Endre søk
RefereraExporteraLink to record
Permanent link

Direct link
Referera
Referensformat
  • apa
  • ieee
  • modern-language-association-8th-edition
  • vancouver
  • Annet format
Fler format
Språk
  • de-DE
  • en-GB
  • en-US
  • fi-FI
  • nn-NO
  • nn-NB
  • sv-SE
  • Annet språk
Fler språk
Utmatningsformat
  • html
  • text
  • asciidoc
  • rtf
Applying Membrane Distillation in High-Purity Water Production for Semiconductor Industry
KTH, Skolan för industriell teknik och management (ITM), Energiteknik, Kraft- och värmeteknologi.
KTH, Skolan för industriell teknik och management (ITM), Energiteknik, Kraft- och värmeteknologi.ORCID-id: 0000-0002-3661-7016
2006 (engelsk)Inngår i: Ultrapure Water: the definitive journal of high-purity water, ISSN 0747-8291, Vol. AprilArtikkel i tidsskrift (Fagfellevurdert) Published
Abstract [en]

While modern ultrapure water (UPW) systems are relatively well developed for semiconductor manufacturing, there is still room for improvement with regards to enhanced reliability, reduced environmental impact, and cost reductions. Membrane distillation (MD) is one promising alternative for high-purity water production that has several advantages compared to reverse osmosis (RO) and other technologies. In short, MD is a thermally driven process utilizing a hydrophobic membrane to produce high-purity water from a contaminated feedstock. Previous studies have shown that MD produces water with equal or superior quality to RO; in addition MD is relatively insensitive to process variations (e.g. pH, TDS levels, etc.), thus opening up the possibility of recycling rinse water. Low-temperature heat sources (i.e. under 100 °C) may be employed, thus allowing MD to be readily integrated into existing processes or even on-site cogeneration.

 

This paper explores the viability of MD for high-purity water production in a typical semiconductor chip fabrication plant. A brief literature review is included along with water quality analysis reports on typical MD product water. System simulations are employed to highlight possible scenarios with cogeneration. Results show that the specific energy consumption in the case study is around 440 kWh/m3 (thermal) and 0.9 kWh/m3 (electrical).  The specific capital cost is around $1.2-1.5/ m3 for the MD facility. These findings provide a strong impetus towards demonstration trials and other follow-on research and development activities.

sted, utgiver, år, opplag, sider
2006. Vol. April
HSV kategori
Identifikatorer
URN: urn:nbn:se:kth:diva-74347OAI: oai:DiVA.org:kth-74347DiVA, id: diva2:489427
Merknad
QC 20120529Tilgjengelig fra: 2012-02-02 Laget: 2012-02-02 Sist oppdatert: 2022-06-24bibliografisk kontrollert

Open Access i DiVA

Fulltekst mangler i DiVA

Person

Martin, Andrew

Søk i DiVA

Av forfatter/redaktør
Liu, ChuanfengMartin, Andrew
Av organisasjonen

Søk utenfor DiVA

GoogleGoogle Scholar

urn-nbn

Altmetric

urn-nbn
Totalt: 798 treff
RefereraExporteraLink to record
Permanent link

Direct link
Referera
Referensformat
  • apa
  • ieee
  • modern-language-association-8th-edition
  • vancouver
  • Annet format
Fler format
Språk
  • de-DE
  • en-GB
  • en-US
  • fi-FI
  • nn-NO
  • nn-NB
  • sv-SE
  • Annet språk
Fler språk
Utmatningsformat
  • html
  • text
  • asciidoc
  • rtf