Krishan Kishor Garg
Current Organizations / Institutes
The organizations/institutes from the scholar's latest article
Research Subjects
Krishan Kishor Garg has a total of 7 co-authors. Here are the top co-authors by number of shared publications:
Basheshwar Prasad
3 shared publicationsBasheshwer Prasad
3 shared publications- Vimal Chandra Srivastava
Department of Chemical Engineering, Indian Institute of Technology Roorkee, Roorkee, Uttarakhand 247667, India
2 shared publications - Basheswar Prasad
Department of Chemical Engineering, Indian Institute of Technology Roorkee, Roorkee-247667, India
1 shared publication - Indra Deo Mall
Department of Chemical Engineering, Indian Institute of Technology, Roorkee, Roorkee 247667, Uttarakhand, India
1 shared publication - Indra Mani Mishra
Department of Chemical Engineering
1 shared publication
Latest Publications
- 1 November 2017
- Published by Elsevier in Environmental Technology & Innovation
- Vol. 8, 191-217
Treatment of toxic pollutants of purified terephthalic acid waste water: A review
- 1 November 2017
- Published by Elsevier in Environmental Technology & Innovation
- Vol. 8, 191-217
Treatment of toxic pollutants of purified terephthalic acid waste water: A review
- 29 January 2016
- Published by Royal Society of Chemistry (RSC) in RSC Advances
- Vol. 6 (20) , 16223-16233
Continuous electrocoagulation treatment of pulp and paper mill wastewater: operating cost and sludge study
The present research deals with the treatment of agri-based pulp and paper mill wastewater by continuous electrocoagulation (CEC) process using iron (Fe) as an electrode material. Effects of flow rates (dm3 h−1): 0.5–4.0 and residence time (τ): 0.5–4.0 h were investigated on degradation of chemical oxygen demand (COD), color, total solid (TS), turbidity, specific energy consumption (SEC), instantaneous current efficiency (ICE) and electrochemical degradation index (EDI). At flow rates of 1.0 and 0.5 dm3 h−1, COD removal efficiency of 78.20 and 82.15%; and color removal efficiency of 79 and 90%, respectively, was achieved. TS concentration of wastewater slurry was also reduced by 65% after 3 h residence time with flow rate of 1 dm3 h−1. The specific energy consumption (kW h per kgCODremoved) was decreased from 16.3 to 14.3 with decrease in τ from 4 to 1 h. At a supply charge concentration of 0.62 A h dm−3, the current efficiency (CE) values were 310% and 274% after τ = 2 and 1 h, respectively. Dissolution and consumption of electrodes were also studied with a change in flow rates. Sludge obtained after the CEC process was analyzed for settling and filterability characteristics, morphology and elemental analysis, point of zero charge, physicochemical and elemental characterization, and TS concentration. The operating cost of the process was also calculated based on the electrical energy and electrode consumption and was found to be 61.0 Indian Rupees (0.9 USD) for the treatment of 1 m3 of wastewater.
- 29 January 2016
- Published by Royal Society of Chemistry (RSC) in RSC Advances
- Vol. 6 (20) , 16223-16233
Continuous electrocoagulation treatment of pulp and paper mill wastewater: operating cost and sludge study
The present research deals with the treatment of agri-based pulp and paper mill wastewater by continuous electrocoagulation (CEC) process using iron (Fe) as an electrode material. Effects of flow rates (dm3 h−1): 0.5–4.0 and residence time (τ): 0.5–4.0 h were investigated on degradation of chemical oxygen demand (COD), color, total solid (TS), turbidity, specific energy consumption (SEC), instantaneous current efficiency (ICE) and electrochemical degradation index (EDI). At flow rates of 1.0 and 0.5 dm3 h−1, COD removal efficiency of 78.20 and 82.15%; and color removal efficiency of 79 and 90%, respectively, was achieved. TS concentration of wastewater slurry was also reduced by 65% after 3 h residence time with flow rate of 1 dm3 h−1. The specific energy consumption (kW h per kgCODremoved) was decreased from 16.3 to 14.3 with decrease in τ from 4 to 1 h. At a supply charge concentration of 0.62 A h dm−3, the current efficiency (CE) values were 310% and 274% after τ = 2 and 1 h, respectively. Dissolution and consumption of electrodes were also studied with a change in flow rates. Sludge obtained after the CEC process was analyzed for settling and filterability characteristics, morphology and elemental analysis, point of zero charge, physicochemical and elemental characterization, and TS concentration. The operating cost of the process was also calculated based on the electrical energy and electrode consumption and was found to be 61.0 Indian Rupees (0.9 USD) for the treatment of 1 m3 of wastewater.
- 1 September 2015
- Published by Elsevier in Journal of Environmental Chemical Engineering
- Vol. 3 (3) , 1731-1739
Removal of para-toulic acid (p-TA) from purified terephthalic acid (PTA) waste water by electrocoagulation process
- 1 September 2015
- Published by Elsevier in Journal of Environmental Chemical Engineering
- Vol. 3 (3) , 1731-1739
Removal of para-toulic acid (p-TA) from purified terephthalic acid (PTA) waste water by electrocoagulation process
- Open Access
- 1 January 2015
- Published by Sci Forschen, Inc. in International Journal of Water and Wastewater Treatment
- Vol. 1 (1)
Removal of Cr (VI) and COD from Electroplating Wastewater by Corncob Based Activated Carbon
- 1 January 2015
- Published by Sci Forschen, Inc. in International Journal of Water and Wastewater Treatment
- Vol. 1 (1)
Open AccessRemoval of Cr (VI) and COD from Electroplating Wastewater by Corncob Based Activated Carbon