CN108017111A - Dust active carbon automatic Dosing System - Google Patents

Dust active carbon automatic Dosing System Download PDF

Info

Publication number
CN108017111A
CN108017111A CN201711432154.8A CN201711432154A CN108017111A CN 108017111 A CN108017111 A CN 108017111A CN 201711432154 A CN201711432154 A CN 201711432154A CN 108017111 A CN108017111 A CN 108017111A
Authority
CN
China
Prior art keywords
dust
active carbon
feeding
dust active
tank
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
Application number
CN201711432154.8A
Other languages
Chinese (zh)
Inventor
崔剑
楚素珍
姜鑫
张卫东
蒋孟君
辛立平
刘珣
林春
贺雄
文传选
张众磊
于承豪
霍毅
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
CHINA NORTH ENERGY CONSERVATION AND ENVIRONMENT PROTECTION Co Ltd
Original Assignee
CHINA NORTH ENERGY CONSERVATION AND ENVIRONMENT PROTECTION Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by CHINA NORTH ENERGY CONSERVATION AND ENVIRONMENT PROTECTION Co Ltd filed Critical CHINA NORTH ENERGY CONSERVATION AND ENVIRONMENT PROTECTION Co Ltd
Priority to CN201711432154.8A priority Critical patent/CN108017111A/en
Publication of CN108017111A publication Critical patent/CN108017111A/en
Pending legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/28Treatment of water, waste water, or sewage by sorption
    • C02F1/283Treatment of water, waste water, or sewage by sorption using coal, charred products, or inorganic mixtures containing them
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2103/00Nature of the water, waste water, sewage or sludge to be treated
    • C02F2103/30Nature of the water, waste water, sewage or sludge to be treated from the textile industry

Landscapes

  • Life Sciences & Earth Sciences (AREA)
  • Hydrology & Water Resources (AREA)
  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Water Treatment By Sorption (AREA)

Abstract

The present invention relates to a kind of dust active carbon automatic Dosing System, belong to field of waste water treatment.Including:Dust active carbon storehouse, feeding wind turbine, blanking machine, feeding system, preparing tank, medicine storing pot, feeding station and add pump;Feeding wind turbine by dust active carbon inhalation of dust charcoal storehouse, then enters preparing tank by feeding station by blanking machine and feeding system, is stirred in preparing tank with water after mixing from flowing into storage tank;Then coagulating basin is squeezed into by adding pump;The dust active carbon of the present invention adds, and overall process is controlled using PLC, and real-time system data, operating status touch-screen are shown, is operated without a large amount of personnel, and package unit carries out chain automatically control by blanking machine helix transporting device with adding pump.Automatization level is high, and labor intensity is low, precise control, stable.

