling process, need using activated alumina bead to working solution carry out absorption except alkali and
Degradation product is regenerated, thus the working solution that can be recycled, and the adsorption process of activated alumina bead is then not effectively reversible
It is regenerated.Alumina globule adsorbent must be replaced after a period of use, to guarantee the regenerated needs of working solution.
Hydrogen peroxide is also known as hydrogen peroxide, drift in chemical industry, pharmaceuticals industry, printing and dyeing industry, intermetallic composite coating, textile,
Military project fuel and civilian disinfectant etc. are all many-sided all with extensive and irreplaceable purposes.The Hydrogen Peroxide Production in China at present
In addition to only a few is still other than using electrolysis method and isopropanol method, the overwhelming majority uses the 2- ethyl hydrazine methods of comparative maturity for enterprise
(also referred to as anthraquinone) production.
Anthraquinone technique is that 2- ethyl hydrazine and organic solvent are configured to working solution, in 3atm, 55~65 DEG C and catalysis
Agent participates in lower plus hydrogen hydrogenation, then carries out counter flow oxidation with air at 40~44 DEG C, through extraction, regeneration, refines and was concentrated to get
Hydrogen oxide aqueous products.In last handling process, need using activated alumina bead to working solution carry out absorption except alkali and
Degradation product is regenerated, thus the working solution that can be recycled, and the adsorption process of activated alumina bead is then not effectively reversible
It is regenerated.Alumina globule adsorbent must be replaced after a period of use, to guarantee the regenerated needs of working solution.
So if recycling for alumina globule may be implemented, so that it may substantially save the cost is small according to aluminium oxide
Ball feature can carry out regeneration treatment to alumina globule by priming reaction, thus realize recycling for alumina globule,
But the alumina globule after has severe toxicity, actual treatment can generate large quantity of exhaust gas waste material and pollute, according to above situation
Applicant designs a kind of full-automatic alumina globule processing generating apparatus and technique again.
Summary of the invention
To solve the above problems, the present invention provides a kind of processing of alumina globule generating apparatus and technique again, leads to
Pipeline system is crossed to handle used alumina globule, and in treatment process mating corresponding exhaust-gas treatment to
Pollution and activation rate are reduced, so that improving the utilization rate of alumina globule reduces production cost, for this purpose, the present invention mentions
For a kind of alumina globule processing roll-over in generating apparatus, including No. 1, roll-over in No. 2, roll-over in No. 3, roll-over, No. 5 in No. 4 again
Middle roll-over, circulating water pool, impregnates elevating conveyor, vibration material grain machine 1, activation equipment furnace, VOCs exhaust-gas treatment at roll-over in No. 6
Mechanism 1, elevating conveyor 1, vibration material grain machine 2, meshbeltfurnace, coolconveyer, elevating conveyor 2, particle jumbo bag
Filling chartered plane, belt or roller conveyor and VOCs waste gas treatment mechanism 2, the circulating water pool includes sedimentation basin and clear water reserviors,
The sedimentation basin has blowdown slag-drip opening, and the clear water reserviors, which have, mends water pipe road junction, and the immersion elevating conveyor lower end is recycling
In the sedimentation basin in pond, roll-over setting is being impregnated below elevating conveyor upper port in described No. 1, the row of roll-over in described No. 1
There is vibration material grain machine 1 below material mouth, the charging of the side of activation equipment furnace is connect below described No. 1 discharge gate of vibration material grain machine
Mouthful, there is VOCs waste gas treatment mechanism 1 above the activation equipment furnace other side, discharging of the roll-over in activation equipment furnace in described No. 2
Mouthful lower section, the lower section of No. 1 lower end discharge gate of roll-over in No. 2 of the elevating conveyor, the feed inlet of roll-over exists in described No. 3
Below No. 1 upper end of elevating conveyor, there are vibration material grain machine 2, the vibration material grain below the discharge gate of roll-over in described No. 3
There is roll-over in No. 4 below No. 2 discharge gates of machine, assembly line charging one is arranged in meshbeltfurnace in the discharge gate of roll-over in described No. 4
It holds, has VOCs waste gas treatment mechanism 2 on the meshbeltfurnace, there are coolconveyer, the cooling conveying in the meshbeltfurnace side
There is row's cooling fan above machine, assembly line connects with assembly line in coolconveyer in the meshbeltfurnace, the cooling conveying
Assembly line, which discharges below one end, in machine roll-over in No. 5, and the discharge port of roll-over is in No. 2 lower ends of elevating conveyor in described No. 5
There is roll-over in No. 6 in top below No. 2 upper ends of the elevating conveyor, has particle ton below roll-over discharge gate in described No. 6
Alumina globule is transported out by packed chartered plane, the belt or roller conveyor below particle jumbo bag dress chartered plane.
