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Shaletekk H Shale Oil Cold Extraction
1
Shaletekk H
After 7 years of research and development we can finally present a viable and credible process/system
which will allow cost-effective cold and environmentally friendly extraction of shale oil from the substrate,
At Naturetekk we are dedicated to the promotion and commercialisation of this process;
Shaletekk M. Acknowledgement and thanks to the Jordanian Government bodies and companies:
The Higher Council
for Science and Technology
Yarmouk University The Natural
Resources Authority
Jordan Petroleum
Refinery Company
Jordan University of
Science and Technology
Extracting oil from oil shale is more complex than
conventional oil recovery.
Hydrocarbons in oil shale are present in the form of
solid, bituminous materials and hence cannot be
pumped directly out of the geologic reservoir. The rock
must be heated to a high temperature, and the resultant
liquid must be separated and collected. The heating
process is called retorting.
Surface mining can recover much higher percentages of
in-place resources. The thickness of oil shale deposits,
the amount of overburden and the presence of
subsurface water can make surface mining difficult.
Shale oil extraction is an industrial process for
unconventional oil production. This process converts
kerogen in oil shale into shale oil by pyrolysis,
hydrogenation or thermal dissolution. The resultant shale
oil is used as fuel oil or upgraded to meet refinery
feedstock specifications by adding hydrogen and
removing sulphur and nitrogen impurities.
As of 2010 shale oil extraction is in operation within
Estonia, Brazil, and China. In 2008 their industries
produced about 930,000 metric tonnes (17,700 barrels
per day) of shale oil. Australia, USA and Canada have
tested shale oil extraction techniques via demonstration
projects and are planning commercial implementation:
Morocco and Jordan have announced their intent to do
the same. Only four processes are in commercial use:
Kiviter, Galoter, Fushun and Petrosix.
Conventional Processes
America’s oil shale reserves will potentially produce
at least 1.5 trillion barrels of oil – approximately five
times the reserves of Saudi Arabia. Nobody is
producing commercial quantities of oil from these
vast deposits.
Obviously, there are some very real obstacles to oil
production from shale. “Oil shale is the fuel of the
future, and always will be,” is a popular saying in
Western Colorado.
2
Shaletekk H
Oil Shale Deposit
Refining
Liquid Fuels By-products
Fracturing
Retorting
Product Recovery
Mining
In-situ Ex-situ (Conventional)
Spent Shale
Crushing
Retorting
Thermal & Chemical
Treating Hydrogenation }
Conventional Processes
Oil Shale Technology Prospects
Processes for producing shale oil generally fall into one of
two groups: mining followed by surface retorting and in-situ
retorting.
Mining and Surface Retorting
Underground mining using the room-and-pillar method or
surface mining. The current state of the art in mining – both
room-and-pillar and surface techniques, such as open pit
mining – appears to be able to meet the requirements for
the commercial development of oil shale.
Surface retorting involves crushing the mined oil shale and
then retorting it at about 900 to 1,000°F. The vessel in which
this heating occurs is called a retort. The hot shale oil
leaving the retort is not stable and must be sent directly to
an upgrading plant for catalytic processing with hydrogen
to remove impurities and produce a stable product.
This stable shale oil can be used as a refinery feedstock
and should compete favourably with sweet, light crude oil.
An oil shale plant operating on a commercial scale – that is,
producing a minimum of 50,000 barrels per day – would
need to incorporate multiple retorts. As the residence time
of oil shale in the hot zone of a retort is nearly a half hour, a
retort designed to produce 50,000 barrels of shale oil per
day would need to be sized to contain more than 1,500
tons of oil shale, which is well beyond the state-of-the-art.
In-Situ Retorting
In-situ retorting entails heating oil shale in place, extracting
the liquid from the ground and transporting it to an
upgrading facility.
The mainstream methods involved burning a portion of the
oil shale underground to produce the heat needed for
retorting the remaining oil shale. This was unsuccessful,
encountering serious problems in maintaining and
controlling the underground combustion process and
avoiding subsurface pollution.
3
Environmental Issues of shale oil extraction
Thermally Conductive In-Situ Conversion
A volume of shale is heated by electric heaters placed in
vertical holes drilled through the entire thickness (more
than a thousand feet) of a section of oil shale. To obtain
even heating over a reasonable time frame, between 15
and 25 heating holes will be drilled per acre. After heating
for two to three years, the targeted volume of the deposit
will reach a temperature of between 650 and 700°F. This
very slow heating to a relatively low temperature
(compared with the plus-900 degrees F temperatures
common in surface retorting) is sufficient to cause the
chemical and physical changes required to release oil
from the shale. On an energy basis, about two-thirds of
the released product is liquid and one third is a gas similar
in composition to natural gas. The released product is
gathered in collection wells positioned within the heated
zone.
