Classifications

• • G—PHYSICS
  • G01—MEASURING; TESTING
  • G01N—INVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
  • G01N33/00—Investigating or analysing materials by specific methods not covered by groups G01N1/00 - G01N31/00
  • G01N33/24—Earth materials
  • G01N33/241—Earth materials for hydrocarbon content
• • G—PHYSICS
  • G01—MEASURING; TESTING
  • G01N—INVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
  • G01N1/00—Sampling; Preparing specimens for investigation
  • G01N1/28—Preparing specimens for investigation including physical details of (bio-)chemical methods covered elsewhere, e.g. G01N33/50, C12Q
  • G01N1/286—Preparing specimens for investigation including physical details of (bio-)chemical methods covered elsewhere, e.g. G01N33/50, C12Q involving mechanical work, e.g. chopping, disintegrating, compacting, homogenising
• • G—PHYSICS
  • G01—MEASURING; TESTING
  • G01N—INVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
  • G01N1/00—Sampling; Preparing specimens for investigation
  • G01N1/28—Preparing specimens for investigation including physical details of (bio-)chemical methods covered elsewhere, e.g. G01N33/50, C12Q
  • G01N1/40—Concentrating samples
  • G01N1/4022—Concentrating samples by thermal techniques; Phase changes
• • G—PHYSICS
  • G01—MEASURING; TESTING
  • G01N—INVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
  • G01N31/00—Investigating or analysing non-biological materials by the use of the chemical methods specified in the subgroup; Apparatus specially adapted for such methods
  • G01N31/12—Investigating or analysing non-biological materials by the use of the chemical methods specified in the subgroup; Apparatus specially adapted for such methods using combustion
• • G—PHYSICS
  • G01—MEASURING; TESTING
  • G01N—INVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
  • G01N1/00—Sampling; Preparing specimens for investigation
  • G01N1/28—Preparing specimens for investigation including physical details of (bio-)chemical methods covered elsewhere, e.g. G01N33/50, C12Q
  • G01N1/40—Concentrating samples
  • G01N1/4022—Concentrating samples by thermal techniques; Phase changes
  • G01N2001/4033—Concentrating samples by thermal techniques; Phase changes sample concentrated on a cold spot, e.g. condensation or distillation

Definitions

• This specification relates to analyzing rock in which hydrocarbon is generated and trapped.
• Hydrocarbon exploration techniques sometimes involve generating computer-generated geological models and calibrating such models using experimental data.
• the experimental data can be provided as inputs to the geological models.
• the experimental data can be obtained from laboratory experiments performed on hydrocarbon source rock, that is, rock in which hydrocarbons are generated.
• the accuracy of the predictions of computer-generated models can depend on the quality of the calibration of the models using measured experimental data, which, in turn, can depend on the conditions under which the laboratory experiments are performed.
• the quality of the experimental data can be high if the conditions under which the laboratory experiments are performed are substantially similar to the conditions experienced by the rock in the subsurface from which the hydrocarbons are produced.
• One input to the geological model can include a characteristic of the hydrocarbon rock to expel trapped hydrocarbons. Pyrolysis is one technique to study the characteristic of hydrocarbon source rock to expel or trap hydrocarbons.
• This specification describes pyrolysis techniques to analyze the characteristics of a hydrocarbon source rock to expel/retain trapped hydrocarbons.
• this specification describes pyrolysis to determine hydrocarbon expulsion efficiency of hydrocarbon source rock.
• An example implementation of the subject matter described within this disclosure is a method with the following features.
• An open system pyrolysis of a first hydrocarbon source rock sample obtained from a natural system is performed within a pyrolysis chamber resulting in a pyrolyzed sample.
• the open system pyrolysis is performed by maintaining the pyrolysis chamber at a substantially constant temperature of 375 °C.
• the first hydrocarbon source rock sample includes hydrocarbon source rocks having an equivalent spherical diameter of substantially at least one centimeter.
• Hydrocarbons are recovered from the pyrolysis chamber released by the first hydrocarbon source rock sample in response to the open system pyrolysis.
• a thermo-vaporization is performed within the pyrolysis chamber on the pyrolyzed sample on which the open system pyrolysis was performed at a substantially constant temperature of 375 °C.
• Hydrocarbons released by the pyrolyzed sample in response to the thermo-vaporization are recovered from the pyrolysis chamber.
• a first hydrocarbon expulsion efficiency of hydrocarbon source rock in the natural system is determined based on the recovered hydrocarbons released by the first hydrocarbon source rock sample in response to the open system pyrolysis and based on the recovered hydrocarbons released by the pyrolyzed sample in response to thermo-vaporization.
• a second hydrocarbon rock sample of a predefined mass is ground resulting in a ground hydrocarbon source rock sample having a grain size less than or equal to or less than 250 micrometers.
• the grinding is performed within an integrated sample-crusher and thermo-vaporization chamber.