The further improvement of present device, the coolconveyer side have row set glue inspection to pick equipment, the set glue
Inspection pick equipment there are two inspection pick confession hand entrance, coolconveyer side be provided with set glue inspection pick equipment alumina globule pass through
Assembly line feeding coolconveyer cool down entering examine by manpower and be picked, and some problematic particles is detected, due to oxygen
Change aluminium bead it is toxic should need to cover glue inspection pick.
The further improvement of present device, the immersion elevating conveyor and circulating water pool lower end are mounted on pairs of
Locking wheel, setting locking wheel can be convenient running fix.
The further improvement of present device, in described No. 1 between roll-over and vibration material grain machine 1 and roll-over in No. 3
With vibration material grain machine 2 between be provided with adjustable quantitative unloader, discharging too fast influence vibration material grain machine work in order to prevent is set
Set adjustable quantitative unloader.
The further improvement of present device, the band plate of roll-over lower part duckbilled in described No. 4, roll-over in described No. 4
Alumina globule can uniformly be ascended a height be sent into assembly line in this way by duckbilled discharge port with bandwidth and with rubbing board.
The further improvement of present device, coolconveyer outlet side are provided with dedusting mechanism, cooling conveying
Machine outlet side has dedusting mechanism to be dusted processing, and coolconveyer sends out that treated, and alumina globule can be with centainly
Therefore dust needs that dedusting mechanism is arranged.
The present invention provides a kind of technique that alumina globule handles again generating apparatus, the specific steps are as follows:
1) alumina globule is sent into circulating water pool and passes through sedimentation basin and clear water reserviors, sedimentation basin passes through blowdown slag-drip opening for sewage
It is discharged with slag, clear water reserviors, which then pass through, mends water pipe road junction progress clear water supplement；
2) it impregnates elevating conveyor to send the alumina globule after cleaning in circulating water pool to roll-over in No. 1, oxygen in roll-over in No. 1
Change aluminium bead and vibration material grain machine 1 be discharged by adjustable quantitative unloader, then by vibration material grain machine No. 1 3-5mm bead is discharged,
Remaining is discharged into trash receptacle, enters activation equipment furnace later and carries out priming reaction；
3) activation equipment furnace carries out priming reaction and passes through VOCs waste gas treatment mechanism 1 simultaneously and be passed through VOCs to carry out exhaust-gas treatment, living
Change machine furnace carries out priming reaction and is sent into roll-over in No. 2, and alumina globule passes through elevating conveyor 1 feeding 3 in roll-over in No. 2
Middle roll-over, alumina globule by adjustable quantitative unloader is discharged into vibration material grain machine 2 in roll-over in No. 3, then by vibration material grain
Machine 2 discharge 3-5mm bead, remaining is discharged into trash receptacle, enter roll-over in No. 4 later, by roll-over in No. 4 by alumina globule
Spread assembly line in meshbeltfurnace；
4) alumina globule is sent into meshbeltfurnace by assembly line and is handled by meshbeltfurnace, has VOCs exhaust-gas treatment at the top of meshbeltfurnace
Mechanism 2, meshbeltfurnace, which handles while being passed through VOCs, carries out exhaust-gas treatment, and alumina globule is sent into cooling defeated by assembly line later
Roll-over in No. 5 is sent into after sending machine to carry out cooling, alumina globule passes through No. 6 transfers of elevating conveyor 2 feedings in roll-over in No. 5
Storehouse, the alumina globule that processing is completed in roll-over in No. 6 are sent into particle jumbo bag and fill chartered plane, and particle jumbo bag fills chartered plane, and aluminium oxide is small
It is sent out by belt or roller conveyor for storage, storage and delivery after the completion of ball packaging.
The further improvement of present invention process, coolconveyer side, which is provided with set glue inspection and picks equipment, in step 4 is aoxidizing
Aluminium bead cool down by assembly line feeding coolconveyer entering examine by manpower and be picked, and the purpose of this step is will be some
Problematic particle detection should need to cover glue inspection since alumina globule is toxic and pick.
