NOVEL MINIMUM BOILING AZEOTROPE OF N-BUTYL-3-HYDROXYBUTYRATE AND N-UNDECANE AND APPLICATION OF THE AZEOTROPE TO SOLVENT CLEANING
20180362894 ยท 2018-12-20
Assignee
Inventors
Cpc classification
C11D7/5031
CHEMISTRY; METALLURGY
International classification
Abstract
A novel minimum boiling binary azeotrope of n-undecane and n-butyl-3-hydroxybutyrate is shown to have utility as a solvent for degreasing of both nonpolar and polar contaminants. The components of the azeotrope are stable against degradation and the composition is largely invariant with pressure, yielding a unique solvent that can be used in cold cleaning and in vapor degreasing at elevated temperatures and over a wide range of pressures.
Claims
1. A minimum-boiling, binary azeotrope comprising a linear alkane comprised of at least 9 carbon atoms and an ester alcohol.
2. The azeotrope according to claim 1, wherein the linear alkane comprises n-undecane.
3. The azeotrope according to claim 1, wherein the ester alcohol comprises n-butyl-3-hydroxybutyrate.
4. The azeotrope according to claim 1, which is homogeneous.
5. The azeotrope according to claim 1, which comprises 18-23 mole % of the ester alcohol and 77-82 mole % of the linear alkane.
6. A solvent for cleaning machined metal parts, the solvent comprising the azeotrope according to claim 1.
7. The solvent according to claim 6, comprising a cold-cleaning solvent.
8. The solvent according to claim 6, comprising a vapor degreasing solvent.
9. A method for cleaning a machined metal part, comprising contacting the machined metal part with the solvent according to claim 7.
10. A method for cleaning a machined metal part, comprising exposing the machined metal part to the vapor of the solvent according to claim 8.
11. The method according to claim 9, which removes both polar and nonpolar contaminants from the machined metal part.
12. The method according to claim 10, which removes both polar and nonpolar contaminants from the machined metal part.
Description
BRIEF DESCRIPTION OF DRAWINGS
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[0018]
[0019]
DETAILED DESCRIPTION
[0020] As a matter of practicality, solvents for vapor degreasing applications have normal boiling points below approximately 195-200 C. As such, pure n-butyl-3-hydroxybutyrate (Eastman Omnia), disclosed in U.S. Pat. No. 9,163,202 which is hereby incorporated by reference in its entirety is an ester alcohol with a normal boiling point of 217 C., is not suitable as a single solvent for vapor degreasing. However, it has been unexpectedly discovered that introduction of a second component and formation of a minimum boiling binary azeotrope with n-butyl-3-hydroxybutyrate can facilitate use of the molecule as a vapor degreasing solvent. Minimum boiling azeotropes occur due to liquid phase non-idealties and are manifested as positive deviations (activity coefficients, .sub.i>1) from Raoult's Law that arises from dispersive forces between molecules in a binary liquid mixture. These interactions are governed by properties inherent to molecular structure and include weak Van der Waals forces, nonpolar-polar effects and influences due to hydrogen bonding. Positive deviations from ideality tend to occur when dissimilar molecules are mixed and arise from disruption of hydrogen bonding networks or interactions between polar and nonpolar molecules. Larger differences in the H-bonding characteristics or polar-nonpolar nature or of the molecules lead to larger activity coefficients.
