CN110354831A - Powder activated carbon regeneration method - Google Patents

Powder activated carbon regeneration method Download PDF

Info

Publication number
CN110354831A
CN110354831A CN201910617539.4A CN201910617539A CN110354831A CN 110354831 A CN110354831 A CN 110354831A CN 201910617539 A CN201910617539 A CN 201910617539A CN 110354831 A CN110354831 A CN 110354831A
Authority
CN
China
Prior art keywords
activated carbon
waste
powdered activated
woven fabrics
active carbon
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
CN201910617539.4A
Other languages
Chinese (zh)
Inventor
胡志杰
陈红锋
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.)
Anhui Xinhui Carbon Industry Co., Ltd
Original Assignee
Nanjing Anjiete Environmental Protection Technology 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 Nanjing Anjiete Environmental Protection Technology Co Ltd filed Critical Nanjing Anjiete Environmental Protection Technology Co Ltd
Priority to CN201910617539.4A priority Critical patent/CN110354831A/en
Publication of CN110354831A publication Critical patent/CN110354831A/en
Pending legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/30Processes for preparing, regenerating, or reactivating
    • B01J20/34Regenerating or reactivating
    • B01J20/3416Regenerating or reactivating of sorbents or filter aids comprising free carbon, e.g. activated carbon
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/30Processes for preparing, regenerating, or reactivating
    • B01J20/34Regenerating or reactivating
    • B01J20/3441Regeneration or reactivation by electric current, ultrasound or irradiation, e.g. electromagnetic radiation such as X-rays, UV, light, microwaves
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/30Processes for preparing, regenerating, or reactivating
    • B01J20/34Regenerating or reactivating
    • B01J20/345Regenerating or reactivating using a particular desorbing compound or mixture
    • B01J20/3475Regenerating or reactivating using a particular desorbing compound or mixture in the liquid phase
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/30Processes for preparing, regenerating, or reactivating
    • B01J20/34Regenerating or reactivating
    • B01J20/3483Regenerating or reactivating by thermal treatment not covered by groups B01J20/3441 - B01J20/3475, e.g. by heating or cooling
    • 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
    • C02F1/66Treatment of water, waste water, or sewage by neutralisation; pH adjustment

Landscapes

  • Chemical & Material Sciences (AREA)
  • Analytical Chemistry (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Physics & Mathematics (AREA)
  • Engineering & Computer Science (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Thermal Sciences (AREA)
  • Materials Engineering (AREA)
  • Hydrology & Water Resources (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Health & Medical Sciences (AREA)
  • Electromagnetism (AREA)
  • General Health & Medical Sciences (AREA)
  • Toxicology (AREA)
  • Water Treatment By Sorption (AREA)
  • Solid-Sorbent Or Filter-Aiding Compositions (AREA)

Abstract

The invention discloses a kind of powdered active carbon regenerating methods, include the following steps: screening-washing-regeneration-acidification-ultrasonic regeneration-collection-neutralization waste water.The present invention is washed waste powdered activated carbon by specific cleaning solution, change previous powdered activated carbon do not allow it is easy to wash, the impurity contained is more, washing step is complicated, and the problem of influencing later regeneration rate, is avoided the problems such as recycling rate is low after regenerating, is washed using ultrasonic unit, hole is not injured, its adsorption capacity is further kept.

