scholarly journals Titanium-Modified MIL-101(Cr) Derived Titanium-Chromium-Oxide as Highly Efficient Oxidative Desulfurization Catalyst

Catalysts ◽  
2020 ◽  
Vol 10 (9) ◽  
pp. 1091
Author(s):  
Xiaolin Li ◽  
Liang Zhang ◽  
Yinyong Sun
Keyword(s):  
Reaction Time ◽  
Surface Area ◽  
Chromium Oxide ◽  
Oxide Catalyst ◽  
Specific Activity ◽  
Oxidative Desulfurization ◽  
Titanium Content ◽  
Titania Content ◽  
Sulfur Containing ◽  
Sulfur Containing Compounds

A titanium-chromium-oxide catalyst was prepared by a facile calcination of titanium-modified MIL-101(Cr). The resulting material, possessing a surface area of 60 m2 g−1 and a titania content of 50.0 wt%, can be directly used as the catalyst for oxidative desulfurization (ODS) reaction of dibenzothiophene (DBT). This novel ODS catalyst can remove 900 ppm sulfur-containing compounds in a reaction time of 30 min at 60 °C. The experimental results showed that the specific activity increased with the titanium content. The specific activity of the catalyst with 50%Ti reached 129 μmol/m2, which was much higher than that of reported Ti-based catalysts.

Highly Ordered Mesoporous WO3 with Excellent Catalytic Performance and Reusability for Deep Oxidative Desulfurization

NANO ◽  
2015 ◽  
Vol 10 (05) ◽  
pp. 1550075 ◽  
Author(s):  
Zhenghua Li ◽  
Heon Jong Jeong ◽  
Kumarsrinivasan Sivaranjani ◽  
Byung Jin Song ◽  
Su Bin Park ◽  
...  
Keyword(s):  
Catalytic Activity ◽  
Surface Area ◽  
High Surface ◽  
High Surface Area ◽  
Oxidative Desulfurization ◽  
High Catalytic Activity ◽  
Ordered Mesoporous ◽  
Model Oil ◽  
Sulfur Containing ◽  
Sulfur Containing Compounds

Highly ordered mesoporous tungsten trioxide ( WO 3) with high surface area (75 m2/g) and well-defined mesopores were successfully prepared through a hard templating method using a mesoporous silica KIT-6 as a template and ( NH 4)6 H 2 W 12 O 40 ⋅ x H 2 O as a tungsten precursor. Oxidative desulfurization of a model oil with H 2 O 2 as the oxidant was carried out at 50°C under atmospheric pressure in order to analyze the catalytic activity. The desulfurization reactions were optimized by various kinds of reaction parameters such as H 2 O 2/ S molar ratio, reaction temperatures and series of sulfur-containing compounds [dibenzothiophene (DBT), benzothiophene (BT) and 4,6-dimethyl dibenzothiophene (4,6-DMBT)]. Excellent catalytic activity for the removal of the sulfur-containing compounds from the model oil was observed with mesoporous WO 3 catalyst, where the activity was maintained during 5 recycle tests without any regeneration process. The high catalytic activity and durability is mainly attributed to well-defined mesopores and high surface area of mesoporous WO 3 catalyst.

Phosphotungstic Acid/Semi-Coke Catalysts for Oxidative Desulfurization of Diesel Fuel

2009 ◽  
Vol 79-82 ◽  
pp. 1683-1686 ◽  
Author(s):  
Liang Wang ◽  
Chun Hu Li ◽  
Ying Fei Hou
Keyword(s):  
Hydrogen Peroxide ◽  
Phosphotungstic Acid ◽  
Oxidative Desulfurization ◽  
Diesel Oil ◽  
Oxidizing Agent ◽  
X Ray Diffraction ◽  
X Ray ◽  
Sulfur Containing ◽  
Sulfur Containing Compounds ◽  
Scanning Electron

This work presents the results obtained in the development of phosphotungstic acid/semi-coke catalysts in the oxidative desulfurization (ODS) process of diesel oil using hydrogen peroxide as the oxidizing agent. Phosphotungstic acid /semi-coke (60wt%) prepared by impregnation. These catalysts were characterized by X-ray diffraction (XRD) and scanning electron microscope (SEM), The effect of the amount of catalyst used , on the efficiency of desulfurization was investigated. In addtion. the diesel after oxidation and extraction was analyzed by GC-FPD for sulfur content. The chromatograph shows that virtually all the sulfur containing compounds in diesel were removed.

scholarly journals OXIDATIVE DESULFURIZATION OF PETROLEUM PRODUCTS

2021 ◽  
Vol 297 (3) ◽  
pp. 199-203
Author(s):  
VIRA RUDENKO ◽  
VITALY CHUMAK ◽  
VALERIY YEFIMENKO ◽  
OLENA KOSENKO ◽  
ОLENA SPAS’KA ◽  
...  
Keyword(s):  
Hydrogen Peroxide ◽  
Activated Carbon ◽  
Sulfur Content ◽  
Oxidative Desulfurization ◽  
Petroleum Products ◽  
Advantages And Disadvantages ◽  
Petroleum Fractions ◽  
Sulfur Containing ◽  
Sulfur Containing Compounds