[0021] A suitable azeotroping agent for n-butyl-3-hydroxybutyrate can be projected by analysis of the structure of the molecule. The potential and extent of H-bonding character can be qualitatively predicted by classification of the molecular functional groups. The n-butyl-3-hydroxybutyrate molecule has three main functional groups: a secondary alcohol group, an ester functionality and a C.sub.4 paraffinic chain connected to the ester oxygen atom. The secondary alcohol functionality is of the H-bond acceptor-donor (HBAD) class and could form a minimum boiling azeotrope with non-bonding (NB) molecules (e.g., paraffins, aprotic halogen salts, thiols, sulfides), molecules with H-bond donating (HBD) groups (e.g., inorganic acids, protic halogen salts), other molecules with HBAD functionalities (e.g., alcohols, glycol ethers, 1 and 2 amines, mono/peracids) and H-bond acceptor (HBA) groups (e.g., ethers, carbonyl compounds, heteroatom aromatics, halogenated paraffins). The ester functionality of n-butyl-3-hydroxybutyrate is of the HBA class and deviations due to H-bonding networks occur with groups from the aforementioned HBAD classification and with molecules containing strongly associative H-bonding (HBSA) groups (e.g., water, 1 and 2 amides, polyacids, polyols, amino alcohols). Although possible, the ester group is less likely to form azeotropes with NB and HBA class functionalities, as these interactions do not affect H-bonding and are likely to be ideal or quasi-ideal. The C.sub.4 paraffinic functionality of n-butyl-3-hydroxybutyrate may form an azeotrope by breaking the H-bonding network of molecules with HBSA or HBAD character. Less probable is the formation of a minimum boiling azeotrope with other NB groups and with molecules having HBD or HBA functionalities, as these systems are also likely ideal.
[0022] The structure and functional groups present in a molecule also affects polar-nonpolar interactions, with large differences in polarity giving rise to greater deviations from ideality. As a result, the moderately polar alcohol and ester functionalities of n-butyl-3-hydroxybutyrate could be expected to form azeotropes with significantly more polar molecules like water or several nonpolar functionalities. The list of nonpolar groups with which n-butyl-3-hydroxybutyrate may display significant non-ideal binary character include, in increasing order of likelihood: ketones, aldehydes, ethers, aromatics, olefins and paraffins. Furthermore, increased branching of more nonpolar azeotroping molecules with n-butyl-3-hydroxybutyrate will also impart higher nonpolar character. Salts, acids and N- and S-containing molecules were omitted from consideration as components of a vapor degreasing solvent. The compounds most likely to form minimum boiling azeotropes with n-butyl-3-hydroxybutyrate are close boiling molecules of hydrocarbons, ethers (including glycol ethers), halogenated paraffins, alcohols (including polyols), and carbonyl compounds like aldehydes, ketones and other esters. Halogenated paraffins were also not considered as these are typically low boiling compounds. In addition to solvency performance, the binary azeotrope must also satisfy physical property requirements for a degreasing solvent. These properties include boiling point, surface tension, flash point, latent heat of vaporization and resistance to thermal degradation and hydrolytic attack. Furthermore, the solvent must possess excellent material compatibility and a favorable EHS profile, including low toxicity, zero ozone depleting potential (ODP), low global warming potential (GWP), low vapor pressure VOC status and not act as a hazardous air pollutant (HAP).
[0023] Described in the present invention is a novel minimum boiling homogeneous azeotrope of n-undecane, a linear alkane, and n-butyl-3-hydroxybutyrate (n-butyl-3-hydroxybutyrate), an ester alcohol, and application of the azeotropic blend to simultaneous degreasing of both nonpolar and polar soils. The alkane component of the azeotrope functions to clean lipophilic contaminants with more nonpolar, water-insoluble character. The ester alcohol molecule of the azeotrope, with ester and alcohol functionalities, serves to provide solvency for hydrophilic water-soluble contaminants. The high hydrogen bonding and polar Hansen solubility parameters of n-butyl-3-hydroxybutyrate exceed the solvating ability of propylene glycol ether-based solvents towards hydrophilic soils. The n-butyl-3-hydroxybutyrate molecule has a unique chemical structure with a very polar ester alcohol functionality and a relatively nonpolar C4 aliphatic chain. The total Hansen solubility parameter of n-butyl-3-hydroxybutyrate exceeds the polar and hydrogen bonding solvency of the propylene glycol ethers and is equivalent to the ethylene glycol ether series of solvents. The highly nonpolar undecane component of the blend imparts greater nonpolar solvency than glycol ethers with aliphatic character like DMM. Furthermore, the amphiphilic nature of n-butyl-3-hydroxybutyrate diminishes deposition of waxy residues that are characteristic of solvents with high paraffinic character by acting as a pseudo-surfactant. In addition to having good solvency power for both nonpolar and polar soils, the azeotropic blend is nonflammable (flash point>60 C.), non-toxic and not a hazardous air pollutant, with zero ozone depleting potential (ODP) and low global warming potential (GWP).
