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Branching ratios for the reactions of OH with ethanol amines used in carbon capture and the ... PDF

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PCCP Accepted Manuscript This is an Accepted Manuscript, which has been through the Royal Society of Chemistry peer review process and has been accepted for publication. Accepted Manuscripts are published online shortly after acceptance, before technical editing, formatting and proof reading. Using this free service, authors can make their results available to the community, in citable form, before we publish the edited article. We will replace this Accepted Manuscript with the edited and formatted Advance Article as soon as it is available. You can find more information about Accepted Manuscripts in the Information for Authors. Please note that technical editing may introduce minor changes to the text and/or graphics, which may alter content. The journal’s standard Terms & Conditions and the Ethical guidelines still apply. In no event shall the Royal Society of Chemistry be held responsible for any errors or omissions in this Accepted Manuscript or any consequences arising from the use of any information it contains. www.rsc.org/pccp Page 1 of 33 Physical Chemistry Chemical Physics Branching ratios for the reactions of OH with ethanol amines used in carbon capture and the potential impact on carcinogen formation in the t p i emission plume from a carbon capture plant† r c s u L. Onel,*a M.A. Blitz,ab J. Breen,a A.R. Rickard,cd and P.W. Seakins*ab n a M a School of Chemistry, University of Leeds, Leeds, LS2 9JT, UK. Email: d e [email protected] t p e c b National Centre for Atmospheric Science (NCAS), University of Leeds, Leeds, c A LS2 9JT, UK s c i c Wolfson Atmospheric Chemistry Laboratories, Department of Chemistry, s y h University of York, York, YO10 5DD, UK P l a d National Centre for Atmospheric Science (NCAS), University of York, York, c i m YO10 5DD, UK e h C † Electronic supplementary information (ESI) available: Details on OH + DMEA reaction in y r the absence/presence of O , OH/OD + d -DMEA reaction with O , OH + t 2 4 2 s i MEA/MMEA/MeOEA reactions in the presence of O /NO, SAR calculations, MESMER m 2 e calculations and atmospheric modelling h C l a c i s y h P 1 Physical Chemistry Chemical Physics Page 2 of 33 Abstract The OH initiated gas-phase chemistry of several amines that are potential candidates for use t p i r in post-combustion carbon capture (PCCC) plants have been studied by laser flash photolysis c s with OH monitored by laser induced fluorescence. The rate coefficients for the reaction of u n OH with methylmonoethanolamine (MMEA) and dimethylmonoethanolamine (DMEA) have a M been measured as a function of temperature (~300 – 500 K): d e (0.790.22) (0.440.12)  T   T  k (8.510.65)1011  , k (6.850.25)1011  . t OHMMEA 298 OHDMEA 298 p e c The results for DMEA lie between previous values. This is the first kinetic study of the OH + c A MMEA reaction. At low pressures in the presence of oxygen, OH is recycled in the DMEA s c reaction as has been observed for other tertiary amines. i s y Branching ratios for OH abstraction with MEA, DMEA and MMEA are dominated by h P abstraction from the α CH group. Abstraction from N-H is determined to be 0.38 ± 0.06 for 2 l a MEA and 0.52 ± 0.06 for MMEA at 298 K. The impact of these studies has been assessed by c i m using a modified chemical box model to calculate downwind concentrations of nitramines e h and nitrosamine formed in the photo-oxidation of MEA. Under clear sky conditions, the C simulations suggest that current safe guidelines for nitramines may be significantly exceeded y r t with predicted MEA emission rates. s i m e h C 1. Introduction l a c One of the most feasible options for the mitigation of carbon dioxide emissions from fossil i s fuel power stations is post-combustion carbon capture (PCCC) using amines.1-4 y h P Monoethanolamine (MEA) is considered as a benchmark solvent in terms of performance, and has been extensively investigated for use as a PCCC solvent although amines blends are 2 Page 3 of 33 Physical Chemistry Chemical Physics most likely to be used in commercial applications.3, 5-7 A range of amines are being investigated, including other primary amines such as 2-amino-2-methylpropan-1-ol, t p secondary amines