Zhihui Liab,
Qiusheng Yanga,
Liya Gaoa,
Yuanyuan Xua,
Dongsheng Zhang*a,
Shufang Wanga,
Xinqiang Zhaoa and
Yanji Wang*a
aHebei Provincial Key Lab of Green Chemical Technology and Efficient Energy Saving, School of Chemical Engineering and Technology, Hebei University of Technology, Tianjin 300130, China. E-mail: zds1301@hebut.edu.cn; yjwang@hebut.edu.cn
bSchool of Energy and Environmental Engineering, Hebei University of Technology, Tianjin 300130, China
First published on 29th August 2016
The reactivity of several sulfobutyl hydrosulfate hydroxylamine ionic liquid salts in the direct synthesis of caprolactam from cyclohexanone under mild conditions was investigated. The results showed that the cyclohexanone conversion was mainly affected by cation species in the molecules of the hydroxylamine ionic liquid salts, and hydroxylamine N,N,N-trimethyl-N-sulfobutyl hydrosulfate salt was a better choice for the direct synthesis of caprolactam. The optimum reaction condition was at 80 °C for 4 h, and the suitable molar ratio of cyclohexanone
:
hydroxylamine ionic liquid salt
:
ZnCl2 was 2
:
1
:
3. Under the optimal reaction conditions, cyclohexanone was almost completely converted into caprolactam, corresponding to 99.1% cyclohexanone conversion and 92.0% caprolactam selectivity. Furthermore, the reaction medium acetonitrile, and the ionic liquid which was combined in the hydroxylamine salt, can be recovered after the reaction, achieving an eco-friendly route for the direct synthesis of caprolactam.
To overcome the above-mentioned problems, we have previously employed a ionic liquid (1-sulfobutyl-3-methyl imidazole hydrosulfate ([HSO3-b-mim]·HSO4)) as an alternative to conventional inorganic acids in hydroxylamine stabilization, and therefore a novel hydroxylamine 1-sulfobutyl-3-methyl imidazole hydrosulfate salt ((NH2OH)2·[HSO3-b-mim]·HSO4) had been obtained and used in the one-step, solvent-free synthesis of CPL from CYC with satisfactory CYC conversions and CPL selectivity.18 However, there are still several problems need to be improved: (1) the [HSO3-b-mim]·HSO4 is very costly, and this remains a barrier for its wider large-scale industrial application; (2) when the reaction was completed, the [HSO3-b-mim]·HSO4 that combined in the hydroxylamine ionic liquid salt, could be recovered but not as well as the fresh one in the color and viscosity due to the influence of high reaction temperature (150 °C).18
Herein, we report the stabilization of hydroxylamine with several relatively low-cost sulfobutyl hydrosulfate ionic liquids (ILs),19 which results in the formation of a series of hydroxylamine ionic liquid salts (denoted (NH2OH)2·ILs). Furthermore, the obtained hydroxylamine ionic liquid salts were successfully applied in direct synthesis of CPL from CYC under mild conditions (below 100 °C), as shown in Scheme 1.