The further improvement of present invention process, coolconveyer outlet side has dedusting mechanism to be dusted place in step 4
Reason, coolconveyer, which sends out treated alumina globule, therefore to be needed that dedusting mechanism is arranged with certain dust.
A kind of alumina globule of the present invention handles generating apparatus and technique again, using full-automatic assembly line to alumina globule
It is handled, handles in engineering and alumina globule is activated by VOCs exhaust treatment system, and carry out dust receipts
Collection, so as to reduce toxic gas discharge, and it is mating pick up refining, so as to filter out useful aluminium oxide to greatest extent
To improve the utilization rate of alumina globule, and then the production cost of alumina globule can be greatly reduced in bead.
Detailed description of the invention
Fig. 1 is present invention process equipment schematic diagram；
Fig. 2 is process flow chart of the invention；
It is now that the label declaration in attached drawing is as follows:
1, roll-over in No. 1, roll-over in 2, No. 2, roll-over in 3, No. 3, roll-over in 4, No. 4, roll-over in 5, No. 5, roll-over in 6, No. 6,
7, circulating water pool, 8, immersion elevating conveyor, 9, vibration material grain machine 1,10, activation equipment furnace, 11, VOCs waste gas treatment mechanism 1
Number, 12, elevating conveyor 1,13, vibration material grain machine 2,14, meshbeltfurnace, 15, coolconveyer, 16, elevating conveyor 2
Number, 17, particle jumbo bag dress chartered plane, 18, belt or roller conveyor；19, VOCs waste gas treatment mechanism 2.
Specific embodiment
Present invention is further described in detail with specific embodiment with reference to the accompanying drawing:
The present invention provides a kind of processing of alumina globule generating apparatus and technique again, by pipeline system to used aluminium oxide
Bead is handled, and mating corresponding exhaust-gas treatment is in treatment process to reduce pollution and activation rate, to improve
The utilization rate of alumina globule reduces production cost.
As a kind of embodiment of structure of the invention, the present invention provides a kind of alumina globule processing generating apparatus again, including No. 1
Roll-over 6, circulating water pool 7, immersion in roll-over 5,6 in roll-over 4,5 in roll-over 3,4 in roll-over 2,3 in middle roll-over 2,2
Elevating conveyor 8, vibration material grain machine No. 19, activation equipment furnace 10, VOCs waste gas treatment mechanism No. 1 11, elevating conveyor No. 1 12,
Vibration material grain machine No. 2 13, meshbeltfurnace 14, coolconveyer 15, elevating conveyor No. 2 16, particle jumbo bag dress chartered plane 17, belt or
Roller conveyor 18 and VOCs waste gas treatment mechanism No. 2 19, it is characterised in that: the circulating water pool 7 includes sedimentation basin and clear water
Pond, the sedimentation basin have blowdown slag-drip opening, and the clear water reserviors, which have, mends water pipe road junction, and 8 lower end of immersion elevating conveyor exists
In the sedimentation basin of circulating water pool 7, the setting of roll-over 1 is being impregnated below 8 upper port of elevating conveyor in described No. 1, No. 1 transfer
There is vibration material grain machine No. 19 below the discharge gate in storehouse 1, connects activation equipment furnace 10 below described No. 19 discharge gates of vibration material grain machine
Side feed inlet, have VOCs waste gas treatment mechanism No. 1 11 above 10 other side of activation equipment furnace, roll-over 2 in described No. 2
Below the discharge port of activation equipment furnace 10, the lower section of No. 1 12 lower ends discharge gate of roll-over 2 in No. 2 of the elevating conveyor, institute
The feed inlet of roll-over 3 in No. 3 is stated below No. 1 12 upper ends of elevating conveyor, is had below the discharge gate of roll-over 3 in described No. 3
Vibration material grain machine No. 2 13 has roll-over 4 in No. 4 below described No. 2 13 discharge gates of vibration material grain machine, roll-over 4 in described No. 4
Discharge gate is arranged in meshbeltfurnace 14 assembly line and feeds one end, has VOCs waste gas treatment mechanism No. 2 19 on the meshbeltfurnace 14, institute
Stating 14 side of meshbeltfurnace has coolconveyer 15, there is row's cooling fan, the meshbeltfurnace 14 above the coolconveyer 15
Interior assembly line connects with assembly line in coolconveyer 15, and assembly line, which discharges below one end, in the coolconveyer 15 No. 5
Middle roll-over 5, the discharge port of roll-over 5 is in the top of No. 2 16 lower ends of elevating conveyor, the elevating conveyor No. 2 16 in described No. 5
There is roll-over 6 in No. 6 below upper end, there is particle jumbo bag to fill chartered plane 17, the belt below 6 discharge gate of roll-over in described No. 6
Or alumina globule is transported out by roller conveyor 18 below particle jumbo bag dress chartered plane 17.
