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Liquefaction of coal
         into transportation fuel
                                                           R&D Project
                                     Bionic Laboratories BLG GmbH, Germany
                                                 in cooperation with
                                         Smeral Brno a.s. , Czech Republic




2/2013   © 2013 Bionic Fuel Knowledge Partners Inc., Oswego, NY                                       1

                                                                    several international patents pending
Introduction
•   Friedrich Bergius (* 11.10.1889, † 31.3.1949)
    In summer 1913 Bergius discovered the process of converting
    lignite coal into organic liquids by applying hydrogen at 150 atm
    pressure and 450 C in an autoclave. His resulting patent was one
    of the reasons that he received, together with Carl Bosch, the
    Nobel Price for high pressure hydrogen processing in 1931.

•   Prof. Dr. Ernst Bayer    (*24.3.1927, † 31.1.2002)

    In 1961 he invented the process of catalytic low temperature
    depolymerisation of organic substances to liquid fuel using
    special zeolite catalysts.

•   Albert Wallace Hull (* 19.4.1880, † 22.11.1966)
    In 1920 his research resulted in the invention of the magnetron,
    the electronic device that generates microwaves. At the time Hull
    anticipated the magnetron would find greater use as an energy converter than in
    communication applications and radar systems.


               2/2013                © 2013 Bionic Fuel Knowledge Partners Inc.,   2
                                                    Oswego, NY
Liquefaction in history
After World War I several plants following the Bergius process were built in
Germany. These plants were extensively used during World War II to fuel
the German Airforce.

In the process, dry coal, finely grinded, is mixed with heavy oil recycled
from the process. A catalyst is typically added to the mixture. The reaction
occurs between 400 °C (752 °F) to 500 °C (932 °F) and 120 to 150 atm
pressure in a hydrogen atmosphere. The reaction can be summarized
chemically as follows:

                       n C + (n + 1) H2 → CnH2 n + 2
    The general mass balance turns out like this:
                       100 kg of lignite coal
          plus         40 kg of heavy oil derived from the process
          plus         5 kg of catalyst
          @            450 - 480°C & 120 - 150 atm hydrogen

                        30 kg light oils + 50 kg heavy oils + 20 kg gas
              2/2013              © 2013 Bionic Fuel Knowledge Partners Inc.,   3
                                                 Oswego, NY
Liquefaction in history
Between 1952 and 2000 the Bergius-Pier process has been enhanced and
optimized in various ways especially in Germany.

– Introduction of the combi-cracker technology (1952-1964)
   (improved catalytic treatment of the gas phase)

– Coal Liquifaction plant in Bottrop, Germany 1981-1988
   (later used for heavy oil upgrading until 2000)

Until today, the Bergius-Pier process demonstrates the highest oil
yields (> 60%) in coal liquefaction mode and the highest conversion
(>90% of 500+°C) in heavy oil upgrading mode, which consequently
also minimizes the CO2 footprint.

This is where Bionic picked up the process for a complete redesign based
on Bionic‘s specific knowledge base in microwave and catalytic
cracking technologies.



            2/2013            © 2013 Bionic Fuel Knowledge Partners Inc.,   4
                                             Oswego, NY
Liquefaction today
•   Combining the different technologies with a specially developed
    nano catalyst, modulated microwave generators, and a microwave
    driven hydrogen gas steam/shift generator, Bionic
    engineers defined an advanced way for an even more
    efficient conversion of coal to liquid (CTL):
     –   lowered hydrogen pressure (60-80 atm)

     –   controlled energy application via modulated microwaves

     –   improved synthetic nano catalysts

     –   feedstock preprocessing in Bionic‘s MWDP reactor

     –   continous production capability

     –   preprocessing and activation of nano-coal aerosol through microwaves

     –   Improved product quality by hydrogenation of carbon and
         parallel depolymerisation of aromatics

     –   Unprocessed char exits as <4nm nano-carbon particles


             - bionic microchar – a char to fuel process -
             2/2013              © 2013 Bionic Fuel Knowledge Partners Inc.,    5
                                                Oswego, NY
Production Layout

Char is processed
in a microfuel unit which
separating the volatile
contents.

Intermediate product is a
nano-size carbon aerosol
which is transported into
the high pressure unit.

In these vessels the
hydrogenation occurs
on a microwave heated
catalyst-net with hydro-
carbons being syntesized.