• a second pyrolysis is performed within the integrated sample-crusher and thermo-vaporization chamber on the ground hydrocarbon source rock sample.
• the second pyrolysis is performed by maintaining the integrated sample-crusher and thermo-vaporization chamber at a substantially constant temperature of 375°C within the integrated sample-crusher and thermo-vaporization chamber.
• a second hydrocarbon expulsion efficiency of the hydrocarbon source rock in the natural system is determined based on performing the second pyrolysis on the second hydrocarbon source rock sample. The first hydrocarbon expulsion efficiency is verified using the second hydrocarbon expulsion efficiency.
• the integrated sample-crusher and thermo-vaporization chamber include electric driven blades.
• the pyrolysis chamber is the sample-crusher and thermo-vaporization chamber.
• Verifying the first hydrocarbon expulsion efficiency includes comparing the first hydrocarbon expulsion efficiency to the second hydrocarbon expulsion efficiency and determining a ratio between the first hydrocarbon expulsion efficiency and the second hydrocarbon expulsion efficiency.
• Performing the open system pyrolysis of the first hydrocarbon source rock sample obtained from a natural system includes starting the open system pyrolysis once the pyrolysis chamber is at a temperature of substantially 375 °C. a constant temperature of substantially 375 °C is maintained throughout the open system pyrolysis. The open system pyrolysis is ended after a set amount of time. The temperature at the set amount of time is substantially 375 °C.
• a quantity of the second hydrocarbon source rock sample is substantially at least 100 grams.
• HCEE1 hydrocarbon expulsion efficiency
• HCEE1 (HCpyroly S i S )xlOO/(HCpyroly S i S +HC3 ⁇ 4ermo -Vaporization +HCCrashingThermo-Vaporization)
• HCpyroiysis is a quantity of hydrocarbons released in response to open system pyrolysis of the hydrocarbon source rock sample
• HCThermo-vaporization is a quantity of hydrocarbons released in response to first thermo-vaporization of previously pyrolyzed hydrocarbon source rock sample in the pyrolysis chamber
• HCcrashingThermo-vaporization is a quantity of hydrocarbons released in response to grinding and performing the second pyrolysis on the second hydrocarbon rock sample.
• HCEE2 (HCpyrolysis) X 100 / HCpowderedSamplePyrolysis
• HCpyrolysis is a quantity of hydrocarbons released in response to open system py- rolysis of the hydrocarbon source rock sample with a grain size of substantially one centimeter
• HCpowderedSamplePyrolysis is a quantity of hydrocarbons released in response to open system pyrolysis of a powdered hydrocarbon source rock sample with a grains size substantially less than or equal to substantially 250 microns.
• aspects of the example implementation which can be combined with eh example implementation alone or in combination, include the following.
• a maturity of residual organic matter is determined, the determined maturity is input into a computer- generated geological model.
• An example implementation of the subject matter described within this disclosure is a system with the following features.
• An integrated sample-crusher and thermo-vaporization chamber is capable of retaining a hydrocarbon rock sample.
• a heating element is capable of heating the integrated sample-crusher and thermo-vaporization chamber.
• a controller is capable of controlling the heating element to a set temperature.
• a sensor is capable of detecting hydrocarbons released within the integrated sample- crusher and thermo-vaporization chamber.
• Controlling the heating element to a set temperature includes heating the integrated sample-crusher and thermo-vaporization chamber to a temperature of substantially 375 °C. A constant temperature of substantially 375 °C is maintained within the integrated sample-crusher and thermo-vaporization chamber while the integrated sample-crusher and thermo-vaporization chamber is in use.
• the integrated sample-crusher and thermo-vaporization chamber includes electrically driven grinding blades.
• Aspects of the example system, which can be combines with the example system alone or in combination, include the following.
• the integrated sample-crusher and thermo-vaporization chamber is capable of containing a sample size of at least 100 grams.
• the integrated sample-crusher and thermo-vaporization chamber has a volume of at least 1 liter.
• An example implementation of the subject matter described within this disclosure is a second method with the following features.
• An open system pyrolysis is performed within a pyrolysis chamber on a hydrocarbon source rock sample that includes fragments having an equivalent spherical diameter of substantially at least one centimeter.
• Performing the open system pyrolysis results in a pyrolyzed rock sample.
• Hydrocarbons released by the rock sample in response to the open system pyrolysis are recovered.
• a first quantity of hydrocarbons released in response to the open system pyrolysis is determined.
• a thermo-vaporization is performed within the pyrolysis chamber on the pyrolyzed rock sample. Hydrocarbons released by the rock sample in the pyrolysis chamber in response to the thermo-vaporization are recovered.
• a second quantity of hydrocarbons released in response to thermo-vaporization in the pyrolysis chamber is determined.
• the sample are placed in a crushing chamber and crushing and performing thermo-vaporization on the pyrolyzed rock sample. Hydrocarbons released by the rock sample in response to crushing and thermo-vaporization are recovered.