As a kind of specific embodiment of structure of the invention, the present invention provides a kind of alumina globule processing as shown in Figure 1 again
Roll-over 6 in roll-over 5,6 in roll-over 4,5 in roll-over 3,4 in roll-over 2,3 in roll-over 2,2 in generating apparatus, including No. 1,
Circulating water pool 7 impregnates elevating conveyor 8, vibration material grain machine No. 19, activation equipment furnace 10, VOCs waste gas treatment mechanism No. 1 11, mentions
Rise conveyer No. 1 12, vibration material grain machine No. 2 13, meshbeltfurnace 14, coolconveyer 15, elevating conveyor No. 2 16, particle jumbo bag
Fill chartered plane 17, belt or roller conveyor 18 and VOCs waste gas treatment mechanism No. 2 19, it is characterised in that: the circulating water pool 7 wraps
Sedimentation basin and clear water reserviors are included, the sedimentation basin has blowdown slag-drip opening, and the clear water reserviors, which have, mends water pipe road junction, and the immersion is promoted
In the sedimentation basin of circulating water pool 7, the immersion elevating conveyor 8 and 7 lower end of circulating water pool are mounted on into 8 lower end of transporter
Pair locking wheel, setting locking wheel can be convenient running fix, in described No. 1 roll-over 1 setting impregnate 8 upper end of elevating conveyor
Below mouthful, there are vibration material grain machine No. 19, described No. 19 discharge gates of vibration material grain machine below the discharge gate of roll-over 1 in described No. 1
Lower section connect activation equipment furnace 10 side feed inlet, have VOCs waste gas treatment mechanism 1 above 10 other side of activation equipment furnace
Numbers 11, roll-over 2 is below the discharge port of activation equipment furnace 10 in described No. 2, and No. 1 12 lower ends of the elevating conveyor are in No. 2 transfers
The lower section of the discharge gate in storehouse 2, the feed inlet of roll-over 3 is below No. 1 12 upper ends of elevating conveyor in described No. 3, No. 3 transfers
There is vibration material grain machine No. 2 13 below the discharge gate in storehouse 3, in described No. 1 between roll-over 2 and vibration material grain machine No. 19 and No. 3
It is provided with adjustable quantitative unloader between middle roll-over 3 and vibration material grain machine No. 2 13, in order to prevent the too fast influence vibration material grain of discharging
Machine work setting adjustable quantitative unloader, there is roll-over 4 in No. 4 below described No. 2 13 discharge gates of vibration material grain machine, and described No. 4
The band plate of middle roll-over lower part duckbilled, the duckbilled discharge port of roll-over can will aoxidize in this way with bandwidth and with rubbing board in described No. 4
Aluminium bead, which is uniformly ascended a height, to be sent into assembly line, and assembly line charging one is arranged in meshbeltfurnace 14 in the discharge gate of roll-over 4 in described No. 4
It holds, has VOCs waste gas treatment mechanism No. 2 19 on the meshbeltfurnace 14, there is coolconveyer 15 in 14 side of meshbeltfurnace, described
There is row's cooling fan above coolconveyer 15, assembly line and assembly line phase in coolconveyer 15 in the meshbeltfurnace 14
Connect, 15 side of coolconveyer has a row to cover glue inspection to pick equipment, the set glue inspection pick equipment there are two inspection pick confession hand into
Enter, coolconveyer side be provided with set glue inspection pick equipment alumina globule by assembly line be sent into coolconveyer carry out it is cold
But enter examine by manpower and pick, some problematic particles are detected, should need to cover glue inspection since alumina globule is toxic
It picks, assembly line, which discharges below one end, in the coolconveyer 15 roll-over 5 in No. 5, and the coolconveyer 15 exports side
It is provided with dedusting mechanism, coolconveyer outlet side has dedusting mechanism to be dusted processing, the processing that coolconveyer is sent out
Therefore alumina globule afterwards can need to be arranged dedusting mechanism with certain dust, the discharge port of roll-over 5 is being promoted in described No. 5
There are roll-over 6 in No. 6, roll-over in described No. 6 in the top of No. 2 16 lower ends of conveyer below No. 2 16 upper ends of the elevating conveyor
There is particle jumbo bag to fill chartered plane 17, the belt or roller conveyor 18 below particle jumbo bag dress chartered plane 17 below 6 discharge gates
Alumina globule is transported out.
