Jobst
Chemical
- Mar 5, 2008
- 32
I have a gas stream as follows:
CO: 22%
H2: 19%
CO2: 56%
N2: 3%
H2S: 500 ppm
The stream is water saturated, 37 C, 4 barg. Flow is approx 380 Nm3/hr.
I want to reduce the sulfur to below 10 ppm. Recovery of the sulfur is not required.
I've spoken to one vendor of iron oxide based adsorbant, and apparently the performence of this technology in a reducing environment is unknown. I assume this can be extended to the more traditional iron sponge tech as well.
From what I understand ZnO based tech requires higher temperatures.
Does anone have any insight as to who to get in touch with next? The big players tend to laugh off this kind of scale...
CO: 22%
H2: 19%
CO2: 56%
N2: 3%
H2S: 500 ppm
The stream is water saturated, 37 C, 4 barg. Flow is approx 380 Nm3/hr.
I want to reduce the sulfur to below 10 ppm. Recovery of the sulfur is not required.
I've spoken to one vendor of iron oxide based adsorbant, and apparently the performence of this technology in a reducing environment is unknown. I assume this can be extended to the more traditional iron sponge tech as well.
From what I understand ZnO based tech requires higher temperatures.
Does anone have any insight as to who to get in touch with next? The big players tend to laugh off this kind of scale...