• a third quantity of hydrocarbons released in response to crushing and thermo-vaporization in the crushing chamber is determined.
• a first hydrocarbon expulsion efficiency of the hydrocarbon source rock is determined as a ratio of a sum of the first quantity of hydrocarbons to a sum of the first quantity of hydrocarbons, the second quantity of hydrocarbons, and the third quantity of hydrocarbons.
• a powdered sample of the hydrocarbon source rock having a grain size less than or equal to substantially 250 microns is pyrolyzed.
• a fourth quantity of hydrocarbons released in response to performing open system pyrolysis on a powdered sample is determined.
• a second hydrocarbon expulsion efficiency of the hydrocarbon source rock is determined as a ratio of the first quantity of hydrocarbons to the fourth quantity of hydrocarbons.
• the hydrocarbon expulsion efficiency is provided as an input to a geological model capable of analyzing a hydrocarbon expulsion from the hydrocarbon source rock through geological history.
• FIG. 1 is a schematic diagram of an example of a system for a Crushing and Thermo-vaporization chamber which will be utilized following open system pyrolysis of hydrocarbon source rock to crush and to liberate any trapped hydrocarbons.
• FIG. 2 is a flowchart of an example of a process for determining a hydrocarbon expulsion efficiency of hydrocarbon source rock.
• FIG. 3 is a plot of an example of pyrolysis temperature intervals (steps).
• FIG. 4 is a plot of an example of a thermo-vaporization in a sample crushing chamber at a constant temperature.
• FIG. 5A is a plot of an example of maturity increase based on pyrolysis temperature steps.
• FIG. 5B is an example of hydrocarbon distributions recovered after pyrolysis and/or crushing-thermo-vaporization stage from a hydrocarbon source rock sample.
• FIG. 6 is a flowchart of another example of a process for determining a hydrocarbon expulsion efficiency of hydrocarbon source rock.
• Powdered hydrocarbon source rock sample does not hold its original texture and porosity so fluid flow barriers no longer exist in powder sample.
• the yields (generated HCs) are immediately removed from the system by carrier gas, whereas in the closed system pyrolysis, the yields remain in the system and are exposed to further heating (e.g., leading to secondary cracking).
• further heating e.g., leading to secondary cracking
• liquid hydrocarbons are retained and cracked to gas at higher experimental temperatures.
• hydrous pyrolysis heating of kerogen in presence of excess water
• this method also leads to secondary reactions and cracking of generated hydrocarbons within a pyrolysis chamber.
• thermo-vaporization of the hydrocarbon source rock sample at 300 °C following pyrolysis has been reported to be sufficient to sweep retained hydrocarbons from the hydrocarbon source rocks samples.
• This specification relates to determining hydrocarbon generation/retention/expulsion characteristics of hydrocarbons source rocks with emphasis on petroleum expulsion characteristics by use of open system pyrolysis and thermo-vaporization (at 375 °C) in a pyrolysis chamber followed by crushing and thermo-vaporization (at 375 °C) of hydrocarbon source rock sample in a crushing and thermo-vaporization chamber. Released hydrocarbons are first trapped and then analyzed by gas chromatography and/or gas chromatography mass spectrometry.
• This specification describes methods and systems associated with the exploration for petroleum.
• this specification describes pyrolysis methods and systems to determine expulsion efficiency of hydrocarbons generated from hydrocarbon source rock.
• the pyrolysis methods and systems described here can be implemented in a laboratory and, in some implementations, the results obtained can be provided as inputs to computer-generated geological models used to study hydrocarbon generation and expulsion from hydrocarbon source rocks.
• the expulsion of hydrocarbons from hydrocarbon source rock into reservoir rock, from which the hydrocarbon can be recovered, is affected by the release of generated hydrocarbons from kerogen and movement (that is, migration) of these hydrocarbons within the source rock.
• the release of liquid hydrocarbons from kerogen is controlled by the absorption or adsorption (or both) of the liquid hydrocarbons within or on the surface (or both) of the kerogen and diffusion of the hydrocarbons through kerogen.
• the efficiency of expulsion is controlled by the amount and oil-proneness (or hydrogen-richness) of kerogen.
• the migration of oil within the source rock is affected by factors including, for example, an amount and type of organic matter, bitumen (oil) saturation threshold, effective migration paths in the hydrocarbon rock, pressure build-up and micro- fracturing, gas availability for the movement of oil in the gaseous phase, combinations of them, or other factors.
• factors including, for example, an amount and type of organic matter, bitumen (oil) saturation threshold, effective migration paths in the hydrocarbon rock, pressure build-up and micro- fracturing, gas availability for the movement of oil in the gaseous phase, combinations of them, or other factors.
• Laboratory pyrolysis is used to artificially mature kerogen and study the processes of hydrocarbon generation within and expulsion from the source rock.
• Laboratory pyrolysis experiments can be conducted in closed or open systems, by isothermal or non-isothermal heating of finely ground (for example, in powder form) hydrocarbon source rock samples, for example, in hydrous or anhydrous tubes.