They are forming a mix
with heavy oil present in the
vessels. This oil-fuel mixture
is then separated in a
distillation column.

The required hydrogen is
produced by a biomass
steam/shift reformer.




                                 2/2013   © 2013 Bionic Fuel Knowledge Partners Inc.,   6
                                                         Oswego, NY
Single Unit Layout




2/2013   © 2013 Bionic Fuel Knowledge Partners Inc.,   7
                        Oswego, NY
Cluster combination Layout


A large scale 4 x 4 cluster
CTL facility.

A single bionicfuel unit
converts biomass to fuel for
the necessary power
production in internal
generators. Separated
water from the biomass
feedstock is used for
hydrogen production in
steam reformers.

Four bionicfuel units
perform the preprocessing
of the char with attached
four hydrogenation units
which are responsible for
the final liquefaction step.

In a large distillation column
the lighter products are
separated for use as
transportation fuel, while
the heavy by products are
returned to the high
pressure vessels.




                                 2/2013     © 2013 Bionic Fuel Knowledge Partners Inc.,   8
                                                           Oswego, NY
Capacities




Single liquefaction Unit:

  1.000 kg / hr              + 110 kg H2                                  520 kg light oil
  char @ 33 MJ/kg            + 370 kg heavy oil                           698 kg heavy oil
                             + 70 kg catalyst                             270 kg gas
                             + 320 kWh @430 C                              80 kg residues




             2/2013         © 2013 Bionic Fuel Knowledge Partners Inc.,                9
                                           Oswego, NY
Sideview of processing block



On the left we have the
conventional bionicfuel unit
separating the volatile
products from the char and
breaking the crystal
structure of the char into a
nano-particle aerosol.

In the middle the
condensers are situated for
water and oil separation
from the volatile particles,
backed by a quench unit.

On the right we find the
high pressure microwave
reactor for hydrogenation of
the char aerosol.




                               2/2013       © 2013 Bionic Fuel Knowledge Partners Inc.,   10
                                                           Oswego, NY
Hydrogen generation
Pictures of a microwave
driven steam/shift reformer.

The process follows:

  CH4+H2O<>CO+3H2,
  dH=+206,2 kJ/mol

and

  CO+H2O<>CO2+H2,
  dH= + 41,2kJ/mol

This unit produces 68% of
hydrogen from conventional
biomass such as wood or
straw. A plasma burner at the
end of the process destroys all
unwanted volatile products and
cleans the remaining gas at
temperatures of 4.000°C.

From 200 kg of biomass
approx. 320 kWh of electric
power can be generated in a
gas-engine which runs on
hydrogen and methane.

This steam reformer is able to
produce sufficient hydrogen for
the microchar facilities. Only a
compressor is required to
increase the hydrogen pressure
to 100 bars for filling the
reaction chambers.




                                   2/2013   © 2013 Bionic Fuel Knowledge Partners   11
                                                      Inc., Oswego, NY
microfuel facility


Three Dimensional view of a
complete plant comprising
of feedstock preparation,
bionicfuel preprocessing
and hydro-processing with a
centralized distillation and
tanks.

On the right a draft of the
control room.




                               2/2013   © 2013 Bionic Fuel Knowledge Partners Inc.,   12
                                                       Oswego, NY
Technical Standards

All Bionic systems comply with the following technical standards:

              DIN EN ISO 9001
              ASME Div 01, Div 02 (AIA TÜV, Germany)
              CE confirmative declaration
              ATEX 94/9/EU explosive protection directive
              Maschinenrichtlinie (machinery directive) 2006/42/EU
              radiation protection of the microwaves by special faraday cages
              double isolation of all oil containing parts
              advanced fire protection system
              hazard protected electronic control equipment
              2nd process emergency control system
              unit fully made of high quality stainless steel
              production and installation certified by German TÜV or SGS




                  2/2013                     © 2013 Bionic Fuel Knowledge Partners Inc.,   13
                                                            Oswego, NY
Stress-approval by CVTS


All parts of the high                               112 MPa


pressure microwave
                                                    152 MPa
                                                    89 MPa


reactors are recalculated by
the CVTS, the Center of
design of forming machines.

The simulation shows the
stress of material when
using high hydrogen
pressure.




