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Hydrodesulfurization equipment | |
Stats | Specification parameter |
Processing capacity | Generally hundreds of thousands of tons/year to millions of tons/year, such as 1.2 million tons/year, 2 million tons/year, etc |
Reaction temperature | 300ºC-400ºC |
Reaction pressure | 3MPa-10MPa |
Hydrogen purity | It is usually required to be above 99% |
Catalyst type | Molybdenum sulfide, cobalt sulfide - molybdenum sulfide, etc |
Desulfurization efficiency | The sulfur content in diesel can be reduced to less than 10ppm |
Adsorption desulfurization equipment | |
Processing capacity | From a few tons per day on a smaller scale to tens of tons per day on a larger scale, such as 5-600 tons per day |
Type of adsorbent | Activated carbon, molecular sieve, etc |
Operating temperature | Room temperature -100 ºC |
Operating pressure | Atmospheric pressure -0.5MPa |
Adsorption capacity | According to the different types and quality of adsorbents, there are generally corresponding saturated adsorption capacity indicators |
Desulfurization efficiency | Generally, the sulfur content can be reduced to a certain extent, such as about 50ppm-200ppm, depending on the raw material sulfur content and equipment design |
Oxidative desulfurization equipment | |
Stats | Specification parameters |
Processing capacity | Can be designed according to actual needs, such as 0.5 tons/hour - 5 tons/hour, etc |
Oxidant type | Hydrogen peroxide, organic peroxide, etc |
Catalyst type | Select suitable catalysts for different oxidants and reaction systems, such as titanium silicon molecular sieve |
Reaction temperature | 30ºC-80ºC |
Reaction time | According to the specific process and processing capacity, generally in 1 hour - several hours |
Extractant type | Used to separate oxidized sulfur compounds, such as furfural, N-methylpyrrolidone, etc |
Desulfurization efficiency | The sulfur content of diesel oil can be reduced to less than 100ppm, and some processes can reach less than 50ppm |