CN101125271A - Method for regenerating filtering absorbing material used for water treatment - Google Patents
Method for regenerating filtering absorbing material used for water treatment Download PDFInfo
- Publication number
- CN101125271A CN101125271A CNA2006101112599A CN200610111259A CN101125271A CN 101125271 A CN101125271 A CN 101125271A CN A2006101112599 A CNA2006101112599 A CN A2006101112599A CN 200610111259 A CN200610111259 A CN 200610111259A CN 101125271 A CN101125271 A CN 101125271A
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- Prior art keywords
- absorbing material
- filtering absorbing
- coal
- saturated
- filtering
- 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.)
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- 238000001914 filtration Methods 0.000 title claims abstract description 57
- 239000011358 absorbing material Substances 0.000 title claims abstract description 53
- 238000000034 method Methods 0.000 title claims abstract description 18
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 11
- 230000001172 regenerating effect Effects 0.000 title abstract 3
- 229920006395 saturated elastomer Polymers 0.000 claims abstract description 24
- 239000003245 coal Substances 0.000 claims abstract description 20
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims abstract description 15
- 238000010438 heat treatment Methods 0.000 claims abstract description 15
- 230000004913 activation Effects 0.000 claims abstract description 13
- 239000003546 flue gas Substances 0.000 claims abstract description 13
- 239000000463 material Substances 0.000 claims abstract description 12
- 238000009835 boiling Methods 0.000 claims abstract description 9
- 239000007789 gas Substances 0.000 claims abstract description 9
- 230000018044 dehydration Effects 0.000 claims abstract description 6
- 238000006297 dehydration reaction Methods 0.000 claims abstract description 6
- 238000000197 pyrolysis Methods 0.000 claims description 8
- 238000010792 warming Methods 0.000 claims description 8
- 238000001035 drying Methods 0.000 claims description 6
- 150000002894 organic compounds Chemical class 0.000 claims description 6
- 238000009418 renovation Methods 0.000 claims description 6
- 239000003610 charcoal Substances 0.000 claims description 3
- 239000005416 organic matter Substances 0.000 claims description 3
- RHZUVFJBSILHOK-UHFFFAOYSA-N anthracen-1-ylmethanolate Chemical compound C1=CC=C2C=C3C(C[O-])=CC=CC3=CC2=C1 RHZUVFJBSILHOK-UHFFFAOYSA-N 0.000 claims description 2
- 239000003830 anthracite Substances 0.000 claims description 2
- 239000000571 coke Substances 0.000 claims description 2
- 238000004939 coking Methods 0.000 claims description 2
- 239000003077 lignite Substances 0.000 claims description 2
- 238000004519 manufacturing process Methods 0.000 claims description 2
- 230000008439 repair process Effects 0.000 claims description 2
- 239000008246 gaseous mixture Substances 0.000 description 6
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 4
- 239000003500 flue dust Substances 0.000 description 4
- 239000000446 fuel Substances 0.000 description 4
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 4
- 238000012545 processing Methods 0.000 description 4
- 239000002994 raw material Substances 0.000 description 4
- 238000007789 sealing Methods 0.000 description 4
- 239000002893 slag Substances 0.000 description 4
- 239000010842 industrial wastewater Substances 0.000 description 3
- 239000010865 sewage Substances 0.000 description 3
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 description 2
- 229910000831 Steel Inorganic materials 0.000 description 2
- 229910002092 carbon dioxide Inorganic materials 0.000 description 2
- 239000001569 carbon dioxide Substances 0.000 description 2
- 229910002091 carbon monoxide Inorganic materials 0.000 description 2
- 239000003034 coal gas Substances 0.000 description 2
- 239000000567 combustion gas Substances 0.000 description 2
- 238000002485 combustion reaction Methods 0.000 description 2
- 238000010411 cooking Methods 0.000 description 2
- 239000000428 dust Substances 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 239000003517 fume Substances 0.000 description 2
- 229910052739 hydrogen Inorganic materials 0.000 description 2
- 239000001257 hydrogen Substances 0.000 description 2
- 125000004435 hydrogen atom Chemical class [H]* 0.000 description 2
- 238000009413 insulation Methods 0.000 description 2
- 238000003913 materials processing Methods 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 238000004321 preservation Methods 0.000 description 2
- 238000011084 recovery Methods 0.000 description 2
- 230000008929 regeneration Effects 0.000 description 2
- 238000011069 regeneration method Methods 0.000 description 2
- 238000001179 sorption measurement Methods 0.000 description 2
- 239000010959 steel Substances 0.000 description 2
- 239000002351 wastewater Substances 0.000 description 2