                                                                      344 N
                                                                      188 N

                                                                     Gravity          109 MPa
                                                                    9.81 ms-2

                                                                    13 000 N
                                                                     Forbidden
                                                                    rotation and
                                                                   displacement




                               2/2013   © 2013 Bionic Fuel Knowledge Partners Inc.,             14
                                                       Oswego, NY
Hydrogen High Pressure Reactor


Illustration of the
construction process of the
high pressure hydrogen-
microwave reactor vessel.

This type of reactor is
usable for processing of
lignite or anthracite coals
into transportation fuel.

Additionally it can be used
as a stabilization unit for
removing oxygen groups
from bio-crude coming out
of pyrolysis processes.

This increases oil quality
and moves the bio-crude
into ASTM specifications
required by law for sale of
the oil on the market.




                                       High pressure vessels


                              2/2013      © 2013 Bionic Fuel Knowledge Partners Inc.,   15
                                                         Oswego, NY
Electronic parts


Pictures showing segments
of the electric cabinets for
the power supply of the
microwave generators.

PLC Control and sensor
control of the reactor.

On the right you can see
the microwave generators,
adapted for the microwave
reactor.

High frequency circuitry is
not shown.




                               2/2013   © 2013 Bionic Fuel Knowledge Partners Inc.,   16
                                                       Oswego, NY
Construction side in China


A possible location for the
microchar units.

A location outside Ordos,
Mongolia in the Peoples
Republic of China.

On the small picture there is
a gas flare of a recently
installed gasification
system.

Microchar units are
designed to work either
behind a gasification
system, or to utilize the
residue charcoal and
convert it into
transportation fuel.




                                2/2013    © 2013 Bionic Fuel Knowledge Partners Inc.,   17
                                                         Oswego, NY
SMERAL manufacturing




2/2013   © 2013 Bionic Fuel Knowledge Partners Inc.,   18
                        Oswego, NY
SMERAL manufacturing




2/2013   © 2013 Bionic Fuel Knowledge Partners Inc.,   19
                        Oswego, NY
SMERAL manufacturing




2/2013   © 2013 Bionic Fuel Knowledge Partners   20
                   Inc., Oswego, NY
//




  Smeral Brno a.s.                            Bionic Laboratories BLG GmbH
    Krenova 65c                                        Helwigstr. 41
   CZ-65825 Brno                                    64521 Groß-Gerau,
   Czech Republic                                       Germany
 +420-532 167 111                                  +49-1525 33 40 500
  www.smeral.cz                                   www.bionic-world.net




All rights reserved including republishing, patents pending

     2/2013          © 2013 Bionic Fuel Knowledge Partners Inc.,        21
                                    Oswego, NY

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Bionic Carbon Liquefaction Through Microwave Hydration (CTL)

