Miho Nitta a, Masaki Hirose a, Toru Abe a, Yukio Furukawa a, *, Hiroshi Sato b, Yasuro Yamanaka c

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Available online at www.sciencedirect.com Energy Procedia 37 (013 ) 869 876 GHGT-11 13 C-NMR Spectroscopic Study on Chemical Species in H O System before and after Heating Miho Nitta a, Masaki Hirose a, Toru Abe a, Yukio Furukawa a, *, Hiroshi Sato b, Yasuro Yamanaka c a Department of Chemistry and Biochemistry, Graduate School of Advanced Science and Engineering, Waseda University, Shinjukuku, Tokyo 169-8555, Japan b Research Laboratory, IHI Corporation, 1, Shin-nakahama-cho, Isogo-ku, Yokohama 35-8501, Japan c Energy Operations, IHI Corporation, 1-1, Toyosu 3-chome, Koto-ku, Tokyo 135-8710, Japan Abstract Chemical reactions associated with the absorption of CO into aqueous solutions of blends of piperazine (PZ) with N- methyldiethanolamine (MDEA), etc. were studied by 13 C-NMR spectroscopy. The coexistence of PZ and MDEA enhanced the initial apparent rate of HCO 3 /CO 3 formation. This result can be explained by considering that PZ monocarbamate rapidly formed works as an organocatalyst in the formation reaction of HCO 3. Concentration changes of chemical species in CO -absorbed aqueous amine solutions upon heating (80 C, 30 min) were studied by 13 C-NMR spectroscopy. Carbon dioxide regeneration originates mainly from HCO 3 /CO 3, and not from carbamate and carbonate. 013 013 The The Authors. Authors. Published Published by by Elsevier Elsevier Ltd. Ltd. Selection and/or peer-review under responsibility of GHGT Keywords: 13 C-NMR; amine; piperazine; carbamate; carbon dioxide. 1. Introduction Aqueous solutions of alkanolamines are widely used as absorbers for removing CO from flue gas of fossil-fueled power plants [1]. An aqueous solution of an alkanolamine absorbs CO chemically at room temperature and releases CO at high temperature. Primary amines such as -aminoethanol (MEA), - amino--methyl-1-propanol (AMP), etc., secondary amines such as -(isopropylamino)ethanol (IPAE), etc. and tertiary amines such as N-methyldiethanolamine (MDEA), 1-dimethylamino--propanol * Corresponding author. Tel.: +81-3-586-344; fax: +81-3-308-70. E-mail address: furukawa@waseda.jp. 1876-610 013 The Authors. Published by Elsevier Ltd. Selection and/or peer-review under responsibility of GHGT doi:10.1016/j.egypro.013.05.179

870 Miho Nitta et al. / Energy Procedia 37 ( 013 ) 869 876 (DMAP), etc. were used as potential candidate absorbers. Their chemical structures are shown in Fig. 1. Since a single amine solution did not show high performance, a blend of two or three amines was used as an absorber. In particular, piperazine (PZ, see Fig. 1f) was used as a so-called "activator" together with an alkanolamine such as MDEA and IPAE. However, the role of PZ remains unclear from a standpoint of molecular chemistry. Fig. 1. Chemical structures of amines: (a) MEA; (b) AMP; (c) IPAE; (d) MDEA; (e) DMAP; (f) PZ. It has been demonstrated [ 10] that 13 C-NMR spectroscopy is a powerful tool for qualitative and quantitative studies of chemical species formed in aqueous solutions containing amines and CO. It was elucidated that amines react with CO, forming ionic species such as bicarbonate ion (HCO 3 ), carbonate ion (CO 3 ), protonated amines, amine carbamates, and amine carbonates, etc. It is believed that a carbamate molecule is formed through the deprotonation of the zwitterion of amine and CO in the presence of a proton acceptor such as an amine or a water molecule. In the aqueous solutions, CO reacts with alkanolamines either