Performance Characteristics of Anaerobic Biodegradation of Synthetic Phenolic Industrial Wastewater

The treatment of toxic and inhibitory phenolic compounds using biological techniques have been pursued vas a promising and widely accepted treatment process due to its easiness of handling, a greater level of stabilization of waste and properly operated to prevent the production of secondary polluta...

Full description

Saved in:
Bibliographic Details
Main Author: Mishu Singh (Author)
Format: Book
Published: Philippine Association of Institutions for Research, Inc., 2015-10-01T00:00:00Z.
Subjects:
Online Access:Connect to this object online.
Tags: Add Tag
No Tags, Be the first to tag this record!

MARC

LEADER 00000 am a22000003u 4500
001 doaj_001257edc7fc438d9ff02058b9af0f60
042 |a dc 
100 1 0 |a Mishu Singh  |e author 
245 0 0 |a Performance Characteristics of Anaerobic Biodegradation of Synthetic Phenolic Industrial Wastewater 
260 |b Philippine Association of Institutions for Research, Inc.,   |c 2015-10-01T00:00:00Z. 
500 |a 2012-3981 
500 |a 2244-0445 
500 |a 10.7719/jpair.v22i1.333 
520 |a The treatment of toxic and inhibitory phenolic compounds using biological techniques have been pursued vas a promising and widely accepted treatment process due to its easiness of handling, a greater level of stabilization of waste and properly operated to prevent the production of secondary pollutants. Up-flow Anaerobic Bio-Reactors (UAFB) has been widely applied for the handling of high organic load industrial wastewater. The treatment of synthetic phenolic wastewater by a single stage anaerobic fixed bed bioreactor with granite stones packing at four different temperatures was studied. The effect of hydraulic retention time on COD reduction and other steady state characteristics and kinetic parameters, which form these characteristics, was also studied. A recirculated single stage up-flow anaerobic bioreactor operated at all the above-given temperatures with initial BOD 1462 mg/l and initial COD 5720 mg/l for a digestion period of 25 days with a working volume of 1000 ml. The performance of the reactor was monitored after every five days and analyzed in terms of percentage (COD, BOD, TS, TDS, VS removal and biogas production). The removal efficiency of BOD, COD, TS, TDS and VS reached a maximum value of 63.20%, 61.24%, 44.88%, 47.67% and 53.12% respectively. With the change in HRT, the maximum COD reduction was 66.04% at 24 hrs HRT at 400C with initial COD of 5000 mg/l. Specific biogas yield increased up to 0.0162 ml/mg CODr. 
546 |a EN 
690 |a phenol 
690 |a anaerobic 
690 |a fixed bed bioreactor 
690 |a wastewater 
690 |a up-flow anaerobic sludge blanket 
690 |a experimental design 
690 |a india 
690 |a Social Sciences 
690 |a H 
690 |a Education 
690 |a L 
655 7 |a article  |2 local 
786 0 |n JPAIR, Vol 22, Iss 1, Pp 17-30 (2015) 
787 0 |n https://philair.ph/index.php/jpair/article/view/333 
787 0 |n https://doaj.org/toc/2012-3981 
787 0 |n https://doaj.org/toc/2244-0445 
856 4 1 |u https://doaj.org/article/001257edc7fc438d9ff02058b9af0f60  |z Connect to this object online.