Ing. Bioquimica

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    Here are some products of White Biotechnology

    Transportation fuels

    New intermediates for the bulk chemical industry New food and feed

    And the technology isFermentation and Bio-catalysis

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    Transportation fuels

    Bio-ethanol

    Bio-butanol Bio-diesel

    Ethanol can be used in mixtures with gasoline in up to 85 % by

    volume. In Brazil 40 % of all private cars drive on 85 % ethanol, theremainder on 25 % ethanol.

    Brazil, USA, India, and perhaps Australia and Thailand will be able tomake bioethanol as cheap as gasoline.

    Butanol can be used by all cars, alone or in mixtures with gasoline. Itis (as yet) more expensive than ethanol.

    England and perhaps other EU countries) and USA are comitted toproduce bio-butanol

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    Production methods for bio-fuels

    Bio-ethanol is produced by fermentation from

    1. Cane sugar or starch (first generation processes)2. Cellulosic material (second generation processes)

    First generation processes: Sugar is fermented using yeastor bacteria (Saccharomyces cerevisiae, Zymomonas sp.)

    Starch is hydrolysed to glucose and used as above

    Second generation processes: Straw, wood chips etc, arehydrolyzed to glucose and other sugars. Thereaftertreated as in First generation processes

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    Production methods for bio-fuels

    Bio-butanol is produced from sugar, household waste or

    some other carbon source.Here the bacterium Clostridium acetobutylicumis used

    About 50 % of the sugar can be converted to butanol,another 25 % to acetone and the remainder to biomassand ethanol.

    The price of butanol is 1100 US$ per ton

    The world market is about 1.3 million tons/year

    BP and DuPont are comitted to produce bio-butanol onthe British market by 2007

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    Production methods for bio-fuels

    Bio-diesel is produced from animal fat (lard) or from

    vegetable oil (e.g. rape seed oil) using a catalytic trans-esterification process (acid, base or enzymes)

    Glycerol-fatty acid + CH3OHMe-fatty acid + glycerol

    A methanol based bio-diesel is very similar to high gradeoil-derived diesel, but no sulphur, less NOx etc.

    This could be a fine outlet for a large MeOH-production!

    As a byproduct glycerol is formed. This could be thestarting point for a chemistry based on glycerol

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    The new raw materials for production of chemicals

    Glucose

    Either directly or derived from starch or cellulosic material

    Polymers (poly-lactic acid, poly-esters)

    Solvents (butanol, acetone etc)

    Pharmaceuticals (antibiotics, proteins and hormones, therapeuticamino-acids, and many others)

    Foods and food ingredients (new sugars, dairy products, citric acid,lactic acid, emulsifiers, thickeners, pro-biotic diets)

    - or glucose can be converted to another compound whichcan serve as starting point for a family of chemicals

    Succinic acid, (CH2 COOH)2, is a good example.

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    Glucose as progenitor of families of chemicals

    Succinic acid

    C6H12O6 + 2 H2 + 2 CO2 2 (CH2COOH)2 + 2 H2O

    Lactic acid

    C6H12O6 2 C3 H6 O3 (formula: CH3-CHOH-COOH)

    1,3 propane diol

    C6H12O6 + 4 H2 2 C3H8O2 + 2 H2O (formula: CH2OH - CH2- CH2OH)

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    Which disciplines are needed to work in Biotechnology?

    Fundamental Bio-Sciences

    Microbiology and Biochemistry

    a. The functioning of the living cell: DNA, RNA, Proteins Growth

    b. The Chemistry of Life: Pathways, Metabolites, Energy

    Applied Physics and Mathematics as in Chemical EngineeringThe conceptof model-driven experimental science

    a. Steady- and unsteady state Pathway Fluxes

    b. The interpretation of large amounts of uncertain data

    Design and optimization of large-scale processes

    a. Reactor design and design of separation processes.

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    Illustrative Examples

    Lactobionic Acid

    Lactose (Galactose-Glucose) + O2 Lactobionic Acid

    A chemical reaction in H2

    O at 38 oC using a commercial enzyme

    Method of investigation:

    a. Find the kinetics of the reaction as a function of [O2] and [Lactose]

    b. Run Pilot Plant experiments to find influence of O2 transfer

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    Why would we make lactobionic acid?