Description

Powder activated carbon regeneration method
Technical field
The present invention relates to technical field of fine, and in particular to a kind of powder activated carbon regeneration method.
Background technique
Active carbon is widely used in chemical industry, food, pharmacy and environmental protection etc. as a kind of excellent high-efficiency adsorbent Every field, used active carbon are discarded, filled or are burned without processing, and not only waste of resource, will also cause two Secondary pollution, actually activated carbon adsorption are a physical processes, by using suitable regeneration techniques by used active carbon The substance of absorption carries out desorption removal, so that it is replied original characterization of adsorption, can achieve the purpose of reuse, both real in this way The minimizing of waste active carbon is showed, innoxious and recycling decreases the waste of the energy.
Currently, the regeneration of waste active carbon mainly has bio-regeneration method, Photocatalytic Regeneration method etc., and still, powdery waste active carbon Because partial size is smaller, lighter weight, traditional Regenevating Waste Activated Carbon method is easy to bring active carbon loss excessive, can go out in the process Existing fugitive dust is excessive, causes secondary pollution to environment.
Summary of the invention
Goal of the invention: the purpose of the invention is to make up the deficiency of existing investigative technique, a kind of powdered work is provided Property carbon regeneration method.
Technical solution: a kind of powdered active carbon regenerating method includes the following steps:
1) it screens: waste powdered activated carbon being dried to moisture content in dryer lower than 40%, by the useless work after drying Property charcoal tiles on the non-woven fabrics for have hole, and non-woven fabrics both sides are connected to the both ends of shaking device, starting shock device, nothing Woven fabric shakes under its drive, and the ash content and solid impurity in waste powdered activated carbon are fallen from the hole of non-woven fabrics;
2) wash: the waste powdered activated carbon that non-woven fabrics upper surface is reserved is collected, and is added in hydrochloric acid solution, and pH concentration is adjusted For 3-4, stirring is heated to 110 DEG C, and flow back 9h, and cooled and filtered, gained filter residue is dry after cleaning solution washs, and is washed Waste powdered activated carbon after washing;
3) it regenerates: powdered activated carbon being put into pond, is constantly passed through vapor from bottom of pond, maintain 90 DEG C or more, and Continuous overturning powdered activated carbon in the process, is arranged sieve in pond, after 1-2h, stops, standing, charcoal upper layer is steeped below active carbon Foam is removed;
4) it is acidified: being passed through water purification, charcoal is washed;Dilute hydrochloric acid is added, adjusts pH value to 1-2;
5) ultrasonic regeneration: being put into ultrasonic processing apparatus for the charcoal after acidification, adjusts the power of ultrasonic unit to 150- 200w;
6) it collects: the charcoal after ultrasonic regeneration being put into a secondary cyclone, is come out from cyclone separator After be transferred to drying converter heating, drying, collect;
7) it neutralizes waste water: the NaOH solution that mass concentration is 2% is added and carries out neutralization waste water, after waste water is in neutrality, thoroughly Lightness is higher and free from extraneous odour can discharge later.
Preferably, the hole of the non-woven fabrics is 2000-2500 mesh.
Preferably, cleaning solution is by anionic surfactant, sodium citrate, potassium chloride, distillation in the step 2) Water, ethyl alcohol;The anionic surfactant: sodium citrate: potassium chloride: distilled water: the mass ratio of ethyl alcohol is 1-2:1.5- 4:3-4:40-50:10-25。
Preferably, the vapor in step 3) after condenser condensation, into wastewater collection pond, can continue next time It uses.
In the present invention, waste powdered activated carbon is washed by specific cleaning solution, changes previous powdered activated carbon Do not allow easy to wash, the impurity contained is more, and washing step is complicated, and the problem of influence later regeneration rate, after avoiding regeneration The problems such as recycling rate is low, is washed using ultrasonic unit, does not injure hole, further keeps its adsorption rate.
Specific embodiment
The present invention will be described below by way of specific embodiments, but the present invention is not limited thereto.In following embodiments The experimental method is unless otherwise specified conventional method;The reagent and material unless otherwise specified can be from business Approach obtains, the scope of the patents that following example is not intended to limit the invention, all equivalence enforcements without departing from carried out by the present invention Or change, it is intended to be limited solely by the scope of this patent.
Embodiment 1:
A kind of powdered active carbon regenerating method, includes the following steps:
1) it screens: waste powdered activated carbon being dried to moisture content in dryer lower than 40%, by the useless work after drying Property charcoal tiles on the non-woven fabrics for have hole, and non-woven fabrics both sides are connected to the both ends of shaking device, starting shock device, nothing Woven fabric shakes under its drive, and the ash content and solid impurity in waste powdered activated carbon are fallen from the hole of non-woven fabrics, nonwoven The hole of cloth is 2000 mesh;
2) wash: the waste powdered activated carbon that non-woven fabrics upper surface is reserved is collected, and is added in hydrochloric acid solution, and pH concentration is adjusted It is 3, stirring is heated to 110 DEG C, and flow back 9h, and cooled and filtered, gained filter residue is dry after cleaning solution washs, and is washed Waste powdered activated carbon afterwards, cleaning solution is by anionic surfactant, sodium citrate, potassium chloride, distilled water, ethyl alcohol;Described Anionic surfactant: sodium citrate: potassium chloride: distilled water: the mass ratio of ethyl alcohol is 1:1.5:3:40:10;
