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WINTER
             Thesis Proposal
                   Template

  Extractive fermentation of succinic acid
  using an external precipitation technique
    การแยกกรดซัก ซิน ิก ควบคู่ก ับ กระบวนการหมัก
ด้ว ยเทคนิค การตกตะกอนนอกถัง หมัก

                   Asst. Prof. Apichat Boontawan
                  Jiraphorn Lubsungnoen M5430116
Content          01
      WINTER
•Background
         Template
•Research Objective
•Research Hypothesis
•Experimental
  - Material & Method
 - Experimental setup
•Expected Result
•Research Plan
Background            02
               WINTER
- Currently, the interest on development of
                  Template
biodegradable plastic since global warming
             problem has come.


- Succinic acid (SA) is promising chemical
  which has a wide range of applications
            in many industries.
Background   03
WINTER
Template
Background          04
                WINTER
- SA can be used as a precursor for synthesis
                  Template
  biodegradable plastic such as polybutyrate
  succinate (PBS) and polyamide to produce
                 bioplastics.
Background            05
                 WINTER
-Thailand is a large producer of raw material
                    Template
 to produce SA such as casava and sugar
cane

- Therefore, the country has high potential for
development of SA production in order to
support bioplastic industry.
Background            06
- Commercial scale production of SA is
petroleum-derived.

-However, Fermentative production of SA
from renewable resource has received
increasing interest .

- SA can be produced by microbial
fermentation using various microorganism.
Background             07
-SA is a common intermediate in the metabolic
                  Template
path way of several anaerobic and facultative
microorganism .


-Those organisms suitable for the efficient
production of SA can be categorized into
bacteria.
Background   08
Template
Background            09
- Many different microorganism have been
                Template
  screened and studied for SA such as ;

      - Actinobacillus succinogenes,
- Anaerobiospirillum succiniciproducens,
  - Mannheimia succiniciproducens and
     - Recombinant Escherichia coli.
Background              10
-Bio-based SA is potential substitute for
                  Template
the current petroleum-based process.

-However, compared with petrochemical-
derived SA , biological SA production is still
 not economically competitive .

-Because of its major draw backs:
low product concentration in fermentation
broth and difficult product recovery.
Background                  11
                 WINTER
-In addition, product inhibition is important
                   Template
factor for bioprocess development .


-The product inhibition effect, which can be
described by specific growth rate equation

                                                    ai
                   S                     P 
  v = v max  '                     ∏ 1 − ' 
             S     (
             K + S + S2 /K'
                           i   )   
                                    
                                     
                                         P 
                                             m 
                                                
Background           12
                  WINTER
- The cost of downstream processing can
  make a very high Template total production
                   portion in the
  cost, more than 50% .



- It is necessary to reduce the production cost
  of fermentation process in order to increase
  its competitiveness with that of petrochemical
  process.
Background        13
                WINTER
-The separation methods studied for SA
                 Template
recovery mainly include ;

-Direct crystallization,
-Precipitation,
-Membrane separation,
-Extraction,
-Chromatography,
-In situ separation.


.
Background   14
WINTER
Template
Background               15
                WINTER
-Formation of byproduct is a major problem
                  Template
that has to be solved because it reduces
SA yield and productivity, while increases
the complexity and cost of SA recovery .


-In situ product removal or extractive
fermentation can be solved the
aforementioned problem.

.
Background             16
                WINTER
- The advantage of in situ process
                  Template
separation that can be improved the final
SA
. concentration and reduces end-product
inhibition.

-Precipitation process is a very interesting
technique due to its simplicity, and no does
not require additional chemical or unit
operation.
Background           17
   -This work, fermentation of SA will used
commercial strain of SA producing bacteria
and using precipitation technique couple with
fermentation SA .


  -Calcium carbonate will be used to control the
pH of the broth.
Background             18
    - Submerge ceramic microfiltration membrane
will be employed for take out the clarified broth
prior to precipitation.

   -As a result, Calcium succinate will be
precipitate out , the remaining will then be
re-circulated back into the fermenter.

  -The precipitate will be harvested ,washed
and dried to produce a high purity calcium
succinate
Research Objectives         19
-To study the precipitation process of
calcium succinate by using synthetic
solution.


-To compare SA production performance in
term of yield and volumetric productivity
between this work and conventional batch
fermentation.
Research Objectives    20

-To obtain a high purity of calcium
succinate powder which facilitates
subsequent downstream processing.
Research Hypothesis         21
- SA can be produced by using
Actinobacillus succinogenes ATCC
55618.