[0024] The existence, composition and boiling point temperature of the azeotrope at isobaric conditions was initially estimated by the Dortmund modified UNIFAC group contribution method. The UNIFAC method uses interactions between characteristic functional groups of each molecule to predict activity coefficients of non-ideal liquid mixtures. The method predicts a minimum-boiling azeotrope with a nearly constant composition of 22 mol % n-butyl-3-hydroxybutyrate and 78 mol % n-undecane over typical vapor degreaser operating pressures. That is, the azeotropic liquid and vapor composition are largely invariant with pressure due to similarities in heats of vaporization of both components of the binary azeotrope. For example, over an operating pressure range of 25-760 Torr, the composition of the azeotrope varies by less than 3 mol %. Since the azeotropic composition does not appreciably change, the liquid solvent as formulated is always, at the very least, near azeotropic and does not enable significant enrichment of the vapor phase with the lighter component. As a result, different blended compositions of n-butyl-3-hydroxybutyrate and n-undecane are not required for operating at different pressures. Moreover, some azeotrope mixtures lose azeotropic behavior all together at reduced pressures. However, the n-butyl-3-hydroxybutyrate-undecane azeotrope retains azeotropic behavior from atmospheric pressure to below 1 Torr of pressure. Such a pressure insensitive azeotrope provides a unique advantage by supplying constant solvency power at any operating pressure and allows for application of the azeotrope to degreasing from pressures below 10 Torr to atmospheric conditions.
[0025] The attractive Hansen solubility parameters of the blend permit application of the formulated solvent to cleaning of polar and nonpolar contaminants. As such, the azeotrope can be employed in both cold cleaning applications (immersion, spraying, wiping) and vapor degreasing of machined metal parts. The azetrope has nearly universal compatibility with metals and broad suitability with most elastomers. Furthermore, the azeotrope has boiling points similar to modified alcohol solvents but a lower surface tension, permitting better part penetration in vapor degreasing applications. The low boiling point permits facile recovery of the azeotrope from high boiling contaminants by vacuum distillation. The azeotrope is only partially miscible with water, with pure component n-butyl-3-hydroxybutyrate displaying solubility up to 3.9% water, while undecane is completely immiscible. At the azeotropic composition, the miscibility limit of water in the solvent blend at 25 C. is only 0.20-0.25 wt. %. As a result, water contamination is easily removed by conventional gravity decantation methods and the ester functionality of n-butyl-3-hydroxybutyrate is largely protected from hydrolytic degradation.
EXAMPLE 1
Vapor-Liquid Equilibrium Measurements
[0026] The true azeotropic composition was determining by measuring activity coefficients at infinite dilution. The non-idealities of the liquid solution were measured under isobaric conditions at 100 Torr assuming ideal vapor behavior by a differential ebulliometry technique. Samples of highly pure (>99.5 wt. %) n-undecane and n-butyl-3-hydroxybutyrate both available from Eastman Chemical Company in Kingsport, Tenn. were used for the measurements. Prior to analysis, the pure liquid samples were dried over calcium sulfate desiccant (Drie-rite) for one week. For measurement of the infinite dilution activity coefficients of n-butyl-3-hydroxybutyrate in n-undecane solvent, 150 mL samples of n-undecane were charged to two equilibrium boiling stills (ebulliometers) connected in parallel to a single pressure manifold through a ballast tank. Pressure was maintained at 100 Torr absolute via a Ruska pressure controller. The boiling chambers were vacuum insulated and silvered and the liquid contents were stirred with magnetic Teflon stir bars. Vapor temperatures above the boiling liquids were measured via centrally-placed thermowells containing calibrated platinum resistance thermometers. Heating of the still pots was accomplished by cartridge heaters that were supplied by rheostats connected to Eurotherm temperature controllers. One ebulliometer always contained pure solvent (reference still) while small (Table 9) calibrated additions of solute were made to the second ebulliometer (addition still) through a septum-sealed injection port. The temperatures and pressures of both ebulliometers were continuously monitored and small changes in the liquid boiling point in the addition still were recorded after each solute injection. Boiling point changes were noted after re-establishment of equilibrium as indicated by stable temperatures and pressures. Temperature changes were measured with a span of less than 0.05 C. and averaged over a recording time of 5 minutes. The solute addition, equilibration and boiling point difference measurement was repeated 5-6 times. The experiment was repeated for n-undecane solute infinitely diluted in n-butyl-3-hydroxybutyrate solvent to define the activity coefficients for both components.
