Method for deeply treating inorganic high-salt industrial wastewater and realizing zero liquid discharge
A technology for industrial waste water and advanced treatment, applied in the field of waste water treatment, can solve the problems of high energy consumption and equipment investment, reduced heat transfer efficiency, limited use and other problems, achieve low cost of hard removal, reduce scaling characteristics, and achieve zero liquid discharge Effect
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Examples
Embodiment 1
[0030] High-salt wastewater with TH / CH>1.0
[0031] Sample wastewater 100kg, temporary hardness 23mmol / L, calcium hardness 12mmol / L, salt content 4000 mg / L, add 2.0kg of 10% lime suspension at a rate of 0.5kg / min, stir for 30min, then add 3% 1.0kg of sodium hydroxide solution was added at a rate of 0.5kg / min. After stirring for 30 minutes, it was transferred to a settler, (including 10kg of ultrafiltered concentrated water returned to the settler) to separate 110kg of clear liquid.
[0032] After the clear liquid is filtered, 0.1 kg of 31% hydrochloric acid is added to adjust the pH value between 7 and 9, and enter the ultrafiltration system. 4300 mg / L, reverse osmosis clean water volume 75-85kg. Salt content 17000 mg / L, used to dissolve raw salt.
Embodiment 2
[0034] The high-salt wastewater with TH / CH<1.0 is fed with carbon dioxide
[0035] Sample wastewater 100kg, temporary hardness 15mmol / L, calcium hardness 20mmol / L, salt content 4000 mg / L, add 0.5-1.0 kg of 10% calcium carbide slag suspension, pH in the water between 8-9, and carbon dioxide 50 g ~ 100 g, after 30 minutes of blowing, TH / CH is 1.6.
[0036] Add 2.5kg of 10% calcium carbide slag suspension at a rate of 0.5kg / min. After stirring for 30 minutes, add 1.0kg of 3% sodium hydroxide solution at a rate of 0.5kg / min. After stirring for 30 minutes, transfer to sedimentation 110kg of supernatant (including 10kg of ultra-filtered concentrated water returned to the settler).
[0037] After the clear liquid is filtered, 0.1 kg of 31% hydrochloric acid is added to adjust the pH value between 7 and 9, and enter the ultrafiltration system. 10 kg of ultrafiltered concentrated water returns to the settler, and 100 kg of ultrafiltered water enters the reverse osmosis system. The amou...
Embodiment 3
[0039] The high-salt wastewater with TH / CH<1.0 is added to the solution containing soluble carbonate alkaline waste residue
[0040] Sample wastewater 100kg, temporary hardness 2.5mmol / L, calcium hardness 10mmol / L, salt content 5000 mg / L, add 1.0kg of 10% waste sodium carbonate solution at a speed of 0.5kg / min, stir for 30min, then add 3% 2.0kg of sodium hydroxide solution, added at a rate of 0.5kg / min, stirred for 30 minutes, then transferred to a settler, (including 10kg of ultrafiltered concentrated water returned to the settler) to separate 110kg of clear liquid.
[0041] After the clear liquid is filtered, 0.1 kg of 31% hydrochloric acid is added to adjust the pH value between 7 and 9, and enter the ultrafiltration system. 10 kg of ultrafiltered concentrated water returns to the settler, and 100 kg of ultrafiltered water enters the reverse osmosis system. The amount of reverse osmosis water is 5100 mg / L, the amount of reverse osmosis clean water is 75-85kg, and the salt c...
PUM
Property | Measurement | Unit |
---|---|---|
Hardness | aaaaa | aaaaa |
Hardness | aaaaa | aaaaa |
Hardness | aaaaa | aaaaa |
Abstract
Description
Claims
Application Information
- R&D Engineer
- R&D Manager
- IP Professional
- Industry Leading Data Capabilities
- Powerful AI technology
- Patent DNA Extraction
Browse by: Latest US Patents, China's latest patents, Technical Efficacy Thesaurus, Application Domain, Technology Topic, Popular Technical Reports.
© 2024 PatSnap. All rights reserved.Legal|Privacy policy|Modern Slavery Act Transparency Statement|Sitemap|About US| Contact US: help@patsnap.com