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Environmental Care, New & Renewable Energy
GreenWorks

GreenWorks makes use of its new and renewable energy technology for the future of mankind

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PLANT

homenextBusiness FieldsnextPLANT

- An Compound with all hydrogens replaced by fluorine on a carbon chain(CF4, C2F6 etc.) (from WIKIPEDIA)
- Including Semiconductor & LCD processing (Etching & CVD) gases (SF6, NF3)
- Very stable, Less harmful on body, Long detention period(SF6 : 3,200 years)
- Big influence on Global Warming
Application Processes Gases

Semiconductor &
LCD Panel processes

Etching

Vapor Etching

HCl, HF, HBr, SF6, Cl2

Plasma Etching

SiF4, CF4, C3F8, C2F6, CHF3, CClF3, O2

Ion Beam Etching

C3F8, CHF3, CClF3, CF4

Cleaning

NF3, CF4, C2F6, C3F8, SF6

CVD (Epitaxy)

SiH4, SiH2Cl2, SiHCl3, SiCl4, GeH4, B2H6, BBr3, BCl3,
AsH3, PH3, TeH2, SnCl4, GeCl4, WF6. NH3, CH4, Cl2, MoF6
(Carrier Gas : High Purified H2, N2)

Photo-voltaic processes

Etching

NF3, CF4, C2F6, C3F8, SF6

- Gas volume : 10~80 CMM (vary from processes and separations of exhaust gases)
- Temperature : 30~40℃
- Concentration of PFCs : 1,000~1,500 ppmV (LCD process)
- SiF4 + 2H2O → 4 HF + SiO2 (fine dust smaller than 5μm)
- High SiO2 in CVD
- SiO2 makes low destruction efficiency and increase maintenance costs
- Design Key Factor : SiO2 Dust, Mist removing with high efficiency
※ Key Points to PFCs abatement system for Semiconductor & LCD gases
1) Minimize air volume by adequate separation of emission gas
2) Competitive initial costs
3) High efficiency in Pre-treatment system(stable against SiO2, Dust, Mist)
4) Maximize PFCs removal efficiency
5) Minimize operation and maintenance cost
1) High efficiency in PFCs breaking (more than 95%)
2) Low energy cost by using regenerative thermal system and catalyst
   (90% less energy costs than Direct Thermal System)
Category RCS(Regenerative Catalytic System) DTS(Direct Thermal System)
Composition

Process → Pre-treatment → Inlet Valve → RCS
→ Outlet Valve → Post-treatment → Fan → ATM

Process → Pre-treatment → Heat Exchanger →
Combustion Chamber → Waste Heat Boiler →
Heat Exchanger → Quencher → Post-treatment
→ Fan → ATM

Temp.

700~800��

1,200~1,300��

Efficiency

~ 96%

~ 65%

LNG consume

1 Nm3/hr

10 Nm3/hr

Differential
pressure

about 200mmAq

about 300mmAq

Fluctuation of
Static pressure

±20mmAq

±20mmAq

Destruction Effi.

90% ↑

90% ↑

Particle effect

Heat sink material and catalyst
get influenced when particle (SiO2) enters

Heat-exchanger and WHB get
influenced when Particle (SiO2) enters

Initial cost

Less 45% than DTS

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*Note : basis 10NCMM