directly or via the acid-base buffer mechanism to form HCO 3. Recently, a density functional theory study [11] suggests that amine, CO, and H O molecules react directly to form HCO 3. The reaction mechanism has not been fully clarified yet. In this paper we focus on quantitative 13 C-NMR studies on concentration changes of chemical species in an aqueous solution of a blend of PZ with an amine (MDEA, DMAP, or IPAE) in the course of CO absorptions and on those upon heating as a simple model of CO regeneration.. Experimental.1. Sample preparation Samples of MEA (Tokyo Chemical Industry), AMP (Acros Organics), IPAE (Tokyo Chemical Industry), MDEA (Tokyo Chemical Industry), DMAP (Tokyo Chemical Industry), and PZ (Acros Organics) were used without further purification. In the experiments of CO absorption kinetics, CO gas was bubbled through an aqueous solution of an amine or a blend at a rate of 150 ml/min. The concentration of PZ was 5 or 10 wt%, and that of an amine was 0 or 30 wt%. In the absorptionregeneration experiments, CO gas was bubbled through an aqueous solution of an amine or a blend at a rate of 50 ml/min at 50 C for 60 min; the solution was heated at 80 C for 30 min as the CO regeneration process. The concentrations of MEA, AMP, and MDEA were 0 wt%, and that of PZ was 10 wt%. A blend of 10 wt% PZ and 0 wt% amine (MDEA, DMAP or IPAE) was used... 13 C-NMR measurements The 13 C-NMR spectra of a D O solution containing an amine or a blend were measured at room temperature on a JEOL JNM-500ECX 500 MHz NMR spectrometer by using the inverse gated proton

Miho Nitta et al. / Energy Procedia 37 ( 013 ) 869 876 871 decoupling method. Because of a long spin-lattice relaxation time, the holding time between scans was set to be 1 min. 18 scans were accumulated for each spectrum. As the standard of chemical shifts, 3- trimethylsilyl-1-propanesulfonic acid-d 6 sodium salt was added into the sample solution. 3. Results and discussion 3.1. CO -absorption kinetics The 13 C-NMR spectrum of an aqueous solution of a blend of PZ (10 wt%) and MDEA (0 wt%) and that after 50-min bubbling of the CO gas are shown in Figs. a and b, respectively. The observed bands have been assigned on the basis of the data in the literature [3, 8]. The assignments of the bands are listed in Table 1. The number of each carbon atom is shown in the chemical structures below. It should be noted that it is not possible to distinguish the signals originating from MDEA and protonated MDEA, because of the fast exchange of a proton between them. Thus a single band is assigned to both the species MDEA/MDEAH +. The chemical shift of this band shifts with increasing CO -bubbling time because the contents of these species are changed. Similar assignments have been made to another species and its protonated species such as HCO 3 and CO 3. Fig.. 13 C-NMR spectra of (a) an aqueous solution of a blend of PZ (10 wt%) and MDEA (0 wt%) and (b) after 50- min CO bubbling. The following species were observed: (i) MDEA and its protonated species; (ii) MDEA carbonate and its protonated species; (iii) PZ and its protonated species; (iv) PZ monocarbamate and its protonated species; (v) PZ biscarbamate; (vi) HCO 3 and CO 3. This result is consistent with the previous report [8]. The intensity of a band attributed to each species was converted to the concentration of the species. The concentration of each species is plotted as a function of CO -bubbling time for an aqueous solution of