- Precipitation of calcium succinate can
be achieved in the precipitation tank.

- Product inhibition can be minimized and
SA production is significantly increased.
Materials            22
-Actinobacillus succinogenes
ATCC 55618

- Glucose        - Calcium carbonate

- Autoclave     - 5 L Bioreactor

- HPLC         - Glucose analyzer
Methods                        23




- Fermentation will be carried out in the absence of oxygen by
flushing CO2 gas at the beginning of fermentation
Methods   24
Methods/ Batch fermentation   25
Methods/ Fed batch fermentation             26
 - Fed batch fermentation will be started with
1.2 L of culture medium and the concentrated
culture medium will be gradually added.

 - pH of broth will be controlled at 6.8

  - Batch fermentation will be carried out first,
feeding of the concentrated culture medium will be
started when amount of glucose is nearly depleted
or lower than 20 g.L-1.
Experimental setup           27
Experimental setup for extractive fermentation
of SA using external precipitation method.




                                    Calcium succinate
Analytical procedure   28
    WINTER
      Template
Analytical procedure            29
               WINTER
-Reducing sugar will be measured by
                  Template
Dinitrosalicylic (DNS) method according
to Miller (1995)

- Cell concentration will be determined by
using UV–VIS Spectrometer. Cell viability
 will be accomplished using fluorescence
microscopy.

- Quantitative analysis of organic acids will
be analyzed by HPLC .
Expected results          30
           WINTER
             Template
1.High yield and volumetric productivity
of succinic acid will be achieved using
the external precipitation method.


2.This simple high efficiency method
can be applied to pilot scale production
of succinic acid.
Research plan
                31
   WINTER
    Template
WINTER
      Template

THANK YOU VERY MUCH


      Jiraphorn Lubsungnoen   M5430116
Extractive fermentation of succinic acid using an external precipitation technique
Extractive fermentation of succinic acid using an external precipitation technique
Extractive fermentation of succinic acid using an external precipitation technique

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Extractive fermentation of succinic acid using an external precipitation technique

