Design and Evaluation of Switchable-Hydrophilicity Solvents

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Introduction
The widespread use of volatile solvents contributes to a variety of 15 health, safety, and environmental problems such as inhalation toxicity, flammability, and smog formation. It is well known that non-volatile organic solvents avoid all of these problems, but they are rarely used in industry because they cannot be distilled. Distillation is the standard method for removing solvent from 20 product at the end of almost any chemical process that uses solvents. Industry's dependence on distillation is responsible for the continued widespread use of volatile organic solvents despite their known hazards. The use of switchable-hydrophilicity solvents (SHSs), in combination with water, has been proposed as 25 an alternative to distillation for solvent removal that does not require the use of volatile compounds. [1][2][3] A SHS is a solvent which is poorly miscible with water in one form but completely miscible with water in another form and which can be switched between these two forms by a simple 30 change in the system. Amidine and tertiary amine SHSs have been identified 1,2 which can be switched between the two forms by the addition or removal of CO 2 from the system. The change in miscibility is due to an acid-base reaction between either hydrated CO 2 or carbonic acid in the carbonated water and the 35 SHS, resulting in the hydrophilic bicarbonate salt of the protonated SHS (Equation 1). This behaviour has been exploited as a method for removing solvent from products such as soybean oil, 1 algae oil, 4,5 bitumen, 6 and high density polystyrene powder. 2 (1) 40 The first known SHSs contained amidine functional groups, but were found to be impractical solvents because they are expensive to manufacture. 1,2 Eight tertiary amine SHSs were then identified which overcame this limitation. 2 However, some of these SHSs have health and safety concerns associated with them, 45 such as toxicity, volatility, or flammability, which would make them less desirable for use in an industrial setting. In this paper, we identify 13 new secondary and tertiary amine SHSs which are commercially available or easily prepared. The amines were selected in order to overcome one or more of the issues presented 50 by previously confirmed SHSs. We compare all of the SHSs in terms of boiling point, flash point, eutrophication potential, toxicity, and effects on skin (where information is available) to identify the safest and most environmentally benign SHSs.
Before we could search for new SHSs, we needed to identify 55 the properties of known SHSs and how they differ from compounds that are not SHS. Amines, amidines, and guanidines that have already been tested for SHS behaviour 1,2 are listed in Table 1. If an organic liquid forms one phase when mixed with water before CO 2 is added, the system is considered monophasic 60 and therefore not an SHS. If an organic liquid forms two phases when mixed with water both before and after CO 2 is added, the system is considered biphasic. If the mixture of organic compound and water forms two phases before CO 2 is added and forms one phase after CO 2 is added, it is an SHS. Some Table 1 Amines, amidines, and guanidines previously tested for their ability to serve as SHSs at room temperature. 1

Results and Discussion
Selecting Amines for Switchable Behaviour 5 A variety of new amines were tested, but not all of them displayed SHS behaviour. Fig. 1 plots all the amines and amidines tested in this study and previous studies 1,2 by the log of their octanol-water partition coefficient (logK ow ) and the strength of their conjugate acids (pK aH ). A trend was observed for the 10 amines tested. First, the amine must have a logK ow between approximately 1.2 and 2.5 in order to be a SHS. Amines with lower logK ow were too hydrophilic and formed monophasic mixtures with water in their neutral form. Amines with higher logK ow were too hydrophobic and formed biphasic mixtures with 15 water even after exposure to CO 2 . This trend has been observed for previously identified tertiary amine SHSs. 2 Also, most amines that displayed switchable miscibility with water had pK aH above 9.5. If an amine has insufficient basicity, it will not react with carbonated water enough for a switch from a biphasic to a 20 monophasic mixture. Although SHSs met these criteria, some amines which were not SHSs met these criteria as well, suggesting that these are necessary but not sufficient requirements for switchable behaviour. The two amidine SHSs did not fit these criteria (see the upper right portion of Fig. 1), and 25 yet behaved as SHSs for reasons which are unclear.

