MAPA and DEEA MAPA with and without CO2 Loading · Aqueous solutions of DEEA‐MAPA with different...

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Freezing Point Depression of Aqueous Solutions of DEEA Freezing Point Depression of Aqueous Solutions of DEEA, MAPA and DEEAMAPA with and without CO 2 Loading Muhammad Waseem Arshad Muhammad Waseem Arshad Supervisor: Assoc. Prof. Kaj Thomsen 2nd ICEPE, 2022 June, 2011

Transcript of MAPA and DEEA MAPA with and without CO2 Loading · Aqueous solutions of DEEA‐MAPA with different...

Page 1: MAPA and DEEA MAPA with and without CO2 Loading · Aqueous solutions of DEEA‐MAPA with different molar ratios 270 275 265 r ature (K) 255 260 ng Tempe DEEA DEEA/MAPA 5:1 DEEA/MAPA

Freezing Point Depression of Aqueous Solutions of DEEAFreezing Point Depression of Aqueous Solutions of DEEA, MAPA and DEEA‐MAPA with and without CO2 Loading 

Muhammad Waseem ArshadMuhammad Waseem Arshad

Supervisor: Assoc. Prof. Kaj Thomsen

2nd ICEPE, 20‐22 June, 2011

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PRESENTATION OUTLINE

IntroductionIntroduction

Materials

i h iReaction Mechanism

Experimental Methodp

Results

ConclusionsConclusions

Future Work

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INTRODUCTION

Freezing Point Depression:The phenomenon in which the freezing point of a LiquidThe phenomenon in which the freezing point of a Liquid(Solvent) is depressed when another compound is added in it.This means that the solution has lower freezing than the purelsolvent.

Why we need Freezing Point Depression Data???Why we need Freezing Point Depression Data???We want to model H2O‐DEEA‐MAPA‐CO2 systemWater activity is a key parameter for the amount of water

t d i th d bevaporated in the desorberLow water activity means less evaporation of water in thedesorber and low energy consumption during solventregenerationWater activity can be determined very accurately fromFreezing point data

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g p

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MATERIALS

2‐(Diethylamino)‐ethanol   OR   DEEA   (99%)l li id i h li h ll lClear liquid with light yellow colour

Freezing point = ‐70 oC

Boiling point = 163 oC g p

pH = 11.5 at 100 g/l at 20 oC 

Completely soluble in water

3‐(Methylamino)propylamine   OR   MAPA   (97‐98%)Clear and colourless liquid

Freezing point = ‐72 oC

Boiling point = 140 oCBoiling point = 140 oC

pH = 13.5 at 100 g/l at 20 oC

Completely soluble in water

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REACTION MECHANISM

2‐(Diethylamino)‐ethanol   OR   DEEA 2 5 R C HR CH CH OH

= −′ = − 2 2

2

DEEA

R CH CH OHR R N

=′∴ =

( )2 2 2 2 3 1R R N H O CO R R N H HCO+ −′ ′+ + → +

Base catalytic effect on hydration of CO2

( )

( )2 2 2 1R R N CO R R NCOO a−′ ′+ ↔Zwitterion mechanism

( )( )

2 2 2

2 2 2 3

1

1

R R N CO R R NCOO a

R R NCOO H O R R N H HCO b− + −

+ ↔

′ ′+ → +

( )2 3 2CO OH HCO− −+ ↔Following reactions may also take place simultaneously

( )2 2 3 3CO H O HCO H− ++ ↔ +

[Ref] Vaidya, P. D.; Kenig, E. Y. A Study on CO2 Absorption Kinetics by Aqueous Solutions of N,N‐Diethylethanolamine and N Ethylethanolamine Chem Eng Technol 2009 32 No 4 556 563

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Diethylethanolamine and N‐Ethylethanolamine. Chem. Eng. Technol. 2009, 32, No. 4, 556‐563

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REACTION MECHANISM

3‐(Methylamino)propylamine   OR   MAPA

P t ti

3 6 3

2

and MAPA

R C H R CHH NRR NH

′= − = −′∴ =

( )( )

2 2 2

2 3

Protonation: 1

2

H NRR NH H H NRR NH

H NRR NH H H NRR NH

+ +

+ +

+ ↔′ ′

+ ↔′ ′ 8 Possible( )2 3

2 3 2 2 H NRR NH H H NRR NH+ + ++ ↔′ ′ ( ) 38 Possible species of MAPA

( )( )