[0027] The limiting activity coefficients for each component were regressed to the Wilson equation by measuring the small changes in boiling point temperatures of solvent that result from additions of accurately weighed injections of solute (to within 0.001 g). Temperature changes were plotted versus mole fraction of solute and the slope of the plot with the saturated vapor pressures were used to calculate the infinite dilution activity coefficients. Wilson parameters at 100 Torr were calculated directly from the measured activity coefficients at infinite dilution. Regression of the Wilson equation parameters at infinite dilution allows for prediction of the activity coefficients for each component over the entire composition range. Calculation of the binary VLE by using the Wilson equation activity coefficient model confirms the existence of a minimum boiling azeotrope at a composition of 19.56 mol % n-butyl-3-hydroxybutyrate and 80.44 mol % n-undecane, in good agreement with the UNIFAC prediction. The ebulliometry data and regressed parameters are in Appendix A.
EXAMPLE 2
Vapor Degreasing of Straight Oil by Weight Loss
[0028] The cleaning efficacy of the n-butyl-3-hydroxybutyrate-undecane azeotrope was first tested against a highly nonpolar heavy straight oil (Castrol MolyDee) containing refined petroleum oil, paraffin waxes as lubricants and chlorinated paraffins as high pressure additive. As a comparison, neat n-undecane and a zeotropic blend of PnB-DMM containing a lower alcohol additive to increase polar solvency were tested as standards. For each experiment, a coating of the straight oil was added to 1 cm5 cm0.2 mm aluminum test coupons and baked on in an 80 C. oven for 16 hrs. For vapor degreasing testing, the cleaning solvent was added to a 2 L thermostatically-jacket glass test reactor. Heating of the solvent was controlled by circulating a high temperature heat transfer fluid through the jacket and vacuum was supplied by a diaphragm-style vacuum pump. Multiple test coupons could be suspended in the vapor space and tested simultaneously. Cleaning efficiency was quantitated by total weight loss of oil contaminant from the aluminum coupons. A total of ten total coupons for each test were used to determine the average weight loss and the standard error in the measurements. For each test, the solvent was pre-heated to the boiling point temperature at the expected operating pressure. The ten pre-weighed coupons were then suspended in the vapor space of the reactor and the pressure rapidly reduced to either 300 or 100 Torr. Once at pressure, the vapor degreasing process was conducted for 15 minutes under total reflux of the solvent. After the elapsed cleaning time, the reactor was backfilled with room air and the test coupons were removed. The just-cleaned dry coupons were immediately weighed to determine the total weight loss of straight oil. Subsequently, visual inspections of the coupons were made to determine the presence of any deposits and each test strip was wiped with a lint-free white cloth to further visualize residual contaminants. The test coupons were also examined by the water break test. Due to the surface tension of water, the presence of residual nonpolar contaminants will cause water to form discrete beads. Conversely, water will flow off the part in a continuous film from a fully cleaned surface. This test was conducted by submerging the piece in distilled water and allowing water to drain from the vertically-oriented test coupon for 15 s. The presence of water break was determined by simple visual inspection. After these subsequent qualitative tests, the coupons were thoroughly cleaned with acetone, hexane and toluene prior to measuring the weight of the blank, unsoiled coupons for weight loss calculations. Table 1 shows the cleaning efficiency results for the three tested solvents for removal of the straight oil contaminant.