Description

Dust active carbon automatic Dosing System
Technical field
The present invention relates to a kind of dust active carbon automatic Dosing System, belong to field of waste water treatment.
Background technology
The system device is used in the sewerage advanced treatment process of the persistent organic pollutants such as chemical industry, printing and dyeing.
Existing general technology activated carbon pond, i.e. waste water carry out activated carbon by loading the structures of a certain number of activated carbons Adsorption treatment, passes through the suction-operated of activated carbon so that the organic matter in sewage is transferred in activated carbon.
There are problem to be for the processing of existing activated carbon pond:
Need to consume when 1. activated carbon pond is built largely manually to be loaded.
2. activated carbon, it is necessary to activated carbon is taken out out of pond, and loads after adsorption saturation and more renews charcoal.Charcoal is taken to replace Time is grown, and labor intensity is big.
The content of the invention
The purpose of the present invention is to solve the above problem, there is provided a kind of dust active carbon automatic Dosing System.The system device The sewerage advanced treatment process of the persistent organic pollutants such as chemical industry, printing and dyeing is used in, can effectively be located by the processing of the present apparatus The organic pollution in water is managed, stablizes wastewater to reach standard or the emergency processing for light concentration organic pollutant.
The purpose of the present invention is what is be achieved through the following technical solutions:
Dust active carbon automatic Dosing System, including:Dust active carbon storehouse, feeding wind turbine, blanking machine, feeding system, preparing tank, drug storage Tank, feeding station and add pump;
Feeding wind turbine by dust active carbon inhalation of dust charcoal storehouse, is then entered by blanking machine and feeding system and matched somebody with somebody by feeding station Tank processed, is stirred with water after mixing in preparing tank from flowing into storage tank;Then coagulating basin is squeezed into by adding pump;
The dust active carbon the top of the warehouse carries vacuum suction material tank, and dust-extraction unit and impulse electromagnetic valve are carried on vacuum suction material tank, The impulse electromagnetic valve control compressed air carries out dust-extraction unit air purge;
The feeding system is fed using screw conveyor;
Blanking machine is furnished with pneumatic hole rapping apparatus;
Air compression system is further included, it is empty for providing compression to pneumatic hole rapping apparatus and dust catcher device air purge Gas;
The course of work:
When powder absorbent charcoal source is small package bag, puts into feeding station, when being conveyed for dust active carbon pump truck, will convey Pipe is directly accessed in negative pressure suction nozzle pipeline, starts feeding wind turbine, and dust active carbon storehouse is sent into through vacuum suction material tank, and when material feeding opens vacuum Dust-extraction unit on material-suction pot, carries out dust removal by filtration to the dust in feed bin, starts air compression system, restart on blanking machine Pneumatic hole rapping apparatus, open the screw(-type) feeder of feeding system, dust active carbon be delivered in Powdered Activated Carbon batch tank, Spray system to be opened at the same time and enters dissolving water, carries out mechanical agitation, host computer can automatically control dust active carbon dosage and water injection rate, The compound concentration that ensure that Powdered Activated Carbon liquid is 5-10%.The Powdered Activated Carbon liquid configured is flow in dust active carbon storage tank certainly. Startup adds pump, and the dust active carbon solution in storage tank is squeezed into flocculation basin.Configuration of storage tanks stainless steel mixer, while powder carbon storage tank Bottom sets residual cake valve, carries out regular automatic discharge.
The control of Powdered Activated Carbon dosing system (is provided simultaneously with auto-manual and switches work(completely using PLC Automatic Controls Can), switch board space of a whole page installation touch-screen display (setting or change operating parameter) observation operational process state.
Beneficial effect
1st, dust active carbon of the invention adds, and overall process is controlled using PLC, and real-time system data, operating status touch screen display Show, operated without a large amount of personnel, package unit carries out chain automatically control by blanking machine helix transporting device with adding pump. Automatization level is high, and labor intensity is low, precise control, stable.
2nd, it is totally-enclosed, without dust pollution that dust active carbon, which adds process, and it is accurate quantitatively to add, and pipeline is without blocking.
Brief description of the drawings
Fig. 1 the device of the invention schematic diagrames;
The process flow chart of Fig. 2 present invention;
Fig. 3 is actual motion COD degradation curve map.
Wherein, 1-dust active carbon storehouse, 2-feeding wind turbine, 3-blanking machine, 4-feeding system, 5-preparing tank, 6-drug storage Tank, 7-feeding station, 8-add pump
Embodiment
In order to better illustrate objects and advantages of the present invention, the content of the invention is done further with example below in conjunction with the accompanying drawings Explanation.
Embodiment 1:
Dust active carbon automatic Dosing System, including:Dust active carbon storehouse 1, feeding wind turbine 2, blanking machine 3, feeding system 4, preparing tank 5th, medicine storing pot 6, feeding station 7, add pump 8;
When powder absorbent charcoal source is small package bag, put into feeding station 7, will be defeated when being conveyed for dust active carbon pump truck Send pipe to be directly accessed in negative pressure suction nozzle pipeline, start feeding wind turbine 2, dust active carbon storehouse 1 is sent into through vacuum suction material tank, when material feeding opens Deduster at the top of feed bin, dust removal by filtration, when pressure increases to over setting value in feed bin, feed bin are carried out to the dust in feed bin Top safety valve automatically opens up pressure release and alarms, and feed bin top and bottom sets level-sensing device, when feed bin activity powdered carbon superelevation or low When material position is designed alarm is sent to be prompted, at the same for prevent in feed bin Powdered Activated Carbon formed in use crane span structure or Cavitation feed bin sets pneumatic air rapping apparatus at the same time.
