Checked by Spencer Eggen and Scott E. Denmark.
1. Procedure
(R)-2-(Benzhydrylidenamino)-3-phenylpropanoic acid tert-butyl ester. An oven-dried, 300-mL, four-necked, round-bottomed flask, equipped with an overhead mechanical stirrer, a 125-mL pressure-equalizing dropping funnel capped with an argon inlet, and two rubber septa (Note 1)) is charged with N-(diphenylmethylene)glycine tert-butyl ester (5.00 g, 16.9 mmol, 1.0 equiv) (Note 2), (S)-4,4-dibutyl-2,6-bis(3,4,5-trifluorophenyl)-4,5-dihydro-3H- dinaphtho[2,1-c:1',2'-e]azepinium bromide [(S)-1] (12.7 mg, 17.0 µmol, 0.001 equiv) (Note 3), benzyl bromide (2.41 mL, 3.47 g, 20.3 mmol, 1.20 equiv) (Note 4), and toluene (56.4 mL) (Note 5). The stirring mixture is cooled to ~0 °C in a 2-propanol bath (Note 6), and aqueous 48% potassium hydroxide solution (56.4 mL) (Note 7) is added dropwise over 33 min through the dropping funnel (Note 8). The mixture is stirred for 20 h at ~0 °C at a constant stirring speed (300 rpm) under an argon atmosphere (Note 9). The reaction mixture is diluted by the addition of water (113 mL) and the 2-propanol bath is removed. After being stirred for 15 min at ambient temperature, the reaction mixture is transferred to a 1-L separatory funnel, and toluene (100 mL) is added. The aqueous layer is separated and extracted twice with toluene (100 mL). The combined organic layers are washed with brine (100 mL) and dried over anhydrous magnesium sulfate (15 g). The resulting suspension is filtered and concentrated on a rotary evaporator (Note 10). The residue is loaded onto a column (diameter: 6 cm) wet-packed with silica gel (150 g) and hexanes/tert-butyl methyl ether (t-BuOMe), 15:1 containing 1% of triethylamine (Note 11). The crude product is purified by gradient elution with hexanes/t-BuOMe (15:1 to 10:1) to afford product (7.87 g) (Note 12). After extensive drying, the product (6.40 g, 98% yield) is obtained as a colorless, viscous oil (Notes 13, 14, 15, 16, and 17).
2. Notes
1.
The oven temperature is ~205 °C. The round-bottomed flask has three 24-40 necks and one 9-30 neck. The addition funnel, mechanical stirrer adapter, and septum are fitted on the 24-40 necks, while the 9-30 neck is fitted with a small rubber septum. The Teflon paddle of the mechanical stirrer is 4.65 cm in length and 1.9 cm in height. The internal temperature was monitored with an Omega Type K microprocessor digital thermometer with 0.2 cm-width probe.
2.
N-(Diphenylmethylene)glycine
tert-butyl ester (99%) was purchased from Alfa Aesar and used as received. The submitters used
N-(diphenylmethylene)glycine
tert-butyl ester (>98%) purchased from Tokyo Chemical Industry Co., Ltd. (TCI) and used as received.
3.
(
S)-4,4-Dibutyl-2,6-bis(3,4,5-trifluorophenyl)-4,5-dihydro-3
H- dinaphtho-[2,1-c:1',2'-e]azepinium bromide [(
S)-
1] (99%) was purchased from Strem Chemicals, Inc. and used as received. The submitters used [(
S)-
1] (> 90%) from Kanto Chemical Co., Inc. as received. The checkers found that an increase in catalyst loading from 0.05 (recommended by the submitters) to 0.10% was essential to obtain enantiomeric ratios greater than 96:4 er.
4.
Benzyl bromide (98%) was purchased from Sigma-Aldrich Co. and was freshly distilled over MgSO
4 (10 mmHg, 73-75 °C) under a nitrogen atmosphere. The submitters used benzyl bromide (98%) purchased from Sigma-Aldrich Co. as received.
5.
Toluene (Certified ACS grade) was purchased from Thermo Fisher Scientific, Inc. and used as received.
6.
The 2-propanol bath temperature (0 ± 2 °C) was maintained by a Thermo Scientific Neslab CC-100 Immersion Cooler with Cryotrol dial controller. As the solution cools, some of the starting material precipitates, forming a whitish, cloudy suspension.
7.
The submitters used 48% potassium hydroxide solution from Kanto Chemical Co., Inc. without purification. The checkers prepared a 48% potassium hydroxide solution from solid pellets (Sigma-Aldrich Co., puriss. p.a., ≥86% (T) pellets) in water purified by a Millipore Milli-Q Integral Water Purification System.
8.
The solution is stirred at 300 rpm until the internal temperature equilibrated to 1 °C. At this time, the addition of the base solution is begun. During the addition of the potassium hydroxide solution, the internal temperature is kept under 3 °C. Upon completion of the addition of base, the addition funnel is replaced by an argon inlet and the large septum is replaced with a glass stopper.