2 2 2

2 2

Carbamate: 4

5H NRR NH CO H NRR NCOO HH NRR NH CO OOCHNRR NH H

− +

− +

+ ↔ +′ ′

+ ↔ +′ ′ ( )( )

2 2

2 2

5 2 2 6

H NRR NH CO OOCHNRR NH HH NRR NH CO OOCHNRR NCOO H− − +

+ ↔ +

+ ↔ +′ ′

2

Protonated Carbamate:H ( )

( )3 7

8NRR NCOO H H NRR NCOO

OOCHNRR NH H OOCHNRR NH

− + + −

− + − +

+ ↔′ ′

+ ↔′ ′

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( )2 8OOCHNRR NH H OOCHNRR NH+ ↔

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EXPERIMENTAL METHOD

A, Thermostatic bath with ethanol 

B, Cooling jacket 

C, Sample glass with magnetic

stirrer 

D, Rubber stopper with sample

glass lidglass lid 

E, Device for manual stirring 

F, Controlled temperature ethanol

bath with magnetic stirrer 

G, Pt100 Thermometer 

H, Data acquisition unit 

Experimental Setup[Ref] Fosbøl, P. L.; Pedersen, M. G.; Thomsen, K. Freezing Point Depressions of Aqueous MEA, MDEA, and MEA‐

d h h l h h f

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MDEA Measured with a New Apparatus. J. Chem. & Eng. Data 2010, Special Issue: John M. Prausnitz Festschrift

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EXPERIMENTAL METHOD

Measured Freezing Point

Heat of Crystallisation

Crystallisationy

[Ref] Fosbøl, P. L.; Pedersen, M. G.; Thomsen, K. Freezing Point Depressions of Aqueous MEA, MDEA, and MEA‐d h h l h h f

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MDEA Measured with a New Apparatus. J. Chem. & Eng. Data 2010, Special Issue: John M. Prausnitz Festschrift

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RESULTS

Aqueous solutions of DEEA and MAPA

270

275

K)

265

erature   (K

255

260

zing

 Tem

pe

DEEA

250Freez

MAPA

245

0 2 4 6 8 10 12

Solvent Molality   (mole / kg water)

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RESULTS

Aqueous solutions of DEEA‐MAPA with different molar ratios

270

275

265

rature   (K)

255

260

ng Tem

per

DEEA

DEEA/MAPA 5:1

DEEA/MAPA 3:1

250Freezi DEEA/MAPA 1:1

DEEA/MAPA 1:3

DEEA/MAPA 1:5

MAPA

245

0 10 20 30 40 50 60

Solvent Mass Percent

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Solvent Mass Percent

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RESULTS

Aqueous solutions of MAPA loaded with CO2

270

272

266

268

rature  (K)

262

264

ng Tem

per

258

260

Freezi 10% MAPA

20% MAPA

27% MAPA256

0 0,2 0,4 0,6 0,8 1 1,2 1,4 1,6 1,8

CO2 Loading   (mol CO2 / mol MAPA)

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RESULTS

Aqueous solutions of DEEA loaded with CO2

271

272

)

269

270

erature  (K

)

267

268

zing

 Tem

pe

265

266Freez

12% DEEA

20% DEEA

0 0,2 0,4 0,6 0,8 1

CO2 Loading (mol CO2 / mol DEEA)

Work in Progress for 30% 

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and 35% DEEA solutions 

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CONCLUSIONS

Freezing point depression (FPD) are measured for H2O‐DEEAd O d l f O f diff land H2O‐MAPA and also for H2O‐DEEA‐MAPA for different molar

ratios of DEEA/MAPA [Data point = 76]

FPD are measured for H2O‐DEEA‐CO2 and H2O‐MAPA‐CO2systems at different CO2 loading [Data points = 57]systems at different CO2 loading [Data points 57]

Measured freezing point data illustrates that the MAPA‐watereasu ed ee g po t data ust ates t at t e ateinteraction is stronger than DEEA‐water interaction

The measured data can be used for modeling CO2 absorption/desorption system when aqueous blend of DEEA/MAPA is used

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FUTURE WORK

Measurement of FPD for 30% and 35% DEEA solutions withdifferent CO2 loadings

Measurement of freezing points For aqueous solutions of DEEA‐MAPA with different molar ratios loaded with CO2

Development of correlations for the freezing points as afunction of the solution compositionp

Thermodynamic modeling of H2O‐DEEA‐MAPA‐CO2 system usingy g 2 2 y gExtended UNIQUAC model

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THANK YOUTHANK YOU FOR 

YOUR ATTENTION

QUESTIONS ?????

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