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Application of Electro-Membrane Technologies in Zero Liquid Discharge Technology

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The document discusses different electro-membrane technologies for water treatment applications including zero liquid discharge (ZLD) processes.

The document discusses cation exchange membrane (CEM), anion exchange membrane (AEM), and bipolar membrane (BPM) as different types of ion exchange membranes.

Electrodialysis with bipolar membrane (EDBM) is discussed as a process that can substitute thermal processes in non-thermal ZLD processes.

Application of electro-membrane technologies

in zero liquid discharge technology

J. Havelka,.T. Jiricek, H. Farova

T. Dornik, J. Kroupa

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MEGA a.s. Czech Republic

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MEGA a.s. Czech Republic

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Ion Exchange membrane

Principal of separation
 different charge of ion and membrane

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Type of in Exchange membrane
 cationexchange membrane (CEM)
 anion exchange membrane (AEM)
 bipolar membrane (BPM)
All can be use in ZLD process
Ion Exchange membrane

Principal of separation
 different charge of ion and membrane

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Type of in Exchange membrane
 cationexchange membrane (CEM)
 anion exchange membrane (AEM)
 bipolar membrane (BPM)
All can be use in ZLD process
Ion Exchange membrane

Principal of separation
 different charge of ion and membrane

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Type of in Exchange membrane
 cationexchange membrane (CEM)
 anion exchange membrane (AEM)
 bipolar membrane (BPM)
All can be use in ZLD process
Ion Exchange membrane

Principal of separation
 different charge of ion and membrane

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Type of in Exchange membrane
 cationexchange membrane
 anion exchange membrane
 bipolar membrane
All can be use in ZLD process
Ion Exchange membrane

Principal of separation
 different charge of ion and membrane

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Type of in Exchange membrane
 cationexchange membrane
 anion exchange membrane
 bipolar membrane
All can be use in ZLD process
Electro dialysis with monopolar membrane

 use mainly with thermal ZLD processes


 allows to importantly increase the concentration of ions

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Electro dialysis with monopolar membrane

 use with thermal ZLD processes


 allows to importantly increase the concentration of ions

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Electro dialysis with monopolar membrane

 use with thermal ZLD processes


 allows to importantly increase the concentration of ions

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Electro dialysis with bipolar membrane

 use in non-thermal ZLD processes


 allow to recovery acid and base from corresponding salt
(inorganic and organic salts)

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Zero liquide discharge

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ZLD application industries
Sea water desalination Pulp and paper
Power plant Food and feed industry
Textile industry Landfill leachate
Steel and metal industry Groundwater remedation
Mining industry Etc.

By Saltworks Technologies -, CC BY-SA 4. https://commons.wikimedia.org/w/index.php?curid=64115897


Case study of chosen India project

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Comparison of both membrane processes

HERO+DTRO EDR process


Recovery 86% 94%
Brine flow 10 m3/h 4m3/h
Energy
473 kW.h 560 kW.h

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consumption
∆ RO-EDR = 87 kW.h
SiO2 increase concentration not effect
HERO – low tolerance
COD EDR – similar to DTRO
DTRO – similar to EDR
Max TDS 79 000 mg/l 160 000 mg/l
Comparison of both MVR after membrane processes

MVR after HER+DTRO MVR after


EDR process
Feed 10 m3/h 4m3/h
Energy 455kW.h 168 kW.h

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consumption
∆ MVR(EDR) - MVR(RO) = 287 kW.h
OPEX Comparison

 EDR+MVR save 20% of OPEX compare to RO+MVR

(counted for price 0.5 RMB / kWh)

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CAPEX Comparison

 EDR+MVR save about 20% of CAPEX compare to RO+MVR


(counted for Chinese market prices of MVR, DTRO, HERO)

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RALEX EDR stacks for industrial applications

ED/EDR-II ED/EDR-III ED/EDR-IF

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Non-Water TDS < 3000 mg/l TDS > 3000 mg/l
Both low or high TDS app. Main focus
recovery of high value liquids
RALEX EDR stacks for industrial applications

EDR-IF/250 Advantages:
• Zero leakages
• No burning

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• Lower CAPEX for systems
• Lower OPEX
• Reduction of maintenance
• Reduction of system Lay-out
• New application potential
• Human safety
Electro dialysis with bipolar membrane

 use in non-thermal ZLD processes


 allow to recovery acid and base from corresponding salt
(inorganic and organic salts)

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GEAM Case study

EDBM-IF/300

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EDBM integration

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Operation costs

 for full scale: 5.13 t/h 4.0% Na2SO4 desalinated to 1.2%


(143 kg of Na2SO4 per hour)

 electric energy 0.064 €/kWh

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 no feed costs, no water costs, no waste costs

 the same frequency of spare parts changes as on existing EDR on


the same feed Operation costs Operation
[€/year] costs [%]
Electric energy 203 510 88
Water (RO permeate) 0 0
 88% electrical energy Chemicals 62 0
Spare parts 27 326 12
 12% spare parts Wastes 0 0
Total operation costs 230 836 100
Operation costs

 chemical prices: 210 €/t 50% NaOH, 55 €/t 94% H2SO4

 price of produced chemicals 317,034 €/year

 minus direct operation costs 230,836 €/year

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 gives operating profit 86,198 €/year

 Preliminary result: EDBM economically feasible only by reduction


of NaOH and H2SO4 purchase!
Conclution

 EDR is applicable in ZLD processes as concentrator before


thermal processes

 EDR can substitute HERO, DTRO or it can supplement them

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(water composition)

 EDBM can substitute the thermal processes in ZLD

 prices of MVR, HERO or DTRO strongly depend on the country


of origin, even with lowcost price on Chines market, ED is still
the most price efficient
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THANK YOU

FOR YOUR ATTENTION

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