TABLE-US-00001 TABLE 1 Cleaning Results of a Straight Oil with Tested Solvents P Cleaning Cleaning Solvent (Torr) T.sub.boil ( C.) Efficiency (%) Appearance PnB-DMM blend + ROH 300 133 98.3 0.7 shiny; free of residue; no water break Omnia-undecane azeotrope 158 98.0 1.3 shiny; free of residue; no water break neat n-undecane 163 95.4 0.4 hazy; slight residue; positive water break PnB-DMM blend + ROH 100 101 98.5 0.4 shiny; free of residue Omnia-undecane azeotrope 125 99.9 0.1 shiny; free of residue neat n-undecane 128 96.6 0.1 hazy; slight residue; positive water break
[0029] At 300 Torr, the modified PnB-DMM blend and the n-butyl-3-hydroxybutyrate-undecane azeotrope cleaned with similar efficiency, in agreement with the observations of clean, residue free surfaces exhibiting no water break. Similar to literature observations, the neat-undecane solvent cleaned with less efficiency and a noticeable, white hazy residue was deposited on the test coupon surfaces. A positive test for water break was also observed on coupons after cleaning with only n-undecane. After cleaning at 100 Torr, the n-butyl-3-hydroxybutyrate-undecane azeotrope cleaned with slightly higher performance than the modified PnB-DMM blend, although both surfaces appeared clean and residue free with further qualitative testing. Again, a waxy residue was observed on the surface of the aluminum coupons cleaned with neat n-undecane.
EXAMPLES 3-4
Cleaning Performance by Ultraviolet Fluorescence
[0030] The cleaning performance of the n-butyl-3-hydroxybutyrate-undecane azeotrope was further evaluated in degreasing of two additional contaminants by fluorescence measurements. Many organic materials in common metalworking soils fluoresce when exposed to ultraviolet radiation. For these measurements, an ultra-heavy duty straight oil (Comminac SCS27) and an emulsifiable oil (Starsol 775AL) were selected. The straight oil is largely nonpolar in nature while the emulsifable/soluble oil contains a number of highly polar amine-based additives and sodium sulfonate surfactants. The n-butyl-3-hydroxybutyrate-undecane azeotrope of the present invention was tested against a PnB-DMM binary blend and a PnB-DMM blend modified with an additional alcohol additive for improved polar solvency. In a similar fashion to previous testing, a coating of the oil contaminant was applied to aluminum test coupons and dried on overnight at room temperature. Before application of the soil and prior to cleaning, the test coupons were placed under a blacklight and a high resolution photograph at close range was taken. The soiled test coupons were then subjected to one of two cleaning steps: cleaning by immersion in the hot solvent at atmospheric pressure for 2 minutes followed by 3 minutes of vapor degreasing at 100 Torr, or a 5 minute cleaning time by vapor degreasing only (also at 100 Torr). Immediately after the prescribed cleaning treatment, the dry test coupons were again placed under a blacklight and photographed.
[0031]
[0032] The left panel shows the blank unsoiled test coupons while the right panel shows representative panels completely soiled with contaminant. In the inset of the right photograph, label A designates the straight oil soil while label B identifies the soluble emulsifiable oil. Using a pixel counting software, the ultraviolet fluorescence intensity was determined and corrected for background fluorescence. Table 2 shows the averages of the mean and maximum background-corrected intensities representative of the blank and soiled coupons.
TABLE-US-00002 TABLE 2 Average Values of Fluorescence Intensities of Blank and Soiled Test Coupons Fluorescence Intensity (a.u.) Mean Maximum Condition Blank Al test coupons <60 <150 Clean Heavy straight oil (A) 155 215 Unclean Emulsifiable oil (B) 206 255 Unclean
[0033] The mean and maximum fluorescence intensities of the unsoiled blank coupons were consistently below values of 60 and 150, respectively. As a result, these limits were assumed as cleanliness boundaries and measured intensities below these values indicate a clean part.
[0034]
[0035] By visual inspection, the PnB-DMM blend appears to thoroughly clean the nonpolar soil (A1 and A2) by both cleaning methods. PnB is formulated with DMM to improve nonpolar solvency and the solvent performs well at removing the straight oil. However, noticeable fluorescent residue remains on the test coupons soiled with a more polar emulsifable oil, regardless of the cleaning method. As expected, a combination cleaning step of immersion and vapor degreasing (B1) yields better cleaning performance than vapor degreasing alone (B2). These qualitative results are in agreement with the direct quantitative measurements of fluorescence intensity as presented in Table 3.