  • 1. WINTER Thesis Proposal Template Extractive fermentation of succinic acid using an external precipitation technique การแยกกรดซัก ซิน ิก ควบคู่ก ับ กระบวนการหมัก ด้ว ยเทคนิค การตกตะกอนนอกถัง หมัก Asst. Prof. Apichat Boontawan Jiraphorn Lubsungnoen M5430116
  • 2. Content 01 WINTER •Background Template •Research Objective •Research Hypothesis •Experimental - Material & Method - Experimental setup •Expected Result •Research Plan
  • 3. Background 02 WINTER - Currently, the interest on development of Template biodegradable plastic since global warming problem has come. - Succinic acid (SA) is promising chemical which has a wide range of applications in many industries.
  • 4. Background 03 WINTER Template
  • 5. Background 04 WINTER - SA can be used as a precursor for synthesis Template biodegradable plastic such as polybutyrate succinate (PBS) and polyamide to produce bioplastics.
  • 6. Background 05 WINTER -Thailand is a large producer of raw material Template to produce SA such as casava and sugar cane - Therefore, the country has high potential for development of SA production in order to support bioplastic industry.
  • 7. Background 06 - Commercial scale production of SA is petroleum-derived. -However, Fermentative production of SA from renewable resource has received increasing interest . - SA can be produced by microbial fermentation using various microorganism.
  • 8. Background 07 -SA is a common intermediate in the metabolic Template path way of several anaerobic and facultative microorganism . -Those organisms suitable for the efficient production of SA can be categorized into bacteria.
  • 9. Background 08 Template
  • 10. Background 09 - Many different microorganism have been Template screened and studied for SA such as ; - Actinobacillus succinogenes, - Anaerobiospirillum succiniciproducens, - Mannheimia succiniciproducens and - Recombinant Escherichia coli.
  • 11. Background 10 -Bio-based SA is potential substitute for Template the current petroleum-based process. -However, compared with petrochemical- derived SA , biological SA production is still not economically competitive . -Because of its major draw backs: low product concentration in fermentation broth and difficult product recovery.
  • 12. Background 11 WINTER -In addition, product inhibition is important Template factor for bioprocess development . -The product inhibition effect, which can be described by specific growth rate equation ai  S   P  v = v max  '  ∏ 1 − '   S (  K + S + S2 /K' i )      P  m  
  • 13. Background 12 WINTER - The cost of downstream processing can make a very high Template total production portion in the cost, more than 50% . - It is necessary to reduce the production cost of fermentation process in order to increase its competitiveness with that of petrochemical process.
  • 14. Background 13 WINTER -The separation methods studied for SA Template recovery mainly include ; -Direct crystallization, -Precipitation, -Membrane separation, -Extraction, -Chromatography, -In situ separation. .
  • 15. Background 14 WINTER Template
  • 16. Background 15 WINTER -Formation of byproduct is a major problem Template that has to be solved because it reduces SA yield and productivity, while increases the complexity and cost of SA recovery . -In situ product removal or extractive fermentation can be solved the aforementioned problem. .
  • 17. Background 16 WINTER - The advantage of in situ process Template separation that can be improved the final SA . concentration and reduces end-product inhibition. -Precipitation process is a very interesting technique due to its simplicity, and no does not require additional chemical or unit operation.
  • 18. Background 17 -This work, fermentation of SA will used commercial strain of SA producing bacteria and using precipitation technique couple with fermentation SA . -Calcium carbonate will be used to control the pH of the broth.
  • 19. Background 18 - Submerge ceramic microfiltration membrane will be employed for take out the clarified broth prior to precipitation. -As a result, Calcium succinate will be precipitate out , the remaining will then be re-circulated back into the fermenter. -The precipitate will be harvested ,washed and dried to produce a high purity calcium succinate
  • 20. Research Objectives 19 -To study the precipitation process of calcium succinate by using synthetic solution. -To compare SA production performance in term of yield and volumetric productivity between this work and conventional batch fermentation.
  • 21. Research Objectives 20 -To obtain a high purity of calcium succinate powder which facilitates subsequent downstream processing.
  • 22. Research Hypothesis 21 - SA can be produced by using Actinobacillus succinogenes ATCC 55618. - Precipitation of calcium succinate can be achieved in the precipitation tank. - Product inhibition can be minimized and SA production is significantly increased.
  • 23. Materials 22 -Actinobacillus succinogenes ATCC 55618 - Glucose - Calcium carbonate - Autoclave - 5 L Bioreactor - HPLC - Glucose analyzer
  • 24. Methods 23 - Fermentation will be carried out in the absence of oxygen by flushing CO2 gas at the beginning of fermentation
  • 25. Methods 24
  • 27. Methods/ Fed batch fermentation 26 - Fed batch fermentation will be started with 1.2 L of culture medium and the concentrated culture medium will be gradually added. - pH of broth will be controlled at 6.8 - Batch fermentation will be carried out first, feeding of the concentrated culture medium will be started when amount of glucose is nearly depleted or lower than 20 g.L-1.
  • 28. Experimental setup 27 Experimental setup for extractive fermentation of SA using external precipitation method. Calcium succinate
  • 29. Analytical procedure 28 WINTER Template
  • 30. Analytical procedure 29 WINTER -Reducing sugar will be measured by Template Dinitrosalicylic (DNS) method according to Miller (1995) - Cell concentration will be determined by using UV–VIS Spectrometer. Cell viability will be accomplished using fluorescence microscopy. - Quantitative analysis of organic acids will be analyzed by HPLC .
  • 31. Expected results 30 WINTER Template 1.High yield and volumetric productivity of succinic acid will be achieved using the external precipitation method. 2.This simple high efficiency method can be applied to pilot scale production of succinic acid.
  • 32. Research plan 31 WINTER Template
  • 33. WINTER Template THANK YOU VERY MUCH Jiraphorn Lubsungnoen M5430116

Notas del editor

  1. This figure show various chemical and products that can be synthesized from SA SA can be use as a precursor of many industries such as food industry, pharmaceuticals industry ,agriculture industry, surfactant ,detergent green solvent especially biodegradable plastic.
  2. This figure show Catabolic pathway leading to synthesis of SA .Bacteria mainly utilize the phosphoenolpyruvate (PEP) carboxylation reaction . 5 key enzyme are responsible for SA production including PEPCK, MDH, Menz,Fm, and Frd
  3. -Different technique have been introduce for recovery technique .
  4. A. succinogenes ATTC 55618 from American Type Culture Collection (USA) Glucose as carbon source Calcium carbonate as the neutralizer Autoclave 5 L Bioreactor for fermentation High performance liquid chromatography (HPLC) Glucose analyzer
  5. Fed batch fermentation will be started with 1.2 L of culture medium and the concentrated culture medium (7  glucose concentration) will be gradually added. The pH of broth will be controlled at 6.8 throughout the fermentation period. Batch fermentation will be carried out first, feeding of the concentrated culture medium will be started when amount of glucose is nearly depleted or lower than 20 g.L -1 .