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| Fig. 1 FTIR spectra (a) and Raman spectra (b) of the novel (NH2OH)2·ILs and HAS. (A) (NH2OH)2·[HSO3-b-N(CH3)3]·HSO4; (B) (NH2OH)2·[HSO3-b-Py]·HSO4; (C) (NH2OH)2·H2SO4. | ||
The thermal stability of (NH2OH)2·[HSO3-b-N(CH3)3]·HSO4 and (NH2OH)2·[HSO3-b-Py]·HSO4 was investigated in a temperature range between 25 and 1000 °C (Fig. 2). As shown in Fig. 2(a) and (b), the TG curves of the two (NH2OH)2·ILs were much the same. Both of the mass loss process included four stages. The initial and final decomposition temperatures of (NH2OH)2·[HSO3-b-N(CH3)3]·HSO4 were at about 160 °C and 592 °C. The values were 150 °C and 623 °C respectively for the (NH2OH)2·[HSO3-b-Py]·HSO4. The weight loss at about 260 °C (with theoretical value of 18.4% for (NH2OH)2·[HSO3-b-N(CH3)3]·HSO4 and 17.4% for (NH2OH)2·[HSO3-b-Py]·HSO4) corresponded to the NH2OHs stabilized by the [HSO3-b-N(CH3)3]·HSO4 and [HSO3-b-Py]·HSO4. Besides, the main mass loss occurred between 260–380 °C, which was resulted from the decomposition of the two sulfobutyl hydrosulfate ionic liquids that were used to stabilize the hydroxylamine. For comparison, the TG curves of (NH2OH)2·HCl and (NH2OH)2·H2SO4 (Fig. 2(c) and (d)) were also presented.18 Their initial decomposition temperatures were close to those of the two (NH2OH)2·ILs. Their final decomposition temperatures were 270 °C and 400 °C, respectively, which were much lower than those of the two (NH2OH)2·ILs. Moreover, their mass loss mainly occurred at about 200 °C, therefore their TG curves were much steeper than those of the two (NH2OH)2·ILs. In summary, (NH2OH)2·[HSO3-b-N(CH3)3]·HSO4 and (NH2OH)2·[HSO3-b-Py]·HSO4 had gentler weight loss curves and much higher final decomposition temperatures, indicating that their thermal stability were much better than those of (NH2OH)2·HCl and (NH2OH)2·H2SO4.
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| Fig. 2 TG curves of the (NH2OH)2·[HSO3-b-N(CH3)3]·HSO4 (a), (NH2OH)2·[HSO3-b-Py]·HSO4 (b), (NH2OH)2·H2SO4 (c) and (NH2OH)2·HCl (d). | ||
| No | Solvent | XCYC (%) | SCPL (%) | SCOX (%) |
|---|---|---|---|---|
a Reaction conditions: CYC 5 mmol, n(CYC) : n((NH2OH)2·[HSO3-b-mim]·HSO4) : n(ZnCl2) = 2 : 1 : 3, solvent 10 mL, 80 °C, 4 h.b Homogeneous phase, others are all heterogeneous phase. |
||||
| 1 | Toluene | 27.3 | 35.5 | 64.5 |
| 2 | N,N-Dimethylformamideb | 79.2 | 19.0 | 81.0 |
| 3 | Acetonitrile | 82.5 | 96.3 | 3.1 |
The present reaction includes oximation of CYC to COX, followed by the Beckmann rearrangement of COX to CPL. Being a multistep process, the outcome of the reaction depends on the reactivity of the substrate towards both oximation and Beckmann rearrangement.15 As for the first step, it is believed that COX is produced through the nucleophilic attack of nitrogen electron pairs in the NH2OH to the C
O carbon in the CYC.26–28 Free NH2OH,16,27 resulted from the decomposition of hydroxylamine salt, is the nucleophile necessary for conversion of CYC to the corresponding COX. It was evident that, the aprotic polar solvents, such as acetonitrile and N,N-dimethylformamide, demonstrated an obvious promotion on the decomposition of hydroxylamine salt to form free NH2OH29–31 since high CYC conversions were obtained in these solvents. This solvent-promoted decomposition in aprotic polar solvents with high ability of electron pairs donor was probably due to the formation of hydrogen bond between the nitrogen electron pairs in the solvent and hydroxyl in the hydroxylamine salts.29,32
Furthermore, solvent also played an important role in the subsequent Beckmann rearrangement. Acetonitrile was found to be a suitable solvent for the rearrangement reaction.33–35 Most probably the beneficial effect of acetonitrile was ascribed to its high reagent solubility,16 especially that of [HSO3-b-mim]·H2SO4 (an in situ catalyst component for the Beckmann rearrangement) resulting from the decomposition of (NH2OH)2·[HSO3-b-mim]·H2SO4. Hence, when acetonitrile was used as solvent, more COX was converted to CPL, which in turn promoted the oximation step (a reversible process) and improved the CYC conversion.17 As for N,N-dimethylformamide, it could promote the oximation reaction. However, its weak basicity probably poisoned the acid catalyst and hindered the Beckmann rearrangement.36–38 Hence, only trace amount of CPL was obtained when N,N-dimethylformamide was used as solvent. Considering the influence on oximation reaction as well as Beckmann rearrangement, acetonitrile seems to be a better choice for direct synthesis of CPL.