9.
TLC analysis of the reaction mixture indicates the consumption of the starting materials after 10 h. The TLC analysis was performed on EMD Millipore Merck silica gel 60 F
254 plates [
N-(diphenylmethylene)glycine
tert-butyl ester (starting material): R
f = 0.31, product: R
f = 0.41, 15:1 hexanes/
t-BuOMe, visualized with 254 nm UV lamp].
10.
The suspension is filtered through a Pyrex 150 mL course fritted glass funnel (packed with 7.0 g of Celite) into a 1-L suction filtration flask. The filtrate is then transferred with toluene to a 1-L teardrop-shape flask. Toluene is removed by rotary evaporation (16.5-38 °C, 18-20 mmHg) to yield 8.20 g (>100%) of crude product.
11.
Neutralization of the silica gel with hexanes/
t-BuOMe, 15:1 containing 1% triethylamine is necessary to minimize hydrolysis of the product on the column. The neutralized silica was rinsed with 20 column volumes of 15:1 hexanes/
t-BuOMe (~5 L total) to achieve an eluate pH near 7. The checkers used silica gel purchased from Sigma-Aldrich Co. (Merck, grade 9385, 230-400 mesh, 60 Å). The submitters used silica gel purchased from Daiso Co., Ltd. (Daisogel IR-60-40/63). The hexanes used were Optima grade (Sigma-Aldrich Co.). The
t-BuOMe used was Reagent Grade (98%) from Sigma-Aldrich Co. The triethylamine was 99% grade from Alfa-Aesar and freshly distilled over calcium hydride under a nitrogen atmosphere.
12.
The column was eluted with hexanes/
t-BuOMe with a ratio of 15:1 (500 mL) followed by 10:1 (1000 mL) (172 fractions, 8 mL fraction size). TLC indicates the presence of the desired alkylation product and benzophenone (
Rf = 0.29, hexanes/
t-BuOMe, 15:1, visualized with a 254 nm UV lamp). Fractions 47-164 were combined and concentrated (11.5 - 20 °C, 18--20 mmHg).
1H NMR analysis indicates the presence of ~136 mole % of hexanes.
13.
The checkers obtained a 92% yield on a 1/2- scale run (e.r. 98:2).
14.
Hexanes were reduced to ~2.7 mole % by using a Büchi GKR-51 Kugelrohr distillation apparatus with continuous turning under vacuum (0.04-0.05 mmHg) at ambient temperature. The amount of hexanes present was determined by
1H NMR spectroscopic analysis of aliquots at 0, 36, 96, and 186 hours. NMR analysis also indicates the presence of ~2.7 mole % benzophenone.
15.
(R)-2-(Benzhydrylidenamino)-3-phenylpropanoic acid
t-butyl ester has the following physical and spectroscopic data: e.r. = 98.5:1.5; [α]
24D = 190.9 (
c = 0.20, CHCl
3);
1H NMR (500 MHz, CDCl
3) d: 1.44 (s, 9 H), 3.16 (dd,
J = 9.4, 13.4 Hz, 1 H), 3.23 (dd,
J = 4.2, 13.4 Hz, 1 H), 4.11 (dd,
J = 4.2, 9.3 Hz, 1 H), 6.60 (br d,
J = 5.4 Hz, 2 H), 7.03-7.08 (m, 2 H), 7.13-7.21 (m, 3 H), 7.24-7.39 (m, 6 H), 7.55-7.59 (m, 2 H);
13C NMR (500 MHz, CDCl
3) d: 28.03, 39.58, 67.92, 81.09, 126.13, 127.64, 127.90, 128.01, 128.05, 128.16, 128.69, 128.85, 130.04, 136.35, 138.35, 139.55, 170.24, 170.80; IR 3060 (m), 3027 (m), 2977 (m), 2929 (m), 1731 (s), 1623 (m), 1446 (m), 1367 (s), 1285 (s), 1148 (s), 697 (s) cm
-1. MS (EI)
m/z (relative intensity): 294.2 (12.7), 285.1 (11.0), 284.1 (47.7), 244.1 (32.8), 243.1 (17.9), 242.1 (100.0), 238.1 (29.9), 227.0 (16.2), 207.1 (14.6), 206.1 (11.8), 193.1 (27.1), 192.1 (70.7), 165.1 (21.6), 117.1 (10.5), 115.1 (25.3), 91.1 (14.0), 77.1 (11.1). HRMS (ESI-TOF) calcd for C
26H
28NO
2+: 386.2120 ([M + H]
+). Found: 386.2112. The enantioselectivity was determined by chiral stationary phase HPLC analysis [Daicel Chiralcel OD-H column, 1% 2-propanol/hexane, 0.50 mL/min, 18 bar, λ = 251 nm, retention times: (
R)-enantiomer (major): 14.19 min, (
S)-enantiomer (minor): 25.91 min]. Chiral HPLC analysis was calibrated using a 77:23 ratio of the two enantiomers.
