STABILIZED ACYCLIC SACCHARIDE COMPOSITE AND METHOD FOR STABILIZING ACYCLIC SACCHARIDES AND APPLICATIONS THEREOF
20220064201 · 2022-03-03
Inventors
- Po-Wen CHUNG (Kaohsiung, TW)
- Chia-Hui Wu (Tainan, TW)
- Yi-Shiuan TSAI (Kaohsiung, TW)
- Chun-An HSIEH (Taipei, TW)
Cpc classification
B01J41/02
PERFORMING OPERATIONS; TRANSPORTING
C07H1/00
CHEMISTRY; METALLURGY
International classification
C07H1/00
CHEMISTRY; METALLURGY
B01J41/02
PERFORMING OPERATIONS; TRANSPORTING
Abstract
Disclosed is a stabilized acyclic saccharide composite, which includes a LDH-based (layered double hydroxide-based) material and acyclic saccharides intercalated in interlayer regions of the LDH-based material. The acyclic saccharides stabilized and trapped in the LDH-based material give an opportunity for direct functionalization to other valuable molecules in the pharmaceutical, chemical or carbohydrate industries. Further, a novel pathway for saccharide transformation and aldol condensation without the drawbacks associated with enzymatic catalysts is achieved through the acyclic saccharides trapped by the LDH-based material.
Claims
1. A stabilized acyclic saccharide composite, comprising: a LDH-based (layered double hydroxide-based) material; and acyclic saccharides, intercalated in interlayer regions of the LDH-based material.
2. The stabilized acyclic saccharide composite of claim 1, wherein the LDH-based material is a M.sup.3+/N.sup.2+-LDH or a metal-loaded M.sup.3+/N.sup.2+-LDH, the M.sup.3+ is a trivalent metal, and the N.sup.2+ is a bivalent metal.
3. The stabilized acyclic saccharide composite of claim 2, wherein the M.sup.3+ is Al.sup.3+, and the N.sup.2+ is Mg.sup.2+.
4. The stabilized acyclic saccharide composite of claim 2, wherein the metal-loaded M.sup.3+/N.sup.2+-LDH is Ru-loaded M.sup.3+/N.sup.2+-LDH or Cu-loaded M.sup.3+/N.sup.2+-LDH.
5. The stabilized acyclic saccharide composite of claim 1, wherein the acyclic saccharides are ring-opened from one or more of glucose, fructose, mannose, cellobiose, galactose, maltose, fucose, and 2-deoxy glucose.
6. The stabilized acyclic saccharide composite of claim 1, wherein the stabilized acyclic saccharide composite is characterized by at least one .sup.13C nuclear magnetic resonance peak found in a chemical shift range of 165 to 190 ppm.
7. A method of stabilizing acyclic saccharides, comprising: providing a collapsed LDH-based (layered double hydroxide-based) material; mixing cyclic saccharides and the collapsed LDH-based material in a solvent; and reconstructing the collapsed LDH-based material into a layered structure and ring-opening the cyclic saccharides to yield and intercalate acyclic saccharides in interlayer regions of the LDH-based material.
8. The method of claim 7, wherein the LDH-based material is a M.sup.3+/N.sup.2+-LDH or a metal-loaded M.sup.3+/N.sup.2+-LDH, the M.sup.3+ is the trivalent metal, and the N.sup.2+ is the bivalent metal.
9. The method of claim 8, wherein the M.sup.3+ is Al.sup.3+, and the N.sup.2+ is Mg.sup.2+.
10. The method of claim 8, wherein the metal-loaded M.sup.3+/N.sup.2+-LDH is Ru-loaded M.sup.3+/N.sup.2+-LDH or Cu-loaded M.sup.3+/N.sup.2+-LDH.
11. The method of claim 7, wherein the cyclic saccharides are one or more of glucose, fructose, mannose, cellobiose, galactose, maltose, fucose and 2-deoxy glucose.
12. The method of claim 7, wherein the collapsed LDH-based material is prepared by calcination of the LDH-based material.
13. The method of claim 7, wherein the solvent is water.
14. The method of claim 7, wherein the reconstructing and ring-opening is performed at a temperature higher than 4° C.
15. A method for isomerization of saccharides, comprising: intercalating acyclic saccharides in interlayer regions of a LDH-based material; and converting the acyclic saccharides to isomerized saccharides in the interlayer regions of the LDH-based material.
