Geri Dön

Gas phase reaction kinetics of boron fiber production

Bor fiber üretimi gaz faz reaksiyon kinetiği

  1. Tez No: 153590
  2. Yazar: FATİH FIRAT
  3. Danışmanlar: PROF. DR. ÖNDER ÖZBELGE, DOÇ. DR. NAİME ASLI SEZGİ
  4. Tez Türü: Yüksek Lisans
  5. Konular: Kimya Mühendisliği, Chemical Engineering
  6. Anahtar Kelimeler: CVD, Boron Fiber Production, Gas Phase Reaction Kinetics, Dicloroborane. iv, CVD, Boron Fiber Production, Gas Phase Reaction Kinetics, Dicloroborane. iv
  7. Yıl: 2004
  8. Dil: İngilizce
  9. Üniversite: Orta Doğu Teknik Üniversitesi
  10. Enstitü: Fen Bilimleri Enstitüsü
  11. Ana Bilim Dalı: Kimya Mühendisliği Ana Bilim Dalı
  12. Bilim Dalı: Belirtilmemiş.
  13. Sayfa Sayısı: Belirtilmemiş.

Özet

ABSTRACT GAS PHASE REACTION KINETICS OF BORON FİBER PRODUCTION Fırat, Fatih M.S., Department of Chemical Engineering Supervisor: Prof. Dr. H. Önder Özbelge Co-supervisor: Assoc. Prof. Dr. Naime Aslı Sezgi June 2004,92 pages in the production of boron fibers using CVD technique, boron deposition and dichloroborane formation reactions take place in a reactor. Boron deposition reaction occurs at the surface while formation of dichloroborane is the result of both gas phase and surface reactions. A CSTR type of reactor was designed and constructed from stainless steel to investigate the gas phase reaction kinetics and kinetic parameters of boron fibers produced from the reaction of boron trichloride and hydrogen gases in a CVD reactor. The gases were heated by passing through the two pipes which were located into the ceramic fiırnace and they were mixed in the CSTR. The effluent gas mixture of the reactor was quenched by passing through a heat exchanger. An FT-IR spectrophotometer was connected to the heat exchanger outlet strearo to perfonn on- iiiline chemical analysis of the effluent gas mixture. Experiments were carried out at atmospheric pressure and a reactor temperature range of 300-600 °C with different inlet reactant concentrations. The analysis of the FT-IR spectra indicated that the gas phase reaction and the surface reaction started at reactor temperatures above 170 °C and 500°C, respectively. it was concluded that reaction rate of the product increased with an increase in the inlet concentration of both reactants (BClj and Ha) and with an increase in the reactor temperature. The gas phase reaction rate was expressed in terms of a * and b * orders with respect to tiıe inlet concentrations of BCb and Ha. The activation energy of the gas phase reaction, a and b were found to be 30.156kJ/mol, 0.54 and 0.64, respectively. The correlation coefficient was 0.9969.

Özet (Çeviri)

ABSTRACT GAS PHASE REACTION KINETICS OF BORON FİBER PRODUCTION Fırat, Fatih M.S., Department of Chemical Engineering Supervisor: Prof. Dr. H. Önder Özbelge Co-supervisor: Assoc. Prof. Dr. Naime Aslı Sezgi June 2004,92 pages in the production of boron fibers using CVD technique, boron deposition and dichloroborane formation reactions take place in a reactor. Boron deposition reaction occurs at the surface while formation of dichloroborane is the result of both gas phase and surface reactions. A CSTR type of reactor was designed and constructed from stainless steel to investigate the gas phase reaction kinetics and kinetic parameters of boron fibers produced from the reaction of boron trichloride and hydrogen gases in a CVD reactor. The gases were heated by passing through the two pipes which were located into the ceramic fiırnace and they were mixed in the CSTR. The effluent gas mixture of the reactor was quenched by passing through a heat exchanger. An FT-IR spectrophotometer was connected to the heat exchanger outlet strearo to perfonn on- iiiline chemical analysis of the effluent gas mixture. Experiments were carried out at atmospheric pressure and a reactor temperature range of 300-600 °C with different inlet reactant concentrations. The analysis of the FT-IR spectra indicated that the gas phase reaction and the surface reaction started at reactor temperatures above 170 °C and 500°C, respectively. it was concluded that reaction rate of the product increased with an increase in the inlet concentration of both reactants (BClj and Ha) and with an increase in the reactor temperature. The gas phase reaction rate was expressed in terms of a * and b * orders with respect to tiıe inlet concentrations of BCb and Ha. The activation energy of the gas phase reaction, a and b were found to be 30.156kJ/mol, 0.54 and 0.64, respectively. The correlation coefficient was 0.9969.

Benzer Tezler

  1. Kinetics of boron fiber production

    Bor elyafı üretim kinetiği

    NAİME ASLI SEZGİ

    Doktora

    İngilizce

    İngilizce

    1996

    Kimya MühendisliğiOrta Doğu Teknik Üniversitesi

    Kimya Mühendisliği Ana Bilim Dalı

    PROF. DR. TİMUR DOĞU

  2. Ergimiş boraks banyosunda çeliklere vanadyum karbür kaplama

    Vc coating of steels in molten borax bath

    SEYED MOHAMMED MOUSAVİ KHOEE

    Doktora

    Türkçe

    Türkçe

    1992

    Metalurji Mühendisliğiİstanbul Teknik Üniversitesi

    PROF. DR. EMEL GEÇKİNLİ

  3. Partikül yüklü, eş eksenli iki jet için karışma ve yanma modeli

    A Mixing and combustion model for particle-laden confined coaxiol jets

    METİN ERGENEMAN

    Doktora

    Türkçe

    Türkçe

    1985

    Uçak Mühendisliğiİstanbul Teknik Üniversitesi

    PROF. DR. HİKMET BİNARK

  4. Beta zeoliti ile MTBE sentezi

    MTBE synthesis on beta zeolite

    BEGÜM TOKAY

    Yüksek Lisans

    Türkçe

    Türkçe

    2001

    Kimya Mühendisliğiİstanbul Teknik Üniversitesi

    PROF.DR. AYŞE ERDEM ŞENATALAR

  5. Antimon sülfürün oksidlenme kinetiğinin incelenmesi

    Başlık çevirisi yok

    GÜLİZ OMAY

    Doktora

    Türkçe

    Türkçe

    1996

    Kimya Mühendisliğiİstanbul Üniversitesi

    Kimya Mühendisliği Ana Bilim Dalı

    PROF. DR. İBRAHİM YUSUFOĞLU