As a kind of specific embodiment of present invention process, the present invention provides a kind of alumina globule processing as shown in Figure 2 again
The technique of generating apparatus, the specific steps are as follows:
Alumina globule is sent into circulating water pool 7 by 1 passes through sedimentation basin and clear water reserviors, and sedimentation basin passes through blowdown slag-drip opening for sewage
It is discharged with slag, clear water reserviors, which then pass through, mends water pipe road junction progress clear water supplement；
2 immersion elevating conveyors 8 send the alumina globule after cleaning in circulating water pool 7 to the roll-over 2 into No. 1 roll-over 2,1
Middle alumina globule is discharged into vibration material grain machine No. 19 by adjustable quantitative unloader, then No. 19 that 3-5mm is small by vibration material grain machine
Ball discharging, remaining is discharged into trash receptacle, enters activation equipment furnace 10 later and carries out priming reaction；
3 activation equipment furnaces 10 progress priming reaction passes through VOCs waste gas treatment mechanism No. 1 11 simultaneously and is passed through VOCs progress exhaust-gas treatment,
Alumina globule passes through elevating conveyor 1 in roll-over 2 in roll-over 2,2 in the progress priming reaction of activation equipment furnace 10 feeding 2
12, which are sent into No. 3 in roll-over 3,3 in roll-over 3 alumina globule, is discharged into vibration material grain machine No. 2 13 by adjustable quantitative unloader,
Again by vibration material grain machine No. 2 13 3-5mm bead is discharged, remaining is discharged into trash receptacle, later enter No. 4 in roll-over 4, by No. 4
Alumina globule is spread assembly line in meshbeltfurnace 14 by roll-over 4；
4 alumina globules are sent into meshbeltfurnace 14 by assembly line and are handled by meshbeltfurnace 14, have VOCs useless at the top of meshbeltfurnace 14
Gas disposal mechanism No. 2 19, meshbeltfurnace 14, which handles while being passed through VOCs, carries out exhaust-gas treatment, and alumina globule passes through assembly line later
Be sent into coolconveyer 15 carry out it is cooling after be sent into roll-over 5 in No. 5,15 side of coolconveyer, which is provided with set glue inspection and picks equipment, to exist
Alumina globule by assembly line be sent into coolconveyer carry out it is cooling enter examine by manpower pick, the purpose of this step be by
Some problematic particle detections, should need to cover glue inspection since alumina globule is toxic and pick, coolconveyer 15, which exports side, to be had
Dedusting mechanism is dusted processing, and coolconveyer sends out that treated therefore alumina globule can be needed with certain dust
Dedusting mechanism is set, and alumina globule passes through 6, No. 6 transfers of roll-over in elevating conveyor No. 2 16 feedings 6 in roll-over 5 in No. 5
The alumina globule that processing is completed in storehouse 6 is sent into particle jumbo bag and fills chartered plane 17, and particle jumbo bag fills chartered plane 17 for alumina globule packet
It is sent out by belt or roller conveyor 18 for storage, storage and delivery after the completion of dress.
The above described is only a preferred embodiment of the present invention, being not the limit for making any other form to the present invention
System, and made any modification or equivalent variations according to the technical essence of the invention, still fall within present invention model claimed
It encloses.