  • 1. Liquefaction of coal into transportation fuel R&D Project Bionic Laboratories BLG GmbH, Germany in cooperation with Smeral Brno a.s. , Czech Republic 2/2013 © 2013 Bionic Fuel Knowledge Partners Inc., Oswego, NY 1 several international patents pending
  • 2. Introduction • Friedrich Bergius (* 11.10.1889, † 31.3.1949) In summer 1913 Bergius discovered the process of converting lignite coal into organic liquids by applying hydrogen at 150 atm pressure and 450 C in an autoclave. His resulting patent was one of the reasons that he received, together with Carl Bosch, the Nobel Price for high pressure hydrogen processing in 1931. • Prof. Dr. Ernst Bayer (*24.3.1927, † 31.1.2002) In 1961 he invented the process of catalytic low temperature depolymerisation of organic substances to liquid fuel using special zeolite catalysts. • Albert Wallace Hull (* 19.4.1880, † 22.11.1966) In 1920 his research resulted in the invention of the magnetron, the electronic device that generates microwaves. At the time Hull anticipated the magnetron would find greater use as an energy converter than in communication applications and radar systems. 2/2013 © 2013 Bionic Fuel Knowledge Partners Inc., 2 Oswego, NY
  • 3. Liquefaction in history After World War I several plants following the Bergius process were built in Germany. These plants were extensively used during World War II to fuel the German Airforce. In the process, dry coal, finely grinded, is mixed with heavy oil recycled from the process. A catalyst is typically added to the mixture. The reaction occurs between 400 °C (752 °F) to 500 °C (932 °F) and 120 to 150 atm pressure in a hydrogen atmosphere. The reaction can be summarized chemically as follows: n C + (n + 1) H2 → CnH2 n + 2 The general mass balance turns out like this: 100 kg of lignite coal plus 40 kg of heavy oil derived from the process plus 5 kg of catalyst @ 450 - 480°C & 120 - 150 atm hydrogen 30 kg light oils + 50 kg heavy oils + 20 kg gas 2/2013 © 2013 Bionic Fuel Knowledge Partners Inc., 3 Oswego, NY
  • 4. Liquefaction in history Between 1952 and 2000 the Bergius-Pier process has been enhanced and optimized in various ways especially in Germany. – Introduction of the combi-cracker technology (1952-1964) (improved catalytic treatment of the gas phase) – Coal Liquifaction plant in Bottrop, Germany 1981-1988 (later used for heavy oil upgrading until 2000) Until today, the Bergius-Pier process demonstrates the highest oil yields (> 60%) in coal liquefaction mode and the highest conversion (>90% of 500+°C) in heavy oil upgrading mode, which consequently also minimizes the CO2 footprint. This is where Bionic picked up the process for a complete redesign based on Bionic‘s specific knowledge base in microwave and catalytic cracking technologies. 2/2013 © 2013 Bionic Fuel Knowledge Partners Inc., 4 Oswego, NY
  • 5. Liquefaction today • Combining the different technologies with a specially developed nano catalyst, modulated microwave generators, and a microwave driven hydrogen gas steam/shift generator, Bionic engineers defined an advanced way for an even more efficient conversion of coal to liquid (CTL): – lowered hydrogen pressure (60-80 atm) – controlled energy application via modulated microwaves – improved synthetic nano catalysts – feedstock preprocessing in Bionic‘s MWDP reactor – continous production capability – preprocessing and activation of nano-coal aerosol through microwaves – Improved product quality by hydrogenation of carbon and parallel depolymerisation of aromatics – Unprocessed char exits as <4nm nano-carbon particles - bionic microchar – a char to fuel process - 2/2013 © 2013 Bionic Fuel Knowledge Partners Inc., 5 Oswego, NY
  • 6. Production Layout Char is processed in a microfuel unit which separating the volatile contents. Intermediate product is a nano-size carbon aerosol which is transported into the high pressure unit. In these vessels the hydrogenation occurs on a microwave heated catalyst-net with hydro- carbons being syntesized. They are forming a mix with heavy oil present in the vessels. This oil-fuel mixture is then separated in a distillation column. The required hydrogen is produced by a biomass steam/shift reformer. 2/2013 © 2013 Bionic Fuel Knowledge Partners Inc., 6 Oswego, NY
  • 7. Single Unit Layout 2/2013 © 2013 Bionic Fuel Knowledge Partners Inc., 7 Oswego, NY
  • 8. Cluster combination Layout A large scale 4 x 4 cluster CTL facility. A single bionicfuel unit converts biomass to fuel for the necessary power production in internal generators. Separated water from the biomass feedstock is used for hydrogen production in steam reformers. Four bionicfuel units perform the preprocessing of the char with attached four hydrogenation units which are responsible for the final liquefaction step. In a large distillation column the lighter products are separated for use as transportation fuel, while the heavy by products are returned to the high pressure vessels. 2/2013 © 2013 Bionic Fuel Knowledge Partners Inc., 8 Oswego, NY