- ZCYVEMRRCGMTRW-UHFFFAOYSA-N 7553-56-2 Chemical compound [I] ZCYVEMRRCGMTRW-UHFFFAOYSA-N 0.000 description 1
- 229910000851 Alloy steel Inorganic materials 0.000 description 1
- BPQQTUXANYXVAA-UHFFFAOYSA-N Orthosilicate Chemical compound [O-][Si]([O-])([O-])[O-] BPQQTUXANYXVAA-UHFFFAOYSA-N 0.000 description 1
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 1
- 230000002745 absorbent Effects 0.000 description 1
- 239000002250 absorbent Substances 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 1
- 230000000712 assembly Effects 0.000 description 1
- 238000000429 assembly Methods 0.000 description 1
- 239000000440 bentonite Substances 0.000 description 1
- 229910000278 bentonite Inorganic materials 0.000 description 1
- SVPXDRXYRYOSEX-UHFFFAOYSA-N bentoquatam Chemical compound O.O=[Si]=O.O=[Al]O[Al]=O SVPXDRXYRYOSEX-UHFFFAOYSA-N 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 229910000019 calcium carbonate Inorganic materials 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 239000013043 chemical agent Substances 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 238000010924 continuous production Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 238000010304 firing Methods 0.000 description 1
- 230000002209 hydrophobic effect Effects 0.000 description 1
- 239000011229 interlayer Substances 0.000 description 1
- 229910052740 iodine Inorganic materials 0.000 description 1
- 239000011630 iodine Substances 0.000 description 1
- 238000012856 packing Methods 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 150000004965 peroxy acids Chemical class 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 230000037452 priming Effects 0.000 description 1
- 238000003672 processing method Methods 0.000 description 1
- 238000010298 pulverizing process Methods 0.000 description 1
- 238000012797 qualification Methods 0.000 description 1
- 238000005096 rolling process Methods 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 238000012216 screening Methods 0.000 description 1
- 239000010802 sludge Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000002918 waste heat 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
- B01J20/30—Processes for preparing, regenerating, or reactivating
- B01J20/34—Regenerating or reactivating
- B01J20/345—Regenerating or reactivating using a particular desorbing compound or mixture
- B01J20/3458—Regenerating or reactivating using a particular desorbing compound or mixture in the gas phase
- B01J20/3466—Regenerating or reactivating using a particular desorbing compound or mixture in the gas phase with steam
-
- 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
- B01J20/3416—Regenerating or reactivating of sorbents or filter aids comprising free carbon, e.g. activated carbon
-
- 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
- B01J20/3483—Regenerating or reactivating by thermal treatment not covered by groups B01J20/3441 - B01J20/3475, e.g. by heating or cooling
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B32/00—Carbon; Compounds thereof
- C01B32/30—Active carbon
- C01B32/354—After-treatment
- C01B32/36—Reactivation or regeneration
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/28—Treatment of water, waste water, or sewage by sorption
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2303/00—Specific treatment goals
- C02F2303/16—Regeneration of sorbents, filters
Abstract
The present invention relates to a regenerating method of filtering absorbing material which is used for water disposing. The method comprises the steps as follows: A) the saturated filtering absorbing material is transported to a dehydrating device for dehydration to make the water ratio of the saturated filtering absorbing material less than 30 percent; B) the saturated filtering absorbing material after being dehydrated is transported to a heating furnace for heating until reaching 120 to 400 DEG C at a speed of 4 DEG C per minute, and the moisture of the filtering absorbing material hole and partial organic with low boiling point volatilize; C) the filtering absorbing material after being dried is also heated until reaching 450 to 650 DEG C at a speed of 6 to 8 DEG C per minute, which makes the filtering absorbing material dry distill and carbonize, the organic with high boiling point of the material decomposes, one part becomes organic with low boiling point which volatilizes later, while the other part is carbonized; D) the filtering absorbing material is continuously heated until reaching 700 DEG C at a speed of 4 to 6 DEG C per minute, and is activated by water vapor and then is activated by flue gas, and the activation time is from 20 minutes to 60 minutes. The mixed gas and the flue gas produced by the rotary heating furnace in the regenerating process of the saturated filtering absorbing material are transported to the hearth of the coal burning furnace for burning.