Claims (9)
1. a kind of alumina globule processing roll-over (2) in generating apparatus, including No. 1, roll-over (2) in No. 2, roll-over (3), 4 in No. 3 again
Roll-over (4) in number, roll-over (5) in No. 5, circulating water pool (7), impregnate elevating conveyor (8), vibration material grain at roll-over (6) in No. 6
Machine 1 (9), activation equipment furnace (10), VOCs waste gas treatment mechanism 1 (11), elevating conveyor 1 (12), vibration material grain machine 2
(13), meshbeltfurnace (14), coolconveyer (15), elevating conveyor 2 (16), particle jumbo bag dress chartered plane (17), belt or roller
Formula conveyer (18) and VOCs waste gas treatment mechanism 2 (19), it is characterised in that: the circulating water pool (7) include sedimentation basin and
Clear water reserviors, the sedimentation basin have blowdown slag-drip opening, and the clear water reserviors, which have, mends water pipe road junction, the immersion elevating conveyor (8)
Lower end is in the sedimentation basin of circulating water pool (7), and roll-over (1) is arranged in the case where impregnating elevating conveyor (8) upper port in described No. 1
It is square, there are vibration material grain machine 1 (9), described vibration material grain machine 1 (9) discharge below the discharge gate of roll-over (1) in described No. 1
The lower section of mouth connects the feed inlet of the side of activation equipment furnace (10), has VOCs exhaust-gas treatment above activation equipment furnace (10) other side
Mechanism 1 (11), roll-over (2) is below the discharge port of activation equipment furnace (10) in described No. 2, the elevating conveyor 1 (12)
The lower section of lower end discharge gate of roll-over (2) in No. 2, the feed inlet of roll-over (3) is at elevating conveyor 1 (12) in described No. 3
Below upper end, there is vibration material grain machine 2 (13) in described No. 3 below the discharge gate of roll-over (3), described vibration material grain machine 2
(13) there are roll-over (4) in No. 4 below discharge gate, the discharge gate of roll-over (4) in described No. 4 is arranged in meshbeltfurnace (14) interior flowing water
Line feeds one end, has VOCs waste gas treatment mechanism 2 (19) on the meshbeltfurnace (14), there is cooling in meshbeltfurnace (14) side
Conveyer (15), there is row's cooling fan above the coolconveyer (15), the interior assembly line of the meshbeltfurnace (14) and cooling
Conveyer (15) interior assembly line connects, and the interior assembly line of the coolconveyer (15), which discharges below one end, roll-over (5) in No. 5,
The discharge port of roll-over (5) is on the top of elevating conveyor 2 (16) lower ends, the elevating conveyor 2 (16) in described No. 5
There are roll-over (6) in No. 6 below end, there is particle jumbo bag to fill chartered plane (17) below roll-over (6) discharge gate in described No. 6, it is described
Alumina globule is transported out by belt or roller conveyor (18) below particle jumbo bag dress chartered plane (17).
2. a kind of alumina globule according to claim 1 handles generating apparatus again, it is characterised in that: the coolconveyer
(15) side has a row to cover glue inspection to pick equipment, and the set glue inspection picks equipment, and there are two inspections to pick the entrance of confession hand.
3. a kind of alumina globule according to claim 1 handles generating apparatus again, it is characterised in that: the immersion promotes fortune
Defeated machine (8) and circulating water pool (7) lower end are mounted on pairs of locking wheel.
4. a kind of alumina globule according to claim 1 handles generating apparatus again, it is characterised in that: roll-over in described No. 1
(2) it is provided with and can set up between vibration material grain machine 1 (9) and in No. 3 between roll-over (3) and vibration material grain machine 2 (13)
Measure unloader.
5. a kind of alumina globule according to claim 1 handles generating apparatus again, it is characterised in that: roll-over in described No. 4
(4) the band plate of lower part duckbilled, the duckbilled discharge port of roll-over (4) is with bandwidth and with rubbing board in described No. 4.
6. a kind of alumina globule according to claim 1 handles generating apparatus again, it is characterised in that: the coolconveyer
(15) outlet side is provided with dedusting mechanism.