• Open system pyrolysis can be conducted using, for example, a few milligrams of ground rock having a size equal to or less than approximately 250 micrometers.
• the yields that is, the hydrocarbons expelled by pyrolysis
• Closed system pyrolysis for example, closed anhydrous systems
• closed system pyrolysis can be implemented in a micro-scale sealed vessel or implemented as gold-bag pyrolysis systems utilizing small amount of hydrocarbon source rock or isolated kerogen.
• the generated hydrocarbons can remain in the system and be exposed to further heating until the end of pyrolysis, for example, until secondary cracking occurs.
• Hydrous pyrolysis involves heating of kerogen in presence of excess water.
• Such pyrolysis is conducted in sealed reactors and leads to secondary reactions and cracking of generated hydrocarbons within the pyrolysis chamber.
• different types of pyrolysis can be implemented to artificially mature kerogen to study the processes of hydrocarbon generation and migration.
• Such artificial kerogen maturation while a useful tool, does not always accurately represent maturation of sedimentary organic matter in natural systems, that is, in the subsurface.
• This disclosure describes an artificial kerogen maturation (and hydrocarbon generation from it as well as migration of generated hydrocarbons) technique that better approximates natural maturation of kerogen relative to the artificial kerogen maturation techniques described earlier.
• the artificial kerogen maturation technique described here can be implemented as a restricted system pyrolysis.
• the pyrolysis system is restricted in that, to be expelled due to pyrolysis, the hydrocarbons in the hydrocarbon source rock need to overcome a physical barrier before the hydrocarbons can reach a space from which the expelled hydrocarbons can be swept away by carrier gas.
• the restricted pyrolysis technique described in this specification studies the ability of the hydrocarbons in the rock sample to traverse through a physical barrier that is similar to the physical barrier that hydrocarbon generated during natural maturation would experience in the subsurface (for example, subsurface hydrocarbon reservoirs).
• the techniques described here can be implemented to predict hydrocarbon accumulations or to predict hydrocarbons retained in hydrocarbon source rocks (or both).
• the techniques can also be implemented to determine an expulsion efficiency of hydrocarbons from hydrocarbon source rock samples, and to input such efficiency in computer-generated geological models, for example, models that can predict hydrocarbon accumulations.
• the expulsion efficiency obtained by implementing the techniques described here can increase a confidence in the computer-generated geographic models implemented in hydrocarbon exploration or recovery or both.
• the expulsion efficiency can be used to calibrate petroleum system and basin modeling simulation which can lead to better understanding and determination of expulsion of hydrocarbons from source rock.
• the calibrated systems and simulations can be implemented to successfully discover hydrocarbon reservoirs, to better predict retained hydrocarbons in such reservoirs, or to identify sweet spots in unconventional resource estimation (or combinations of them). The time and effort in performing such processes can thereby be reduced to increase efficiency.
• An open system pyrolysis apparatus is used for artificially maturing a hydrocarbon source rock sample, as well as separating and trapping hydrocarbon generated by maturation process.
• the hydrocarbon source rock sample can include fragments of the rock sample having an equivalent spherical diameter of substantially at least one centimeter (for example, ranging between 0.9 cm and several centimeters).
• the equivalent spherical diameter of the fragments of the rock sample is the diameter of a sphere having an equivalent volume as the rock sample.
• the hydrocarbon source rock sample can include multiple pieces of hydrocarbon rock at least some of which have the equivalent spherical diameter of substantially at least one centimeter. Some fragments can have an equivalent spherical diameter different from (that is, lesser than or greater than) at least one centimeter.
• the hydrocarbon source rock sample can have a size that is substantially similar to the size of equivalent hydrocarbon rock that is found in the subsurface from which the rock sample is obtained.
• the hydrocarbon source rock sample can be obtained from a hydrocarbon source rock to be studied.
• the grain size of hydrocarbon source rock in the subsurface affects a distance through which hydrocarbons generated and trapped in the rock need to traverse before being released during natural kerogen maturation.
• the hydrocarbon source rock sample is selected to have a grain size that is substantially similar to a grain size of hydrocarbon rock in the subsurface.
• the experimental conditions of the artificial kerogen maturation can be made closer to the conditions of natural kerogen maturation. That is, in such conditions, the hydrocarbon in the rock sample will need to traverse a distance that is closer to the distance through which the hydrocarbons trapped in the rock need to traverse before being released during natural kerogen maturation.
• the hydrocarbon expulsion efficiency determined for the hydrocarbon source rock sample 104 following the artificial kerogen maturation will, consequently, be a more accurate prediction of the hydrocarbon expulsion efficiency of the hydrocarbon source rock in the subsurface following natural kerogen maturation.
• the pyrolysis chamber of an open system pyrolysis apparatus can be larger than conventional pyrolysis chambers used in the pyrolysis of hydrocarbon source rock samples.