During feeding, the screw(-type) feeder of feeding system 4 is opened, dust active carbon is delivered to 5 in Powdered Activated Carbon batch tank, together When open spray system and enter dissolving water, carry out mechanical agitation, host computer can automatically control dust active carbon dosage and water injection rate, protect The compound concentration for having demonstrate,proved Powdered Activated Carbon liquid is 5-10%.The Powdered Activated Carbon liquid configured is flow in dust active carbon storage tank 6 certainly.Open It is dynamic to add pump 8, the dust active carbon solution in storage tank 6 is squeezed into flocculation basin.Storage tank 6 configures stainless steel mixer, while powder carbon stores up Pot bottom sets residual cake valve, carries out regular automatic discharge.
Dust active carbon storehouse 1 describes:
Powder carbon material bottom cone is designed, four foot supports, carbon feed bin uses carbon steel structure, interior resin resistant.Match somebody with somebody at the same time Put:With vacuum suction material tank, level-sensing device (Central Control Room by 3 level-sensing devices control a high positions stop material, the anti-hole of middle position, low level into Material), dust remover for storage bin (design use bag filter, using air pulse blowback dedusting), safety valve is (when pressure liter in feed bin When height exceedes setting value, feed bin top safety valve automatically opens up pressure release and alarms).
Blanking machine 3 describes:
Equipped with pneumatic hole rapping apparatus (crane span structure destructor), activated vibration hopper, (installation shakes gas in feed bin cone bottom Pad, cone bottom 1/3 installation activation orlop, effectively prevent feed bin hole, the hardened problem of powder wall built-up, powder carbon).
Feeding system 4 describes:
Equipped with screw(-type) feeder and screw conveyor, screw(-type) feeder uses frequency conversion screw(-type) feeder, by controlling motor Frequency controls the gear reducer revolution speed of screw to realize Variable Control.Screw conveyor uses frequency conversion screw conveyor, and batcher is defeated The powder carbon gone out is delivered to powder carbon preparation system.
Preparing tank 5 describes:
304 stainless steels, closure designs are used in it, are set jet flow negative pressure damp-proof device and spray system, are prevented powder Dustiness contaminates, and prepares 304 stainless cylinder of steel mixers, 304 stainless steels spray water curtain dust excluder, entering water electromagnetic valve, electromagnetic flowmeter.
Storage tank 6 describes:
304 stainless steels, inside set 304 mixers, tank level indicator, ensures that Powdered Activated Carbon is dense during adding Degree is uniform.
Add the description of pump 8:
Added using 304 stainless steels and pump anti-wear, anticorrosion, pump discharge sets flowmeter
The course of work, as shown in Fig. 2, the water outlet of advanced treating biochemical device flows into coagulating basin, adds from dust active carbon in pond The dust active carbon solution of throwing device, through being sufficiently mixed with waste water, water outlet adds flocculant from flocculation basin is flowed into pond, accelerate powder After the aggregation of last charcoal, water outlet enters horizontal sedimentation tank and carries out dust active carbon precipitation, and supernatant flows into clear water reserviors, qualified discharge certainly.
Horizontal sedimentation tank base sludge, filter cake can be used as absorption material to be back in high concentrated organic wastewater after dehydration.
When powder absorbent charcoal source is small package bag, put into feeding station 7, will be defeated when being conveyed for dust active carbon pump truck Send pipe to be directly accessed in negative pressure suction nozzle pipeline, start feeding wind turbine 2, dust active carbon storehouse 1 is sent into through vacuum suction material tank, when material feeding opens Deduster at the top of feed bin, dust removal by filtration, when pressure increases to over setting value in feed bin, feed bin are carried out to the dust in feed bin Top safety valve automatically opens up pressure release and alarms, and feed bin top and bottom sets level-sensing device, when feed bin activity powdered carbon superelevation or low When material position is designed alarm is sent to be prompted, at the same for prevent in feed bin Powdered Activated Carbon formed in use crane span structure or Cavitation feed bin sets pneumatic air rapping apparatus at the same time.
During feeding, the screw(-type) feeder of feeding system 4 is opened, dust active carbon is delivered to 5 in Powdered Activated Carbon batch tank, together When open spray system and enter dissolving water, carry out mechanical agitation, host computer can automatically control dust active carbon dosage and water injection rate, protect The compound concentration for having demonstrate,proved Powdered Activated Carbon liquid is 5-10%.The Powdered Activated Carbon liquid configured is flow in dust active carbon storage tank 6 certainly.Open It is dynamic to add pump 8, the dust active carbon solution in storage tank 6 is squeezed into flocculation basin.Storage tank 6 configures stainless steel mixer, while powder carbon stores up Pot bottom sets residual cake valve, carries out regular automatic discharge.
Actual motion effect is shown in Fig. 3.
1 is see the table below using equipment processing waste water effect
Certain the large-scale waste water project COD degradation actual motion effect list of table 1
Sequence number Influent COD mg/L Water outlet CODmg/L Removal rate Remarks
1 66.56 31.99 52%
2 57.24 30.28 47%
3 57.57 35.36 39%
4 54.5 28.02 49%
5 51.25 34.24 33%
6 72.76 34.85 52%
Conclusion:COD average removal rates are 45%
I takes charge of the coking wastewater project that has been used to this project, handles hardly degraded organic substance.
Above-described specific descriptions, have carried out further specifically the purpose, technical solution and beneficial effect of invention It is bright, it should be understood that the foregoing is merely the specific embodiment of the present invention, the protection model being not intended to limit the present invention Enclose, within the spirit and principles of the invention, any modification, equivalent substitution, improvement and etc. done, should be included in the present invention Protection domain within.

