Bu çalışmada kompleksleştirme yöntemiyle eşmolar
oranda Ti-V-Fe ve Ti-V-Cr katalizörleri sentezlenmiş ve H2S’ün
seçici oksidasyon reaksiyonuyla elementel kükürt eldesindeki aktiviteleri
incelenmiştir. Katalizörlerin katalitik aktiviteleri dolgulu kolon reaktör
sisteminde farklı sıcaklık (200°C, 250°C, 300°C) ve stokiyometrik gaz (O2/H2S:0,5)
bileşiminde incelenmiştir. Katalizörlerin yapısal özellikleri N2
adsorpsiyon-desorpsiyon, XRD, TPR, SEM-EDS analizleri ile belirlenmiştir.
Sentezlenen katalizörlerin mezogözenekli yapıya sahip olduğu tespit edilmiştir.
Ti-V-Cr katalizörünün kristal yapısı TiO2’in rutile fazı ve Cr2O3
bileşiklerinden oluşurken, Ti-V-Fe katalizörü kompleks bir kristal yapı
sergilemiştir. Bu katalizörün yapısında Fe2TiO5, V2O5,
FeV2O4, rutile TiO2 ve Fe2O3
bileşikleri görülmüştür. Sentezlenen her iki katalizörle de 250°C reaksiyon
sıcaklığında % 100 H2S dönüşümü elde edilmiştir. Reaksiyon
sıcaklığındaki artış ve azalış katalizörlerde elde edilen H2S
dönüşümünde azalmaya sebep olmuştur. Bunun yanı sıra çalışılan tüm şartlarda
her iki katalizörle de oldukça yüksek (≥% 97) elementel kükürt seçiciliği elde
edilmiştir. Özellikle 200°C sıcaklıkta,
yapısında kompleks bileşikleri içeren Ti-V-Fe katalizörü ile (% 73 H2S
dönüşümü) Ti-V-Cr katalizörüne kıyasla (% 51 H2S dönüşümü) daha
yüksek dönüşüm elde edilmiştir.
In this study, Ti-V-Fe and Ti-V-Cr catalysts
were synthesized by complexation method and their activities were investigated
for H2S selective oxidation reaction to elemental sulfur. Structural
properties of the catalysts were determined by N2
adsorption-desorption, XRD, TPR, SEM-EDS analyzes. According to the analysis
results, it has been found that the synthesized catalysts have a mesoporous
structure. Ti-V-Fe catalyst exhibits a complex crystal structure, while the
crystal structure of the Ti-V-Cr catalyst is comprised of the rutile phase of
TiO2 and Cr2O3 compounds. In this catalyst
structure, Fe2TiO5, V2O5, FeV2O4,
rutile TiO2 and Fe2O3 compounds were observed.
The catalytic activities of the catalysts were investigated in a packed column
reactor system at different temperatures (200°C, 250°C, 300°C) and
stoichiometric gas composition (O2/H2S:0.5). 100% H2S
conversion was obtained at 250°C reaction temperature with both catalysts
synthesized. The increase and decrease in the reaction temperature led to a
decrease in the conversion of H2S obtained with the catalysts due to
the increase in sulfur deposition in the catalyst structure. In addition, under
all conditions studied, elemental sulfur selectivity was high (≥ 97%) with both
catalysts. Espe,cially at 200°C, a higher conversion was obtained with Ti-V-Fe (73%
H2S conversion) catalyst which has complex compounds in the
structure compared to Ti-V-Cr catalyst (51% H2S conversion).
Primary Language | Turkish |
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Subjects | Engineering |
Journal Section | Research Articles |
Authors | |
Publication Date | August 31, 2018 |
Submission Date | November 28, 2017 |
Acceptance Date | June 25, 2018 |
Published in Issue | Year 2018 Volume: 23 Issue: 2 |
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