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Predicting the Temperature of
Hydrocarbon Expulsion from
Oil
Asphaltene Kinetics and
Oil
Source
Correlation
:
A
Case
Study of South Cambay
Basin
, India*
By
Shishir Kant Saxena1, R.K.Saxena1, Rashmi Anand1, K.P.Singh1, Harvir Singh1, and R.R Singh1
Search and Discovery Article #40266 (2007)
Posted November 28, 2007
*Adapted from extended abstract prepared for presentation at AAPG Annual Convention, Long Beach, California, April 1-4, 2007
Editor’s note: Please refer to “Petroleum
Systems of the Mumbai Offshore
Basin
, India, by Goswami et al. (Search and
Discovery Article #10154 (2007).
1Geochemistry
Labs, KDM Institute of petroleum Exploration,
Oil
and Gas Corporation Ltd 9
Kaulagarh Road, Dehradun-248195, India ([email protected])
The
oil
asphaltene has structural similarity with
parent kerogen. The kinetic data based on actual data from the reservoir
oil
is
found to be a better method in reducing the risks associated with
oil
exploration and assessing the petroleum generation characteristics. An attempt
has been made to assess the petroleum expulsion temperature/timing for
predicting the kitchen in South Cambay
Basin
using
oil
asphaltene kinetics.
The Gandhar field covers an area of about 800 km2
and is located on the rising northwestern flank of the Broach depression in the
Jambusar-Broach block. The Olpad Formation was deposited during the Paleocene.
The Eocene Cambay Shale, unconformably overlying the Olpad Formation, has
excellent source rock characteristics. The Hazad Member of south Cambay
Basin
is
a major hydrocarbon reservoir, and it consists of 12-individual sand units from
GS-XII-GS-I.
The
oil
asphaltene kinetic/expulsion temperature studies have been carried out
on Rock Eval-6 instrument having Optikin and GENEX-1D software. The
saturate/aromatic biomarkers data and fatty acid studies are also integrated
with the present study. The Gandhar oils are placed into three groups. The group
C oils (GS-XII & GS-XI) indicate that the temperature of expulsion from
asphaltene kinetics (Tasph 90-112oC) corresponds to isothermal
sequence of source rock from 2500 to 800m). Group B (GS- IX-IV) oils indicate
that Tasph (119-132oC) corresponds to isothermal sequence of 2900 to
3200m, whereas Group A oils (GS-III-I) indicate that expulsion temperature
(141-142oC) corresponds to the 3600-3800m sedimentary sequence.
Asphaltene expulsion temperature data has shown positive
correlation
with
biomarker maturity data and fatty acid distribution pattern and good matching
with actual identified source rock units. The expulsion temperature determined
by light hydrocarbons has no
correlation
with asphaltene expulsion temperature.
This study will be very useful in fine-tuning the existing petroleum system
where source rock data is not available.
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The timing of hydrocarbon expulsion, as well
as the quantity and quality of expelled hydrocarbons, is controlled by
the type of sedimentary organic matter, lithology of source rock,
tectonic stress, and burial history, as well as the related temperature
and pressure. Asphaltene represents the macromolecular fraction of
reservoir
Di Primo and Horsfield (2000) applied kinetic
concept to
In the present paper, we focused on expulsion
temperature ranges derived from asphaltene kinetics and lighter
hydrocarbons. Fatty acids distribution pattern and routine biomarkers
are also included to under stand the effect of maturity on these
parameters. The study area, Gandhar field, is located in the rising
northwestern flank of the Broach depression in the Jambusar-Broach
block. The generalized stratigraphy of the southern part of Cambay
Sample Selection and Study Area
The
Source Rock Development Status
The effective source rock for commercial
viable hydrocarbons in south Cambay
The kinetic analysis was performed on about 3
mg of isolated asphaltene mixed with inert substance to make up 100 mg
sample on Rock Eval-6 at four different heating rates of 5, 10, 15 and
25oC from 180 to 650oC, using Optkin software. The
light hydrocarbons were analyzed on a whole
Ctemp (oC) = 140+ 15{ln (2.4-DMP/2.3-DMP)}
For fatty acid isolation, 20g of crude
Results and Discussion The bottom hole temperature (BHT) recorded in studied wells varies between 110oC and 120oC. The API gravity of studied oils was in the range of 38-43o. The n-alkane profile indicates that these oils are normal oils, and there is no sign of biodegradation.
