Petrochemistry is highly significant for the chemical industry, since petroleum provides raw materials for the fabrication of plastics and other ubiquitous products  . In particular, alkenes in petroleum are of great value, because they are easier to transform than alkanes. The typical methods of converting alkene into synthetically versatile carbonyl compounds are hydroformylation (to afford aldehydes)     and Wacker oxidation (to afford methyl ketones)   . These reactions are industrially useful, since the requisite gaseous reagents are often very inexpensive and work-up after the reaction can be easily performed by their diffusion. Hydroformylation has become one of the largest industrially applied processes, and more than seven million tons of oxygenated products such as aldehydes and alcohols are produced per year  . Recently, hydroformylation has also been used for the synthesis of natural products     and heterocyclic compounds     , as exemplified by our hydroformylation-based synthesis of (±)-muscone  . Despite hydroformylation being a very efficient method for the transformation of alkenes, it is not commonly employed in laboratories, because of the following major problems: 1) the need for safe treatment of flammable/toxic nature of hydrogen and carbon monoxide, and the requirement of high-pressure batch equipment; 2) low hydroformylation yield; 3) the necessity to separate the desired aldehyde and unreacted alkene; and 4) need to recycle of the unreacted alkene.
We herein focused on conducting safe hydroformylation. Recently, flow chemistry has emerged as an important alternative to conventional batch chemistry     , frequently enhancing the safety profiles of synthetic processes. It has also emerged as an effective method for conducting hazardous reactions (such as hydroformylation) involving toxic reagents or high-pressure gases   . To the best of our knowledge, only one example of hydroformylation in a flow reactor has been reported earlier  , which was conducted by Ley et al., who performed safety hydroformylation of styrene analogs by utilizing a tube-in-tube reactor     . To expand the above field, we report the safe hydroformylation of oct-1-ene, a relatively low-reactive aliphatic alkene.
2. Materials and Methods
NMR spectra were recorded on a JEOL Model ECA-500 instrument, and chemical shifts were reported in parts per million (ppm) relative to internal standard (tetramethylsilane; 0.0 ppm) or solvent (CDCl3; 7.26 ppm for 1H NMR and 77.1 ppm for 13C NMR) peaks. 1H NMR spectral data were reported as chemical shift (δ, ppm), multiplicity (s, singlet; d, doublet; t, triplet; q, quartet; sp, septet; m, multiplet; br, broad), coupling constant (J, Hz), and integral value. 13C NMR data were reported as chemical shift (δ, ppm) followed by multiplicity and coupling constants where applicable. All reactions were monitored by thin-layer chromatography using 0.25 mm E. Merck silica gel plates (60F254), with visualization performed by UV light (254 nm) irradiation or staining with p-anisaldehyde, ceric sulfate, or 10% ethanolicphosphomolybdic acid followed by heating. Column chromatography was performed using silica gel (Chromatorex PSQ 100B, Fuji Silysia Chemical Ltd.). All reagents and chemicals were purchased from Tokyo Chemical Industry Co., Ltd., and used as received.
2.2. Flow Reactor Setup
The flow system used in this work (Figure 1) comprised a stainless steel T-shaped micromixer (inner diameter: 500 μm; YMC Co., Ltd.) and a stainless steel tube (inner diameter: 1000 μm; GL Sciences, Inc.). Back-pressure regulator was purchased from GL Sciences, Inc. Solutions were introduced using a syringe pump (Harvard PHD ULTRA) equipped with gastight syringes (SGE Analytical
Figure 1. Flow system used for hydroformylation.
Science Pty., Ltd.). Hydrogen and carbon monoxide were delivered to the micromixer at a constant rate utilizing a mass flow controller (Brooks Instrument) from a CO/H2(1:1) gas cylinder. System pressure was controlled by using a back-pressure regulator and monitored using a pressure sensor attached to the mass flow controller.
2.3. General Hydroformylation Procedure
To a solution of oct-1-ene (71.5 mg, 0.637 mmol, 1.00 equiv.) in solvent (4.00 mL) were added Rh(CO)H(PPh3)3 (11.7 mg, 0.0127 mmol, 0.0200 equiv.) and Xantphos (28.8 mg, 0.0497 mmol, 0.0780equiv.) at room temperature. The obtained mixture was introduced into the T-shaped micromixer using the syringe pump (flow rate) and passed through the stainless steel tube (inner diameter: 1000 μm, length: 8.0 m) at 100˚C under CO/H2(1:1) (flow rate 200 mL/min, 18 atm). The product yield was determined by gas chromatography.
3. Results and Discussion
The flow reactor for the hydroformylation of oct-1-ene(1) is schematically depicted in Figure 2. Initially, a solution of oct-1-ene, Rh(CO)H(PPh3)3, and Xantphos  in toluene was introduced into the T-shaped micromixer at 100˚C under a CO/H2 (flow rate 200 mL/min, 18 atm) atmosphere using the syringe pump, and hydroformylation was carried out by passing the above solution through the stainless steel tube (inner diameter: 1000 μm, length: 8.0 m) to afford nonanal, followed by optimization of the flow rate (mL/min) of the solution.
Flow rate of the solution was examined at 0.10, 0.40, 0.70, and 1.0 mL/min (Figure 3). Among the conditions, the best yield of nonanal (8%) was achieved at an intermediate flow rate of 0.40 mL/min, as observed by Ley and coworker for the hydroformylation of styrene analogs  . This behavior was ascribed to high flow rates, which resulted in insufficient reaction times; low flow rates did not allow the gaseous reagents and the substrate solution to mix efficiently.
Subsequently, we optimized the solvent (Table 1). The best yield (19%) was
Figure 2. Schematic representation of the flow reactor.
Figure 3. Optimization of flow rate for hydroformylation in a flow reactor.
Table 1. Solvent optimization for hydroformylation in a flow reactor.
a. Reaction conditions: 100˚C, CO/H2 pressure: 18 atm, flow rate: 0.40 mL/min, and tube length: 8.0 m; b. Yield was determined by gas chromatography.
accomplished in the case of chlorobenzene, whereas toluene and 1,4-dioxane gave lower yields of 8 and 4%, respectively. The above yield of 19% can be further improved by recycling the unreacted substrate, which makes this method suitable for large-scale production as it allows the reaction work-up to be easily performed by gaseous reagent diffusion. The recycling of the unreacted substrate was achieved in batch system by the normal distillation. The development of the recycling system in flow reactor is currently under way.
In summary, we successfully and safely hydroformylated an aliphatic alkene in a flow reactor. The maximum yield of the target aldehyde (19%) was achieved at 0.40 mL/min flow rate in chlorobenzene. The developed method can be easily up scaled, because the reaction work-up can be easily performed by gaseous reagent diffusion. Although the yield of the target aldehyde is low, it can be improved by recycling the unreacted alkene.
This work was supported by the Asahi Glass Foundation. We would like to thank Prof. Ilhyong Ryu and Dr. Takahide Fukuyama at Osaka Prefecture University for assistance with the flow reactor setup. We also thank Dr. Kenichiro Yagi at the Yokohama University of Pharmacy for assistance with GC analysis.
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