Description
Technical field
The invention belongs to a kind of material processing method, be specifically related to a kind of renovation process that is used to handle the filtering absorbing material of industrial wastewater, municipal sewage.
Background technology
Present most of municipal sewage and industrial wastewater (the especially big industrial wastewater of discharge capacity) all adopt biochemistry, anaerobism, aerobic, activated sludge, add method such as chemical agent handles, the said method floor space is big, the power consumption height, produce a large amount of mud in the processing procedure, and can't handle high salt, peracid, the high waste water that is difficult to biochemistry of COD content.The solid absorbent that is used for water treatment at present has multiple, as active carbon, charcoal, bentonite, diatomite, calcium carbonate, slag, coke powder, slag etc.Filtering absorbing material is after using after a while, inorganic matter and organic matter in waste water, the sewage have been adsorbed, these pollutants make filtering absorbing material hydrophobic, occupy the movable lattice of filtering absorbing material, organic continuous accumulation progressively reduces the adsorption capacity of filtering absorbing material, has influenced the performance of filtering absorbing material.Method by regeneration can make filtering absorbing material recover adsorption capacity, and can reuse, and has reduced the expense of water treatment.
Summary of the invention
The object of the present invention is to provide a kind of renovation process that is used for the filtering absorbing material of water treatment.
For achieving the above object, renovation process provided by the invention, its step is as follows:
A) saturated filtering absorbing material is transported in the dehydration equipment dewaters, make moisture content＜30% of saturated filtering absorbing material;
B) will carry the swinging heating furnace to carry out drying through the saturated filtering absorbing material of processed, heat up, rise to 120-400 ℃ with 4 ℃ of/minute clock rate, in this dry run, moisture in the filtering absorbing material hole and the volatilization of a part of low-boiling-point organic compound;
C) be warming up to 450-650 ℃ through the follow-up continuous speed with 6-8 ℃/minute of super-dry, make filtering absorbing material destructive distillation and charing, contained high boiling point organic compound produces and decomposes in the material, and wherein a part is volatilized after becoming low-boiling point material, another part charing;
When D) continuing to be warming up to 700 ℃ with 4-6 ℃/minute speed again, use earlier steam activation, activate with flue gas then, the time of activation is 20-60 minute.Mass recovery 〉=96%.
E) with in the saturated filtering absorbing material regenerative process, mixed gas that produces in the swinging heating furnace and hot flue gas are transported in the coal-burning boiler burner hearth and burn.
The filtering absorbing material that the present invention regenerates, be meant that adopting anthracite, meager coal, lean coal, coking coal, rich coal, bottle coal, jet coal, brown coal is raw material, also can adopt coal converted products such as coke, basket charcoal, breeze is the filtering absorbing material that feedstock production forms, through pulverizing, screening, place warm 120-150 ℃ of beginning to heat up the raw material of particle diameter＜10mm, raw material is carried out drying processing prior to 4 ℃ of/minute clock rate; Continuation is warming up to 510-650 ℃ with 6-8 ℃/minute speed, constant temperature 40-70 minute, makes raw material destructive distillation and charing; Use earlier steam activation when continuing to be warming up to 800 ℃ with 4-6 ℃/minute speed again, activate with flue gas then, the time of activation is 20-60 minute, and activation temperature is 840-950 ℃.
