2013 wcu's poster presentation(modifiedii)

1
Poster template by ResearchPosters.co.za Fouling of carbon electrode by humic substance and its cleaning in capacitive deionization Wannacha Limthanakul, Taeyoung Kim, Seoni Kim, Jeyong Yoon School of Chemical and Biological Engineering, College of Engineering, Seoul National University, Seoul, Korea Introduction Objectives Experimental Works Results Summary Carbon Electrode Carbon Electrode + - + + + + - - - - - - - - - + + + + + + + + - - Treated Water Concentrated Water Anode Cathode Fig. 1. Schematic diagram of CDI process Capacitive deionization (CDI) is a technology for desalination and water treatment in which ions are removed from water by applying an electric field between two porous (carbon) electrodes. Advantages: - Environmentally clean technology - Energy and cost saving - Simply operating Further study need Because electrode materials used in CDI has been fabricated from high- surface area carbon, the accumulation of organic material could effect the electrode property contributed to diminish the CDI performance. . 2. Accumulation of organic matter on carbon surface Source: wateensolutions.com.au To investigate the effects of organic matter to CDI performance. To investigate the electrochemical property change of the electrodes after organic fouling. For organic fouling remediation, chemical cleaning approach has been applied to observe the recovery of CDI performance. Carbon Electrodes: Materials: Activated carbon YP50 + Super P + PTFE Fabrication: Rolling Press method(RP) Dissolved Organic Solution 100 mg/L of Humic Acid(HA) Soaking period 24 hr 100 mg/L of Humic Acid Roller Roller Carbon mixtur e 50 mm 0.3 mm (a ) (b ) Fig. 3. Schematic of organic fouling on carbon electrode. (a) electrodes were fabricated by RP method. (b) Fabricated electrodes were soaked in humic acid solution for 24 hr. Desalination Reactor CDI cell : Flow type Feed Solution NaCl : 10 mM Operating Conditions Applied potential : 1.2 V Cycle time : 5 min charging, 5 min discharging 5 cycles Flow rate 10 ml/min Organic fouling Potentiostat Outlet Conductivity meter CDI cell NaCl 10mM Peristaltic pump Graphite sheet Graphite sheet Electrode Electrode Spacers Fig. 4. Schematic of experimental system for desalination Cleaning agent: 10 mM of NaOH Cleaning time: 10,25 and 50 min Fouling Remediation (1) Effect of organic fouling to desalination performance and electrochemical property of electrodes (a) (b) Fig. 5. Desalination performance of HA fouled electrode and virgin carbon electrode: (a) ion removal aspect; (b) amount of accumulated ion removal during charging step Electrode s Specific Capacitance (F/g carbon) Virgin YP50 81 HA fouled 73 Fig. 6. Cyclic voltammograms of HA fouled electrode and virgin electrode. (2) Recovery of desalination performance and electrochemical property by alkaline cleaning agent(NaOH) (a) ( b ) Fig. 7. Desalination performance of HA fouled electrode and different time cleaned electrodes. : (a) ion removal aspect; (b) amount of accumulated ion removal during charging step Electrodes Capacitanc e (F/g carbon) Virgin YP50 81 Fouled YP50 73 10 min cleaning 78 25 min cleaning 77 50 min cleaning 91 Fig. 8. Cyclic voltammograms of HA fouled electrode and different time cleaned electrodes. The deionization performance after operating with HA fouled electrodes was significantly declined Decreasing in amount of ion removal (11 3 mg/g) and capacitance (8173 F/g) The deionization performance and capacitance were recovered by 10 mM of NaOH as a cleaning agent for 50 min. In particular, the capacitance became higher than the virgin electrode after cleaning. Contact Information Biofilm Engineering Laboratory env.snu.ac.kr 302 Bld. Room No.513(5 th floor) Tel: 82-2-880-8941 Fax: 82-2-876-8911 Email: [email protected] r Acknowledgments This research was supported by WCU (World Class University) program through the Korea Science and Engineering Foundation by the Ministry of Education, Science and Technology (R31-10013), and also supported by Korea Ministry of Environment as “Converging technology project” (223-111-003).

