TMAH Recovery Process from the Waste Water In Taiwan , three - - PowerPoint PPT Presentation

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TMAH Recovery Process from the Waste Water In Taiwan , three - - PowerPoint PPT Presentation

TMAH Recovery Process from the Waste Water In Taiwan , three operators died due to TMAH TMAH TMAH is is Fatal to Human Highly Bio-toxicity + in waste Main Source of NH 4 T etr etra M eth yl A mmon ium H ydr ethyl mmonium droxide xide CH 3


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SLIDE 1

TMAH Recovery Process from the Waste Water

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SLIDE 2

due to TMAH In Taiwan, three operators died

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SLIDE 3

TMAH TMAH is

is

Main Source of NH4

+ in waste

Highly Bio-toxicity Fatal to Human

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SLIDE 4

Tetr

etraMeth ethyl ylAmmon mmonium ium Hydr droxide xide

N+ CH3 CH3 CH3 CH3 OH-

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SLIDE 5

Because we need them

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SLIDE 6

50,000 100,000 150,000 200,000 250,000 2012 2013 2014 2015 2016 2017 2018

25%TMAH demand, m3 Year

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SLIDE 7

EX

Faci cili lity ty Inve vestment= stment= 100M 0M Running nning Cost= st=6M 6M ROI=0.7y 0.7year ear

100 100 CMD 0.5 % 3000 3000 CMD 30 30 ppm ppm 167 167 ppm ppm 5.56 138.9 NT/m3 152 152 MNTD/year Unit price charge CH=

H=

Total charge= Pd/P /Psd

sd=

TMAH Waste= TMAH= Volume of total Waste= Criterion Psd

sd=

Average Pd=

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SLIDE 8

4(CH3)4N + + 8H2O → 12CH4 + 4CO2 + 4NH4

+

NH4

+ + 2O2 → NO3

  • + 2H+ + H2O

NO3

  • → NO2
  • → NO → N2O → N2
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SLIDE 9

 Large Space Required?

2,000m2 enough?

 Cost?

Hundreds of Millions Resource gone?

 Long lead time for decomposition

more then 10 hours?

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SLIDE 10

新 信

2007 R&D 2008 Leading Product (IDB) 2009 Permit for waste reuse(trial) 2010 Commercial Run

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SLIDE 11

500 1,000 1,500 2,000 2,500 3,000

10 20 30

TMAHConc.,ppm Raiton of Flow Quantity vs Resin Bed Volume

Efficiency of TMAH removal

TMAH

創新 誠信 簡樸

Remove TMAH from waste by Resin

TMA+ TMA+

Cation Exchange Resin

H H H H H H H H TMA TMA

Cation Exchange Resin

H+ H+ H H H H H H

TMA+OH- + H+-Resin →TMA+-Resin + H2O

HX TMAX

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SLIDE 12

創新 誠信 簡樸

Recover to 25%TMAH by ElectroDialysis

+

  • TM

TMAX TM TMAX TM TMA+ X- HX HX TM TMAH OH OH- 2H 2H2O+2e O+2e- ↓ 2OH 2OH-+H +H2 H2O ↓ 2e 2e-+1/2O2+2H +2H+ H+

TMAX →TMA+ + X + X-

Anolyte :

TMA TMA +

+ +OH

+OH- →TMAH TMAH

Catholyte :

H +

+ +X

+X- →HX HX

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SLIDE 13

Lithography TMAH Waste Resin Tower Purification Electrolysis

25% TMAH

Effluent TMAH<10ppm Cond.<20μS/cm Water Recovery All metal<2ppb Customer Site SanFu Site

1. 1.Cus

ustom tomer er Orien rienta tation tion

1.Space Saving 2.Cost Saving 3.Resource Recycling

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SLIDE 14

2.

  • 2. All

ll Rec ecycla lable ble

TMAH HX TMAH Waste HX

TMAH Recycling System

Low Contamination

(EL Grade) (EL Grade)

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SLIDE 15

3.

  • 3. Qua

uali lity ty Relia eliabl bly

※ Commercial TMAH Manufacturing Process

1.High 1.High Yield Yield 2.High 2.High Qua Quali lity ty

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SLIDE 16

 Large Space Required?

2,000m2 enough?

 Cost?

Hundreds of Millions Resource gone?

 Long lead time for decomposition

more then 10 hours?

 Small Space Req

hundreds SQM

 Low Initial Cost

simple & easy

 Instant TMAH removal

stable & reliable

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SLIDE 17
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SLIDE 18

For More Information

  • Pls contact Chih-Ming Huang

San Fu ext. (06) 583-7608 ext. 750 Cell phone 0972-245-779

  • r E-mail: cmhuang@sfchem.com.tw