87 Miho Nitta et al. / Energy Procedia 37 ( 013 ) 869 876 MDEA (0 wt%), PZ (10 wt%), PZ (10 wt%) MDEA (0 wt%) blend, and PZ (10 wt%) MDEA (30 wt%) blend in Figs. 3a-3d, respectively. Table 1. Assignments of observed bands in PZ MDEA CO H O system. chemical shift / ppm Species Numbering a) MDEA and its protonated species 1 MDEA carbonate and its protonated species 4 PZ monocarbamate and its protonated species 11 PZ and its protonated species 9 PZ monocarbamate and its protonated species 10 46.7 PZ biscarbamate 1 MDEA and its protonated species 3 MDEA carbonate and its protonated species 6 MDEA and its protonated species MDEA carbonate and its protonated species 5 MDEA carbonate and its protonated species 8 MDEA carbonate and its protonated species 13 HCO 3 and CO 3 PZ monocarbamate and its protonated species 14 165.4 PZ biscarbamate 15 a) The numbering of carbon atoms is shown in the chemical structures below. In the MDEA CO H O system (Fig. 3a), the concentration of HCO 3 /CO 3 increases with increasing time. The initial apparent rate of HCO 3 /CO 3 formation from 0 to 10 min was 0.049 mol/l min. Probably, this rate depends on the rate of CO absorption into the solution. The concentration of HCO 3 /CO 3 becomes equilibrium at 50 min. The formation of a small amount of carbonate indicates that carbonate does not play an important role in the CO absorption-regeneration process. In the acidbase buffer mechanism, equilibrium reactions can be written as follows: CO HO H HCO 3 (1) HO H OH () HCO3 H CO 3 (3) + NCH 3(CH CHOH) H N HCH 3(CH CHOH) (4)

Miho Nitta et al. / Energy Procedia 37 ( 013 ) 869 876 873 In the termolecular mechanism [11], the following reaction will proceed. + NCH 3(CH CHOH) CO HO N HCH 3(CH CH OH) HCO 3 (5) Fig. 3. Concentrations (mol/l) of HCO 3 /CO 3 ( ), MDEA ( ), carbonate ( ), PZ ( ), PZ monocarbamate ( ), PZ biscarbamate ( ), total CO equivalent content ( ), and ph ( ) in aqueous solutions of (a) MDEA (0 wt%), (b) PZ (10 wt%), (c) PZ (10 wt%) MDEA (0 wt%), and (d) PZ (10 wt%) MDEA (30 wt%) as a function of CO - bubbling time. In the PZ H O CO system (Fig. 3b), the concentrations of monocarbamate and HCO 3 /CO 3 increase. The concentration of monocarbamate is higher than that of HCO 3 /CO 3. It is believed that a carbamate molecule is formed from the zwitterion of PZ and CO. Thus, the following reactions are proposed: (6) (7)

874 Miho Nitta et al. / Energy Procedia 37 ( 013 ) 869 876 The initial apparent rate of PZ monocarbamate formation from 0 to 10 min was 0.087 mol/l min. The initial rate of the HCO 3 /CO 3 formation from 0 to 10 min was 0.040 mol/l min. In the PZ (10 wt%) MDEA (0 wt%) CO H O system (Fig. 3c), the initial rate of HCO 3 /CO 3 formation from 0 to 10 min was 0.033 mol/l min; this is smaller than that (0.049 mol/l min) in MDEA (0 wt%) CO H O system. This decrease is due to the rapid formation of PZ monocarbamate. In this system, the rate of HCO 3 /CO 3 formation from 10 to 0 min was 0.066 mol/l min, whereas in the MDEA (0 wt%) CO H O system the corresponding rate was 0.058 mol/l min. This result indicates that the coexistence of PZ and MDEA enhances the rate. Similar rate enhancements were also observed for PZ (10 wt%) MDEA (30 wt%) CO H O, PZ (5 wt%) MDEA (0 wt%) CO H O, and PZ (10 wt%) DMAP (0 wt%) CO H O systems. This enhancement of the apparent rate was observed for tertiary amines MDEA and DMAP. Since the rate of CO absorption is low for tertiary amines, this rate enhancement with PZ carbamate can be observed. In order to explain this rate enhancement, we consider a novel mechanism of HCO 3 formation decomposition reactions as follows. The formation reaction of PZ monocarbamate can be expressed as follows: (8) A proton generated from the reaction of PZ and CO is accepted by an MDEA molecule. In addition, we assume the decomposition reaction of PZ monocarbamate as follows: (9) The combination of Eqs (8) and (9) leads to Eq (5). In Eq (5) PZ monocarbamate does not appear. Thus, the PZ monocarbamate molecule helps the formation of HCO 3 like an organocatalyst. Since similar reactions associated with PZ biscarbamate are possible, the PZ biscarbamate molecule also may help the formation of HCO 3 as an organocatalyst. 