EMISSION TREATMENT PROCESS FROM NATURAL GAS DEHYDRATORS
The off-gas from the still and flash tank of an existing glycol-based dehydration unit (containing water vapor, methane, BTEX (benzene, toluene, ethylbenzene, xylene), VOCs (volatile organic compounds)) is sent directly to a gas separation membrane system for dehydration. The gas separation membrane has a high selectivity for water over organic compounds (for example, the membrane described in WO2005/007277A1). The driving force for water permeation is established by applying a vacuum on the permeate side of the membrane unit or by flowing a sweep gas, for example warm, dry air through the permeate side of the unit.
1 . A process comprising the steps of,
collecting a gas containing water vapor and one or more of BTEX, VOCs or methane from a natural gas dehydrator; and,
extracting water vapor from the gas through a vapor separation membrane to produce a dehydrated gas still containing one or more of BTEX, VOCs or methane.
2 . The process of claim 1 , further comprising returning the dehydrated gas to a product natural gas stream.
3 . The process of claim 2 further comprising compressing the dehydrated gas before returning the dehydrated gas to the product natural gas stream.
4 . The process of claim 1 wherein the dehydrated gas is recycled to the natural gas dehydrator.
5 . The process of claim 4 wherein the dehydrated gas is mixed with wet product natural gas before the wet product natural gas is compressed upstream of the natural gas dehydrator.
6 . The process of claim 1 wherein the water vapor is extracted from the gas through a vapour separation membrane.
7 . An apparatus comprising,
a) a natural gas dehydration unit having a wet gas inlet, a product dry gas outlet, and a second gas outlet; and,
b) a vapor separation membrane unit having a feed inlet, a retentate outlet, and a permeate outlet,
wherein the second gas outlet of the dehydration unit is connected to the feed inlet of the membrane unit.
8 . The apparatus of claim 7 wherein the retentate outlet of the membrane unit is connected in communication with a pipe carrying product natural gas.
9 . The apparatus of claim 8 wherein the retentate outlet is connected to a pipe carrying product natural gas upstream of the natural gas dehydration unit.
10 . The apparatus of claim 9 wherein the retentate outlet is connected to a pipe carrying product natural gas upstream of a compressor feeding into the natural gas dehydration unit.
11 . The apparatus of claim 7 further comprising a compressor in communication with the retentate upstream of where the retentate is connected to the pipe carrying product natural gas.