Amines with High Boiling and Flash Points
Non-volatile SHSs can be designed to capitalize on the previously described advantages of SHS separations. In order to reduce volatility, SHSs with large molecular weights are 30 preferred, but increasing the molecular weights by simply extending the alkyl chains would increase the logK ow excessively so that the bicarbonate salt of the amine would not be sufficiently soluble in carbonated water and the amine will therefore not be a 35 Fig. 1 All compounds tested for switchable miscibility with water at room temperature and 1:1 or 2:1 volume ratio of water to amine, plotted by their logKow and pKaH and coloured by their observed behaviour: monophasic (blue), irreversible (yellow), SHS (green), biphasic (red), and precipitation upon CO2 addition (black). All amine SHSs fall within the 40 green oval. No oval is shown for the amidines because the boundaries of the acceptable area for amidines are unknown.
SHS. By including hydrophilic functional groups in the structure of an amine while increasing the length of the alkyl chains, the solvent can be tailored to be less volatile and yet still fit within 45 the logK ow range required for SHS behaviour. Hydrophilic functional groups also affect the basicity of the amine. The inductive effects of a functional group can decrease the pK aH of the amine, depending on the proximity of the group to the N centre. When designing a SHS with these functional 50 groups, the exact positions of the amine and the electron withdrawing group must be considered so that the amine will be a sufficiently strong base to act as a SHS.
Of the tertiary amines tested which incorporated other functional groups, six formed monophasic mixtures with water, five formed biphasic mixtures with water, and six displayed switchable miscibility (Table 2). These six new SHSs all followed the logK ow and pK aH criteria suggested in Fig 1 except for N,N-dimethylbenzylamine. At a 1:1 volume ratio of water to 5 amine, mixtures of water and N,N-dimethylbenzylamine remain biphasic even after prolonged bubbling of CO 2 through solution. This behaviour is expected because N,N-dimethylbenzylamine (pK aH = 9.03) is a weaker base than most SHSs and will not be sufficiently protonated by carbonated water to form a monophasic 10 mixture with water at a 1:1 volume ratio. At a 5:1 volume ratio of water to amine, the amine displays switchable miscibility. Adding more water to the mixture increases the amount of amine in the aqueous phase enough to form a monophasic mixture after addition of CO 2 without also resulting in a monophasic mixture 15 when CO 2 is removed. Thus a liquid can be a SHS at one volume ratio, but not a SHS at another volume ratio. The different functional groups investigated were alcohols, esters, ketones, acetals, and aromatic rings, each of which will affect the pK aH of the amine differently. Alcohols placed two 20 carbons away from a tertiary amine do not lower the amine's pK aH enough to prevent an amino alcohol from displaying SHS behaviour. Aromatic rings must also be 2 carbons away from a tertiary amine for SHS behaviour to be observed at a 1:1 volume ratio of water to amine. N,N-Dimethylaniline (pK aH 5.18) is not a 25 strong enough base have SHS behaviour, while N,Ndimethylbenzylamine (pK aH 9.03) displays SHS behaviour in a 5:1 volume ratio of water to amine. Finally, N,Ndimethylphenethylamine (pK aH 9.51) has SHS behaviour at a 1:1 volume ratio of water to amine. Ester groups must be 3 carbons 30 away from a tertiary amine for an amino ester to display switchable miscibility, as evidenced by the glycine derivative and amino propanoates, which are not SHSs, and the amino butanoate, which is an SHS.
The SHSs identified in Table 2 are less volatile than 35 trialkylamine SHSs. The SHSs with additional functional groups all have boiling points above 180 o C and predicted flash points above 50 o C (Table 5,  SHSs with additional functional groups shows that the design strategy for less-volatile SHSs is successful.

Secondary Amines
Secondary amines have an alternate reactivity pathway which 45 allows them to uptake CO 2 faster than tertiary amines. Like amidines and tertiary amines, secondary amines can be converted to bicarbonate salts upon exposure to carbon dioxide and water, but they can also undergo a direct reaction with carbon dioxide to form ammonium carbamate salts (Equation 2). This alternative 50 reaction occurs faster than the bicarbonate salt formation, so secondary amine SHSs are likely to switch faster than tertiary amines. 25 However, the energy and temperature required to remove CO 2 from an aqueous ammonium carbamate solution is much larger than that required to remove CO 2 from an 55 ammonium bicarbonate solution. 25 Therefore, using a secondary amine SHS can be more energy-intensive than using a tertiary amine SHS.
While the increased rate of reaction of secondary amines is appealing, the higher energy cost of regeneration is not, so it is 65 important to prevent significant formation of carbamate salts of an SHS. Sterically hindered amines are known to either not form carbamates or form destabilized carbamates which are rapidly hydrolyzed to bicarbonates. 25 Carbamates may form as a kinetic product before being converted to bicarbonates, allowing for 70 rapid uptake of CO 2 without the large energy requirements for removing CO 2 . 25 Therefore, a sterically hindered secondary amine SHS may switch rapidly without increased energy requirements.