3.. CO regeneration upon heating Molar concentrations of the chemical species in amine CO H O system before and after heattreatment for MEA, AMP, MDEA, and PZ are shown in Fig. 4. In an MEA aqueous solution bubbled with CO, the concentrations of carbamate and HCO 3 /CO 3 were 1.34 and 0.79 mol/l, respectively. After heat-treatment, the concentration of carbamate increased to 1.55 mol/l. This suggests that carbamate is not decomposed to CO and MEA upon heating. The concentration of HCO 3 /CO 3 species decreased to 0.37 mol/l; 0.4 mol/l of CO was regenerated from the HCO 3 /CO 3 species. In an AMP aqueous solution bubbled with CO, the concentrations of HCO 3 /CO 3 and carbonate were.6 and 0.05 mol/l, respectively. After heat-treatment, the concentrations of HCO 3 /CO 3 and carbonate

Miho Nitta et al. / Energy Procedia 37 ( 013 ) 869 876 875 decreased to 1.84 and 0.04 mol/l, respectively. In an MDEA aqueous solution bubbled with CO, the concentration of HCO 3 /CO 3 was 1.3 mol/l; upon heating, the concentration decreased to 0.76 mol/l. The 0.56 mol/l of CO was regenerated from the HCO 3 /CO 3 species. In an aqueous solution of PZ bubbled with CO, there exist HCO 3 /CO 3 (0.31 mol/l), PZ monocarbamate (0.75 mol/l), and PZ biscarbamate (0.03 mol/l). The concentrations of HCO 3 /CO 3, monocarbamate, and biscarbamate were changed to 0.4, 0.63, and 0.10 mol/l, respectively. This result indicates that mono- and bis-carbamates are not decomposed to PZ and CO. Carbon dioxide is mainly saved in an aqueous amine solution as the chemical species of HCO 3 /CO 3, monocarbamate, and biscarbamate. Carbonate may be ignored because the concentration of carbonate is low. The observed data suggests that upon heating, the regeneration of CO mainly originates from the HCO 3 /CO 3 species. This is probably attributed to the temperature dependence of chemical equilibrium in reactions (1) (4). Fig. 4. Concentrations of HCO 3 /CO 3 (black), monocarbamate (pink), biscarbamate (yellow), and carbonate (blue). Bars in the left- and right-hand sides for each amine are before and after heat-treatment, respectively. The concentrations of HCO 3 /CO 3, PZ monocarbamate, PZ biscarbamate, and amine carbamate in the aqueous solution of a PZ blend with an amine such as MDEA, DMAP, or IPAE before and after heat-treatment are listed in Table. Table. Concentrations (mol/l) of HCO 3 /CO 3, PZ monocarbamate, PZ biscarbamate, and amine carbamate before and after heating. species heating equivalent CO change MDEA PZ PZ MDEA PZ DMAP PZ IPAE HCO 3 /CO 3 before 1.3 0.31 1.00 1.4 1.5 after 0.76 0.4 0.40 0.64 0.78 1 0.56 0.07 0.60 0.78 0.47 PZ monocarbamate before 0.75 0.74 0.68 0.67 after 0.63 0.59 0.55 0.50 0.1 0.15 0.13 0.17 PZ biscarbamate before 0.03 0.18 0.7 0.9 after 0.10 0. 0.40 0.44 3 0.07 0.04 0.13 0.15 + 3 0.0 0.07 0.13 0.13 carbamate before 0.0 after 0.0 4 0.0 = 1 + + 3 + 4 0.56 0.05 0.67 0.65 0.34 Table shows the concentration changes upon heating in HCO 3 /CO 3 ( 1 ), PZ monocarbamate ( ),PZ biscarbamate ( 3 ), amine carbamate ( 4 ) and total equivalent CO content ( = 1 + + 3 + 4 ). In