Claims (6)

1. dust active carbon automatic Dosing System, it is characterised in that:Including:Dust active carbon storehouse (1), feeding wind turbine (2), blanking machine (3), give Material system (4), preparing tank (5), medicine storing pot (6), feeding station (7) and add pump (8);
Feeding wind turbine (2) by dust active carbon inhalation of dust charcoal storehouse (1), then passes through blanking machine (3) and feed system by feeding station (7) System (4) enters preparing tank (5), oneself is stirred with water after mixing in preparing tank (5) and flows into storage tank (6);Then by adding Pump (8) squeezes into coagulating basin.
2. dust active carbon automatic Dosing System as claimed in claim 1, it is characterised in that:Air compression system is further included, is used for Compressed air is provided to pneumatic hole rapping apparatus and dust catcher device air purge.
3. dust active carbon automatic Dosing System as claimed in claim 1, it is characterised in that:Carried at the top of the dust active carbon storehouse (1) Vacuum suction material tank, carries dust-extraction unit and impulse electromagnetic valve on vacuum suction material tank, the impulse electromagnetic valve control compressed air into Row dust-extraction unit air purge.
4. dust active carbon automatic Dosing System as claimed in claim 1, it is characterised in that:The feeding system (4) is using spiral Conveyer is fed.
5. dust active carbon automatic Dosing System as claimed in claim 1, it is characterised in that:The blanking machine (3) is equipped with pneumatic empty Cave rapping apparatus.
6. the dust active carbon automatic Dosing System as described in an any of the above-described claim, it is characterised in that:The throwing of the system Adding method is:When powder absorbent charcoal source is small package bag, put into feeding station (7), will when being conveyed for dust active carbon pump truck Delivery pipe is directly accessed in negative pressure suction nozzle pipeline, starts feeding wind turbine (2), is sent into dust active carbon storehouse (1) through vacuum suction material tank, material feeding Dust-extraction unit on Shi Kaiqi vacuum suction material tanks, carries out dust removal by filtration to the dust in feed bin, starts air compression system, then open Pneumatic hole rapping apparatus on dynamic blanking machine (3), opens the screw(-type) feeder of feeding system (4), dust active carbon is delivered to powder In last activated carbon batch tank (5), while open spray system and enter dissolving water, carry out mechanical agitation, host computer can automatically control Dust active carbon dosage and water injection rate, the compound concentration that ensure that Powdered Activated Carbon liquid are 5-10%;The Powdered Activated Carbon configured Liquid is flow in dust active carbon storage tank (6) certainly;Startup adds pump (8), and the dust active carbon solution in storage tank (6) is squeezed into flocculation basin;Storage tank (6) stainless steel mixer is configured, while powder carbon tank bottom sets residual cake valve, carries out regular automatic discharge.
CN201711432154.8A 2017-12-26 2017-12-26 Dust active carbon automatic Dosing System Pending CN108017111A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201711432154.8A CN108017111A (en) 2017-12-26 2017-12-26 Dust active carbon automatic Dosing System

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201711432154.8A CN108017111A (en) 2017-12-26 2017-12-26 Dust active carbon automatic Dosing System

Publications (1)

Publication Number Publication Date
CN108017111A true CN108017111A (en) 2018-05-11

Family

ID=62071858

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201711432154.8A Pending CN108017111A (en) 2017-12-26 2017-12-26 Dust active carbon automatic Dosing System

Country Status (1)

Country Link
CN (1) CN108017111A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110563108A (en) * 2019-09-26 2019-12-13 沈阳环境科学研究院 Landfill leachate tail water emergency treatment method
CN112429414A (en) * 2020-11-12 2021-03-02 枣庄学院 Automatic sodium carbonate adding system
CN113289516A (en) * 2021-05-11 2021-08-24 九江德福科技股份有限公司 Device and method for preparing and adding activated carbon solution
CN114314731A (en) * 2021-12-31 2022-04-12 江苏长江水务股份有限公司 Emergency water treatment is with powdered activated carbon dosing system