Of the secondary amines tested for switchable behaviour, three 75 formed monophasic mixtures with water, five formed biphasic mixtures with non-carbonated water but formed a precipitate upon exposure to CO 2 , and six displayed switchable miscibility (Table 3). X-ray crystallography of the precipitate formed from dibutylamine confirmed that it was the bicarbonate salt of the 80 amine ( Fig. 2). This result suggests that the bicarbonate salts of some secondary amines are not sufficiently soluble in water to make the amines useful as SHSs at a 1:1 volume ratio. Increasing the temperature of the mixture or increasing the volume ratio of water to amine might result in complete 85 dissolution of the bicarbonate salt in the water. A precipitate forms when CO 2 is bubbled through a 1:1 mixture of water and propyl-3-(sec-butylamino)propanoate at room temperature. If the volume ratio is adjusted to 2:1 water to amine and the mixture is heated to 50 o C, bubbling CO 2 through the mixture forms a 90 monophasic liquid which can be returned to a biphasic mixture if argon is bubbled through it while it is heated to 65 o C. Other secondary amines which form precipitates might display SHS behaviour under different conditions. Some secondary amines, such as N-propyl-sec-butylamine, form precipitates in carbonated 95 water at room temperature but the heat released from the exothermic reaction of the amine and carbonated water can warm the solution enough to dissolve the bicarbonate salts completely. Six secondary amines were confirmed to display SHS behaviour. With the exception of dipropylamine, each of these secondary amine SHSs contained sec-butyl or isopropyl groups to destabilize carbamate salts. Converting bicarbonate salts of sterically hindered secondary amine SHSs to CO 2 and neutral 10 amine was achieved at 65 o C while passing N 2 through solution. Dipropylamine/water mixtures became biphasic upon heating to 65 o C even without bubbling N 2 through solution, but the solution became monophasic again when cooled to room temperature. Dipropylamine's temperature-dependent miscibility with 15 carbonated water has been observed before, 26 but is not the desired behaviour for a SHS. When the solution was heated to 90 o C for 2 h without N 2 passing through it, it became biphasic and remained biphasic when cooled to room temperature. The increased temperature requirement to remove CO 2 from the 20 solution is consistent with the formation of carbamate salts, as expected for sterically unhindered secondary amines such as dipropylamine. 13 C NMR analysis of carbonated water/dipropylamine solutions confirmed the presence of both bicarbonate salts and carbamate salts in solution, while no 25 carbamates were observed for mixes of carbonated water with sterically-hindered secondary amine SHSs (See Supplementary  Information).
Every secondary amine SHS, except di-sec-butylamine, switched from a biphasic solution to a monophasic solution after 30 less than 10 min of bubbling CO 2 through the solution, while tertiary amines switch after 20 to 120 min. Di-sec-butylamine switched at a pace comparable to tertiary amine SHSs. The two sec-butyl groups may be either decreasing the rate of carbamate formation substantially or preventing carbamate formation 35 completely. Evidently, one branching group near the amine is enough to lower the energy requirements for removing CO 2 while still allowing for a rapid switch from biphasic to monophasic solutions.
While most of these amines were only tested for one full 40 switching cycle, we tested CyNMe 2 and butyl 3-(isopropylamino)propanoate for their ability to handle multiple cycles. The former was used for many cycles without difficulty but the latter can only be used for one cycle, because of significant hydrolysis of the ester during the removal of the CO 2 . 45 This problem may exist for other amino-esters as well.

Risk Evaluation of SHSs
In order for SHSs to be considered for use industrially, it is important to consider their effects on health and the environment, preferably in comparison to the solvents that they would replace.