such as piperazine (PZ) and diethanolamine, and tertiary amines such as N- i r c methyldiethanolamine (MDEA) and triethanolamine.8 Other ethanolamines such as N- s u methylethanolamine (MMEA) and N,N-dimethylethanolamine (DMEA) have also been n a M studied as PCCC potential solvents, and for our studies are useful model systems to help d understand issues associated with the formation of toxic degradation products in the e t atmosphere.9, 10 In addition, both MMEA and DMEA have been identified as potential p e products of the in situ degradation of MDEA during natural gas desulphurization and PCCC.8, c c A 11 s c Given the substantial volumes of amines needed for efficient CO2 capture, large scale i s y use of PCCC will potentially result in significant amine emissions to the atmosphere. A h P PCCC plant using MEA to remove ~1 Mt CO per year is predicted to emit 40 - 160 tonnes 2 l a of MEA per year.12 Previous studies of MEA, piperazine (PZ) and methylamines have shown c i m that, once these amines are released into the atmosphere, their gas-phase processing, e primarily initiated by OH radical reactions, will compete with heterogeneous uptake h C (lifetimes range from 15 min – 1 hour at peak OH concentrations, typically 5 × 106 molecule y r cm-3).13-18 The atmospheric removal of amines by reaction with Cl atoms in gas-phase has t s i m been found to be a minor sink for amines (lifetime of ~20 days for typical peak Cl e concentrations, around 2 × 103 molecule cm-3).19, 20 A major concern with PCCC is the h C impact of carcinogenic nitrosamines (R N-NO) and nitramines (R N-NO ), formed in the 2 2 2 l a gas-phase processing of amines, on human health.19, 21-24 The yield of these toxic products c i s depends on the fraction of amine processed in the gas-phase (hence on the overall rate y h coefficient for the OH + amine reaction), and on the branching ratios in the initial OH P abstraction reaction. 3 Physical Chemistry Chemical Physics Page 4 of 33 MEA has four potential sites for OH abstraction: HOCH CH NH + OH  HOCH CHNH + H O  abstraction (R1a) 2 2 2 2 2 2 t p i r HOCH2CH2NH2 + OH  HOCH2CH2NH + H2O N-H abstraction (R1b) c s u HOCH CH NH + OH  HOCHCH NH + H O  abstraction (R1c) n 2 2 2 2 2 2 a M HOCH CH NH + OH  OCH CH NH + H O O-H abstraction (R1d) 2 2 2 2 2 2 2 d e Previous determinations of the branching ratios in reaction R1 used analysis of concentration t p e profiles of secondary-generated products obtained by chamber experiments23, 25 and c c theoretical calculations.26 Experiments carried out in the European Photoreactor (EUPHORE) A s suggested that > 80% of the initial OH abstraction occurs through reaction R1a. In contrast, c i the theoretical work of Xie et al. found that  C-H: C-H = 0.39:0.43, 26 while calculations s y h using the structure-activity relationships (SARs) predict that  C-H:N-H = 0.45:0.47 (Table P S2, ESI†).19, 27, 28 l a c i The N-centred radical generated by reaction R1b reacts with NO and NO to form 2- m 2 e nitrosoaminoethanol, HOCH2CH2NHNO and 2-nitroaminoethanol, HOCH2CH2NHNO2 h C respectively (reactions R2 and R3). Reactions R2 and R3 are potentially in competition with y r reaction R4 forming 2-iminoethanol, HOCH2CHNH; little is known about R4, but it is t s predicted to be slow (~1 × 10-19 cm3 molecule-1 s-1) .23, 29 mi e HOCH CH NH + NO  HOCH CH NHNO (R2) 2 2 2 2 h C HOCH CH NH + NO  HOCH CH NHNO (R3) 2 2 2 2 2 2 l a HOCH CH NH + O  HOCH CHNH + HO (R4) c 2 2 2 2 2 i s HOCH CH NHNO was not detected in the EUPHORE studies.23, 25 The theoretical y 2 2 h calculations of Tang et al. conclude that primary nitrosamines, RCH NH-NO, are not stable P 2 and rapidly form imines by isomerization to RCHNHNOH followed by reaction with O .30 2 4 Page 5 of 33 Physical Chemistry Chemical Physics However, based on the theoretical study of da Silva, RNH-NO are significant products in RNH + NO reactions.31 t p The branching ratio for the abstraction at the N-H site, r , was reported to be < 0.10 i 1b r c by Nielsen et al.25, 0.15 by Karl et al.23 and 0.17 by Xie et al.26 The SAR calculations lead to s u r = 0.47.19, 27, 28 Given the discrepancies between the reported branching ratios in reaction n 1b a M R1, there is a clear need for the direct experimental determination of r – r . 