3) it regenerates: powdered activated carbon being put into pond, is constantly passed through vapor from bottom of pond, maintain 90 DEG C or more, and Continuous overturning powdered activated carbon in the process, is arranged sieve in pond, after 1h, stops, standing, by charcoal upper foam below active carbon It removes, in this step, vapor, into wastewater collection pond, can continue to use next time after condenser condensation;
4) it is acidified: being passed through water purification, charcoal is washed;Dilute hydrochloric acid is added, adjusts pH value to 1;
5) ultrasonic regeneration: being put into ultrasonic processing apparatus for the charcoal after acidification, adjusts the power of ultrasonic unit to 150w;
6) it collects: the charcoal after ultrasonic regeneration being put into a secondary cyclone, is come out from cyclone separator After be transferred to drying converter heating, drying, collect;
7) it neutralizes waste water: the NaOH solution that mass concentration is 2% is added and carries out neutralization waste water, after waste water is in neutrality, thoroughly Lightness is higher and free from extraneous odour can discharge later.
Embodiment 2:
A kind of powdered active carbon regenerating method, includes the following steps:
1) it screens: waste powdered activated carbon being dried to moisture content in dryer lower than 40%, by the useless work after drying Property charcoal tiles on the non-woven fabrics for have hole, and non-woven fabrics both sides are connected to the both ends of shaking device, starting shock device, nothing Woven fabric shakes under its drive, and the ash content and solid impurity in waste powdered activated carbon are fallen from the hole of non-woven fabrics, nonwoven The hole of cloth is 2500 mesh;
2) wash: the waste powdered activated carbon that non-woven fabrics upper surface is reserved is collected, and is added in hydrochloric acid solution, and pH concentration is adjusted For 3-4, stirring is heated to 110 DEG C, and flow back 9h, and cooled and filtered, gained filter residue is dry after cleaning solution washs, and is washed Waste powdered activated carbon after washing, cleaning solution is by anionic surfactant, sodium citrate, potassium chloride, distilled water, ethyl alcohol;It is described Anionic surfactant: sodium citrate: potassium chloride: distilled water: the mass ratio of ethyl alcohol be 2:4:3:50:25;
3) it regenerates: powdered activated carbon being put into pond, is constantly passed through vapor from bottom of pond, maintain 90 DEG C or more, and Continuous overturning powdered activated carbon in the process, is arranged sieve in pond, after 2h, stops, standing, by charcoal upper foam below active carbon It removes;
4) it is acidified: being passed through water purification, charcoal is washed;Dilute hydrochloric acid is added, adjusts pH value to 2;
5) ultrasonic regeneration: being put into ultrasonic processing apparatus for the charcoal after acidification, adjusts the power of ultrasonic unit to 200w;
6) it collects: the charcoal after ultrasonic regeneration being put into a secondary cyclone, is come out from cyclone separator After be transferred to drying converter heating, drying, collect;
7) it neutralizes waste water: the NaOH solution that mass concentration is 2% is added and carries out neutralization waste water, after waste water is in neutrality, thoroughly Lightness is higher and free from extraneous odour can discharge later.
Vapor in step 3), into wastewater collection pond, can continue to use next time after condenser condensation.
Embodiment 3:
A kind of powdered active carbon regenerating method, includes the following steps:
1) it screens: waste powdered activated carbon being dried to moisture content in dryer lower than 40%, by the useless work after drying Property charcoal tiles on the non-woven fabrics for have hole, and non-woven fabrics both sides are connected to the both ends of shaking device, starting shock device, nothing Woven fabric shakes under its drive, and the ash content and solid impurity in waste powdered activated carbon are fallen from the hole of non-woven fabrics, nonwoven The hole of cloth is 2300 mesh;
2) wash: the waste powdered activated carbon that non-woven fabrics upper surface is reserved is collected, and is added in hydrochloric acid solution, and pH concentration is adjusted For 3-4, stirring is heated to 110 DEG C, and flow back 9h, and cooled and filtered, gained filter residue is dry after cleaning solution washs, and is washed Waste powdered activated carbon after washing, cleaning solution is by anionic surfactant, sodium citrate, potassium chloride, distilled water, ethyl alcohol;It is described Anionic surfactant: sodium citrate: potassium chloride: distilled water: the mass ratio of ethyl alcohol be 1-2:1.5-4:3-4:40-50: 10-25;
3) it regenerates: powdered activated carbon being put into pond, is constantly passed through vapor from bottom of pond, maintain 90 DEG C or more, and Continuous overturning powdered activated carbon in the process, is arranged sieve in pond, after 1-2h, stops, standing, charcoal upper layer is steeped below active carbon Foam is removed;
4) it is acidified: being passed through water purification, charcoal is washed;Dilute hydrochloric acid is added, adjusts pH value to 1.5;
5) ultrasonic regeneration: being put into ultrasonic processing apparatus for the charcoal after acidification, adjusts the power of ultrasonic unit to 180w;
6) it collects: the charcoal after ultrasonic regeneration being put into a secondary cyclone, is come out from cyclone separator After be transferred to drying converter heating, drying, collect;
7) it neutralizes waste water: the NaOH solution that mass concentration is 2% is added and carries out neutralization waste water, after waste water is in neutrality, thoroughly Lightness is higher and free from extraneous odour can discharge later.
In order to further embody beneficial effects of the present invention, spy proposes following test example:
The adsorption experiment of the organic matter progress active carbon in sewage, the product in embodiment 1-3 are replaced using methylene blue When being detected, methylene blue adsorptive value is measured according to GB/T12496.10-1999;Experiment shows to implement in the present invention The more former charcoal adsorption capacity of activated carbon adsorption power in example 1-3 improves 30-40%, and recycling rate promotes 30-40%, conversion ratio It is 50%.