In the process that saturated filter material is regenerated, produce in the swinging heating furnace cylinder and contain the gaseous mixture that one-tenth such as methane, hydrogen, carbon monoxide, carbon dioxide, ethene are grouped into and enter closed chamber, by cyclone separator the flue dust in the gaseous mixture is separated, the flue dust that separates is sent back in the cylinder again; Be transported to settler through the gaseous mixture after the cyclone separator dust removal process, the raw gas after settler is handled is transported to the auxiliary fuel of the boiler room of enterprise as boiler by gas exhaust machine.Be transported to the boiler room of enterprise after the tar slag of being separated by settler is discharged by the equipment of slagging tap, mix afterwards fuel with the boiler oil coal as boiler.
The key data of this filtering absorbing material and parameter:
Serge blue: 30～85mg/g
Ash content: 8～15%
Packing density: 200～550g/l
Iodine number: 260～720mg/g
Specific area: 200～490m
2/ g
Priming reaction temperature: 800 ℃～950 ℃
Soak time: 20min～60min
Filtering absorbing material yield: 400kg～600kg/t. coal
COD (COD) adsorbance: 200～3,000mg/g.
The specific embodiment
Saturated filtering absorbing material in the water treatment facilities is dewatered after discharging, make moisture content＜30% of saturated filtering absorbing material.To be transported in the heating furnace through the saturated filtering absorbing material of processed, heat up with 4 ℃ of/minute clock rate, rise to 120-400 ℃, saturated filtering absorbing material is carried out drying handle, moisture in the dry run in the filtering absorbing material hole and the volatilization of a part of low-boiling-point organic compound.Saturated filtering absorbing material is warming up to 450-650 ℃ through the follow-up continuous speed with 6-8 ℃/minute of super-dry, make organic matter destructive distillation and charing in the saturated filtering absorbing material, contained high boiling point organic compound produces and decomposes in the material, and wherein a part is volatilized after becoming low-boiling point material, another part charing; When continuing to be warming up to 700 ℃ with 4-6 ℃/minute speed again, use earlier steam activation, activate with flue gas then, the time of activation is 20-60 minute.After regeneration is handled, the mass recovery of filtering absorbing material 〉=96%.
The equipment that the present invention is used to prepare filtering absorbing material can be known equipment, is substantially: dehydration equipment, conveying equipment, steam boiler and the heating furnace that can be warmed to drying, destructive distillation, charing and activation temperature.Dehydration equipment wherein (as centrifugal drier) is to be used for saturated filtering absorbing material is dewatered; Conveying equipment is that the saturated filtering absorbing material that after the reason through dewatering is delivered in the heating furnace; Steam boiler is to be used for producing steam so that the filtering absorbing material through super-dry, destructive distillation, charing is activated; Heating furnace is the common heating device that is used for saturated filtering absorbing material is carried out dry and charing that has the control that heats up.It is " the swinging carbocoal filtering processing unit " that 200410100439.8 (publication number CN1660964) provide that the comparatively ideal equipment that carries out drying, destructive distillation, charing and activation act can adopt application number.When using this unit filtering absorbing material is regenerated, can realize automatic continuous production, thereby enhance productivity.According to the disclosed data of this patent application, the operation principle of the structure of this unit of brief description.Need to prove which kind of equipment the present invention adopts do not have strict qualification, as long as can satisfy dehydration and meet the requirements of dry and dry distillation charring temperature.So only this unit is done a summary here, is to wish to help those skilled in the art further to understand essence technology contents of the present invention, thereby implements.This swinging carbocoal filtering processing machine series cylinder is a double-barrel structure, is made of inner core and urceolus, adopts heat-resisting alloy steel to make, and inner diameter of steel flue is 900-4, and 000mm, urceolus diameter are 1,500-5, and 200mm, the cylinder draw ratio is 12: 1; Be respectively equipped with gear ring, stiffening ring, rolling ring, sliding sealing device at the outside different