16.
Some hydrolysis of the product to the free amine and benzophenone is observed during large-scale chromatographic separation. On the basis of
1H NMR integration, there is 2.3 mole % benzophenone relative to product. A pure sample was prepared as follows. A small portion of the product (150 mg) contaminated with benzophenone from the first chromatographic separation can be further purified by a second chromatographic separation at reduced temperature. The product is loaded onto a jacketed column (diameter: 2 cm) wet-packed with silica gel (29 g) and hexanes/
t-BuOMe, 49:1. The product is purified by gradient elution (hexanes/
t-BuOMe, 49:1 to 9:1) to yield 0.145 g of product
(Note 16), which required extensive drying to remove solvent
(Note 17).
17.
A portion of silica gel (150 g) was neutralized by stirring with 5 mL of triethylamine, 10 mL of
t-BuOMe, and 485 mL of hexanes in a 1-L round-bottom flask. The suspension was filtered through a 150-mL coarse fritted funnel and the silica gel was dried by rotary evaporation (17-22 °C, 18--20 mm Hg). The neutralized silica gel was rinsed with 750 mL
t-BuOMe then with 1.0 L of hexanes/
t-BuOMe, 49:1 prior to loading. Poly(vinyl) tubing is attached to the jacketed column is run through a water/ice slush. Gradient elution proceeds with 100 mL of each solution (49:1 through 9:1) in increments of 49:1, 24:1, etc. (146 fractions, 2.5 mL fraction size). The solutions were pre-chilled in a water/ice slush. Fractions 79-130 were combined and concentrated (15.5--22 °C, 18--20 mm Hg). TLC conditions were the same as those in Note
12, except that the TLC plates were first neutralized with 4% triethylamine in dichloromethane.
18.
The product was transferred to a one-piece medium Kugelrohr distillation bulb and attached to a diffusion pump apparatus. The apparatus consists of a Büchi GKR-50 heating chamber connected to an Edwards SI100 Diffusion Pump with 90 V AC pump heater electrical supply. The product was heated between 50-70 °C at a pressure range of 2.9-3.0×10
-5 mm Hg. The viscosity of the product oil dramatically decreases as temperature is increased, but the oil does not distill under these conditions.
The procedures in this article are intended for use only by persons with prior training in experimental organic chemistry. All hazardous materials should be handled using the standard procedures for work with chemicals described in references such as "Prudent Practices in the Laboratory" (The National Academies Press, Washington, D.C., 2011 www.nap.edu). All chemical waste should be disposed of in accordance with local regulations. For general guidelines for the management of chemical waste, see Chapter 8 of Prudent Practices.
These procedures must be conducted at one's own risk. Organic Syntheses, Inc., its Editors, and its Board of Directors do not warrant or guarantee the safety of individuals using these procedures and hereby disclaim any liability for any injuries or damages claimed to have resulted from or related in any way to the procedures herein.
3. Discussion
α-Amino acids are a biologically significant class of compounds, since they are the basic building blocks for peptides and proteins, and they are the biopolymers responsible for both the structure and function of most living things. Accordingly, the development of truly efficient methods for the preparation of α-alkyl-α-amino acid, especially in an enantiomerically pure form, has become of great importance. Asymmetric synthesis of α-amino acids by phase-transfer alkylation using a chiral catalyst and a prochiral protected glycine derivative would provide a particularly attractive method for the preparation of optically active α-alkyl-α-amino acids.
2 First catalytic asymmetric alkylation of a glycine derivative under phase-transfer conditions was achieved by using a cinchona alkaloid derived chiral phase-transfer catalyst
2a with moderate enantioselectivity.
3 The
N-9-anthracenylmethyl group substituted catalyst
2b was developed to improve the enantioselectivity.
4,5 After these reports, many types of cinchona-derived chiral phase-transfer catalysts were developed for the reaction.
2 Purely synthetic binaphthyl-modified new
N-spiro-type chiral phase-transfer catalyst (
S,
S)-
3 was also developed for the reaction.
6 Compared to other phase-transfer catalysts, such as cinchona-derived catalysts, binaphthyl-modified
N-spiro-type catalysts of type
3 generally require lower catalyst loading (1 mol%) and provide alkylated products in higher enantiomeric excesses. Based on the design of binaphthyl-modified
N-spiro-type catalysts of type
3, very reactive high-performance catalyst (
S)-
1 was developed.
7 Most notably, the reaction proceeded smoothly under mild phase-transfer conditions in the presence of only 0.05~0.1 mol% of (
S)-
1 to afford the corresponding alkylation products with excellent enantioselectivities (Table 1).
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