1a 1d d The overall rate coefficient k and the branching ratios in the reactions of OH OH+MMEA e t with MMEA (HOCH CH NH(CH )) and DMEA (HOCH CH N(CH ) ) have not previously p 2 2 3 2 2 3 2 e c been studied. c A Here we report on the determination of the rate coefficients of OH + MMEA and s c DMEA reactions and their temperature dependence using laser flash photolysis (LFP) for OH i s y generation and laser induced fluorescence (LIF) for time-resolved OH monitoring. We find h P OH regeneration in the OH + DMEA reaction in the presence of oxygen. The OH/OD signals l a obtained by 248 nm photolysis of (CH3)2N(CD2)2OH ( d4-DMEA) in the presence of O2 are c i m then used to determine the dominant H-abstraction site for DMEA. e h On the millisecond scale of the OH + MEA/O /NO and OH + MMEA/O /NO C 2 2 y LFP/LIF experiments, HO is generated through reaction R5 and reacts further with NO 2 r t s (reaction R6) to give back OH. i m e HOCH CHNHR + O  HO + HOCH CHNR (R5) 2 2 2 2 h C HO + NO  OH + NO (R6) 2 2 l a c i The HO2 yield and the branching ratios in the initial OH reaction are determined using the s y method developed previously for OH reactions with amines such as dimethylamine (DMA) h P and ethylamine (EA).32 Calculations using the MESMER (Master Equation Solver for Multi- 5 Physical Chemistry Chemical Physics Page 6 of 33 Energy Well Reactions) package33 show that, at the relatively low pressures used in our experiments, the O addition producing a stabilised peroxy species (reaction R7) does not 2 t p compete with reaction R5 to affect our results. However, the O addition is in competition i 2 r c with O abstraction at atmospheric pressure. s 2 u n HOCH CHNHR + O + M  HOCH CH(O )NHR + M (R7) a 2 2 2 2 M The impact of this work on the downwind formation of nitrosamines and nitramines d e t following emission of MEA from a typical PCCC plant is assessed using an atmospheric p e chemistry box model. MEA and NOx emissions are based on the PCCC pilot plant located at c c Mongstad, on the west coast of Norway.24, 34 The model also incorporates typical gas-phase A s chemistry of background compounds and MEA, heterogeneous uptake and reactions, and c i s plume dispersion described by a time dependent Gaussian equation. y h P l a 2. Experimental c i m This work has been carried out in a slow-flow pulsed LFP – LIF system that has been e h described in several previous publications.13, 16, 32 The flows of the OH/OD precursor, amine C (MEA and DMEA: Sigma-Aldrich, ≥99.5%, MMEA and 2-methoxyethanolamine (MeOEA): y r t Alfa Aesar, 99%), O2 (if used, BOC 99.999%), nitrogen monoxide (if used, BOC >99.9%) s i m and bath gas (N , BOC oxygen free) were regulated through calibrated mass flow controllers, 2 e h mixed in a manifold and introduced into a stainless steel reactor. The OH precursor was C tertiary butylhydroperoxide (Sigma-Aldrich, 70% in water) and the OD precursor was l a deuterated acetone (acetone-d ) in the presence of O 35 or (CH ) COOD/N + D O.32 The c 6 2 3 3 2 2 i s total pressure in the cell was controlled via a needle valve on the exhaust line and measured y h P using a capacitance manometer. Temperatures were measured close to the observation region using a K-type thermocouple. 6 Page 7 of 33 Physical Chemistry Chemical Physics DMEA was prepared as a diluted mixture in nitrogen in a glass bulb. Gaseous mixtures of MEA and MMEA could not be prepared because of the low vapour pressures of t p these amines at 298 K.36 Therefore, MEA and MMEA were introduced into the reactor from i r c a glass bubbler by flowing N gas over liquid amine samples. The concentrations of MEA s 2 u and MMEA were determined using the technique developed previously using in situ n a absorption measurements at 185 nm.16, 18 Absorptions were converted into concentrations M d using the absorption cross sections of amines,  = (8.53 ± 0.24) × 10-18 cm2 185 nm, MEA e t molecule-1,16 and  =(9.71 ± 0.37) × 10-18 cm2 molecule-1 (this work). p 185 nm, MMEA e c c Radicals were generated by excimer laser flash photolysis at 248 nm (Lambda Physik A 210, typically 5 - 15 mJ cm-2, 5 Hz repetition rate). OH radicals were probed by off- s c resonance laser induced fluorescence at an excitation wavelength of ~282 nm generated from i s y a YAG pumped dye laser (Powerlite Precision II 8010, Sirah PRSC-DA-24, operating with h P Rhodamine 6G dye) introduced perpendicularly to the photolysis laser. OH fluorescence l a centred at 308 nm was observed with a