parts of cylinder; Interlayer between inner core and the urceolus is the combustion gas heating chamber; Inner core is the coal charge cooking camber; Cooking camber is divided into dryer section and retort section; When adopting swinging carbocoal filtering materials processing unit to prepare filtering absorbing material, the unit inner core has increased activation section.The cylinder of unit tilts to place, and is seated on two carrying roller assemblies, is driven by the gear ring on the cylinder by transmission device, and the rotating speed of cylinder changes for per minute 3-5; Temp measuring system is installed on the cylinder, is used to monitor the temperature of each section of cylinder; Urceolus one end and the combustion chamber of cylinder link, and the other end and flue gas collecting chamber link; Inner core one end and the last closed chamber of cylinder link, and the other end and lower seal chamber link; Point of attachment all has sliding sealing device, and sealing device structure is piston ring type, labyrinth type or steam formula; Between fume emission device and the flue gas collecting chamber heat exchanger is installed, is used for reclaiming by the waste heat of combustion gas heating chamber through the flue gas of flue gas collecting chamber discharge.Connect by pipeline between fume emission device, flue gas collecting chamber and the heat exchanger.Last closed chamber is equipped with screw(-type) feeder, sealing adds coal bin, coal store, and cyclone separator, gas cleaning device and coal gas system also are installed; The unit combustion chamber is equipped with igniter, the coal gas ignition that unit adopts gas generator to provide; Firing rate is 4 ℃/min during igniting.The outside of unit is an insulating, and the heat-insulation and heat-preservation material at cylinder position adopts alumina silicate fiber felt, the containment vessel that encased steel plate is made, and common heat-insulation and heat-preservation material is adopted according to surface temperature in other positions.
Adopt in the process that swinging carbocoal filtering materials processing unit regenerates to saturated filter material, produce in the cylinder and contain the gaseous mixture that one-tenth such as methane, hydrogen, carbon monoxide, carbon dioxide, ethene are grouped into and enter closed chamber, by cyclone separator the flue dust in the gaseous mixture is separated, the flue dust that separates is sent back in the cylinder again; Be transported to settler through the gaseous mixture after the cyclone separator dust removal process, the raw gas after settler is handled is transported to the auxiliary fuel of the boiler room of enterprise as boiler by gas exhaust machine.Be transported to the boiler room of enterprise after the tar slag of being separated by settler is discharged by the equipment of slagging tap, mix afterwards fuel with the boiler oil coal as boiler.
Claims (2)
1. renovation process that is used for the filtering absorbing material of water treatment, its step is as follows:
A) saturated filtering absorbing material is transported in the dehydration equipment dewaters, make moisture content＜30% of saturated filtering absorbing material;
B) will be transported to the swinging heating furnace through the saturated filtering absorbing material of processed and carry out drying, heat up, rise to 120-400 ℃ with 4 ℃ of/minute clock rate, in this dry run, moisture in the filtering absorbing material hole and the volatilization of a part of low-boiling-point organic compound;
C) be warming up to 450-650 ℃ through the follow-up continuous speed of super-dry with 6-8 ℃/minute, make organic matter destructive distillation and charing in the filtering absorbing material, contained high boiling point organic compound produces and decomposes in the material, and wherein a part is volatilized after becoming low-boiling point material, another part charing;
When D) continuing to be warming up to 700 ℃ with 4-6 ℃/minute speed again, use earlier steam activation, activate with flue gas then, the time of activation is 20-60 minute.
E) with in the saturated filtering absorbing material regenerative process, mixed gas that produces in the swinging heating furnace and hot flue gas are transported in the coal-burning boiler burner hearth and burn.
2. renovation process as claimed in claim 1, wherein saturated filtering absorbing material for adopting anthracite, meager coal, lean coal, coking coal, rich coal, bottle coal, jet coal, brown coal, coke, basket charcoal or/and breeze be that feedstock production forms, be used for the filtering absorbing material after the water treatment.