As part of site preparation, Shell’s current plan is to use
ground-freezing technology to establish an underground
barrier around the perimeter of the extraction zone.
A “freeze wall” would be created by circulating a
refrigerated fluid through a series of wells drilled around
the extraction zone. In addition to preventing groundwater
from entering the extraction zone, the freeze wall is
intended to keep hydrocarbons and other products
generated by retorting, from leaving the project perimeter
during ground heating, product extraction, and post
extraction ground cooling. The site preparation stage also
involves the construction of power plants and power
transmission lines needed to supply electricity to the
underground heaters.
Post-production cleanup involves steam flushing to remove
remaining mobile hydrocarbons, ground cooling, removing
the freeze wall, and site reclamation.
Shell plans to use ground-freezing technology to control
groundwater during production. Ground-freezing
technology is a well-established method for controlling
groundwater during construction and mining operations.
Multi-kilometer barriers have been constructed and
sustained for years.
“The ICP process is clearly energy-intensive,
as its driving force is the injection of heat into
the subsurface.”
At the moment, Shell is not sure what the optimal size of
production zones ought to be. The issue here is how big
can a freeze-wall be to become effective, freezing the
groundwater surrounding a shale deposit? The test
projects as you can see, were quite small. Shell doesn’t
know, or isn’t saying, what the optimum size is for each
“pod” or “cell”.
Nonetheless, applying ground-freezing to in-situ
conversion of oil shale requires resolving significant
technical uncertainties to ensure that the frozen
barrier is structurally sound. Substantial uncertainties
remain regarding the impact of in-situ retorting on the
quality of groundwater. Retorting and removing
hydrocarbons will change aquifer properties and will likely
result in an increase in hydraulic conductivity. After the
removal of the freeze wall, such changes in aquifer
properties could result in the leaching and transport of
mineral salts and trace metals that are mixed with oil shale
deposits.
4
No heating process required
• The oil separation and extraction does not require ANY
heating of the Shale liquid mix (The soup);
• The "treatment" takes place at room temperature!!!!
(about 23 degrees celsius).
No waste and pollution
• The bio-surfactant is water based;
• The bio-surfactant is recyclable (important as there is no
waste, water/land pollution etc. particularly in places
where the access to water is an issue, limited or non).
High yield recovery
• 60%/62% and over of the available % oil on the shale
deposits worlwide (Based on extensive Lab tests so far).
Fast and easy recovery
Extremely cost effective production cost, plant,
equipment and installations.
Patentable.
General Info:
Chemical kinetics, also known as reaction kinetics, is the
study of rates of chemical processes. Chemical kinetics
includes investigations of how different experimental
conditions can influence the speed of a chemical reaction
and yield information about the reaction's mechanism and
transition states, as well as the construction of
mathematical models that can describe the characteristics
of a chemical reaction.
It deals with the experimental determination of reaction
rates from which rate laws and rate constants are derived.
Relatively simple rate laws exist for zero-order reactions (for
which reaction rates are independent of concentration),
first-order reactions, and second-order reactions, and can
be derived for others. In consecutive reactions, the rate-
determining step often determines the kinetics. In
consecutive first-order reactions, a steady state
approximation can simplify the rate law. The activation
energy for a reaction is experimentally determined through
the Arrhenius equation and the Eyring equation. The main
factors that influence the reaction rate include: the physical
state of the reactants, the concentrations of the reactants,
the temperature at which the reaction occurs, and whether
or not any catalysts are present in the reaction.
The active catalyst in this process is a proprietary
BIO-SURFACTANT PRODUCING BACTERIA.
Shale oil cold extraction process
Process based on the kinetics of hydrocarbon extraction from oil shale
using bio-surfactant producing bacteria. energy conservation and management.
Nationality
Jordanian
Place and Date of Birth
Karak – Jordan, 23/8/1951.
Scientific Skills
• Experimental Design, Surface Response Methodology,
Kinetic Models Analysis.
• Computer Modelling in Food Science and Nutrition
Instrumental Analysis Skills
• HPLC,GC,Spectroscopic Methods (UV/VIS, IR, AAS, ICP,
Fluorescence). Gel Filtration, Ion Exchange
Chromatography, Electrophoresis (Vertical,and
Horizontal), Rheological Techniques
• Microbiological techniques, Cell Culture Techniques(plant
and animal cells techniques), Biotechnology Techniques
(Bioreactors, Immobilization for biocatalysts, bio
separation techniques, bioconversion, microbial and
enzymes maintenance and production)
Over 38 scientific publications, 7 published books and
10 scientific papers presented to conferences
• Ph.D. in Food Science, The University of Reading 1986.