photomultiplier tube (Thorn EMI model 9813 QKB) c i m through an interference filter (Andover, 308 ± 10 nm). The time delay between the photolysis e h and the probe laser was varied using an in-house LabView program to build up an entire C time-dependent OH profile. Depending on signal to noise ratios, 6 - 20 laser shots were y r t averaged for each time point. s i m 2.1. OH + amine reactions in the absence of NO e h The reactions were carried out under pseudo-first-order conditions using amine C l concentrations in large excess over the initial OH concentration (~1000:1). Under these a c conditions, in the absence of NO, the fluorescence intensity, I, which is proportional to [OH], i f s y decayed according to the single exponential eqn E1 (see the inset of Figure 1 and Figure S1 h P as examples). 7 Physical Chemistry Chemical Physics Page 8 of 33 I (t) I (0)exp(k' t) (E1) f f OH t p where k’ = k [amine] + k . Here k is the bimolecular rate coefficient for the reaction OH OH loss OH i r of OH with amine and k is the pseudo-first-order rate coefficient for OH loss by diffusion c loss s u and reaction with OH precursor. Figure 1 shows an example of bimolecular plot for the OH + n a MMEA reaction. M d e t p e c c A s c i s y h P l a Fig. 1 Bimolecular plot for MMEA, (8.01 ± 0.92) × 10-11 cm3 molecule-1 s-1, at 298 K and a c total pressure of 17 Torr of N . The error bars are at  level. A typical OH fluorescence decay 2 i m trace and fit to eqn E1 is shown in the inset. e h For the reaction OH + DMEA in the presence of O , the experiments were performed C 2 using sufficiently high O concentration (~1016 molecule cm-3) to obtain single exponential y 2 r t s OH decays. Examples of bimolecular plots for the DMEA + OH reaction in the i m absence/presence of O are shown in Figure S1. 2 e h C 2.2. OH + MEA/MMEA and OD + deuterated MEA/MMEA reactions in the presence of l a O /NO 2 c i Pseudo-first-order conditions were ensured by having amine (0.5 – 6.0 × 1014 molecule cm-3), s y h O and NO concentrations in great excess over the initial radical concentration (0.5 - 2.0 × 2 P 1011 molecule cm-3). The O concentration was higher by a factor of ~100 than the NO 2 8 Page 9 of 33 Physical Chemistry Chemical Physics concentration and typically [NO] = 0.1 – 1.0 × 1015 molecule cm-3. Biexponential decays of OH were generated under these conditions due to reaction R6 regenerating OH and were t p analysed as described previously.32 i r c s In the reactions of OD with DOCH2CH2ND2 (d3-MEA) and DOCH2CH2ND(CH3) (d2- u n MMEA) (CH ) COOD was used as OD precursor. The deuteration of amine and radical a 3 3 M precursor were achieved by H/D exchange in the delivery tubing of the cell using D O (99.9 2 d atom % D), as described elsewhere.32 e t p e 2.3. Synthesis of [1,1,2,2-2H ]-2-dimethylaminoethanol (d -DMEA) 4 4 c c Ethyl 2-(dimethylamino)-2-oxoacetate (5.00 g, 34.4 mmol) was added slowly over 20 min to A s a stirred solution of LiAlD (3.47 g, 82.6 mmol) in dry THF (200 mL) at 0 °C. The mixture 4 c i was heated under reflux for 6 h and the reaction cooled to 0 °C. The reaction was quenched s y h by the drop-wise addition of saturated Na SO solution until effervescence ceased and a 2 4 P white solid formed. After stirring for 30 min, the precipitate was collected by filtration and l a c extracted into tetrahydrofuran (600 ml) by Soxhlet extraction for 18 hours to give a pale i m yellow solution. The solvent was removed in vacuo to give a yellow oil, which was purified e h by distillation (131134 °C), to give d -DMEA (1.98 g, 62 %) as a colourless oil; 1H NMR C 4 y (500 MHz, CDCl ): δ 2.04 (6H, s, CH ); 13C NMR (125 MHz, CDCl ): δ 45.2 (CH ), 57.9 3 3 3 3 r t s (1J 21.7, CD N), 60.0 (1J 20.2, CD OH); m/z (EI+) 93.1 . CD 2 CD 2 i m e h C 3. Results and discussion l a c 3.1. Kinetics of OH + MMEA and DMEA i s The averages of the measured room temperature rate coefficients, k = (8.26 ± 0.82) × y OH+MMEA h 10-11 cm3 molecule-1 s-1 and k = (7.29 ± 0.72) × 10-11 cm3 molecule-1 s-1, are similar to P OH+DMEA k = (7.61 ± 0.76) × 10-11 cm3 molecule-1 s-1.16 The errors in the bimolecular rate OH+MEA 9

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a YAG pumped dye laser (Powerlite Precision II 8010, Sirah PRSC-DA-24, operating with G. T. Rochelle, Science, 2009, 325, 1652-1654. 8.
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