Priority Applications (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2006101112599A CN100562352C (en) | 2006-08-17 | 2006-08-17 | A kind of renovation process that is used for the filtering absorbing material of water treatment |
| PCT/CN2007/002482 WO2008022562A1 (en) | 2006-08-17 | 2007-08-17 | A regeneration method for filtering and adsorbing material used in water treatment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2006101112599A CN100562352C (en) | 2006-08-17 | 2006-08-17 | A kind of renovation process that is used for the filtering absorbing material of water treatment |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN101125271A true CN101125271A (en) | 2008-02-20 |
| CN100562352C CN100562352C (en) | 2009-11-25 |
Family
ID=39093455
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNB2006101112599A Expired - Fee Related CN100562352C (en) | 2006-08-17 | 2006-08-17 | A kind of renovation process that is used for the filtering absorbing material of water treatment |
Country Status (2)
| Country | Link |
|---|---|
| CN (1) | CN100562352C (en) |
| WO (1) | WO2008022562A1 (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103663754A (en) * | 2012-09-26 | 2014-03-26 | 上海宝钢化工有限公司 | Regeneration method of cyclodextrin absorbent for water treatment |
| CN110745934A (en) * | 2019-10-22 | 2020-02-04 | 庆泓技术(上海)有限公司 | Modified high-activity inorganic fiber composite material and preparation and regeneration method thereof |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CL2013003788A1 (en) | 2013-12-30 | 2014-05-02 | Univ Santiago Chile | Procedure for the activation and regeneration of a filter material; and filter material obtained. |
| CN112044396B (en) * | 2020-08-25 | 2023-06-09 | 煤炭科学技术研究院有限公司 | Adsorbent capable of being regenerated in situ and preparation method and application thereof |
Family Cites Families (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4268417A (en) * | 1977-09-26 | 1981-05-19 | American Minechem Corporation | Method of making activated carbon |
| JPS6034412B2 (en) * | 1979-08-10 | 1985-08-08 | 住友重機械工業株式会社 | Reactivation method for carbonaceous adsorbent for desulfurization |
| AU7033681A (en) * | 1981-04-10 | 1982-11-04 | Sasaki, Y. | Apparatus for regenerating activated carbon |
| CN85100619B (en) * | 1985-04-02 | 1986-11-26 | 中国市政工程西北设计院 | Forced electric discharge reactivating technique and device for the activated carbon |
| JPH05154379A (en) * | 1991-04-26 | 1993-06-22 | Matsushita Electric Works Ltd | Heat regenerating device for active carbon |
| RU2108968C1 (en) * | 1997-03-18 | 1998-04-20 | Олег Гурьевич Алексеев | Method of preparing adsorbent |
| KR100381903B1 (en) * | 2000-12-16 | 2003-05-01 | 한국염색기술연구소 | recycle system of Activated Carbon Fiber cartridge and its method |
| CN1381305A (en) * | 2001-04-16 | 2002-11-27 | 谢仁智 | Process for regenerating activated carbon |
| CN1413907A (en) * | 2001-10-26 | 2003-04-30 | 中国科学院山西煤炭化学研究所 | Process for preparing active coke |
| CN1298624C (en) * | 2005-02-28 | 2007-02-07 | 昆明理工大学 | Method for preparing activated carbon by waste tobacco stalk treated by physical method |
-
2006
- 2006-08-17 CN CNB2006101112599A patent/CN100562352C/en not_active Expired - Fee Related
-
2007
- 2007-08-17 WO PCT/CN2007/002482 patent/WO2008022562A1/en active Application Filing
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103663754A (en) * | 2012-09-26 | 2014-03-26 | 上海宝钢化工有限公司 | Regeneration method of cyclodextrin absorbent for water treatment |
| CN110745934A (en) * | 2019-10-22 | 2020-02-04 | 庆泓技术(上海)有限公司 | Modified high-activity inorganic fiber composite material and preparation and regeneration method thereof |
Also Published As
| Publication number | Publication date |
|---|---|
| CN100562352C (en) | 2009-11-25 |
| WO2008022562A1 (en) | 2008-02-28 |
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