THE DECOMPOSITION OF POSIDONIA SHALE AND GREEN RIVER SHALE KEROGENS USING MICROSCALE SEALED VESSEL (MSSV) PYROLYSIS

被引:45
作者
HORSFIELD, B
DUEPPENBECKER, SJ
机构
[1] Institute for Petroleum and Organic Geochemistry, Jülich Research Centre (KFA), D-5170 Jülich
关键词
GAS CHROMATOGRAPHY; KEROGEN; MICROSCALE SEALED VESSEL PYROLYSIS; PYROLYSIS; SHALE;
D O I
10.1016/0165-2370(91)80066-H
中图分类号
O65 [分析化学];
学科分类号
070302 ; 081704 ;
摘要
Microscale sealed vessel (MSSV) pyrolysis was used to simulate the compositional evolution of products generated from Posidonia Shale and Green River Shale kerogens with increasing maturity. Conversion was measured using a pseudo-Rock-Eval approach. Temperatures in the range 300-350-degrees-C and heating times between 1 and 10 days resulted in a 10-90% conversion of Posidonia Shale kerogen and 3-60% conversion of Green River Shale kerogen into volatile products. Single step GC analysis (C1-C30 range) revealed the presence of aliphatic hydrocarbons, aromatic hydrocarbons, sulphur-containing compounds and a complex mixture of unresolved components. The Posidonia Shale kerogen was inferred to have generated mainly heavy bitumen for all low temperature (300-degrees-C) experiments and for higher temperature experiments of short duration. At higher temperatures and longer heating times this material, possibly derived from alkyl-substituted naphthenoaromatic units in the kerogen, decomposed to yield products, detectable by gas chromatography, with an enhanced "gas to oil" ratio. Bitumen generated from Green River Shale appears to have a lower average molecular weight and/or polarity. Normal alkanes with a fixed chain length distribution were generated from what appears to be biopolymeric structures in both kerogen types.
引用
收藏
页码:107 / 123
页数:17
相关论文
共 51 条
[1]  
ANDERS DE, 1984, RAMG, P513
[2]   CHEMICAL MODELING OF THE STRUCTURE OF KEROGENS AND ASPHALTENES AS A FUNCTION OF THEIR ORIGIN AND EVOLUTION STAGE [J].
BEHAR, F ;
VANDENBROUCKE, M .
REVUE DE L INSTITUT FRANCAIS DU PETROLE, 1986, 41 (02) :173-188
[3]   OIL-SHALE PYROLYSIS - KINETICS AND MECHANISM OF OIL PRODUCTION [J].
BRAUN, RL ;
ROTHMAN, AJ .
FUEL, 1975, 54 (02) :129-131
[4]  
Burlingame A.L., 1969, ADV ORG GEOCHEM, P85
[5]  
BURNHAM AK, 1983, ACS SYM SER, V230, P335
[6]   ON THE MECHANISM OF KEROGEN PYROLYSIS [J].
BURNHAM, AK ;
HAPPE, JA .
FUEL, 1984, 63 (10) :1353-1356
[7]   FURTHER COMPARISON OF METHODS FOR MEASURING KEROGEN PYROLYSIS RATES AND FITTING KINETIC-PARAMETERS [J].
BURNHAM, AK ;
BRAUN, RL ;
SAMOUN, AM .
ORGANIC GEOCHEMISTRY, 1988, 13 (4-6) :839-845
[8]   KINETICS OF OIL GENERATION FROM COLORADO OIL-SHALE [J].
CAMPBELL, JH ;
KOSKINAS, GH ;
STOUT, ND .
FUEL, 1978, 57 (06) :372-376
[9]  
CLEMENTZ DM, 1979, AAPG BULL, V63, P2227
[10]  
CORNFORD C, 1983, PETROLEUM GEOCHEMIST, P175