Claims (4)

1. a kind of powdered active carbon regenerating method, characterized by the following steps:
1) it screens: waste powdered activated carbon being dried to moisture content in dryer lower than 40%, by the waste active carbon after drying It tiles on the non-woven fabrics for have hole, non-woven fabrics both sides are connected to the both ends of shaking device, starting shock device, non-woven fabrics It is shaken under its drive, the ash content and solid impurity in waste powdered activated carbon are fallen from the hole of non-woven fabrics;
2) wash: the waste powdered activated carbon that non-woven fabrics upper surface is reserved is collected, and is added in hydrochloric acid solution, and adjusting pH concentration is 3- 4, stirring is heated to 110 DEG C, and flow back 9h, and cooled and filtered, gained filter residue is dry after cleaning solution washs, after obtaining washing Waste powdered activated carbon;
3) it regenerates: powdered activated carbon being put into pond, is constantly passed through vapor from bottom of pond, maintains 90 DEG C or more, and process In constantly overturn powdered activated carbon, sieve is set below active carbon in pond, after 1-2h, stops, standing, charcoal upper foam is clear It removes;
4) it is acidified: being passed through water purification, charcoal is washed;Dilute hydrochloric acid is added, adjusts pH value to 1-2;
5) ultrasonic regeneration: being put into ultrasonic processing apparatus for the charcoal after acidification, adjusts the power of ultrasonic unit to 150-200w;
6) it collects: the charcoal after ultrasonic regeneration is put into a secondary cyclone, turn after being come out from cyclone separator Enter to drying converter heating, drying, collects;
7) it neutralizes waste water: the NaOH solution that mass concentration is 2% is added and carries out neutralization waste water, after waste water is in neutrality, transparency It can be discharged after higher and free from extraneous odour.
2. powdered active carbon regenerating method as described in claim 1, it is characterised in that: the hole of the non-woven fabrics is 2000-2500 mesh.
3. powdered active carbon regenerating method as described in claim 1, it is characterised in that: in the step 2), cleaning solution by Anionic surfactant, sodium citrate, potassium chloride, distilled water, ethyl alcohol;The anionic surfactant: sodium citrate: Potassium chloride: distilled water: the mass ratio of ethyl alcohol is 1-2:1.5-4:3-4:40-50:10-25.
4. powdered active carbon regenerating method as described in claim 1, it is characterised in that: the vapor in step 3) is by condensation After device condensation, into wastewater collection pond, it can continue to use next time.
CN201910617539.4A 2019-07-10 2019-07-10 Powder activated carbon regeneration method Pending CN110354831A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201910617539.4A CN110354831A (en) 2019-07-10 2019-07-10 Powder activated carbon regeneration method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201910617539.4A CN110354831A (en) 2019-07-10 2019-07-10 Powder activated carbon regeneration method

Publications (1)