• the pyrolysis chamber can have a volume of substantially one liter (for example, ranging between 0.8 liters and few liters), and can be configured to hold several hundred grams (for example, up to nearly 800 g) of hydrocarbon source rock sample.
• the pyrolysis chamber can further be configured to heat the hydrocarbon source rock sample to temperatures as high as 650 °C.
• the pyrolysis chamber can be configured to heat the hydrocarbon source rock sample at different temperature gradients and different temperature steps as described below with reference to FIG. 3 (only temperatures up to 550 °C are shown).
• Temperatures shown in FIG. 3 are final temperatures of pyrolysis windows, for instance 400 °C means a pyrolysis step with temperature range from 300 to 400 °C and a temperature of 425 °C means a pyrolysis step with temperature range from 300 to 425 °C and so on.
• the hydrocarbon source rock sample can additionally be characterized in terms of the Total Organic Carbon (TOC) content as weight percent (wt %) of the source rock and determination of kerogen type using conventional organic geochemical techniques.
• the TOC content can be determined by LECO TOC analyzer where the organic carbon is measured after removal of carbonate carbon.
• the TOC content can also be determined by Source Rock Analyzers which have pyrolysis and oxidation ovens.
• FIG. 1 is a schematic diagram of an example of an integrated sample- crushing and thermo-vaporization apparatus 150.
• the apparatus 150 includes an integrated sample-crusher and thermo-vaporization chamber 152 in which the previously pyrolyzed hydrocarbon source rock sample is placed.
• this chamber can include a sample crusher apparatus (electric driven crushing blades 174), simultaneous to sample crushing, thermo-vaporization, a heating element, and a controller that can be control the heating element to heat the pyrolyzed hydrocarbon source rock sample to a set temperature, such as 375 °C. Crushing blades 174 can impact against the sample fragments while revolving.
• a sample crusher apparatus electrical driven crushing blades 174
• simultaneous to sample crushing, thermo-vaporization a heating element
• a controller that can be control the heating element to heat the pyrolyzed hydrocarbon source rock sample to a set temperature, such as 375 °C.
• Crushing blades 174 can impact against the sample fragments while revolving.
• a hydrocarbon transport (carrier gas) apparatus can be connected to the sample crushing and thermo-vaporization apparatus 150.
• the hydrocarbon transport apparatus can include tubing 156 connected to a bottom side of the sample crushing and thermo-vaporization chamber 152.
• hydrocarbons transport 158 can be flowed through the thermo-vaporization chamber 152.
• the hydrocarbons recovery apparatus can also include tubing 159 connected to the thermo-vaporization chamber 152 (for example, on an upper side or other side) through which the hydrocarbons transport 158 can transport the hydrocarbons released during crushing and thermo-vaporization of the previously pyrolyzed hydrocarbon source rock sample 154 thermo-vaporization.
• the hydrocarbon transport (carrier gas) apparatus can include one or more valves (for example, valve 162) to control the flow of the recovered hydrocarbons.
• the apparatus can include additional tubing (for example, tubing 160, tubing 164, tubing 170) to transport all or portions of the recovered hydrocarbons to one or more cold traps.
• the apparatus can also be configured to flow all or portions of the recovered hydrocarbons to instrumentation 172 (for example, a chromatograph or other instrumentation) that is configured to analyze the hydrocarbons, for example, to determine chemical composition.
• FIG. 2 is a flowchart of an example of a process 200 for determining a hydrocarbon expulsion efficiency of hydrocarbon source rock.
• the process 200 can be implemented, for example, using the systems described above with reference to FIG. 1.
• an open system pyrolysis can be performed on fragments of a hydrocarbon source rock sample obtained from the subsurface.
• the hydrocarbon source rock sample can include fragments having an equivalent spherical diameter of substantially at least one centimeter.
• a pre-defined mass of the hydrocarbon source rock sample 104 used in open system pyrolysis can of a substantial enough quantity to be a representative sample of the source.
• the sample can be of sufficient mass to counteract the effects of heterogeneity within the sample, such as a few hundred grams (for example, substantially 100 grams).
• the hydrocarbon source rock sample 104 is placed in the pyrolysis chamber 152 and heated non-isothermally.
• the temperature of the pyrolysis chamber 152 can be increased at different heating rates.
• FIG. 3 is a plot 300 of an example of pyrolysis temperature steps according to which the hydrocarbon source rock sample 104 can be pyrolyzed in the open system pyrolysis apparatus 100.
• the temperature of the pyrolysis chamber 152 can be increased at a heating rate of substantially about 25 °C per minute (or lower or higher heating rates).
• the pyrolysis can be conducted in multiple heating rates, for example, eight temperature stages (steps); from starting temperature of 300 °C to 400 °C, from starting temperature of 300 to 425 °C, and so on.
• the heating rate can be the same or different in each temperature stage.
• the increase in the heating rate between any consecutive temperature steps can be the same or different. For example, the increase in the heating gradient between consecutive temperature steps can remain 5 °C per minute for all temperature steps.