    Because we wish to find use of a byproduct from cheese production

    A normal size cheese factory produces per hour 15 m3 waste water

    with 4.5 wt % lactose. Why pay to clean it up?

    Because we find many applications for Lactobionic acid, once acheap production method has been developed

    Lactobionic acid is an excellent chelating compound, i.eit bindsmetal ions: This property can be used to

    a. make functional foods (e.g with a high Ca-content)

    b. make new detergents without polyphosphates (added to prevent

    the formation of C-soaps when using hard water, but givesterrible pollution problems due to discharge of phosphates)

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    Excerpts from the laboratory scale investigation (1 L):

    The enzyme deactivates when strong base is used to keep pH constantThe rate is virtually independent of the lactose concentration.

    0

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    0 1 2 3 4 5 6 7 8

    Time (h)

    Baseadditionrate(mmol/h)

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    Production of LBA in 600 L tank using RJHThe laboratory results are confirmedWe can provide a sufficient O2 transport

    0 2 4 6 8 10 120

    1

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    y2=1.1059x-5.502

    R2=0.9999

    y1=0.2021x+0.095

    R2=0.9987

    Totalbase

    added

    [k

    g]

    Time [hr]

    0 2 4 6 8 10 12

    0

    20

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    Middle

    Bottom

    Loop

    Dissolvedoxygentension[%]

    Time [hr]

    Airflow 100 L min-1

    10 L min-1

    DO measured in system

    10 L min-1 100 L min-1

    Red : DO in loop

    Green orblue: DO in tank

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    Fast recirculation ofliquid back to the

    V = 3.4 m3 tank.

    Gas and substrate areadded in the loop.

    A plate-type heatexchanger w ith U ~5000 W m-2 C-1 is partof the loop.

    Gas

    Rotary jet head

    Bulk mixing in a more effective way

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    Gearing

    Nozzle diameter,d = 10mm

    The rotary jet head

    IM20 is a 4 nozzle jet headwhich gives a 3-D flow pattern

    Pressure energy is convertedinto kinetic energy

    The functioning of Rotary Jet Heads

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    The production of Single Cell Protein from Methane or Methanol

    Why would this process be contemplated?

    1. Most animals require a diet with both plant- and animal protein

    2. Animal protein (fish-meal) is rapidly becoming expensive

    3. The protein obtained from SCP production is animalprotein

    4. The price of fish-meal is now 1200 US $/ ton up from 700US $/ ton in mid 2006.

    5. SCP from CH4 or CH3OH is indistinguishable from fish-meal

    6. Natural microorganisms (no GMO) are used.

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    Methylococcus capsulatuswith membranes of the crucial enzymeMethane-monooxygenase

    CH4 + H 2 + O2 CH3OH + H2O

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    .more on the biochemistry ofMethylococcus capsulatus

    The Methanol produced from methane is dehydrogenated

    CH3OH HCHO (formaldehyde) + H2

    Formaldehyde is oxidized to CO2 to create energy (ATP)

    - or it is used together with NH3 and minerals to build cellmass.

    HCHO + O2 CO2 + H2O

    HCHO + NH3 + P + S +.. Protein, lipids, carbohydrates +

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    Some numbers on Carbon and Oxygen demand for SCP

    From 1.25 kg methane one obtains 1 kg biomassThis corresponds to 1 kg biomass per 1.75 N m3 methane

    or Ysx = 0.520 C-mole biomass per mole methane

    The O2 demand is (8 0.5204.20) / 4 = 1.45 mol O2 per CH4or 2.53 N m3 O2 / kg biomass = 3.62 kg O2 / kg biomass.

    Stoichiometry of methane conversion to biomass:CH4 + 1.45 O2 + 0.104 NH3 0.52 CH1.8O0.5N0.2 + 0.48 CO2 + 1.69 H2O

    .

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    Some process conditions

    1. Continuous fermentation at 45 oC and 1-3 bar

    pressure (to improve mass transfer of gases to liquid)

    2. The flow rate of liquid through the reactor is

    1 volume/ volume reactor /5 hours (D = 0.2 h-1)

    3. The gas flow rate is much, much higher

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    500 L pilot fermentor (height 6.5 m) used at DTU

    6

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    89

    11

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    66

    1111

    44

    1122

    55

    77

    1010

    33

    1010

    8899

    1111

    1111

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    250 m3 reactor (9000 t / year SCP) in Norway