In order to identify the safety and environmental effects of SHSs, 55 the LD 50 (oral, rat), boiling point, flash point, eutrophication potential (EP), and skin effects of all SHSs identified in this study and previous studies 1,2 are compared in Table 5. The reported safety and environmental data reveal trends in the safety risks and environmental impacts of SHSs. We used hexane and toluene as 60 representative conventional (non-switchable) solvents for comparison. The toxicities of SHSs were compared using oral LD 50 data (rat). Many SHSs do not have reported LD 50 values. In these cases, the U.S. Environmental Protection Agency's Toxicity 65 Estimation Software Tool (TEST) was used to predict oral LD 50 values. 29 We find that the predicted toxicities of amines are within a factor of 3 of reported LD 50 values 95% of the time (see supplementary information). Despite the inherent inaccuracy of toxicity predictions, we expect that SHSs with predicted LD 50 70 values above 2000 mg/kg are less toxic than SHSs with LD 50 values of around 500 mg/kg or lower. Oxygen-containing SHSs have consistently higher LD 50 values than dialkyl-and trialkylamine SHSs. Multiple different oral LD 50 values have been reported for toluene. While toluene is less toxic than 75 dialkyl-and trialkylamine SHSs, the varying reports of its LD 50 and the uncertainty of the predicted LD 50 values for other SHSs prevent us from drawing further conclusions. According to the LD 50 data, hexane is much safer than every SHS. However, LD 50 is a measure of acute toxicity, so solvents with chronic toxicity 80 may appear safe even though they are not. For example, hexane is a known chronic neurotoxin, a serious problem that is not made evident by LD 50 data. [30][31][32] The more volatile SHSs are not advantageous over toluene in terms of inhalation toxicity but the less volatile SHSs are 85 probably much safer than toluene. There is little data regarding this form of toxicity for the SHSs. The inhalation LC 50 Journal Name  Dimethylcyclohexane has a reported LC 50 (rat, 2 h) of 1.9 g/m 3 . 33 The . Almost every SHS is safer than toluene and hexane in terms of volatility and flammability. SHS containing another functional group in addition to an amine were designed to be less volatile and less flammable, and the data confirms that they are 35 safer than other SHSs by these metrics. Under the UN globallyharmonized system of classification, these heavier SHSs would be classified as combustible rather than flammable liquids (flash points > 60 o C). 83 The eutrophication potential of the SHSs was calculated using 40 a modified version of the equation described by Heijungs et. al, 84 replacing chemical oxygen demand with theoretical oxygen demand, which was calculated using an equation described by Baker, Milke, and Mihelcic. 85 The implications of these equations are that lower nitrogen content and higher oxygen content in a 45 compound lowers its eutrophication potential. As a result, oxygen containing SHS have less eutrophication potential than other SHSs, with amino esters having the lowest potential. Indeed, amino ester SHSs have eutrophication potentials similar to toluene and lower than hexane, despite their nitrogen content. 50 Skin effects are another concern for SHSs; 13 of the SHSs are corrosive. In order to differentiate between different levels of corrosion, different classes of corrosion as defined by the Globally Harmonized System were used where information was available. 83 A class 1A corrosive substance shows effects after 3 minutes of exposure and less than 1 hour of observation. A class 1B corrosive substance shows effects after 1 hour of exposure 5 and less than 14 days of observation. Class 1A corrosive SHSs should be avoided. Fortunately, two of the SHSs and many conventional solvents like toluene and hexane are irritants, rather than corrosive liquids. For many of the SHSs, skin effect data is unavailable. 10 Bioaccumulation is not a concern for SHSs. Compounds with logK ow values below 3.5 are considered to have low bioaccumulation potential. 86 All known amine SHSs have logK ow between approximately 1.2 and 2.5. The amidine SHSs would not bioaccumulate, despite their high logK ow values, because they are 15 hydrolytically unstable and therefore would not likely persist in the environment long enough to pose a bioaccumulation risk. Some conventional solvents (e.g. hexane) have moderate bioaccumulation potential, while others have low potential (e.g. toluene). 20 The use of volatile solvents results in volatile organic compound emissions and contributes to smog formation. 87 With regards to this environmental concern, solvents are generally expected to be more benign if they are less volatile. SHSs with additional functional groups are much less volatile than 25 conventional solvents like hexane and toluene. While volatile SHSs like triethylamine will have no advantages over conventional solvents, the low-volatility SHSs likely have less potential to contribute to smog formation than conventional solvents. 30 The persistence of a solvent when it is released into the environment is another concern. Compounds can degrade by a number of different pathways and it can be difficult to predict their persistence. However, some degradation trends relating to chemical structures have been observed. 88 Quaternary carbon 35 centres, extensive branching, heterocycles, and tertiary amines tend to decrease degradability. Features that increase degradability are oxygen atoms (particularly esters), unsubstituted alkyl chains of 4 or more, and unsubstituted phenyl rings. Secondary amine SHSs are also expected to be more 40 biodegradable than tertiary amine SHSs. Howard et al. found that tertiary amines are poorly biodegradable. 89 Eide-Haugmo et al. suggest that secondary amines are more degradable than tertiary amines. 90 Although amine biodegradation data is sparse and many exceptions are apparent, the literature data does support the 45 notion that secondary amines will biodegrade more readily than tertiary amines. [89][90][91][92][93][94] For example, dipropylamine is biodegradable while triethylamine is not. 94,95 Not all tertiary amines will persist however. The biodegradation of N,N-dimethylcyclohexylamine is not rapid, but it is considered to be biodegradable in an aqueous 50 environment (Zahn-Wellens test). 96 The available data also indicates that compounds with quaternary carbons are more resistant to biodegradation than straight chain compounds. A common opinion is that any branching will decrease biodegradability. However, Boethling et al. report that this is an 55 oversimplification and only extensive branching and quaternary carbons show a trend of decreasing degradability. 88 Many secondary amine SHS contain a branching group to destabilize carbamate formation. An ideal secondary amine SHS would include one branching group to destabilize the carbamate product 60 without significantly decreasing its biodegradability.