7. a kind of alumina globule handles again the technique of generating apparatus, specific step is as follows, it is characterised in that:
1) alumina globule is sent into circulating water pool (7) and passes through sedimentation basin and clear water reserviors, sedimentation basin will be dirty by blowdown slag-drip opening
Water and slag discharge, clear water reserviors, which then pass through, mends water pipe road junction progress clear water supplement；
2) it impregnates elevating conveyor (8) to send the alumina globule after cleaning in circulating water pool (7) to roll-over (2) in No. 1, No. 1
Alumina globule is discharged into vibration material grain machine 1 (9) by adjustable quantitative unloader in middle roll-over (2), then by vibration material grain machine 1
(9) 3-5mm bead is discharged, remaining is discharged into trash receptacle, enters activation equipment furnace (10) later and carries out priming reaction；
3) activation equipment furnace (10) carry out priming reaction simultaneously pass through VOCs waste gas treatment mechanism 1 (11) be passed through VOCs carry out exhaust gas
Processing, activation equipment furnace (10) carry out priming reaction and are sent into roll-over (2) in No. 2, and alumina globule process mentions in roll-over (2) in No. 2
It rises conveyer 1 (12) and is sent into roll-over (3) in No. 3, alumina globule is arranged by adjustable quantitative unloader in roll-over (3) in No. 3
Enter vibration material grain machine 2 (13), then 3-5mm bead is discharged by vibration material grain machine 2 (13), remaining is discharged into trash receptacle, later
Into roll-over (4) in No. 4, alumina globule is spread into meshbeltfurnace (14) interior assembly line by roll-over (4) in No. 4；
4) alumina globule is sent into meshbeltfurnace (14) by assembly line and is handled by meshbeltfurnace (14), has at the top of meshbeltfurnace (14)
VOCs waste gas treatment mechanism 2 (19), meshbeltfurnace (14), which handles while being passed through VOCs, carries out exhaust-gas treatment, later alumina globule
It is sent into after coolconveyer (15) carry out cooling by assembly line and is sent into roll-over (5) in No. 5, aluminium oxide is small in roll-over (5) in No. 5
Ball warp crosses elevating conveyor 2 (16) and is sent into roll-over (6) in No. 6, and the alumina globule that processing is completed is sent in roll-over (6) in No. 6
Enter particle jumbo bag dress chartered plane (17), particle jumbo bag dress chartered plane (17) is conveyed after the completion of packing alumina globule by belt or roll-type
Machine (18) is sent out for storage, storage and delivery.
8. the technique that a kind of alumina globule according to claim 7 handles again generating apparatus, it is characterised in that:
In step 4 coolconveyer (15) side be provided with set glue inspection pick equipment alumina globule by assembly line be sent into it is cold
But conveyer (15) cool down entering examine by manpower and be picked.
9. the technique that a kind of alumina globule according to claim 7 handles again generating apparatus, it is characterised in that: in step 4
Coolconveyer (15) outlet side has dedusting mechanism to be dusted processing.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910676931.6A CN110523367A (en) | 2019-07-25 | 2019-07-25 | A kind of processing of alumina globule generating apparatus and technique again |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910676931.6A CN110523367A (en) | 2019-07-25 | 2019-07-25 | A kind of processing of alumina globule generating apparatus and technique again |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN110523367A true CN110523367A (en) | 2019-12-03 |
Family
ID=68660991
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201910676931.6A Pending CN110523367A (en) | 2019-07-25 | 2019-07-25 | A kind of processing of alumina globule generating apparatus and technique again |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN110523367A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113426432A (en) * | 2021-07-07 | 2021-09-24 | 江苏磊金环境工程有限公司 | Production line and process for utilizing regenerated resources of saturated activated alumina pellets |
| CN113441123A (en) * | 2021-07-07 | 2021-09-28 | 江苏磊金环境工程有限公司 | Thermal desorption regeneration production line and process for saturated activated alumina pellets |
Citations (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102499448A (en) * | 2011-10-11 | 2012-06-20 | 中国烟草总公司郑州烟草研究院 | Production line for bagged buccal smokeless tobacco product preparation |
| CN103394686A (en) * | 2013-07-25 | 2013-11-20 | 莱芜钢铁集团有限公司 | Two-stage dry mixing method for powder metallurgy iron-based mixed powder |
| CN204198710U (en) * | 2014-08-19 | 2015-03-11 | 北京乾海环保科技有限公司 | Semicoke produces civilian clean moulded coal production line |
