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A small volume of condensate is completely soaked up, and char crumbs are formed.
The production data have shown that the concentration of H2S is not clearly related to the gas volume of condensate reservoirs in O1y reservoirs, but correlated to the volume of formation water and the content of condensates.
Water usage and volume of condensate were significantly different between devices, but delivered airway temperatures were not.
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Since we approximate the gas phase by a single component, it is equivalent to the chemical potential of the gas phase, which is defined as the partial specific Gibbs free energy (A.5) The chemical potential of the condensates, which the suffix c denotes, is written as (A.6) where it is assumed that the volume of condensates are negligible in the last line of the right-hand side.
The volume of the condensate dropped out from the gas phase is determined by the in situ pressure in the reservoir matrix pores.
For a given production rate, the higher number of wells drilled, the lower per well pressure drop will result so that the volume of recovered condensate until reaching an ultimate pressure will increase.
It is assumed that the volume of the condensates is negligible.
A certain volume of non-condensate gas injected along with steam can effectively decrease heat loss from steam chamber to top-layer.
Application of steam flushing after air flushing produced a significant increase in contaminant removal rate for the first 4 to 5 pore volumes of steam condensate.
The passage of a steam volume corresponding to 11 pore volumes of steam condensate reduced the total VOC concentration in the soil gas (at 20°C) by a factor of 20 to 0.07 mg/l.
The volume of the primary condensate should be considered even higher because the condensate is dispersed to the high surface of the bags and has to be harvested.
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