With regard to this information, secondary amino ester SHSs are expected to be the least persistent, particularly butyl 3-(isopropylamino)propanoate because it contains an n-butyl group. Tertiary amine SHSs containing other functional groups and 65 dialkylamine SHSs are second choices, while trialklyamine SHSs will likely persist longer than the other SHSs. Toluene and hexane contain groups favourable to degradation and no groups resistant to degradation. These conventional solvents are both biodegradable. 97,98 Trialkylamine SHSs should be more persistent 70 than conventional solvents, but we expect secondary amine SHSs and tertiary amine SHS with a second functional group to have biodegradability comparable to or better than conventional solvents.
While no SHS can be identified as being ideal, the structural 75 features that generate the most benign SHSs can be determined from the above trends. The data available for oxygen-containing SHSs suggest that they are less toxic and less volatile than di-and tri-alkyl amine SHSs. They are also no more corrosive and have lower eutrophication potentials, making them the most benign 80 SHSs identified according to the metrics listed in this study. However, the risk of hydrolysis, which limit the reusability of aminoesters, suggests that they may not be ideal. The amidine SHSs also have favourable safety and environmental properties apart from a larger eutrophication potential and likely corrosivity, 85 but they are unlikely ever to be used because of their high cost of synthesis. No differences between secondary and tertiary amine SHSs are apparent from the data in Table 5, but the secondary amines are likely to be more biodegradable. Not every risk is identified in Table 5. There is insufficient data to comment on 90 chronic toxicity or carcinogenicity. Because of these uncertainties, we do not recommend a single SHS as the most benign but rather we recommend consideration of all of their properties before one is used and more research including the identification of even better SHS. 95 There are other considerations which can also be used to differentiate between SHSs. Some SHSs, such as the amino acetal, the aminoesters, and the amidines are prone to hydrolysis and are likely to degrade over time. Dipropylamine forms a stable carbamate salt and more energy must be put into the system to 100 convert the salt back into CO 2 and neutral amine. Some SHSs also require different amounts of water to display switchability. Most SHSs work at a 1:1 volume ratio, but some require a 2:1 or even 5:1 water:amine volume ratio. The amount of energy required to heat the water when removing CO 2 increases as the 105 amount of water increases. Some SHSs switch faster than others as well. In particular, secondary amines switch from biphasic to monophasic mixtures faster than tertiary amines. None of these factors are apparent from the information given in Table 5, but they can affect the overall viability of an SHS. an exception (pK aH 9.03), but is only switchable if the volume of water is much larger than the volume of amine. Secondary amines can also display switchable behaviour but can form carbamate salts and precipitate as bicarbonate salts. Secondary amine SHSs can be designed to avoid significant carbamate 5 formation by making them sterically hindered. Amines incorporating other functional groups are more benign than other SHSs, commonly having lower toxicity, volatility, flammability, and eutrophication potential. Compared to toluene, the secondary amine ester SHSs are predicted to be safer for health and the 10 environment in terms of flammability, smog formation, inhalation toxicity, and bioaccumulation (lower K ow ). They are comparable to toluene in terms of eutrophication and possibly biodegradation. The variety of compounds identified and their different properties show that SHSs can be designed to meet the requirements of an 15 application.