Publication Number Publication Date
CN110354831A true CN110354831A (en) 2019-10-22

Family

ID=68218383

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201910617539.4A Pending CN110354831A (en) 2019-07-10 2019-07-10 Powder activated carbon regeneration method

Country Status (1)

Country Link
CN (1) CN110354831A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN114073943A (en) * 2021-11-25 2022-02-22 宁夏锦鹏炭业有限公司 Powdered activated carbon regeneration device based on airflow heating and regeneration process thereof
CN114229843A (en) * 2021-12-24 2022-03-25 贵州重力科技环保有限公司 Method for activating and regenerating waste activated carbon after harmless treatment of waste mercury catalyst

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102989435A (en) * 2012-12-28 2013-03-27 湖北君集水处理有限公司 Method for regenerating activated carbon
CN103084155A (en) * 2011-11-03 2013-05-08 中国地质大学(北京) Microwave-assisted activated carbon regeneration method

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103084155A (en) * 2011-11-03 2013-05-08 中国地质大学(北京) Microwave-assisted activated carbon regeneration method
CN102989435A (en) * 2012-12-28 2013-03-27 湖北君集水处理有限公司 Method for regenerating activated carbon

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN114073943A (en) * 2021-11-25 2022-02-22 宁夏锦鹏炭业有限公司 Powdered activated carbon regeneration device based on airflow heating and regeneration process thereof
CN114229843A (en) * 2021-12-24 2022-03-25 贵州重力科技环保有限公司 Method for activating and regenerating waste activated carbon after harmless treatment of waste mercury catalyst

Similar Documents

Publication Publication Date Title
CN110354831A (en) Powder activated carbon regeneration method
CN102515830A (en) Reproducible phosphorus-uptake ceramsite and preparation method thereof
JP2013132600A (en) Pulp recovery facility
CN108176373A (en) A kind of graphene oxide corn straw modification charcoal and preparation method thereof and in sewage is removed heavy metal application
CN108479204A (en) A kind of exhaust dust device with bag with filter bag monitoring function
JP2009226265A (en) Water selectivity adsorbent and manufacturing method
CN107963628A (en) The preparation of walnut shell activated carbon and its method for eluent in adsorption recovery phenanthrene-polluted soil leacheate
CN108554125A (en) Remove the method and device of Pu'er tea production harmful substances from flue gases
CN204219976U (en) A kind of precipitated calcium carbonate carbonization tails dedusting machine
CN107952414A (en) A kind of oily waste water adsorbent and preparation method thereof
CN107456951A (en) A kind of rice straw adsorbent of modification and its preparation method and application
JP4227524B2 (en) Method and apparatus for producing lime-treated corn paste
CN101209407A (en) Regeneration method aluminum fabrication plant production garbage diatomite filter aid waste residue
CN107126816A (en) The method that heavy metal in high-temperature flue gas is removed using active boron nitride
CN110270307A (en) A kind of adsorbent and preparation method thereof and the application in absorption volatile organic contaminant
CN105268419A (en) Waste white clay recycling process
CN207002896U (en) A kind of wool recovery device with dust removing effects for carding machine
CN105621524A (en) Environment-friendly sewage treatment agent and preparation method thereof
CN103601320B (en) A kind of low concentration salt marsh brine recycling utilizes method and apparatus
JP2792820B2 (en) High-performance activated carbon and its production method
CN102319536A (en) Purification system and method for high-dust concentration supersaturated peculiar smell gas
CN102527362A (en) Regeneration method of active carbon for treating decoloring process of analgin
CN108212135A (en) The recycling and processing device and method of dead catalyst in a kind of Bravo synthesis technology
CN112811837B (en) System equipment and method for dehydrating and drying phosphogypsum by using high-temperature waste heat of regenerated aggregate
CN213687725U (en) Active carbon drying 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
TA01 Transfer of patent application right

Effective date of registration: 20211110

Address after: 233000 in the original nursing home, Xiaoxi Town, Wuhe County, Bengbu City, Anhui Province

Applicant after: Anhui Xinhui Carbon Industry Co., Ltd

Address before: 211500 Room 215, building 6, standard room, Nanjing Siqiao economic Park, Donggou, Longpao street, Liuhe District, Nanjing, Jiangsu Province

Applicant before: Nanjing anjiete Environmental Protection Technology Co., Ltd

TA01 Transfer of patent application right