The modern world market makes stringent requirements for the quality of motor fuels, in particular for sulfur content in them. The main classes of sulfur-containing compounds in petroleum fractions are thiols, dialkyl and cycloalkyl sulfides, alkylaryl sulfides, as well as heteroaromatic compounds – benzothiophene, dibenzothiophene and their alkyl derivatives. They have a negative impact on the quality of petroleum products. Growing demands on the quality of oil and petroleum products have led to the search for ways to reduce the sulfur content in oils and which would not lead to deterioration of physicochemical parameters of oil, such as viscosity, density, acidity, elemental and fractional composition, etc. Among the existing methods of desulfurization of oils and their fractions, special attention is drawn to oxidation methods that allow organic sulfur compounds to be converted into sulfoxides and sulfones which are easily removed by conventional separation methods, in particular by extraction or adsorption. The prospects of the oxidation method are due to the possibility of practical use of sulfoxides and sulfones in various sectors of the economy. The most common oxidants in the processes of oxidative desulfurization of petroleum fractions are hydrogen peroxide and alkylhydroperoxides in combination with catalysts that provide high selectivity and speed of the process. Transition metal compounds (Mo, V, W,) are most often used as catalysts because they are able to form peroxocomplexes in the presence of peroxides. Heterogeneous catalytic systems consisting of various solid carriers (salts, oxides, activated carbon, zeolites) and peroxide oxidants (hydrogen peroxide or alkyl hydroperoxides) are actively developing. Molybdenum-containing catalysts are one of the most efficient heterogeneous systems for oxidative desulfurization of diesel fuel. There is proved the effectiveness of oxidative desulfurization, which is a combination of catalytic oxidation of sulfur-containing compounds in the presence of a heterogeneous catalyst and adsorption on activated carbon. Methods of oxidative desulfurization with their advantages and disadvantages can be logical addition to large-tonnage hydrotreating processes, and also potentially can be used as an independent method of deep purification of oil and petroleum products from sulfur-containing compounds.

HYDROGENOLYSIS OF CARBOHYDRATES: IV. 1,2-O-ISOPROPYLIDENE-D-GLUCOFURANOSE

1958 ◽  
Vol 36 (4) ◽  
pp. 661-666 ◽  
Author(s):  
P. A. J. Gorin ◽  
A. S. Perlin
Keyword(s):  
Chromium Oxide ◽  
Oxide Catalyst ◽  
Specific Activity ◽  
Starting Material ◽  
Reaction Conditions ◽  
Copper Chromium ◽  
Total Specific Activity

1,2-O-isopropylidene-D-glucofuranose was treated with hydrogen at 180 °C. and 2900 p.s.i. using copper chromium oxide catalyst and dioxane as solvent. The major isolated products were a hexanediol (2.4%), a mixture of hexanetriols (6.5%), a hexanetetrol (4.3%), and an isopropylidene-aldohexose (4.2%) which differed from the starting material. The latter product yielded L-idose on hydrolysis, showing clearly that isomerization of carbon 5 of monoacetone-D-glucose occurs under the reaction conditions used.The diol and the major components of the triol mixture were found to possess a 1,2-glycol group which was derived mainly from the 5,6-glycol group of the original monoacetone-D-glucose. Thus, hydrogenolysis of 1,2-O-isopropylidene-D-glucofuranose-l-C14 afforded the 1,2-hexanediol and mixed triols containing only about 30% of the total specific activity in carbon 1. The tetrol was shown to be 1,2,5,6-hexanetetrol. The results suggest that the carbon–oxygen bonds at carbons 5 and 6 of isopropylidene-D-glucose are least prone to hydrogenolysis and that those at carbons 3 and 4 are most readily cleaved.

scholarly journals Nanocatalysts for Oxidative Desulfurization of Liquid Fuel: Modern Solutions and the Perspectives of Application in Hybrid Chemical-Biocatalytic Processes

Catalysts ◽  
2021 ◽  
Vol 11 (9) ◽  
pp. 1131
Author(s):  
Olga Maslova ◽  
Olga Senko ◽  
Argam Akopyan ◽  
Sergey Lysenko ◽  
Alexander Anisimov ◽  
...  
Keyword(s):  
Liquid Fuel ◽  
Oxidative Desulfurization ◽  
Liquid Fuels ◽  
Bacterial Cells ◽  
Advantages And Disadvantages ◽  
4S Pathway ◽  
Oil Fractions ◽  
Hybrid Technologies ◽  
Sulfur Containing ◽  
Sulfur Containing Compounds

