I2P
Chemical
- Jan 20, 2003
- 38
We have a tri ethylene glycol dehydration contactors and regeneration units for the same. I have read some literature from US Env. Protection agency regarding the methane losses in glycol operated dehydration towers. Since we are also in the processes of optimisation of dehydration operations, I would like to know how to exactly quantify the cubic ft of methane absorbed per gallon of glycol circulated.While it is true that low temperature favours water absorption, it also leads to hydrocarbon absorption and thus the need to work out the inlet gas temperature which would give the desired dew point depression and minimise the methane loss. Presently we are operating at an inlet temp of 45 to 47 deg c, with an inlet water content of 90 lb/mmscf and outlet content spec of 7 lb/mmscf. Tower pr. is 65 bar.Our design temp range for gas inlet temp is upto 55 deg C. How much of methane absorption would I be preventing if I raise the inlet temp to 55 deg C?
thanks in advance
thanks in advance