(U.K.)
• M.Sc. in Food Science, The University of Reading 1982.
(U.K.)
• Qualifying Year in Food Science, ( 1980-1981),
The University of Reading. (U.K.)
• M.Sc. in Animal Genetics, Mosul University, 1977.
• B.Sc. in Animal Science, Mosul University, 1974.
Analytical services and consultations
Different analytical services were carried out to
many public and private sectors.
These include the following analysis:
• Microbiological analyses to food samples
• Chemical analyses to food and non food samples.
• Physical analyses.These services were carried out under
the supervision of the consultation center for technical
studies of the University of Jordan. 1996-2002.
Consultative work with following institutions:
• Cosultative work with the Higher Council for Science and
technology in building a modern dairy plant in the north
of Jordanian Badia (Tel-Alremah area) and also in
establishing a modern dairy camels farm near the
dairy plant.
Membership of different committees
1. Committees within the department of nutrition and
food technology
• Library committee
• Community services committee.
• Laboratory equipment committee..
• Safety committee.
2. Different Minestry of Health.committees such as food
additives and food safety committees.
3. In the committees of the Institute of Specifications
and Standards. These Include:
• Dairy products committee
• Laboratory accriditation committee
• Sampling committee.
• Food additives
4. Member in two committees in the Minestry of
Enviroment, the first on is involved in Biosafety
Framework, and the second one is involved in the olive
oil processing environmental pollution.
Prizes
Two prizes were won in 1996 and 2003.
The first prize was won on the following researches:
• The research paper was published in the USA Periodical:
Poultry Science. The paper entitled: The influence of
Lactbacillus acidophilus on the production and chemical
composition of hens eggs.; Poultry Science (1996)75:
491-494.The prize was provided by The Scientific
Foundation of Hisham Adeeb Hijjawi.
• The second prize was won on the research work entitled:
Utilization of tomato pomace as asubstrate for the
production of vitamin B12-a preliminary appraisal.
Bioresource Technology (2001)78: 225-2
Naturetekk Ltd 111 Guthrum Place Newton Aycliffe
Co. Durham DL5 4QE United Kingdom +44 (0)7587 494141
info@naturetekk.co.uk www.naturetekk.co.uk
Dr. Malik S.Y. Haddadin
Profile

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Shaletekk H Brochure

  • 1. Shaletekk H Shale Oil Cold Extraction
  • 2. 1 Shaletekk H After 7 years of research and development we can finally present a viable and credible process/system which will allow cost-effective cold and environmentally friendly extraction of shale oil from the substrate, At Naturetekk we are dedicated to the promotion and commercialisation of this process; Shaletekk M. Acknowledgement and thanks to the Jordanian Government bodies and companies: The Higher Council for Science and Technology Yarmouk University The Natural Resources Authority Jordan Petroleum Refinery Company Jordan University of Science and Technology Extracting oil from oil shale is more complex than conventional oil recovery. Hydrocarbons in oil shale are present in the form of solid, bituminous materials and hence cannot be pumped directly out of the geologic reservoir. The rock must be heated to a high temperature, and the resultant liquid must be separated and collected. The heating process is called retorting. Surface mining can recover much higher percentages of in-place resources. The thickness of oil shale deposits, the amount of overburden and the presence of subsurface water can make surface mining difficult. Shale oil extraction is an industrial process for unconventional oil production. This process converts kerogen in oil shale into shale oil by pyrolysis, hydrogenation or thermal dissolution. The resultant shale oil is used as fuel oil or upgraded to meet refinery feedstock specifications by adding hydrogen and removing sulphur and nitrogen impurities. As of 2010 shale oil extraction is in operation within Estonia, Brazil, and China. In 2008 their industries produced about 930,000 metric tonnes (17,700 barrels per day) of shale oil. Australia, USA and Canada have tested shale oil extraction techniques via demonstration projects and are planning commercial implementation: Morocco and Jordan have announced their intent to do the same. Only four processes are in commercial use: Kiviter, Galoter, Fushun and Petrosix. Conventional Processes America’s oil shale reserves will potentially produce at least 1.5 trillion barrels of oil – approximately five times the reserves of Saudi Arabia. Nobody is producing commercial quantities of oil from these vast deposits. Obviously, there are some very real obstacles to oil production from shale. “Oil shale is the fuel of the future, and always will be,” is a popular saying in Western Colorado.
