Apparatus and method for reducing catalyst poisoning in an andrussow process
A catalyst, hydrogen cyanide technology, applied in chemical instruments and methods, separation methods, preparation/purification/separation of hydrogen cyanide, etc., can solve the problems of reducing HCN catalyst life, increasing downtime, increasing by-product preparation, etc.
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Embodiment 1
[0044] Example 1 - Comparing the Andrussow method
[0045] This example demonstrates that the Andrussow process using a desulfurization unit can reduce the sulfur content in the feed stream.
[0046] In the Andrussow process, the sulfuric acid (H 2 S) was removed by first heating the natural gas to 100° C. with a shell and tube exchanger using steam. The shell and tube exchanger is designed to heat natural gas from 25°C to 100°C with a flow of 3,100 lb / hr of steam to the shell. The system was optimized to remove H at 100 °C 2 S.
[0047] Two vessels in series contain zinc oxide (ZnO) desulfurization pellets. ZnO loading on the inclined screen. The catalyst has a density of 65 lbs / ft3. At 100°C, the catalyst will absorb 5% by weight of sulfur before being exhausted. Average H at 2.0ppm 2 S feed concentration, expected catalyst lifetime of 3 years. However, substantially longer lifetimes are expected because of the H in methane from natural gas plant (NGP) units 2 S co...
Embodiment 2
[0048] Example 2 - Comparative Andrussow process with varying oxygen feed concentration
[0049] This example demonstrates that the Andrussow process using an enriched source of oxygen generally reduces HCN catalyst lifetime.
[0050] Hydrogen cyanide is produced via various Andrussow processes. One process, the air Andrussow process, uses air containing 21% oxygen by volume as the oxygen-containing gas. The second process, the air-enriched Andrussow process, employs an oxygen-containing gas having greater than about 21 vol% oxygen and less than about 100 vol% oxygen. A third process, the oxygen Andrussow process, employs an oxygen-containing gas of about 100 volume percent oxygen. Platinum-containing catalysts were used for all processes. A 4 inch inner diameter stainless steel reactor with a ceramic insulating liner inside was used for the pilot test. Forty sheets of 90wt%Pt / 10wt%Rh 40 mesh gauze from Johnson Matthey (USA) were loaded as catalyst beds. A perforated alum...
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