Experimental
Chemicals were used as received. Amines were commercially available (Sigma-Aldrich, TCI, Fisher) except for amino propanoate/butanoate esters and amino ketones, which were 25 synthesized and characterized as described below. Argon (99.998%) and CO 2 (chromatographic grade) were purchased from Praxair.

Testing for Switchable Behaviour
To confirm the switchable miscibility, amines were mixed with 30 water in a 1:1 volume ratio. If two phases were observed, CO 2 was bubbled into the solution through a gas dispersion tube (Ace Glass, 25-50 micron porosity) for 2 h. If the mixture became monophasic, N 2 was bubbled into the solution through a gas dispersion tube for 2 h while the solution was heated to 65 o C. If 35 the mixture became biphasic again, the amine was classified as a SHS. Other volume ratios were attempted for some amines.

Evaluation
LogK ow values were predicted using ALOGPS 2.1. [17][18][19] pK aH values were found from literature or determined titrimetrically. 40 Flash points, skin effects, and LD 50 values were found from literature or MSDS. If flash point or LD 50 values were unavailable, they were calculated using the TEST program. 29 Eutrophication potentials (EP) were calculated using a variation of the method proposed by Heijungs et al., which calculates the 45 eutrophication potential of a compound based on its molecular weight (MW), the number of phosphorus and nitrogen atoms it contains (ν P and ν N ), and its theoretical oxygen demand (ν ThOD )(equations 3 and 4). 84 Theoretical oxygen demands were calculated using the method described by Baker, Milke, and 50 Mihelcic (equations 5 and 6), 85 Dibutylammonium Bicarbonate Crystal Formation 60 Dibutylamine (5 mL) and water (5 mL) were combined in a vial. CO 2 was bubbled through the mixture until a large quantity of precipitate formed. The mixture was heated to 40 o C, resulting in a biphasic mixture with no solids. Upon cooling to room temperature, needle-like crystals formed at the interface between 65 the liquid phases.

Observation of Secondary Amine Speciation in Carbonated Water
Amine (dipropylamine, di-sec-butylamine, or secbutylisopropylamine, 1 mL) was mixed with 1 mL H 2 O in a vial 70 and CO 2 was bubbled through the solution until it became monophasic. CH 3 CN (0.2 mL) was added to solution as a reference compound and the solution was characterized by 13 C { 1 H} NMR spectroscopy.
Measuring the pK aH of amines 75 For most amines, a ~20 mL solution containing ~0.02 g amine in distilled water was titrated with ~0.1 M HCl. The pH of the solution was recorded after each addition of titrant (Orion 4 Star pH meter, Thermo Scientific). The equivalence point was determined using a derivative plot and the pH at the half 80 equivalence point was taken as the pK aH of the amine. Titrations were performed at least twice.
Dibutylaminobutanol and dibutylaminopropanol were not sufficiently soluble in water to measure their aqueous pK aH directly. The pK aH of these compounds were measured in ethanol- 85 water solutions and extrapolated to a completely aqueous solution using the method described by Gowland and Schmid. 99 Synthesis Amino esters and ketones were synthesized using procedures adapted from literature for similar compounds. 100,101 NMR spectra 90 were collected on a Bruker Avance-500 or a Bruker Avance-300 NMR spectrometer. IR spectra were collected with a Varian 640 FT-IR spectrometer. Mass Spectra were collected with a Perkin Elmer Clarus 600 T mass spectrometer connected to a Perkin Elmer Clarus 680 gas chromatograph. 95 Ethyl 3-(diethylamino)propanoate. Ethyl acrylate (9.2 g, 0.092 mol) and diethylamine (6.7 g, 0.092 mol) were added to a round bottom flask and stirred for 24 h. Distillation under vacuum afforded the pure product (14.9 g, 94% yield); bp 57  Distillation afforded the pure product (3.9 g, 60% yield); bp 72 o C (4 torr): 1  Propyl 3-(sec-butylamino)propanoate. Using the same procedure as for ethyl 3-(sec-butylamino)propanoate, 2.1 g (0.021 mol) of propyl acrylate and 2.7 g (0.037 mol) of sec-butylamine yielded 3.2 g of product (92.7% yield); bp 74 o C (4 torr): 1 H