TABLE-US-00003 TABLE 3 Fluorescence Intensities of Post-Cleaned Coupons with PnB-DMM Blended Solvent Fluorescence Intensity (a.u.) Mean Maximum Condition Straight Oil + Immersion + Vapor (A1) 60 150 Clean Soluble Oil + Immersion + Vapor (B1) 68 194 Unclean Straight Oil + Vapor Only (A2) 60 150 Clean Soluble Oil + Vapor Only (B2) 85 183 Unclean
[0036] The cleaning performance of the simple PnB-DMM solvent was compared directly to a PnB-DMM blend modified with an alcohol for improved polar solvency.
[0037] The PnB-DMM azeotrope with an alcohol additive again performs well for cleaning the straight oil (Al and A2), presumably by the PnB-DMM solvency of the mixture. Visual inspection of cleaning efficacy for the more polar soluble oil (B1 and B2) reveals improved degreasing capability over the more lipophilic unmodified PnB-DMM solvent. However, by vapor degreasing alone, the presence of fluorescent residue is readily apparent. Table 4 displays the post-cleaning fluorescence measurements for degreasing with PnB-DMM+ROH.
TABLE-US-00004 TABLE 4 Fluorescence Intensities of Post-Cleaned Coupons with PnB-DMM + ROH Solvent Fluorescence Intensity (a.u.) Mean Maximum Condition Straight Oil + Immersion + Vapor (A1) 60 150 Clean Soluble Oil + Immersion + Vapor (B1) 60 150 Clean Straight Oil + Vapor Only (A2) 60 150 Clean Soluble Oil + Vapor Only (B2) 78 246 Unclean
[0038] The quantitative fluorescence results agree with the conclusions reached by visual inspection of the cleaned test coupons. The added polar solvency resulted in noticeable improvement over the unmodified PnB-DMM blend, although the more polar soluble oil was not completely removed solely by vapor degreasing. The post-cleaning degreasing performance of the novel n-butyl-3-hydroxybutyrate-undecane azeotrope is displayed in
[0039] From visual inspection, the n-butyl-3-hydroxybutyrate-undecane azeotrope appears to clean both nonpolar and polar contaminants equally well, showing improved polar solvency compared to the PnB-DMM blend and the alcohol modified solvent. No fluorescent residue is perceptible on any cleaned test coupons, suggesting broad solvency for both types of soils. Furthermore, the n-butyl-3-hydroxybutyrate-undecane azeotrope appears to successfully clean the test coupons by vapor degreasing alone, a marked improvement over the two control solvents. As shown in Table 5, the fluorescence measurements agree with the visual observations of the novel azeotrope degreasing performance.
TABLE-US-00005 TABLE 5 Fluorescence Intensities of Post-Cleaned Coupons with n-butyl-3- hydroxybutyrate-Undecane Azeotrope Solvent Fluorescence Intensity (a.u.) Mean Maximum Condition Straight Oil + Immersion + Vapor (A1) 60 150 Clean Soluble Oil + Immersion + Vapor (B1) 60 150 Clean Straight Oil + Vapor Only (A2) 60 150 Clean Soluble Oil + Vapor Only (B2) 60 150 Clean
EXAMPLE 5
Hydrolytic Stability of n-butyl-3-hydroxybutyrate-Undecane Azeotrope
[0040] The carbonyl carbons of esters are susceptible to nucleophilic attack by water to form the corresponding alcohol and carboxylic acid by the process of hydrolysis. For n-butyl-3-hydroxybutryate (n-butyl-3-hydroxybutyrate), the molecule will hydrolyze to n-butanol and 3-hydroxybutyric acid. After production, the ester alcohol contains nearly 1-2 wt. % water from the synthesis process. In order to determine the hydrolytic stability of n-butyl-3-hydroxybutyrate, the n-butyl-3-hydroxybutyrate-undecane azeotrope was subjected to repeated boiling-cooling cycles. For each cycle, the azeotrope was refluxed (at 160 C.) for 1 hour at 300 Torr and subsequently cooled to room temperature. After each cycle, a small sample of the azeotrope was collected and analyzed by gas chromatography for the presence of hydrolysis products. Over five cycles, no evidence of n-butyl-3-hydroxybutyrate hydrolysis products were detected. Table 6 shows the normalized compositions of n-butyl-3-hydroxybutyrate (nBHB), water and the hydrolysis products n-butanol (n-BuOH) and 3-hydroxybutyric acid (3-HBA) after each cycle.