With increasing of ZnCl2 ratio, the CYC conversions changed a little. But the CPL selectivity increased greatly and reached a maximum value of 96.3% when the molar ratio of ZnCl2 to CYC was 1.5, indicating that ZnCl2 and the [HSO3-b-mim]·HSO4 was an excellent composite catalyst for the Beckmann rearrangement. Most of the COX produced from the CYC and (NH2OH)2·[HSO3-b-mim]·HSO4 could be transformed to CPL. Nevertheless, when ZnCl2 amount was further increased, the CPL selectivity decreased a little. As a result, 1.5 molar ratio of ZnCl2 to CYC was sufficient to achieve a high CYC conversion and CPL selectivity.
The influence of reaction temperature and time were also investigated systematically. As depicted in Fig. 4(b) and (c), the CPL selectivity depended greatly on the reaction temperature and time. It increased rapidly with rising temperature from 50 to 80 °C, and then increased slightly when further rising the temperature. Concerning the reaction time, the CPL selectivity first increased, passing through a maximum at 4 h, and then decreased slightly by further prolonging reaction time. Hence, higher temperature (80–90 °C) and longer time (4 h) was suitable for CPL selectivity. The CYC conversion was less affected by the reaction temperature and time. It increased slightly from 50 to 70 °C, and then reduced a little with the temperature above 70 °C. This may be due to easier self-catalysis decomposition of hydroxylamine ionic liquid salt at higher temperature.39,40 As for the influence of reaction time, the CYC conversion was nearly constant with prolonging reaction time, and a relatively higher CYC conversion can be obtained at a longer time. Hence, considering the CYC conversion and CPL selectivity, the optimum reaction condition was at 80 °C for 4 h.
Under the above mentioned optimal conditions, the CYC conversion and CPL selectivity were 82.5% and 96.3%, respectively. Our previous result was 100% CYC conversion and 91.3% CPL selectivity under solvent free conditions.18 As we can see, when acetonitrile was used as solvent, the reaction temperature was remarkably decreased from 150 to 80 °C. Although the CYC conversion was decreased a little, the CPL selectivity was increased to 96.3%. Then the reactivity of the two novel prepared hydroxylamine ionic liquid salts on direct synthesis of CPL was also investigated as a contrast under the above optimal conditions.
| No | (NH2OH)2·ILs | XCYC (%) | SCPL (%) | SCOX (%) |
|---|---|---|---|---|
a Reaction conditions: CYC 5 mmol, n(CYC) : n((NH2OH)2·ILs) : n(ZnCl2) = 2 : 1 : 3, acetonitrile 10 mL, 80 °C, 4 h. |
||||
| 1 | (NH2OH)2·[HSO3-b-mim]·HSO4 | 82.5 | 96.3 | 3.1 |
| 2 | (NH2OH)2·[HSO3-b-Py]·HSO4 | 86.2 | 83.4 | 16.6 |
| 3 | (NH2OH)2·[HSO3-b-N(CH3)3]·HSO4 | 99.1 | 92.0 | 8.0 |
The present reaction was carried out in the presence of a strong Lewis acid ZnCl2, together with the acid ionic liquid that released from the hydroxylamine ionic liquid salt. In order to demonstrate the role of ZnCl2 and the acid ionic liquid in the rearrangement process, Beckmann rearrangement of COX was performed using catalytic amount of [HSO3-b-(CH3)3]·H2SO4 and/or ZnCl2 as shown in Table S1.† It could be seen that ZnCl2 was the main catalytic species for the Beckmann rearrangement. [HSO3-b-(CH3)3]·H2SO4 alone showed little catalytic activity. However, when combined with ZnCl2, it could effectively enhance the catalytic activity of ZnCl2. The results suggested that the cooperative effect between ZnCl2 and ionic liquid played an important role in the rearrangement.41 Furuya et al.42 reported that HCl and ZnCl2 could promote the rearrangement probably due to their chelation with nitrogen atoms of oxime. The intermediate formed through this process, respected to the COX, has a lower electronic density on the nitrogen atom and consequently a greater tendency to rearrange even without Brønsted acid.37,43 Accordingly, it could be inferred that the cooperative effect between [HSO3-b-(CH3)3]·H2SO4 and ZnCl2 was probably better than the other two ionic liquids and ZnCl2, which was favor for the formation of the intermediate. Therefore, (NH2OH)2·[HSO3-b-(CH3)3]·H2SO4 was found to be the best hydroxylamine salt in the present study.
