JPS5614410A - Granular activated carbon regenerating method - Google Patents
Granular activated carbon regenerating methodInfo
- Publication number
- JPS5614410A JPS5614410A JP8830379A JP8830379A JPS5614410A JP S5614410 A JPS5614410 A JP S5614410A JP 8830379 A JP8830379 A JP 8830379A JP 8830379 A JP8830379 A JP 8830379A JP S5614410 A JPS5614410 A JP S5614410A
- Authority
- JP
- Japan
- Prior art keywords
- liquor
- activated carbon
- tower
- granular activated
- regenerating
- 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.)
- Granted
Links
Landscapes
- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
Abstract
PURPOSE: To recover the org. matter adsorbing power of granular activated carbon to that of fresh activated carbon by instantaneously mixing waste liquors discharged by regenerating anion and cation exchange resins so that the mixed liquor is made acidic, passing the liquor through granular activated carbon after removing free carbonic acid, and regenerating the carbon.
CONSTITUTION: Waste liquor 1 discharged by regenerating a cation exchange resin and waste liquor 2 discharged by regenerating an anion exchange resin are received in receiving vessels 3, 4, respectively, and they are mixed instantaneously with ejector 7. At this time, acid 10 is added to liquor 2 so that the pH of the mixed liquor becomes ≤3. The mixed liquor of ≤3pH is allowed to flow into the top of deoxidation tower 11 to remove free carbonic acid in the liquor with air fed from a lower portion of tower 11 with blower 12, and the liquor is passed through adsorption towers 15A, 15B packed with regenerated granular activated carbon 14 to remove org. matter in the liquor by adsorption. The resulting acidic treated liquor is reneutralized with alkali to about 7pH at which electric discharge is enabled using ejector 7'. On the other hand, granular activated carbon in an adsorption tower such as tower 15C satd. with org. matter and separated from the liquor feeding cource is carried to rotary kiln through receiving vessel 19, regenerated by usual roasting, and repacked into tower 15C.
COPYRIGHT: (C)1981,JPO&Japio
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP54088303A JPS5817127B2 (en) | 1979-07-13 | 1979-07-13 | How to regenerate granular activated carbon |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP54088303A JPS5817127B2 (en) | 1979-07-13 | 1979-07-13 | How to regenerate granular activated carbon |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS5614410A true JPS5614410A (en) | 1981-02-12 |
JPS5817127B2 JPS5817127B2 (en) | 1983-04-05 |
Family
ID=13939152
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP54088303A Expired JPS5817127B2 (en) | 1979-07-13 | 1979-07-13 | How to regenerate granular activated carbon |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS5817127B2 (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101708468A (en) * | 2009-12-10 | 2010-05-19 | 大连交通大学 | Powdered carbon regeneration method |
JP2014004511A (en) * | 2012-06-22 | 2014-01-16 | Daiki Ataka Engineering Co Ltd | Method for regenerating activated carbon |
-
1979
- 1979-07-13 JP JP54088303A patent/JPS5817127B2/en not_active Expired
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101708468A (en) * | 2009-12-10 | 2010-05-19 | 大连交通大学 | Powdered carbon regeneration method |
JP2014004511A (en) * | 2012-06-22 | 2014-01-16 | Daiki Ataka Engineering Co Ltd | Method for regenerating activated carbon |
Also Published As
Publication number | Publication date |
---|---|
JPS5817127B2 (en) | 1983-04-05 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
IE800293L (en) | Water treating | |
US3852410A (en) | Sulfur dioxide and particulate contaminant removal from industrial stack gases | |
JPS5614410A (en) | Granular activated carbon regenerating method | |
JPS5781881A (en) | Treatment of water containing boron | |
JPS5367682A (en) | Regenerating method for condensate water demineralization apparatus | |
GB1268421A (en) | Water purification process | |
JPS55104500A (en) | Removing method for impurity ion from tin plating liquid | |
JPS5528738A (en) | Regenerating method of mixed ion exchange resin | |
JPS5528762A (en) | Condensed water treating method | |
JPS55119446A (en) | Regenerating method of ion exchange resin | |
JPS565192A (en) | Highly advanced treatment of waste water | |
JPS5244053A (en) | Method for processing waste water containing synthetic amino resin | |
JPS5594650A (en) | Method of regenerating anion exchange resin of mixed-bed type ion exchange equipment of out-of-tower regeneration system | |
JPS56130300A (en) | Waste liquid treatment in coke oven gas refining | |
JPS5617608A (en) | Method and apparatus for continuous precipitation and dehydration of sludge | |
JPS5528729A (en) | Regenerating method of mixed ion exchange resin | |
JPS5823156B2 (en) | Pure water production method | |
JPS57107229A (en) | Improvement of wet type waste gas desulfurization method | |
JPS5528735A (en) | Method and apparatus for treating condensed water | |
DE3676157D1 (en) | REGENERATION OF AN ION EXCHANGE RESIN FOR THE REMOVAL OF NITRATES FROM WATER. | |
JPS5613081A (en) | Neutralization treatment method of regeneration waste liquid in ion exchange apparatus | |
JPS56141843A (en) | Treatment of ion exchange resin | |
JPS5721980A (en) | Treating method for circulating cooling water containing chromic acid ion | |
JPS5561976A (en) | Clarification of water | |
JPS5390178A (en) | Water purifying method |