876 Miho Nitta et al. / Energy Procedia 37 ( 013 ) 869 876 this equation 3 is times by, because a biscarbamate molecule is made from two CO molecules. In all the solutions, 1 decreases upon heating, indicating that HCO 3 /CO 3 species contribute to CO regeneration. On the other hand, the sum of the equivalent CO contents in PZ monocarbamate and biscarbamate + 3 increases for PZ DMAP and PZ IPAE and decreases for PZ MDEA. The total equivalent CO change = 1 + + 3 + 4 is large for PZ MDEA and PZ DMAP. The observed data suggests that the regeneration of CO upon heating mainly originates from the HCO 3 /CO 3 species. Carbamate has a negative effect in CO regeneration upon heating. 4. Conclusions We have studied the concentration changes of chemical species in an aqueous solution of a blend of PZ and an amine such as MDEA, DMAP, or IPAE as a function of CO -bubbling time by 13 C-NMR spectroscopy. At the beginning of the reaction, PZ carbamate was formed. The coexistence of PZ and MDEA or DMAP enhanced the initial rate of HCO 3 /CO 3 formation. This result probably indicates that PZ monocarbamate rapidly formed works as an organocatalyst in the formation reaction of HCO 3. We have studied the concentrations of chemical species in CO -absorbed aqueous amine (MEA, AMP, MDEA, PZ, PZ MDEA, PZ DMAP, and PZ IPAE) solutions upon heating (80 C, 30 min) by 13 C- NMR spectroscopy. The results indicate that CO regeneration originates from the HCO 3 /CO 3 species, and not from mono- and bis-carbamates and carbonate. 13 C-NMR spectroscopy is a powerful tool for qualitative and quantitative analyses of chemical species in amine absorbers of CO. Acknowledgements The authors are grateful to Professors H. Nakai and N. Kanomata, and Dr. H. Yamamoto of Waseda University for valuable discussion and suggestions. References [1] Aarou D, Tsouris C. Separation of CO from flue gas: review. Sep Sci Technol 005; 40: 31 48. [] Suda T, Iwaki T, Mimura T. Facile determination of dissolved species in CO amine H O system by NMR spectroscopy. Chem Lett 1996; 777 8. [3] Bishnoi S, Rochelle GT. Absorption of carbon dioxide in aqueous piperazine: reaction kinetics, mass transfer and solubility. Chem Eng Sci 000; 55: 5531 43. [4] Bishnoi S, Rochelle GT. Thermodynamics of piperazine/methyldiethanolamine/water/carbon dioxide. Ind Eng Chem Res 00; 41: 606 1. [5] Jakobsen JP, Krane J, Svendsen HF. Liquid-phase composition determination in CO H O alkanolamine systems: an NMR study. Ind Eng Chem Res 005; 44: 9894 903. [6] Hartono A. da Silva EF, Grasdalen H, Svendsen F. Qualitative determination of species in DETA H O CO system using 13 C NMR spectra. Ind Eng Chem Res 007; 46: 49 54. [7] Böttinger W, Maiwald M, Hasse H. Online NMR spectroscopic study of species distribution in MEA H O CO and DEA H O CO. Fluid Phase Equilibria 008; 63: 131 43. [8] Böttinger W, Maiwald M, Hasse H. Online NMR spectroscopic study of species distribution in MDEA H O CO and MDEA PIP H O CO. Ind Eng Chem Res 008; 47: 7917 6. [9] Yamada H, Shimizu S, Okabe H, Matsuzaki Y, Chowdhury FA, Fujioka Y. Prediction of basicity of aqueous amine solutions and the species distribution in the amine H O CO system using the COSMO-RS method. Ind Eng Chem Res 010; 49: 449 55. [10] Ciftja AF, Hartono A, da Silva EF, Svendsen HF. Study on carbamate stability in the AMP/CO /H O system from 13 C- NMR spectroscopy. Energy Procedia 011; 4:614 0. [11] Yamada H, Matsuzaki Y, Higashii T, Kazama S. Density functional theory study on carbon dioxide absorption into aqueous solutions of -amino--methyl-1-propanol using a continuum solvation model. J Phys Chem A 011; 115: 3076 86.