  • 3. 2 Shaletekk H Oil Shale Deposit Refining Liquid Fuels By-products Fracturing Retorting Product Recovery Mining In-situ Ex-situ (Conventional) Spent Shale Crushing Retorting Thermal & Chemical Treating Hydrogenation } Conventional Processes Oil Shale Technology Prospects Processes for producing shale oil generally fall into one of two groups: mining followed by surface retorting and in-situ retorting. Mining and Surface Retorting Underground mining using the room-and-pillar method or surface mining. The current state of the art in mining – both room-and-pillar and surface techniques, such as open pit mining – appears to be able to meet the requirements for the commercial development of oil shale. Surface retorting involves crushing the mined oil shale and then retorting it at about 900 to 1,000°F. The vessel in which this heating occurs is called a retort. The hot shale oil leaving the retort is not stable and must be sent directly to an upgrading plant for catalytic processing with hydrogen to remove impurities and produce a stable product. This stable shale oil can be used as a refinery feedstock and should compete favourably with sweet, light crude oil. An oil shale plant operating on a commercial scale – that is, producing a minimum of 50,000 barrels per day – would need to incorporate multiple retorts. As the residence time of oil shale in the hot zone of a retort is nearly a half hour, a retort designed to produce 50,000 barrels of shale oil per day would need to be sized to contain more than 1,500 tons of oil shale, which is well beyond the state-of-the-art. In-Situ Retorting In-situ retorting entails heating oil shale in place, extracting the liquid from the ground and transporting it to an upgrading facility. The mainstream methods involved burning a portion of the oil shale underground to produce the heat needed for retorting the remaining oil shale. This was unsuccessful, encountering serious problems in maintaining and controlling the underground combustion process and avoiding subsurface pollution.
  • 4. 3 Environmental Issues of shale oil extraction Thermally Conductive In-Situ Conversion A volume of shale is heated by electric heaters placed in vertical holes drilled through the entire thickness (more than a thousand feet) of a section of oil shale. To obtain even heating over a reasonable time frame, between 15 and 25 heating holes will be drilled per acre. After heating for two to three years, the targeted volume of the deposit will reach a temperature of between 650 and 700°F. This very slow heating to a relatively low temperature (compared with the plus-900 degrees F temperatures common in surface retorting) is sufficient to cause the chemical and physical changes required to release oil from the shale. On an energy basis, about two-thirds of the released product is liquid and one third is a gas similar in composition to natural gas. The released product is gathered in collection wells positioned within the heated zone. As part of site preparation, Shell’s current plan is to use ground-freezing technology to establish an underground barrier around the perimeter of the extraction zone. A “freeze wall” would be created by circulating a refrigerated fluid through a series of wells drilled around the extraction zone. In addition to preventing groundwater from entering the extraction zone, the freeze wall is intended to keep hydrocarbons and other products generated by retorting, from leaving the project perimeter during ground heating, product extraction, and post extraction ground cooling. The site preparation stage also involves the construction of power plants and power transmission lines needed to supply electricity to the underground heaters. Post-production cleanup involves steam flushing to remove remaining mobile hydrocarbons, ground cooling, removing the freeze wall, and site reclamation. Shell plans to use ground-freezing technology to control groundwater during production. Ground-freezing technology is a well-established method for controlling groundwater during construction and mining operations. Multi-kilometer barriers have been constructed and sustained for years. “The ICP process is clearly energy-intensive, as its driving force is the injection of heat into the subsurface.” At the moment, Shell is not sure what the optimal size of production zones ought to be. The issue here is how big can a freeze-wall be to become effective, freezing the groundwater surrounding a shale deposit? The test projects as you can see, were quite small. Shell doesn’t know, or isn’t saying, what the optimum size is for each “pod” or “cell”. Nonetheless, applying ground-freezing to in-situ conversion of oil shale requires resolving significant technical uncertainties to ensure that the frozen barrier is structurally sound. Substantial uncertainties remain regarding the impact of in-situ retorting on the quality of groundwater. Retorting and removing hydrocarbons will change aquifer properties and will likely result in an increase in hydraulic conductivity. After the removal of the freeze wall, such changes in aquifer properties could result in the leaching and transport of mineral salts and trace metals that are mixed with oil shale deposits.
