H. Rassamdana et al., Asphalt flocculation and deposition. V. Phase behavior in miscible and immiscible injections, ENERG FUEL, 13(1), 1999, pp. 176-187
Asphalt formation and precipitation under primary oil recovery conditions a
s well as secondary recovery by immiscible gas injection were studied. The
crude oils were from a carbonate and highly fractured reservoir. No asphalt
precipitated under these conditions. Since the oil reservoir had experienc
ed significant formation damage and plugging of its well's tubing due to as
phalt formation and precipitation, the absence of asphalt precipitation in
our experiments points to the important influence on asphalt formation of f
low of the oil, the streaming potentials arising from the flow, and their i
nteraction with the electrical properties of the asphalt aggregates. Also i
nvestigated was asphalt precipitation when an enriched gas was injected int
o the oil under dynamic (multiple contact) miscibility conditions. Only tra
ce amounts of asphalt precipitated when the dilution ratio R was high enoug
h. However, significant asphalt precipitation occurred in completely miscib
le injections. For this case, we report extensive new experimental data for
the amount of the precipitated asphalt formed with various precipitation a
gents over wide ranges of pressure, temperature, and crude oil composition.
Increasing the pressure decreases the amount of asphalt precipitation. How
ever, depending on the crude oil, two opposite trends in the amount of the
precipitated asphalt were observed when the temperature of the system was r
aised. A scaling equation of state is shown to provide accurate predictions
for the data. The scaling equation also yields a novel analytical equation
for R-c, the critical dilution ratio (measured in cm(3) of the diluent or
the precipitation agent per gram of crude oil) at the onset of the precipit
ation given by R-c = c(MT)(1/4), where M is the (average) molecular weight
of the precipitation agent, T is the temperature in degrees C, and c is a c
onstant on the order of 10(-2). The predictions of this equation are in exc
ellent agreement with the experimental data. Thus, this equation may be use
d in the design of gas injection operations for enhanced oil recovery, such
that precipitation of the asphalt aggregates in the reservoir can be preve
nted.