Upload: wannacha-limthanakul

Post on 11-Feb-2017

239 views

Category:

Documents


2 download

TRANSCRIPT

Page 1: 2013 WCU's Poster Presentation(ModifiedII)

Poster template by ResearchPosters.co.za

Fouling of carbon electrode by humic substance and its cleaning in capacitive deionization

Wannacha Limthanakul, Taeyoung Kim, Seoni Kim, Jeyong YoonSchool of Chemical and Biological Engineering, College of Engineering, Seoul National University, Seoul, Korea

Introduction

Objectives

Experimental Works

Results

Summary

Carbon Electrode

Carbon Electrode

+-

++

++-

--

-- - - - -

++ + + + + + +

- -Treated WaterConcentrated Water

Anode

Cathode

Fig. 1. Schematic diagram of CDI process

Capacitive deionization (CDI) is a technology for desalination and water treatment in which ions are removed from water by applying an electric field between two porous (carbon) electrodes.

Advantages: - Environmentally clean technology- Energy and cost saving- Simply operating

Further study needBecause electrode materials used in CDI has been

fabricated from high-surface area carbon, the accumulation of organic material could effect the electrode property contributed to diminish the CDI performance.

Fig. 2. Accumulation of organic matter on carbon surfaceSource: wateensolutions.com.au

⧄ To investigate the effects of organic matter to CDI performance.

⧄ To investigate the electrochemical property change of the electrodes after organic fouling.

⧄ For organic fouling remediation, chemical cleaning approach has been applied to observe the recovery of CDI performance.

⧄ Carbon Electrodes:Materials: Activated carbon YP50 + Super P + PTFEFabrication: Rolling Press method(RP)

⧄ Dissolved Organic Solution100 mg/L of Humic Acid(HA)

⧄ Soaking period24 hr

100 mg/L of Humic Acid

Roller

Roller

Carbonmixture

50 mm0.3 mm

(a) (b)

Fig. 3. Schematic of organic fouling on carbon electrode. (a) electrodes were fabricated by RP method. (b) Fabricated electrodes were soaked in humic acid solution for 24 hr.

Desalination ⧄ ReactorCDI cell : Flow type ⧄ Feed SolutionNaCl : 10 mM ⧄ Operating ConditionsApplied potential : 1.2 V Cycle time :

5 min charging, 5 min discharging 5 cyclesFlow rate

10 ml/min

Organic fouling

Potentiostat

Outlet

Conductivity meter

CDI cell

NaCl 10mM

Peristaltic pump

Graphite sheet

Graphite sheet

Electrode

ElectrodeSpacers

Fig. 4. Schematic of experimental system for desalination

⧄ Cleaning agent: 10 mM of NaOH ⧄ Cleaning time: 10,25 and 50 min

Fouling Remediation

(1) Effect of organic fouling to desalination performance and electrochemical property of electrodes

(a)

(b)

Fig. 5. Desalination performance of HA fouled electrode and virgin carbon electrode: (a) ion removal aspect; (b) amount of accumulated ion removal during charging step

Electrodes Specific Capacitance (F/g carbon)

Virgin YP50 81

HA fouled 73

Fig. 6. Cyclic voltammograms of HA fouled electrode and virgin electrode.

(2) Recovery of desalination performance and electrochemical property by alkaline cleaning agent(NaOH)

(a)

(b)

Fig. 7. Desalination performance of HA fouled electrode and different time cleaned electrodes. : (a) ion removal aspect; (b) amount of accumulated ion removal during charging step

Electrodes Capacitance(F/g carbon)

Virgin YP50 81

Fouled YP50 73

10 min cleaning 78

25 min cleaning 77

50 min cleaning 91

Fig. 8. Cyclic voltammograms of HA fouled electrode and different time cleaned electrodes.

⧄ The deionization performance after operating with HA fouled electrodes was significantly declined Decreasing in amount of ion removal (11 3 mg/g) and capacitance (8173 F/g)

⧄ The deionization performance and capacitance were recovered by 10 mM of NaOH as a cleaning agent for 50 min.

⧄ In particular, the capacitance became higher than the virgin electrode after cleaning.

Contact InformationBiofilm Engineering Laboratoryenv.snu.ac.kr

302 Bld. Room No.513(5th floor)

Tel: 82-2-880-8941Fax: 82-2-876-8911

Email: [email protected]

Acknowledgments

This research was supported by WCU (World Class University) program through the Korea Science and Engineering Foundation by the Ministry of Education, Science and Technology (R31-10013), and also supported by Korea Ministry of Environment as “Converging technology project” (223-111-003).