gas improvements and multiple condensation stages achieves certain symbiotic benefits in combination the improvements to the injection side and the collection side of the well may be used independently of one another this third condenser stage in particular is applicable to industries outside of the petroleum industry for example the general gas industry the chemical industry and others cooling coils are typically used in the first two condenser stages the invention is not limited in this regard however in that other known devices such as coolant filled u2018 thumbs u2019 may alternatively be used all of the products recovered by condensers one and two are liquid products at stp in the oil industry heavy medium and light crudes are separated by api numbers which are indicative of density heavy crude is collected from condenser 1 whereas light and medium crudes are collected by condenser 2 the light crude comes out with water which is delivered to an oil water separator known in the art the heavy crude is preferably pumped back into a reflux chamber in the bottom half of condenser 1 to continue to crack the heavy crude and recover a higher percentage of sweet and light crude products this also creates more gas products in condenser 3 as flow rate is an important consideration in condensation a distinction should be made between cfm cubic feet per minute and acfm or actual cfm which takes temperature into account at 600 u00b0 f the temperature of the processing gas entering the well could have a flow rate of approximately 500 acfm exiting the well the temperature will be near 600 u00b0 f but the flow rate could reach as high as 1000 acfm depending on product content once the liquid products are removed and the gases get cooled down.