TABLE-US-00006 TABLE 6 Ester Hydrolysis of n-butyl-3-hydroxybutyrate-Undecane Azeotrope Component (Normalized wt. %) Cycle nBHB Water n-BuOH 3-HBA 1 97.97 2.01 0.01 0.01 2 98.15 1.80 0.05 0.00 3 98.11 1.82 0.07 0.00 4 98.12 1.81 0.07 0.00 5 98.13 1.82 0.05 0.00
[0041] The results of Table 6 show no evidence of significant ester hydrolysis. The small presence of n-butanol is an impurity present from the manufacture of n-butyl-3-hydroxybutyrate. No evidence for formation of 3-hydroxybutyric acid was observed. Furthermore, the amount of intrinsic water present in the samples is near the saturation point of n-butyl-3-hydroxybutyrate and representative of typical upper limits of water contamination in solvent cleaning.
EXAMPLE 6
Acid Hydrolysis Stability of n-butyl-3-hydroxybutyrate-Undecane Azeotrope
[0042] Extreme pressure additives are often supplemented to machining oils in order to provide improved lubrication during high pressure machining processes. These additives chemically react with the microscopic asperities of the metallic surface at high pressures to form a smooth sacrificial film that prevents deleterious friction. Extreme pressure additives are typically organic phosphorus, sulfur or chlorine compounds and include species such as polysulfides, sulfurized hydrocarbons and chlorinated paraffins, respectively. Chlorinated hydrocarbons are widely used as lubricating additives but are known to readily hydrolyze to form HCl in the presence of water and high temperatures, both during machining and degreasing processes. The generation of HCl leads to rapid corrosion of the metal parts and cleaning solvents are often augmented with amine-based stabilizers to neutralize the acid. The presence of HCl can also catalyze the acid-promoted hydrolysis of n-butyl-3-hydroxybutyrate. In order to determine the acid hydrolysis stability of the n-butyl-3-hydroxybutyrate-undecane azeotrope, a highly chlorinated straight oil (Prodraw 2300) containing chlorinated paraffins was added to the azeotrope at a concentration of 1 wt. %. The contaminated solvent was then refluxed at 100 Torr (125 C.). Samples of the solvent were collected at 2, 4, 6 and 24 hours of reflux time and analyzed by gas chromatography for the presence of hydrolysis products. Table 7 shows the results for detection of hydrolysis products of n-butyl-3-hydroxybutyrate.
TABLE-US-00007 TABLE 7 Acid Hydrolysis Stability of n-butyl-3-hydroxybutyrate-Undecane Azeotrope Reflux Time Component (Normalized wt. %) (hr) nBHB Undecane Water n-BuOH 3-HBA 2 21.89 78.10 0.08 0.01 0.00 4 21.97 78.03 0.00 0.00 0.00 6 21.93 78.07 0.05 0.00 0.00 24 21.96 78.04 0.00 0.00 0.00
[0043] The results in Table 7 reveal no evidence of acid promoted hydrolysis of n-butyl-3-hydroxybutyrate in the presence of a highly chlorinated straight oil. No formation of the n-butyl-3-hydroxybutyrate hydrolysis products, n-butanol and 3-hydroxybutyric acid, were detected, even after 24 hours at elevated temperatures.
EXAMPLE 7
Water Miscibility in n-butyl-3-hydroxybutyrate-Undecane Azeotrope
[0044] The discovery that the ester functionality of the n-butyl-3-hydroxybutyrate molecule was largely resistant to hydrolytic attack in both the presence of water and hydrolyzed chlorinated paraffins was an interesting discovery. The hydrolytic decomposition of esters to their corresponding alcohol and carboxylic acid substituents is typically a facile process. However, in the presence of low water concentrations in the organic phase, such reactions are typically suppressed. The actual concentration of water in the n-butyl-3-hydroxybutyrate-undecane azeotrope was investigated further by mixing the azeotrope with an appreciable amount of water past the miscibility limit. A 100 g sample of the azeotrope was prepared by mixing 80.05 g of dry n-undecane with 19.95 g of dry n-butyl-3-hydroxybutyrate. To this mixture, 10.00 g of water was added slowly, immediately forming a second heavy water layer. After the full water addition, the mixture was gently stirred for 2 hours at room temperature to allow for equilibration between the two liquid layers. After settling, a sample of each layer was collected. The heavy water layer was analyzed by gas chromatography while the lighter organic layer was analyzed by Karl Fischer titration. Table 8 below shows the partitioning of n-butyl-3-hydroxybutyrate and undecane into the heavy water layer, as analyzed by GC, and the total water content of the lighter organic azeotrope phase, by Karl Fischer titration.