| CN105384372A (en) * | 2015-11-27 | 2016-03-09 | 山东先罗输送机械有限公司 | Method and device for preparing building gypsum from desulfurized gypsum |
| CN105664857A (en) * | 2016-04-20 | 2016-06-15 | 福建元力环境工程有限公司 | Clean, environment-friendly and efficient activated carbon regeneration device |
| CN205833182U (en) * | 2016-07-05 | 2016-12-28 | 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 |
| CN205868282U (en) * | 2016-07-05 | 2017-01-11 | 江苏中科睿赛污染控制工程有限公司 | Industry abandonment al2O3 bobble regeneration system |
| CN107583635A (en) * | 2017-09-23 | 2018-01-16 | 江苏中科睿赛污染控制工程有限公司 | Industrial waste alumina globule is segmented regenerating unit |
| CN107617413A (en) * | 2017-09-28 | 2018-01-23 | 江苏中科睿赛污染控制工程有限公司 | Industrial waste alumina globule regenerative system and renovation process |
| CN211159809U (en) * | 2019-07-25 | 2020-08-04 | 江苏中海华核环保有限公司 | Regeneration facility is handled to aluminium oxide bobble |
-
2019
- 2019-07-25 CN CN201910676931.6A patent/CN110523367A/en active Pending
Patent Citations (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102499448A (en) * | 2011-10-11 | 2012-06-20 | 中国烟草总公司郑州烟草研究院 | Production line for bagged buccal smokeless tobacco product preparation |
| CN103394686A (en) * | 2013-07-25 | 2013-11-20 | 莱芜钢铁集团有限公司 | Two-stage dry mixing method for powder metallurgy iron-based mixed powder |
| CN204198710U (en) * | 2014-08-19 | 2015-03-11 | 北京乾海环保科技有限公司 | Semicoke produces civilian clean moulded coal production line |
| CN105384372A (en) * | 2015-11-27 | 2016-03-09 | 山东先罗输送机械有限公司 | Method and device for preparing building gypsum from desulfurized gypsum |
| CN105664857A (en) * | 2016-04-20 | 2016-06-15 | 福建元力环境工程有限公司 | Clean, environment-friendly and efficient activated carbon regeneration device |
| CN205833182U (en) * | 2016-07-05 | 2016-12-28 | 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 |
| CN205868282U (en) * | 2016-07-05 | 2017-01-11 | 江苏中科睿赛污染控制工程有限公司 | Industry abandonment al2O3 bobble regeneration system |
| CN107583635A (en) * | 2017-09-23 | 2018-01-16 | 江苏中科睿赛污染控制工程有限公司 | Industrial waste alumina globule is segmented regenerating unit |
| CN107617413A (en) * | 2017-09-28 | 2018-01-23 | 江苏中科睿赛污染控制工程有限公司 | Industrial waste alumina globule regenerative system and renovation process |
| CN211159809U (en) * | 2019-07-25 | 2020-08-04 | 江苏中海华核环保有限公司 | Regeneration facility is handled to aluminium oxide bobble |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113426432A (en) * | 2021-07-07 | 2021-09-24 | 江苏磊金环境工程有限公司 | Production line and process for utilizing regenerated resources of saturated activated alumina pellets |
| CN113441123A (en) * | 2021-07-07 | 2021-09-28 | 江苏磊金环境工程有限公司 | Thermal desorption regeneration production line and process for saturated activated alumina pellets |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN110523367A (en) | A kind of processing of alumina globule generating apparatus and technique again | |
| CN208626952U (en) | The desulfuring and denitrifying apparatus of NO_x Reduction by Effective | |
| CN206882393U (en) | Dangerous waste handles complexes | |
| CN211159809U (en) | Regeneration facility is handled to aluminium oxide bobble | |
| CN219771235U (en) | Dustproof dye feeding device | |
| CN208593825U (en) | A kind of Pneumatic conveyer that nitrogen circulation uses | |
| CN203903429U (en) | Material receiving belt conveyer of tripper car | |
| CN109550449A (en) | A kind of uranium ore concentrate dissolution system and method | |
| CN108974948A (en) | A kind of Pneumatic conveyer that nitrogen circulation uses | |
| CN207658546U (en) | Environmental-protecting dust-removing closes conveyer | |
| CN210065879U (en) | Full-automatic galvanizing line | |
| CN210456712U (en) | Bagged cement dress lane dust collector | |
| CN212550381U (en) | Screening positive-pressure granular cotton conveying system | |
| CN211070020U (en) | Powder mixing and stirring system | |
| CN209715028U (en) | A kind of batch mixer dustless material feeding device | |
| CN207698673U (en) | A kind of pipe chain conveying equipment for melon seeds transport | |
| CN220424803U (en) | Pneumatic conveying elutriation exhaust filter | |
| CN204923747U (en) | Hot -blast furnace converter drying device | |
| CN216500071U (en) | Centrifuge pouring device | |
| CN205760294U (en) | A kind of cleaning system utilizing paint slag to reclaim coating cloud | |
| CN215044412U (en) | Powder conveying system | |
| CN209576217U (en) | A kind of organic exhaust gas recovering device with spraying function | |
| CN205145920U (en) | Vertical active carbon exhaust gas purifying apparatus | |
| CN220244896U (en) | Belt conveyor dust collector | |
| CN110369381A (en) | A kind of industrial waste alumina globule soaking and washing feeding system |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20191203 |