The objective of the study was to determine
temperature of expulsion of hydrocarbons based on lighter and heavier
ends. The asphaltene kinetic parameters with minimum error function
(0.06-0.10) were considered for the study. The lighter hydrocarbons were
analyzed with the help of 2.3-DMP and 2.4- DMP standards. The results of
asphaltene kinetics evaluation in terms of activation energy
distribution and prediction of asphaltene transformation
ratio/temperature for the oils reservoired from GS-I to GS-XII sands are
shown in Figure 3. The activation energy
distribution observed is typical for In order to compare the effects of the calculated kinetics on the asphaltene degradation behavior, the geological extrapolations were made using a constant heating rate of 3oK per My. The fractions of reacted asphaltene were normalized to 100 and are plotted as a function of geological temperature using a constant heating rate. The wide variation in the asphaltene degradation behaviour indicates the difference of organic matter richness and their types. The asphaltene degradation of GS-I, GS-II, GSXI and GS-XII are smooth, indicating homogenous distribution of organic matter while GS-VIII shows wide range of temperature variation. The expulsion temperatures defined by these curves correspond to the temperatures at which the asphaltene starts to be transformed to volatile hydrocarbons. In order to avoid the possible impact of contamination (volatile entrants in asphaltene), the asphaltene temperatures were determined at a value of 10% of asphaltene transformation. Based on biomarker, fatty acid, and asphaltene temperature ranges, Gandhar oils can be classified into three distinct groups . The asphaltene expulsion temperature of the studied oils from GS-I to GS-III is in the range of 141 to 142oC under geological conditions and can be classified as Group A (Table 1; Figure 4). Further GS-IV and GS-IX show asphaltene expulsion temperature of 119 to 132oC; these oils can be classified as Group B, indicating contribution from mixed source input and variability in organic facies at different maturity levels. The asphaltene temperatures are in the range of 90 to 112oC for GS-XI and GS-XII and can be classified as Group C. Comparison of temperatures calculated from asphaltene kinetics and those calculated from light hydrocarbons (Table 1) shows variation; namely in Group A oils, Ctemp<Tasph (124oC vs. 142oC), while Group B oils show both Ctemp<Tasph and Ctemp>Tasph and Group C oils show Ctemp>Tasph. From the integration of light hydrocarbons, classical biomarkers ratios, and fatty acid distribution pattern it may be inferred that there were multiple source rocks and charging of the Hazad reservoirs. The hydrocarbons from deep source rock are getting mixed with low-maturity oils coming from shallower source rocks. The biomarkers data demonstrate that most of the biomarker maturity parameters have reached their equilibrium value so they may not show any trend with temperature variation data of Tasph.
Generation Model Predicted Based on Asphaltene Kinetics
The hydrocarbon generation model based on
expulsion temperatures of asphaltene kinetics and light hydrocarbon is
shown in Figure 5. The subsidence and
maturity history of source rock unit responsible for charging GS-1 to
GS-3 are at the temperature of 142oC with average Ctemp at
124oC. The calculated temperature of sediments indicates that
this temperature corresponds to the older Cambay Shale (OCS). Further,
it is observed that the GS-V sands (Tasph 152oC) have
received hydrocarbons from a deeper source. Based on
Behar, F., and Pelet, R., 1985, Characterization of asphaltene by pyrolysis and chromatography: Journal of Analytical and Applied Pyrolysis, v. 7, p. 121-135. Di.Primo, R., and Horsfield, B., 2000, Determining the temperature of petroleum formation from the kinetic properties from petroleum asphaltene: Nature, v. 406, p.173-176.
Dieckmann, V., Caccialanza, P.G.,
and Galimberti, R., 2001, Evaluating the timing of Eglinton, T.I., Larter, S.R., and Boon, J.J., 1991, Characterization of kerogens, coals, and asphaltenes by quantitative pyrolysis-mass spectrometry: Journal of Analytical and Applied Pyrolysis, v. 20, p. 25-45. Horsfield, B.,1989, Practical criteria for classifying kerogen. Some observations from pyrolysis gas chromatography: Geochimica et Cosmachimica Acta, v. 53, p. 891-901. Horsfield, B., 1997, The bulk composition of first-formed petroleum in source rocks: Springer Verlag, Heidelberg, Federal Republic of Germany, 335-402p. Kawamura, Kimitaka, and Kaplan, I.R., 1987, Dicarboxylic acids generated by thermal alteration of kerogen and humic acids: Geochemica et Cosmochimica Acta, v. 51, p. 3201-3207. Mango, F.D., 1987, An invariance in the isoheptanes of petroleum: Science, v. 237, p. 514-517. Schaefer, R.G., Schenk, H.J., Hardelauf, H., and Harms, R., 1990, Determination of gross kinetic parameters for petroleum formation from Jurassic source rocks of different maturity levels by means of laboratory experiments, in A. Durand and F. Behar, eds., Advances in organic geochemistry 1989: Organic Geochemistry, v. 16, p. 115-120. Surdan, R.C., and Stanley, K.O., 1984, Diagenesis and maturation of hydrocarbons in the Monterey formation, Pismo Syncline, California: SEPM Guidebook 2, p. 84-94. |