• hydrocarbons released by the hydrocarbon source rock sample in response to the open system pyrolysis can be recovered.
• the pyrolysis chamber 152 can be continuously flushed with the inert hydrocarbons transport 108 (for example, helium or other inert gases) using the hydrocarbon transport apparatus.
• the hydrocarbons transport 108 can be flowed into the pyrolysis chamber 152 through tubing 106 and out of the pyrolysis chamber 152 with the expelled hydrocarbons through tubing 1 10.
• the hydrocarbons transport 108 can carry the expelled hydrocarbons out of the pyrolysis chamber 152.
• hydrocarbons expelled from the hydrocarbon source rock sample 104 can be flushed out of the pyrolysis chamber 152 after each temperature stage (e.g. from starting temperature of 300 °C to 450 °C).
• each temperature stage e.g. from starting temperature of 300 °C to 450 °C.
• both tubings 106 and 110 are continuously open to flush the expelled hydrocarbons.
• each cold trap can be a fused silica column submerged in a container filled with liquid nitrogen or other low temperature (for example, as low as -100 °C).
• Each cold trap can trap at least a portion of the hydrocarbons released by the hydrocarbon source rock sample either after open system pyrolysis or after thermo-vaporization.
• the cold trap may not trap methane gas.
• the cold trap can be heated first to a temperature of about 60 °C and then to an elevated temperature of about 375 °C for a set amount of time to purge the gaseous and liquid pyrolysis products, respectively. In this manner, the hydrocarbons trapped by the cold trap 1 18 can be released.
• the hydrocarbon transport apparatus can be implemented to split the hydrocarbons carried by the hydrocarbons transport and flowing out of the pyrolysis chamber 152 into multiple streams.
• the valve 112 can split the hydrocarbons transport flowing from the pyrolysis chamber 152 into a first gas stream and a second gas stream.
• the first gas stream can be directed to the removable cold trap 1 18 and the second portion can be directed to the cold trap 116.
• the first gas stream flowed through the removable cold trap 1 16 can then be flowed to another instrumentation (not shown) to determine a composition of the hydrocarbons.
• the first gas stream can be purged, for example, released to the atmosphere in a controlled vacuum hood.
• the gas stream exiting the pyrolysis chamber 152 can be split into multiple streams (that is, more than two streams). One of the streams can be flowed to the cold trap 118 and then to the instrumentation 172. Another stream can be flowed to the removable cold trap 116 and then to another instrumentation. A third stream can be purged, and so on.
• the splitting of the gas stream exiting the pyrolysis chamber 152 into multiple gas streams and the flow of the gas streams can be controlled, for example, using the valve 112.
• a first quantity of hydrocarbons (A) released in response to performing the open system pyrolysis can be determined.
• the hydrocarbons carried by the hydrocarbons transport 108 out of the pyrolysis chamber 152 can be flowed to instrumentation 172 that can analyze composition of the expelled hydrocarbons.
• the instrumentation 114 can include a sensor, such as a gas chromatograph (GC) or gas chromatography mass spectrometer (GC-MS).
• the instrumentation 172 can be implemented to characterize the hydrocarbons expelled from the hydrocarbon source rock sample 104.
• the instrumentation 172 can be implemented to quantify, for example, in micrograms of hydrocarbons per gram of hydrocarbon source rock sample.
• thermo-vaporization is performed on the pyrolyzed hydrocarbon sample within pyrolysis chamber.
• hydrocarbons released by the hydrocarbon source rock sample in response to thermo-vaporization in the pyrolysis chamber can be recovered.
• a second quantity of hydrocarbons (B) released in response to performing the open system pyrolysis can be determined.
• FIG. 5A is a plot of an example of pyrolysis temperature (only up to 550 °C are shown) to maturity increase of hydrocarbon source rock sample.
• FIG. 5B is an example of hydrocarbon class (methane, wet gas, light oil, heavy oil, etc.) distribution in hydrocarbons recovered from a hydrocarbon source rock sample.
• the two figures show the maturity of the residual organic matter within hydrocarbon source rock sample 152 reached at the end of each pyrolysis stage.
• the two figures also show with expected variations of hydrocarbon class distribution (Ci (methane), C2-C4 (ethane, propane and butane), C5+ (pentane and heavier hydrocarbons)) with increasing maturity.
• a crushing and thermo-vaporization (within the thermo-vapori- zation chamber) at a temperature of 375 °C can be performed on the hydrocarbon source rock sample on which the open system pyrolysis was performed.
• the hydrocarbon source rock sample is removed from the pyrolysis chamber 152, crushed and thermally vaporized.
• the crushing and thermo-vaporization of the previously pyrolyzed hydrocarbon source rock sample can be performed simultaneously.
• thermo-vaporization the pyrolyzed hydrocarbon source rock sample 154 is placed in the crushing and thermo-vaporization chamber 152 and heated to 375 °C for a set amount of time.
