separated from the processed fluid fig1 and 13 depict an embodiment adapted to process a larger quantity of fluid and separating three fluids from the processed fluid specifically a gas and two liquids having different specific gravities more specifically gaseous hydrocarbons oil and water as depicted in fig1 a main inlet line 270 supplies the fluid being processed to a pair of inlet valves 272 as noted above inlet valves 272 may be controlled to manage the fluid levels in the collection chamber 256 based upon output from conventional sensors in the collection chamber 256 check valves 274 are adjacent to the inlet valves 272 the system depicted has a pair of optional agitation chambers 218 as described above each agitation chamber 218 supplies fluid to two separation chambers 236 as previously described each separation chamber 236 is connected to the collection chamber 256 by collection chamber inlet piping 252 in the embodiment described for a flow rate of 250 gpm it is contemplated that the separation inlet piping 234 has a diameter of 8 inches the separation chambers 236 have a 60 inch inside diameter the base of the first baffle 242 is 2 feet 1 and 13 16th inches from the bottom of the separation chambers 236 the base of the second baffle 244 is one foot 3 13 16 inches from the base of the first baffle 242 the apex of the third baffle 248 is one foot 7 5 16 inches from the base of the second baffle 244 each baffle 242 244 248 tapers approximately 1 5 to 2 degrees from horizontal as it progresses from base to apex the separation chambers 236 are eight feet 5 inches tall the base of the collection chamber 256.