TABLE-US-00008 TABLE 8 Phase Partitioning of n-butyl-3-hydroxybutyrate-Undecane Azeotrope + Water Component (Normalized Wt. %) Layer nBHB Undecane Water top (by KF titration) 0.22 bottom (by GC) 3.17 0.07 97.76
[0045] The bottom water layer contains a very small amount of n-undecane and n-butyl-3-hydroxybutyrate partitions to the water phase to the known solubility of n-butyl-3-hydroxybutyrate in water (3.0-3.5 wt. %). The amount of water in the lighter organic phase is only 0.22 wt. % at equilibrium. As a result, the presence of water tramp solvent in vapor degreasing can be easily removed by decantation. Furthermore, the low amount of water present in the organic phase may suppress the hydrolytic decomposition of the n-butyl-3-hydroxybutyrate ester functionality, due to the high hydrophobicity of the solvent phase.
APPENDIX A
n-butyl-3-hydroxybutyrate-Undecane Vapor Liquid Equilibrium Data and Plots
[0046]
TABLE-US-00009 TABLE 9 Ebulliometry Data at 100 Torr T ( C.) T ( C.) mol % Undecane 150.942 0.000 0.00 149.062 1.880 0.74 148.132 2.810 1.12 147.182 3.760 1.50 146.397 4.545 1.87 145.822 5.120 2.22 127.213 0.740 95.71 127.321 0.632 96.54 127.450 0.503 97.39 127.590 0.363 98.24 127.758 0.195 99.11 127.953 0.000 100.00
TABLE-US-00010 TABLE 10 Calculated VLE for n-butyl-3-hydroxybutyrate T ( C.) x.sub.1 y.sub.1 x.sub.2 y.sub.2 .sub.1 .sub.2 150.59 0.0000 0.0000 1.0000 1.0000 5.16 1.00 140.97 0.0500 0.3340 0.9500 0.6660 4.24 1.01 136.08 0.1000 0.4709 0.9000 0.5291 3.53 1.02 133.25 0.1500 0.5429 0.8500 0.4571 2.99 1.05 131.47 0.2000 0.5871 0.8000 0.4129 2.59 1.08 130.26 0.2500 0.6172 0.7500 0.3828 2.27 1.12 129.39 0.3000 0.6396 0.7000 0.3604 2.02 1.18 128.74 0.3500 0.6575 0.6500 0.3425 1.83 1.24 128.23 0.4000 0.6728 0.6000 0.3272 1.66 1.31 127.82 0.4500 0.6865 0.5500 0.3135 1.53 1.39 127.47 0.5000 0.6997 0.5000 0.3003 1.42 1.49 127.18 0.5500 0.7128 0.4500 0.2872 1.33 1.60 126.92 0.6000 0.7265 0.4000 0.2735 1.26 1.73 126.70 0.6500 0.7415 0.3500 0.2585 1.19 1.89 126.52 0.7000 0.7584 0.3000 0.2416 1.14 2.07 126.40 0.7500 0.7782 0.2500 0.2218 1.10 2.30 126.35 0.8000 0.8021 0.2000 0.1979 1.06 2.57 126.35 0.8044 0.8044 0.1956 0.1956 1.06 2.59 126.40 0.8500 0.8320 0.1500 0.1680 1.04 2.90 126.60 0.9000 0.8709 0.1000 0.1291 1.02 3.31 127.06 0.9500 0.9238 0.0500 0.0762 1.00 3.83 127.95 1.0000 1.0000 0.0000 0.0000 1.00 4.50 .sub.2Undecane .sub.1Azeotrope at 100 Torr