Resourceful treatment method for organic waste
A technology of organic waste and treatment method, which is applied in the field of organic waste resource treatment, can solve the problems of loss of feasibility, increase of process cost, complicated technical route, etc., to reduce chemical oxygen demand, reduce environmental pollution, reduce The effect of process cost
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Examples
Embodiment 1
[0022] Pour 25L corn steep liquor into a 25L cylindrical plastic reactor, and add 0.5% lactic acid bacteria strain activated bacterial liquid at the same time, the initial pH value in the plastic reactor is 6.8, the temperature is 30 ° C, and the stirring speed is 80r / min, after 3 days of lactic acid fermentation, the maximum concentration of lactic acid was 23747mg / L, and the pH dropped to 3.8. The fermentation broth is transferred to the sedimentation tank for solid-liquid separation, the solid waste residue is discharged, and the supernatant enters the adjustment tank through the storage tank, and then transferred to the 5L medium-chain fatty acid reactor. Clostridium IV is immobilized in the reactor, and the lactic acid in the raw material is consumed during the carbon chain extension process to maintain the pH value in the reactor within the range of 5.5-6.5. The temperature in the medium-chain fatty acid reactor is 30°C, and the hydraulic retention time (HRT) is 5 days. ...
Embodiment 2
[0024]Add 25L corn steep liquor into a 25L cylindrical plastic reactor, add 1% lactic acid bacteria freeze-dried powder, the initial pH in the plastic reactor is 6.8, the temperature is 30°C, and the stirring speed is 80r / min. During the 3-day lactic acid fermentation process, the maximum lactic acid concentration was 33741mg / L, and the pH dropped to 3.5. After solid-liquid separation, the fermentation broth enters a 5L medium-chain fatty acid biosynthesis reactor. The pH value of the reactor is maintained in the range of 5.5-6.5, and Clostridium IV is immobilized in the reactor. The temperature in the biosynthesis reactor was 30°C, and the hydraulic retention time (HRT) was 5 days. After one month of operation, the effluent concentration of medium chain fatty acid caproic acid was 15427mg / L.
Embodiment 3
[0026] Add 25L of fruit and vegetable waste into a 25L cylindrical plastic reactor, add 0.5% lactic acid bacteria freeze-dried powder, the initial pH in the plastic reactor is 7.0, the temperature is 30°C, and the stirring speed is 80r / min. During the 3-day lactic acid fermentation process, the maximum lactic acid concentration was 11568 mg / L, and the pH dropped to 4.0. After solid-liquid separation, the fermentation broth enters a 5L medium-chain fatty acid reactor. The pH value of the reactor is maintained in the range of 5.5-6.5, and Clostridium IV is immobilized in the reactor. The temperature in the reactor is 40°C, and the hydraulic retention time (HRT) is 5 days. After running for one month, the effluent concentration of medium-chain fatty acid caproic acid is 8258mg / L.
PUM
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