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102101714A (en) * 2010-12-16 2011-06-22 北京中兵北方环境科技发展有限责任公司 Device and method for quantitatively charging lime automatically
CN102923809A (en) * 2012-11-15 2013-02-13 广东卓信水处理设备有限公司 Automatic preparation and wet-type adding device for powdered activated carbon
CN105174541A (en) * 2015-09-18 2015-12-23 浙江省环境保护科学设计研究院 Deep sewage treatment device and method by means of membrane coagulation reaction and powdered activated carbon adsorption
CN205820929U (en) * 2016-06-07 2016-12-21 北京中电加美环保科技有限公司 A kind of Powdered Activated Carbon wet method automatic dilution adds unit and wet method throwing device
CN106365238A (en) * 2016-08-31 2017-02-01 潍坊和创环保设备有限公司 Powdered activated carbon dry-method feeding system
CN106629976A (en) * 2016-12-28 2017-05-10 江苏华达环境工程有限公司 Integrated powdered activated carbon adding device and adding system thereof

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102101714A (en) * 2010-12-16 2011-06-22 北京中兵北方环境科技发展有限责任公司 Device and method for quantitatively charging lime automatically
CN102923809A (en) * 2012-11-15 2013-02-13 广东卓信水处理设备有限公司 Automatic preparation and wet-type adding device for powdered activated carbon
CN105174541A (en) * 2015-09-18 2015-12-23 浙江省环境保护科学设计研究院 Deep sewage treatment device and method by means of membrane coagulation reaction and powdered activated carbon adsorption
CN205820929U (en) * 2016-06-07 2016-12-21 北京中电加美环保科技有限公司 A kind of Powdered Activated Carbon wet method automatic dilution adds unit and wet method throwing device
CN106365238A (en) * 2016-08-31 2017-02-01 潍坊和创环保设备有限公司 Powdered activated carbon dry-method feeding system
CN106629976A (en) * 2016-12-28 2017-05-10 江苏华达环境工程有限公司 Integrated powdered activated carbon adding device and adding system thereof

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
上海市政工程设计研究院主编: "《给水排水设计手册 第3册 城镇给水 第2版》", 30 April 2004, 中国建筑工业出版社 *

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110563108A (en) * 2019-09-26 2019-12-13 沈阳环境科学研究院 Landfill leachate tail water emergency treatment method
CN112429414A (en) * 2020-11-12 2021-03-02 枣庄学院 Automatic sodium carbonate adding system
CN112429414B (en) * 2020-11-12 2022-06-17 枣庄学院 Automatic sodium carbonate adding system
CN113289516A (en) * 2021-05-11 2021-08-24 九江德福科技股份有限公司 Device and method for preparing and adding activated carbon solution
CN114314731A (en) * 2021-12-31 2022-04-12 江苏长江水务股份有限公司 Emergency water treatment is with powdered activated carbon dosing system

Similar Documents

Publication Publication Date Title
CN108017111A (en) Dust active carbon automatic Dosing System
CN101659456B (en) Automatic adding system of powdered activated carbon
CN202479201U (en) Continuous fly ash stabilizing treatment device
CN212864244U (en) Flocculating agent dosing system
JP5918017B2 (en) Biological wastewater treatment equipment
CN208995168U (en) Phenol cyanogen effluent disposal system
CN208502701U (en) A kind of discarded oil-base mud recycling and processing equipment of drilling well
CN105800907A (en) Device and method for treating drilling mud without falling on the ground
CN213569885U (en) Sewage treatment pond is used in polyurethane production with multiple stage filtration function
IL274592B1 (en) Plant and method for treating urban waste water
CN206232456U (en) A kind of sewage-treatment plant of environmental protection
CN108203179A (en) A kind of intelligence fast sewage treatment device
CN204051572U (en) Full-automatic lime chemicals dosing plant
CN209480752U (en) A kind of carbon dioxide pressure break discharge device
CN207330501U (en) The MBR biochemical treatment systems of cutting waste fluid
CN208049882U (en) A kind of powder water treatment agent dispensation apparatus for preventing from blocking pipeline
CN207446144U (en) Coking wastewater deep treatment water purification agent chemicals dosing plant
CN206720998U (en) A kind of sewage disposal device applied widely
CN209778424U (en) Sewage treatment's flocculating agent charge device
CN206000493U (en) Mud disposal system based on separation of solid and liquid
CN204395834U (en) A kind of mining polyacrylamide medicine system
CN110251879B (en) Decyanation system and method for cyanamide waste residues
CN105110453A (en) Agent dosing system for sewage biochemical treatment equipment
CN217103493U (en) Chemical water treatment device based on activated carbon-activated sludge coupling method
CN210080345U (en) A ectopic prosthetic devices for polycyclic aromatic hydrocarbon pollutes soil

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
WD01 Invention patent application deemed withdrawn after publication

Application publication date: 20180511

WD01 Invention patent application deemed withdrawn after publication