| No | Hydroxylamine salt | XCYC (%) | SCPL (%) | SCOX (%) |
|---|---|---|---|---|
a Reaction conditions: CYC 5 mmol, n(CYC) : n(NH2OH) : n(ZnCl2) = 2 : 2 : 3, acetonitrile 10 mL, 80 °C, 4 h. |
||||
| 1 | NH2OH·HCl | 93.2 | 91.2 | 8.8 |
| 2 | (NH2OH)2·H2SO4 | 96.6 | 91.8 | 8.2 |
| 3 | (NH2OH)2·[HSO3-b-N(CH3)3]·HSO4 | 99.1 | 92.0 | 8.0 |
While (NH2OH)2·H2SO4 was used, the CYC conversion and CPL selectivity were higher than those of HAL, meaning that CPL could be efficiently produced from CYC and (NH2OH)2·H2SO4. As for (NH2OH)2·[HSO3-b-N(CH3)3]·HSO4, the CYC conversion and CPL selectivity were the highest, which were 99.1% and 92.0%, respectively. It shows that [HSO3-b-N(CH3)3]·HSO4 not only can stabilize the hydroxylamine, but also can catalytic the Beckmann rearrangement of COX to CPL. Additionally, its reactivity is much the same, even better than H2SO4. Furthermore, as (NH2OH)2·[HSO3-b-N(CH3)3]·HSO4 was employed in CPL production, no strong acids was released. Therefore, less equipment corrosion and environmental pollution problems were encountered and no ammonium sulfate by-product was produced.
At the end of the reaction, the resulting mixture was cooled to room temperature. ZnCl2 and acetonitrile were recovered by centrifugal separation and vacuum distillation, respectively. Then the substrate was extraction four times with diethyl ether to sufficiently remove the possible organic compound, such as CYC, COX or CPL.34 The leaving mixture was distilled with a rotary evaporator under vacuum to recover the [HSO3-b-N(CH3)3]·HSO4. The FTIR spectra of the recovered and fresh [HSO3-b-N(CH3)3]·HSO4 was presented in Fig. 5. It can be seen that they were highly similar except for a little peak at 3175 cm−1 from characteristic vibrations of CPL.33,44 It was thus deduced that a little amount of CPL left in the recovered ionic liquid led to the subtle difference in the two FTIR spectra. The ionic liquid was structurally stable after the reaction. Further study was undertaken to understand the recyclability of the reaction media.
• Several novel relatively low-price hydroxylamine ionic liquid salts, (NH2OH)2·[HSO3-b-N(CH3)3]·HSO4 and (NH2OH)2·[HSO3-b-Py]·HSO4 were prepared, which proved to a certain degree that all of the sulfobutyl hydrosulfate ionic liquids with different cation could be used in hydroxylamine stabilization to form hydroxylamine ionic liquid salts.
• The three sulfobutyl hydrosulfate hydroxylamine ionic liquid salts were successfully applied in direct synthesis of CPL from CYC under mild conditions. (NH2OH)2·[HSO3-b-N(CH3)3]·HSO4 demonstrated improved reactivity than NH2OH·HCl and (NH2OH)2·H2SO4, the highest CYC conversion and CPL selectivity were 99.1% and 92.0%, respectively.
• When (NH2OH)2·[HSO3-b-N(CH3)3]·HSO4 was used in CPL production, the ionic liquid that combined in the (NH2OH)2·[HSO3-b-N(CH3)3]·HSO4 could be recovered. Therefore, less equipment corrosion and environmental pollution problems were encountered and no ammonium sulfate by-product was produced, achieving an eco-friendly route for direct synthesis of caprolactam.
Footnote |
| † Electronic supplementary information (ESI) available. See DOI: 10.1039/c6ra12918h |
| This journal is © The Royal Society of Chemistry 2016 |