  • 9. Capacities Single liquefaction Unit: 1.000 kg / hr + 110 kg H2 520 kg light oil char @ 33 MJ/kg + 370 kg heavy oil 698 kg heavy oil + 70 kg catalyst 270 kg gas + 320 kWh @430 C 80 kg residues 2/2013 © 2013 Bionic Fuel Knowledge Partners Inc., 9 Oswego, NY
  • 10. Sideview of processing block On the left we have the conventional bionicfuel unit separating the volatile products from the char and breaking the crystal structure of the char into a nano-particle aerosol. In the middle the condensers are situated for water and oil separation from the volatile particles, backed by a quench unit. On the right we find the high pressure microwave reactor for hydrogenation of the char aerosol. 2/2013 © 2013 Bionic Fuel Knowledge Partners Inc., 10 Oswego, NY
  • 11. Hydrogen generation Pictures of a microwave driven steam/shift reformer. The process follows: CH4+H2O<>CO+3H2, dH=+206,2 kJ/mol and CO+H2O<>CO2+H2, dH= + 41,2kJ/mol This unit produces 68% of hydrogen from conventional biomass such as wood or straw. A plasma burner at the end of the process destroys all unwanted volatile products and cleans the remaining gas at temperatures of 4.000°C. From 200 kg of biomass approx. 320 kWh of electric power can be generated in a gas-engine which runs on hydrogen and methane. This steam reformer is able to produce sufficient hydrogen for the microchar facilities. Only a compressor is required to increase the hydrogen pressure to 100 bars for filling the reaction chambers. 2/2013 © 2013 Bionic Fuel Knowledge Partners 11 Inc., Oswego, NY
  • 12. microfuel facility Three Dimensional view of a complete plant comprising of feedstock preparation, bionicfuel preprocessing and hydro-processing with a centralized distillation and tanks. On the right a draft of the control room. 2/2013 © 2013 Bionic Fuel Knowledge Partners Inc., 12 Oswego, NY
  • 13. Technical Standards All Bionic systems comply with the following technical standards: DIN EN ISO 9001 ASME Div 01, Div 02 (AIA TÜV, Germany) CE confirmative declaration ATEX 94/9/EU explosive protection directive Maschinenrichtlinie (machinery directive) 2006/42/EU radiation protection of the microwaves by special faraday cages double isolation of all oil containing parts advanced fire protection system hazard protected electronic control equipment 2nd process emergency control system unit fully made of high quality stainless steel production and installation certified by German TÜV or SGS 2/2013 © 2013 Bionic Fuel Knowledge Partners Inc., 13 Oswego, NY
  • 14. Stress-approval by CVTS All parts of the high 112 MPa pressure microwave 152 MPa 89 MPa reactors are recalculated by the CVTS, the Center of design of forming machines. The simulation shows the stress of material when using high hydrogen pressure. 344 N 188 N Gravity 109 MPa 9.81 ms-2 13 000 N Forbidden rotation and displacement 2/2013 © 2013 Bionic Fuel Knowledge Partners Inc., 14 Oswego, NY
  • 15. Hydrogen High Pressure Reactor Illustration of the construction process of the high pressure hydrogen- microwave reactor vessel. This type of reactor is usable for processing of lignite or anthracite coals into transportation fuel. Additionally it can be used as a stabilization unit for removing oxygen groups from bio-crude coming out of pyrolysis processes. This increases oil quality and moves the bio-crude into ASTM specifications required by law for sale of the oil on the market. High pressure vessels 2/2013 © 2013 Bionic Fuel Knowledge Partners Inc., 15 Oswego, NY
  • 16. Electronic parts Pictures showing segments of the electric cabinets for the power supply of the microwave generators. PLC Control and sensor control of the reactor. On the right you can see the microwave generators, adapted for the microwave reactor. High frequency circuitry is not shown. 2/2013 © 2013 Bionic Fuel Knowledge Partners Inc., 16 Oswego, NY
  • 17. Construction side in China A possible location for the microchar units. A location outside Ordos, Mongolia in the Peoples Republic of China. On the small picture there is a gas flare of a recently installed gasification system. Microchar units are designed to work either behind a gasification system, or to utilize the residue charcoal and convert it into transportation fuel. 2/2013 © 2013 Bionic Fuel Knowledge Partners Inc., 17 Oswego, NY
  • 18. SMERAL manufacturing 2/2013 © 2013 Bionic Fuel Knowledge Partners Inc., 18 Oswego, NY
  • 19. SMERAL manufacturing 2/2013 © 2013 Bionic Fuel Knowledge Partners Inc., 19 Oswego, NY
  • 20. SMERAL manufacturing 2/2013 © 2013 Bionic Fuel Knowledge Partners 20 Inc., Oswego, NY
  • 21. // Smeral Brno a.s. Bionic Laboratories BLG GmbH Krenova 65c Helwigstr. 41 CZ-65825 Brno 64521 Groß-Gerau, Czech Republic Germany +420-532 167 111 +49-1525 33 40 500 www.smeral.cz www.bionic-world.net All rights reserved including republishing, patents pending 2/2013 © 2013 Bionic Fuel Knowledge Partners Inc., 21 Oswego, NY