• a quantity of the pyrolyzed hydrocarbon source rock sample 154 used in thermo-vaporization can be a few tens of grams (for example, substantially 20 g).
• FIG. 4 is a plot 400 of an example of a thermo- vaporization temperature gradient according to which the pyrolyzed hydrocarbon source rock sample 154 can be thermally vaporized in the thermo-vaporization apparatus 150.
• the temperature of the chamber 152 can be kept constant at substantially 375 °C time. Thermo-vaporization can purge any retained hydrocarbons in the rock sample.
• the chamber 152 can be continuously flushed with the inert carrier gas 158 (for example, helium or other inert carrier gas) using the hydrocarbons recovery apparatus.
• the carrier gas 158 can be flowed into the thermo-vaporization chamber 152 through tubing 156 and out of the chamber 152 with the expelled hydrocarbons through tubing 160.
• the carrier gas 158 can carry the expelled hydrocarbons out of the crushing and thermo-vaporization chamber 152.
• the third quantity of hydrocarbons (C) released in response to performing the open system pyrolysis can be determined.
• each cold trap can be a fused silica column submerged in a container filled with liquid nitrogen or other low temperature (for example, as low as -100 °C).
• the cold trap can be heated first to a temperature of about 60 °C and then to an elevated temperature of about 375 °C to purge the gaseous and liquid pyrolysis products, respectively. In this manner, the hydrocarbons trapped by the cold trap 168 can be released.
• the hydrocarbons recovery apparatus can be implemented to split the hydrocarbons flowing out of the thermo-vaporization chamber 152 into multiple gas streams.
• the valve 162 can split the gas flowing from the crushing and thermo-vaporization chamber 152 into a first gas stream and a second gas stream.
• the first gas stream can be directed to a removable cold trap 168 and the second portion can be directed to the cold trap 166.
• the first gas stream flowed through the removable cold trap 166 can then be flowed to another instrumentation (not shown) to determine a composition of the gas stream.
• the first gas stream can be purged, for example, released to atmosphere.
• the gas stream exiting the crushing and thermo- vaporization chamber 152 can be split into multiple streams (that is, more than two streams). One of the streams can be flowed to the cold trap 168 and then to the instrumentation 172. Another stream can be flowed to the removable cold trap 166 and then to another instrumentation. A third stream can be purged, and so on.
• the splitting of the gas stream exiting the crushing and thermo-vaporization chamber 152 into multiple gas streams and the flow of the gas streams can be controlled, for example, using the valve 162.
• the hydrocarbons carried by the carrier gas 158 out of the crushing and thermo-vaporization chamber 152 can be flowed to instrumentation 172 that can analyze a composition of the expelled hydrocarbons.
• the instrumentation 172 can include a gas chromatograph (GC) or gas chromatography - mass spectrometry (GC-MS).
• GC gas chromatograph
• GC-MS gas chromatography - mass spectrometry
• the instrumentation 172 can be implemented to characterize the hydrocarbons expelled from the pyrolyzed hydrocarbon source rock sample 154.
• the instrumentation 172 can be implemented to quantify, for example, in micrograms of hydrocarbons per gram of hydrocarbon source rock sample.
• the hydrocarbon source rock sample 104 was placed in a pyrolysis chamber 152 during open system pyrolysis, and the pyrolyzed hydrocarbon source rock sample 154 was then placed in a separate and distinct sample crushing and thermo-vaporization chamber 152 during thermo-vaporization.
• the pyrolysis chamber 152 can be used as the sample crushing and thermo-vaporization chamber 152.
• the pyrolyzed hydrocarbon source rock sample 154 can be placed in (or can remain in) the pyrolysis chamber 152. Sample crushing and thermo-vaporization of the pyrolyzed hydrocarbon source rock sample can then be performed as described above.
• the maturity of the residual kerogen can be determined using procedures such as geochemical techniques (for example, vitrinite reflectance measurements, open system pyrolysis Tmax, or other geochemical techniques). In this manner, after each step, a determined maturity level for the source rock which has generated, expelled, or retained hydrocarbons can be characterized.
• geochemical techniques for example, vitrinite reflectance measurements, open system pyrolysis Tmax, or other geochemical techniques.
• a first hydrocarbon expulsion efficiency of the hydrocarbon rock can be determined.
• the efficiency can be determined as a ratio of a sum of the first quantity of hydrocarbons (i.e., the hydrocarbons released during open system pyrolysis of the hydrocarbon source rock sample 104 - HCpyroiysis) to the sum of the first, the second (from thermo-vaporization at 375 °C in the pyrolysis chamber 152- HCThermo- vaporization), and third (i.e., the hydrocarbons released during crushing and thermo-vaporization at 375 °C of the pyrolyzed hydrocarbon source rock sample 154- HCcmshingThermo- Vaporization).
• the hydrocarbon expulsion efficiency (HCEE) can be determined using Equation 1 shown below.
