RI 6530 Cost Estimates of Processes for Separating Mixtures of Methane and Hydrogen

- Organization:
- The National Institute for Occupational Safety and Health (NIOSH)
- Pages:
- 51
- File Size:
- 1635 KB
- Publication Date:
- Jan 1, 1964
Abstract
Capital and operating costs have been estimated for separating methane
and hydrogen in gas - separating plants designed to produce 90 million scf per
day of product gas containing a minimum of 90 percent methane .
After a preliminary
literature review of various separation techniques , three different
processes --moving - bed adsorption using active carbon , oil absorption , and
liquefaction -- were chosen for the cost estimates . Three different methane
feed gas concentrations , 5 , 20 , and 50 percent ( cases 1 , 2 , and 3 , respectively
) , were chosen as representative methane concentrations for the separation
estimates . Capital and operating costs were lowest for the moving - bed
adsorption process in all three cases investigated . Operating costs declined
from $ 0.24 to $ 0.06 per 1,000 cu ft of product gas , and capital costs declined
from $47,490,800 to $7,411,200 as the percentage of methane in the feed gas
increased from 5 to 50 percent .
Citation
APA:
(1964) RI 6530 Cost Estimates of Processes for Separating Mixtures of Methane and HydrogenMLA: RI 6530 Cost Estimates of Processes for Separating Mixtures of Methane and Hydrogen. The National Institute for Occupational Safety and Health (NIOSH), 1964.