Degradation of amines in CO2Capture

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    Degradation of amines

    in CO2 Capture

    Gary T. Rochelle, Stephanie Freeman, Alex Voice,Fred Closmann

    Luminant Carbon Management Program

    The University of Texas at Austin

    Presented at

    TCCS-6

    June, 2011

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    Messages

    Stripper energy use is constrained by the maxT permitted by thermal degradation

    TMEA < TMDEA Tertiary > Piperazine

    Amine degradation must be minimized to

    manage secondary environmental impact. Volatile Products can leave with flue gas

    Nonvolatile products make up reclaimer waste

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    Where is degradation most likely to occur?

    Flue Gas

    10% CO25-10% O2

    Purified Gas

    1% CO2

    30% MEA

    = 0.4-0.5

    1 mM Fe+3

    CO2

    H2O(O2)

    30% MEA

    = 0.3-0.4

    Reboiler

    Absorber

    40 -70 oC

    1 atm

    Stripper

    120 oC

    1 atm

    Cross

    Exchanger

    Oxidative

    Degradation

    Thermal Degradation

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    Thermal Degradation

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    180

    240

    300

    360

    5 10 15 20 25 30 35

    Wtotal(kW

    h/tonneC

    O2)

    (HCO2-HH20)(1/T) (kJ/gmol-K)

    HCO2=60 kJ/mole

    70

    80

    erma egra a on m s s r pperperformance because

    Greater Tstrip & HCO2 reduce Weq

    MEA 120 C

    PZ

    Single stage flash at 90-150CCompression to 150 bar

    Lean PCO2 = 0.5 kPa at 40C

    90 C 150 C

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    5 Mechanisms for Thermal Degradation

    1. Carbamate Polymerization - MEA

    2. Cyclic Urea - Ethylenediamine

    3. Arm Switching/Elimination - Tertiary Amine 4. SN2 Ring Opening Piperazine

    5. Blend Synergism Piperazine/MEA

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    Carbamate Polymerization

    MEA Carbamate Oxazolidone

    MEA HEEDA

    NHOH CO

    2-

    NHO

    O

    + O-

    H

    NHO

    O

    OHNH2 + OH

    NHNH

    2 +

    O

    O

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    Primary & Secondary Alkanolamines Deg T

    Amine k1 = 2.91 10-8 s-1 Structure T (oC)

    2-methyl-aminoethanol 103

    Monoethanolamine 120

    3-amino-propanol 126

    2-piperidine ethanol 127

    Diglycolamine 133

    2-methyl-2-amino-propanol 137

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    Cyclic urea

    NH2

    NH2 + O O

    O

    NHNH

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    1o & 2o Diamines = cyclic ureas Deg TAmine Structure T (oC)

    Dimethylethylenediamine 100

    Diethylenetriamine 105

    Methylaminopropanolamine 114

    Hydroxyethylethylenediamine 114

    Ethylenediamine 121

    Hexamethylenediamine 156

    CH3

    NH

    NH

    CH3

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    2 Tertiary Quaternary + Secondary

    +

    CH3

    OH

    N

    OH

    CH3

    OH

    NH+

    OH

    + OHNH

    OH

    CH3

    CH3

    OH

    N+

    OH

    Tertiary1 + Secondary2 Tertiary2+ Secondary1

    Tertiary1 + Quaternary2 Tertiary2+ Quaternary1

    Elimination

    CH3

    CH3

    OH

    N+

    OH

    +

    +CH3

    CH3

    OH

    NH+

    OH

    OH

    OH2

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    3o amines2o amines + other 3o aminesAmine Structure T (oC)

    Dimethylmonoethanolamine 122

    Tetramethylethylenediamine 125

    Methyldiethanolamine 128

    N-(2-Hydroxyethyl)PZ 132

    N,N-Dimethylpiperazine 139

    1-methyl-piperazine 148

    CH3 N N CH3

    CH3

    CH3

    N

    CH 3

    CH3N

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    Ring Opening

    NH NH2

    +

    NH

    NH

    N NH3

    +

    NH NH +

    NH2

    O

    OH NH O + OH2

    Ring Closing

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    Cyclic LinearAmine Structure T (oC)

    Diglycolamine 133

    Homopiperazine 133

    Pyrrolidine 135

    2-Methyl-Piperazine 152

    Hexamethylenediamine 156

    Piperazine 162

    Morpholine 169

    CH3

    NH

    NH

    NH NH

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    Interactive Blends Carbamate Polymerization

    NHNH

    NH

    O O+ N

    NH

    NH

    OH

    O

    +

    + OHNH

    2

    +

    OH

    NHNH NH

    +

    OH OH

    NNH

    Secondary2 + Tertiary1 Tertiary2+ Secondary1

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    Total Amine Loss in BlendsAmine (m) Structure T (oC)

    MEA/PZ 104

    MEA/AMP 123

    4 AMP/6 PZ 135

    7 MDEA/2 PZ 138

    4 PZ/4 2MPZ 155

    3.9 PZ/3.9 1MPZ/

    0.2 14DMPZ

    160

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    Oxidation

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    O2 solubility & Mass Transfer

    0,E+0

    2,E-5

    4,E-5

    6,E-5

    2,E-04 2,E-03 2,E-02

    Amine

    Oxidation(m

    ol/molCO2)

    Oxygen Rate Constant (s-1)

    Total

    AbsorberExchanger

    Sump

    PZMEAMDEA

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    Degradation Products and

    Environmental Impact

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    7 m MDEA/2 m PZ Oxidized at 120oC

    Products (CO2 carrying)

    C-Loss

    (%)Diethanolamine/Methylaminoethanol 40

    1-methyl PZ 8.4

    1,4-Dimethyl PZ 0.9Aminoethyl PZ 3.5

    N-formyl PZ (amide) 8.3

    Formate & other acids 2.5Bicine 5.3

    Hydroxyethyl sarcosine 10.5

    ~79.5

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    Message on Thermal Degradation

    Stripper energy is constrained by the max Tpermitted by Degradation

    Linear alkanolamines and diamines degrade

    by polymerization & urea formation at 100-130oC

    Tertiary amines degrade by arm switching &

    elimination at 120-140o

    CPiperazine and related cyclic amines degrade

    by ring opening at 150-165oC.

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    Message on Oxidation

    As amines become more resistant, oxidation

    shifts from the absorber to the heat exchanger

    MEA & alkanolamines readily oxidize in the

    absorber unless inhibited by radical or

    peroxide scavengers

    Tertiary amines inhibit self oxidation,

    probably by scavenging peroxides

    Piperazine oxidizes only at the higher T of

    the heat exchanger exit

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    Message on Environmental Impact

    Amine degradation must be minimized tomanage secondary environmental impact.

    Volatile Products can leave with flue gas Aldehydes, formate, ammonia, volatile amines,

    amides

    Nonvolatile products make up reclaimer

    waste Polyamines, Cyclic urea, amino acids

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    A review of previous Work

    University of Texas

    Thermal: Austgen, Freeman, Closmann

    Oxidation: Goff, Sexton, Voice

    IFP Thermal, Oxidation

    Lepaumier, Carrette, et al.

    NTNU Thermal, oxidation

    Lepaumier, Eide-Haugm, et al.