• HCEE (HCpyroiysis) X 100 / (HCpyroiysis + HCThermo-Vaporization +
• HCpyroiysis is the quantity (for example, in micrograms per gram of sample) of hydrocarbons released in response to open system pyrolysis of the hydrocarbon source rock sample 104.
• HCThermo-Vaporization is the quantity (for example, in micrograms per gram of sample) of hydrocarbons released in response to thermo-vaporization of previously pyrolyzed hydrocarbon source rock sample 104.
• HCcmshingThermo- vaporization is the quantity (for example, in micrograms per gram of sample) of hydrocarbons released in response to crushing and thermo-vaporization of the previously pyrolyzed hydrocarbon source rock sample 154.
• a second hydrocarbon source rock sample can be obtained from the same hydrocarbon source rock from which the hydrocarbon source rock sample 104 can be obtained.
• the rock sample can be ground to have grain sizes in the micrometer range (for example, less than substantially 250 ⁇ ).
• an open system pyrolysis can be performed on the powdered rock sample.
• a quantity of the powder size hydrocarbon source rock sample for the open system pyrolysis can be a few hundreds of milligrams to one gram (for example, substantially less than 1 gram).
• the open system pyrolysis on the second hydrocarbon rock sample can be performed using the open system pyrolysis apparatus 100 using techniques similar to those described above.
• a fourth quantity of hydrocarbons released in response to performing the open system pyrolysis of the powder hydrocarbon source rock sample can be determined using techniques similar to those described above.
• Equation 2 As a verification of the first HCEE found by using Equation 1, the second HCEE can also be determined using Equation 2 shown below.
• HCEE (HCpyrolysis) X 100 / HCpowderedSampl ePyrolysis (Equation
• HCpyrolysis is the quantity (for example, in micrograms per gram of sample) of hydrocarbons released in response to open system pyrolysis of the hydrocarbon source rock sample 104
• HCpowderedSampiePyroiysis is the quantity (for example, in micrograms per gram of sample) of hydrocarbons released in response to open system pyrolysis of the powdered hydrocarbon source rock sample 104.
• HCCE calculated here is based on the ratio of hydrocarbons released from pyrolysis of chip grain size (e.g., 1 cm) of the hydrocarbon source rock to hydrocarbons released from pyrolysis of powder form of the same hydrocarbon source rock.
• Hydrocarbon expulsion efficiency in case of powdered sample is considered to be not effected by any barriers and the amount of hydrocarbons released is assume to be maximum (e.g., hydrocarbons generated equals hydrocarbon released from the hydrocarbon source rock). It is expected that hydrocarbons released from pyrolysis of chip grain size (e.g., 1 cm) of the same hydrocarbon source rock sample will be comparatively less and the HCCE will be less than 100%.
• the hydrocarbon expulsion efficiency can be provided as an input to a geological model to study hydrocarbon expulsion from the hydrocarbon source rock through geological history.
• FIG. 6 shows a flowchart of another example method 600 for determining a hydrocarbon expulsion efficiency of hydrocarbon source rock.
• an open system pyrolysis of a first hydrocarbon source rock sample obtained from a natural system is performed within a pyrolysis chamber. This results in a pyrolyzed sample.
• the open system pyrolysis is performed by maintaining the pyrolysis chamber at a substantially constant temperature of 375 °C.
• the first hydrocarbon source rock sample includes hydrocarbon source rocks having an equivalent spherical diameter of at least substantially one centimeter.
• hydrocarbons released by the first hydrocarbon source rock sample are recovered from the pyrolysis chamber in response to the open system pyrolysis.
• thermo-vaporization is performed (within the pyrolysis chamber) on the pyrolyzed sample on which the open system pyrolysis was performed at a substantially constant temperature of 375 °C.
• hydrocarbons released by the pyrolyzed sample are recovered from the pyrolysis chamber in response to the thermo-vaporization.
• a first hydrocarbon expulsion efficiency of hydrocarbon source rock in the natural system is determined based on the recovered hydrocarbons released by the first hydrocarbon source rock sample in response to the open system pyrolysis and based on the recovered hydrocarbons released by the pyrolyzed sample in response to thermo- vaporization.
• a second hydrocarbon rock sample of a pre-defined mass is ground resulting in a ground hydrocarbon source rock sample having a grain size less than or equal to or less than 250 micrometers.
• the grinding is performed within an integrated sample-crusher and thermo-vaporization chamber.
• a second pyrolysis is performed (within the integrated sample-crusher and thermo-vaporization chamber) on the ground hydrocarbon source rock sample. The second pyrolysis is performed by maintaining the integrated sample-crusher and thermo-vaporization chamber at a substantially constant temperature of 375 °C within the integrated sample-crusher and thermo- vaporization chamber.
• a second hydrocarbon expulsion efficiency of the hydrocarbon source rock in the natural system is determined based on performing the second pyrolysis on the second hydrocarbon source rock sample.
• the first hydrocarbon expulsion efficiency is verified using the second hydrocarbon expulsion efficiency.

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