In this paper, the current advantages and disadvantages of using metal-containing nanocatalysts (NCs) for deep chemical oxidative desulfurization (ODS) of liquid fuels are reviewed. A similar analysis is performed for the oxidative biodesulfurization of oil along the 4S-pathway, catalyzed by various aerobic bacterial cells of microorganisms. The preferences of using NCs for the oxidation of organic sulfur-containing compounds in various oil fractions seem obvious. The text discusses the development of new chemical and biocatalytic approaches to ODS, including the use of both heterogeneous NCs and anaerobic microbial biocatalysts that catalyze the reduction of chemically oxidized sulfur-containing compounds in the framework of methanogenesis. The addition of anaerobic biocatalytic stages to the ODS of liquid fuel based on NCs leads to the emergence of hybrid technologies that improve both the environmental characteristics and the economic efficiency of the overall process. The bioconversion of sulfur-containing extracts from fuels with accompanying hydrocarbon residues into biogas containing valuable components for the implementation of C-1 green chemistry processes, such as CH4, CO2, or H2, looks attractive for the implementation of such a hybrid process.

A Review on the Methods in Diesel Desulfurization

2020 ◽  
Vol 16 ◽  
Author(s):  
Muhammad Shahid Nazir ◽  
Sadaf Ahmad ◽  
Zaman Tahir ◽  
Sadaf ul Hassan ◽  
Zulfiqar Ali ◽  
...  
Keyword(s):  
Ionic Liquid ◽  
Review Paper ◽  
Oxidative Desulfurization ◽  
Diesel Oil ◽  
Adsorptive Desulfurization ◽  
Oil Refineries ◽  
Adsorption Desulfurization ◽  
Sulfur Containing ◽  
Economical Process ◽  
Sulfur Containing Compounds

BACKGROUND: Diesel mainly consists of paraffin and thio-aromatic compounds. Sulfur present in diesel exhaust is the major challenge for oil refineries. Sulfur is an oxidizing element that discharges as acute pollutant in the environment which has adverse effects on human and on animal life. INTRODUCTION: The scope of this review paper is to discuss and to highlight the recent advancements in process of desulfurization of diesel oil to explore the less energy intensive and more economical process. METHOD: Recently, different techniques are widely used for desulfurization of diesel oil to remove sulfur containing compounds from diesel. These techniques mainly involve hydrodesulfurzation, oxidative desulfurization, biodesulfurization, ionic liquid desulfurization, and adsorption desulfurization. CONCLUSION: Adsorptive desulfurization technique is green, less energy incentive, and more economical technique than hydro-desulfurization, oxidative desulfurization, ionic liquid desulfurization and bio desulfurization. Optimization of adsorptive desulfurization technique may yield up to 100% desulfurization of diesel oil.

scholarly journals ZnO-Activated Carbon Blended as a Catalyst for Oxidative Desulfurization of Dibenzothiophene

2021 ◽  
Vol 16 (4) ◽  
pp. 881-887
Author(s):  
Wega Trisunaryanti ◽  
Maria Ulfa ◽  
Yatim Lailun Nikmah ◽  
Satriyo Dibyo Sumbogo ◽  
Safa Annissa Novianti ◽  
...  
Keyword(s):  
Activated Carbon ◽  
Reaction Time ◽  
Surface Area ◽  
Simple Procedure ◽  
Oxidative Desulfurization ◽  
Xrd Analysis ◽  
X Ray Diffraction ◽  
X Ray ◽  
Desulfurization Process ◽  
Physical Blending

The problem of sulfur content in heavy oil is a challenge for researchers to meet the needs of environmentally friendly fuels. The catalyst preparation plays an important role in the desulfurization process. The synthesis of ZnO-activated carbon as a catalyst and its activity in oxidative desulfurization (ODS) reaction has been successfully carried out. In this work, the ZnO and activated carbon (AC) were blended by a solid-solid reaction. The ZnO, AC, and ZnO-AC were then characterized using acidity test with pyridine vapor adsorption, Fourier Transform Infra-Red (FTIR), X-ray Diffraction (XRD), Scanning Electron Microscope-Energy Dispersive X-Ray (SEM-EDX), and Surface Area Analyzer (SAA). ODS of dibenzothiophene (DBT) reaction was performed by using H2O2 under variation of the reaction time (30, 60, 120, and 150 min) for the ZnO-AC catalyst. The efficiency of ODS-DBT was analyzed by a UV-Visible spectrophotometer. The XRD analysis result showed that ZnO-AC blended displays new crystal peaks of Zn in the AC diffractogram. The surface area (734.351 m2/g) and acidity (4.8780 mmol/g) of ZnO-AC were higher than ZnO and AC themselves. ZnO-AC produced the highest efficiency of ODS-DBT which was 93.83% in the reaction time of 120 min. Therefore, the simple procedure of this physical blending was proved effective to homogenize between ZnO and AC into ZnO-AC so that it has good physicochemical properties as an ODS-DBT catalyst. Copyright © 2021 by Authors, Published by BCREC Group. This is an open access article under the CC BY-SA License (https://creativecommons.org/licenses/by-sa/4.0). 

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