  • 5. 4 No heating process required • The oil separation and extraction does not require ANY heating of the Shale liquid mix (The soup); • The "treatment" takes place at room temperature!!!! (about 23 degrees celsius). No waste and pollution • The bio-surfactant is water based; • The bio-surfactant is recyclable (important as there is no waste, water/land pollution etc. particularly in places where the access to water is an issue, limited or non). High yield recovery • 60%/62% and over of the available % oil on the shale deposits worlwide (Based on extensive Lab tests so far). Fast and easy recovery Extremely cost effective production cost, plant, equipment and installations. Patentable. General Info: Chemical kinetics, also known as reaction kinetics, is the study of rates of chemical processes. Chemical kinetics includes investigations of how different experimental conditions can influence the speed of a chemical reaction and yield information about the reaction's mechanism and transition states, as well as the construction of mathematical models that can describe the characteristics of a chemical reaction. It deals with the experimental determination of reaction rates from which rate laws and rate constants are derived. Relatively simple rate laws exist for zero-order reactions (for which reaction rates are independent of concentration), first-order reactions, and second-order reactions, and can be derived for others. In consecutive reactions, the rate- determining step often determines the kinetics. In consecutive first-order reactions, a steady state approximation can simplify the rate law. The activation energy for a reaction is experimentally determined through the Arrhenius equation and the Eyring equation. The main factors that influence the reaction rate include: the physical state of the reactants, the concentrations of the reactants, the temperature at which the reaction occurs, and whether or not any catalysts are present in the reaction. The active catalyst in this process is a proprietary BIO-SURFACTANT PRODUCING BACTERIA. Shale oil cold extraction process Process based on the kinetics of hydrocarbon extraction from oil shale using bio-surfactant producing bacteria. energy conservation and management.
  • 6. Nationality Jordanian Place and Date of Birth Karak – Jordan, 23/8/1951. Scientific Skills • Experimental Design, Surface Response Methodology, Kinetic Models Analysis. • Computer Modelling in Food Science and Nutrition Instrumental Analysis Skills • HPLC,GC,Spectroscopic Methods (UV/VIS, IR, AAS, ICP, Fluorescence). Gel Filtration, Ion Exchange Chromatography, Electrophoresis (Vertical,and Horizontal), Rheological Techniques • Microbiological techniques, Cell Culture Techniques(plant and animal cells techniques), Biotechnology Techniques (Bioreactors, Immobilization for biocatalysts, bio separation techniques, bioconversion, microbial and enzymes maintenance and production) Over 38 scientific publications, 7 published books and 10 scientific papers presented to conferences • Ph.D. in Food Science, The University of Reading 1986. (U.K.) • M.Sc. in Food Science, The University of Reading 1982. (U.K.) • Qualifying Year in Food Science, ( 1980-1981), The University of Reading. (U.K.) • M.Sc. in Animal Genetics, Mosul University, 1977. • B.Sc. in Animal Science, Mosul University, 1974. Analytical services and consultations Different analytical services were carried out to many public and private sectors. These include the following analysis: • Microbiological analyses to food samples • Chemical analyses to food and non food samples. • Physical analyses.These services were carried out under the supervision of the consultation center for technical studies of the University of Jordan. 1996-2002. Consultative work with following institutions: • Cosultative work with the Higher Council for Science and technology in building a modern dairy plant in the north of Jordanian Badia (Tel-Alremah area) and also in establishing a modern dairy camels farm near the dairy plant. Membership of different committees 1. Committees within the department of nutrition and food technology • Library committee • Community services committee. • Laboratory equipment committee.. • Safety committee. 2. Different Minestry of Health.committees such as food additives and food safety committees. 3. In the committees of the Institute of Specifications and Standards. These Include: • Dairy products committee • Laboratory accriditation committee • Sampling committee. • Food additives 4. Member in two committees in the Minestry of Enviroment, the first on is involved in Biosafety Framework, and the second one is involved in the olive oil processing environmental pollution. Prizes Two prizes were won in 1996 and 2003. The first prize was won on the following researches: • The research paper was published in the USA Periodical: Poultry Science. The paper entitled: The influence of Lactbacillus acidophilus on the production and chemical composition of hens eggs.; Poultry Science (1996)75: 491-494.The prize was provided by The Scientific Foundation of Hisham Adeeb Hijjawi. • The second prize was won on the research work entitled: Utilization of tomato pomace as asubstrate for the production of vitamin B12-a preliminary appraisal. Bioresource Technology (2001)78: 225-2 Naturetekk Ltd 111 Guthrum Place Newton Aycliffe Co. Durham DL5 4QE United Kingdom +44 (0)7587 494141 info@naturetekk.co.uk www.naturetekk.co.uk Dr. Malik S.Y. Haddadin Profile