16. The method of claim 15, wherein the intercalating cyclic saccharides is performed by equilibration of the collapsed LDH-based material and the saccharides in the solvent.
17. The method of claim 16, wherein the collapsed LDH-based material is prepared by calcination of the LDH-based material.
18. The method of claim 16, wherein the solvent is water.
19. The method of claim 16, wherein the equilibration is performed at a temperature higher than 4° C.
20. The method of claim 15, wherein the conversion of the acyclic saccharides is conducted in a water-containing environment.
21. The method of claim 15, wherein the LDH-based material is a M.sup.3+/N.sup.2+-LDH or a metal-loaded M.sup.3+/N.sup.2+-LDH, the M.sup.3+ is the trivalent metal, and the N.sup.2+ is the bivalent metal.
22. The method of claim 21, wherein the M.sup.3+ is Al.sup.3+, and the N.sup.2+ is Mg.sup.2+.
23. The method of claim 21, wherein the metal-loaded M.sup.3+/N.sup.2+-LDH is Ru-loaded M.sup.3+/N.sup.2+-LDH or Cu-loaded M.sup.3+/N.sup.2+-LDH.
24. A method for preparing an aldol condensation product, comprising: providing the stabilized acyclic saccharide composite of claim 1; and condensing the acyclic saccharides of the stabilized acyclic saccharide composite with a carbonyl-active compound to form the aldol condensation product by mixing the stabilized acyclic saccharide composite with the carbonyl-active compound.
25. The method of claim 24, wherein the carbonyl-active compound is a ketone compound.
26. The method of claim 25, wherein the carbonyl-active compound is acetone.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
[0022] The accompanying drawing explanation.
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DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS
Chemicals
[0043]
Methods
Preparation of the Collapsed LDH-Based Material
[0044] A mixture of Mg.sup.2+ and Al.sup.3+ methanolic solution (containing Mg.sup.2+ and Al.sup.3+ in molar ratio of 3:1) was prepared by dissolving both Mg(NO.sub.3).sub.2.6H.sub.2O (20.00 mmol) and Al(NO.sub.3).sub.3.9H.sub.2O (6.60 mmol) in MeOH/H.sub.2O (1:1, v/v, 200 mL). To facilitate the condensation of metal hydrates for hydrotalcite synthesis, the alkali solution containing NaOH (44.25 mmol) and Na.sub.2CO.sub.3 (15.79 mmol) was prepared as well in MeOH/H.sub.2O (1:1, v/v, 200 mL). Then the Mg.sup.2+/Al.sup.3+ nitrate mixture was dropwise added into methanolic solution (MeOH/H.sub.2O (v/v)=1/1, 200 mL) in a rate of 2 mL/min, while regulating the pH at 10 by adding the aforementioned alkali solution. After the addition, the slurry was aged in a closed system at 65° C. for 24 h in a conventional oven and the resulting material was collected by filtration after cooling down at room temperature. The cake-like chunk was dried at 90° C. for 16 h in the muffle furnace and grinded subsequently. The resulting powder, as known as hydrotalcite (HT), was dried at 110° C. for 6 h and then calcined under air at 110° C. for 6 h and 550° C. for 12 h with a heating ramp of 2° C./min in the muffle furnace, to form hydrotalcite oxide (HTO) as an example of the collapsed LDH-based material.
[0045] Another prepared material is metal incorporated hydrotalcite, was prepared by co-precipitation, in which aluminum ions are partially replaced by ruthenium or copper ions with 1,2, 5 or 10 wt. % to form metal hydrotalcite (M-HT; M=Cu or Ru). The synthesis was performed as the same method as mentioned above, through co-precipitation, aging, and filtration followed by drying and calcination process (M-HTO).
[0046] As another example of the collapsed LDH-based material, metal loaded hydrotalcite oxide (M@HTO; M=Cu or Ru) was synthesized by the wet impregnation method, with 2 wt. % of the metal on the hydrotalcite oxide support. Briefly, RuCl.sub.3.nH.sub.2O (26.1 mg; 39% Ru) was dissolved in deionized water (20 mL) and then added into a 50 mL round bottom flask containing hydrotalcite oxide (HTO; 500 mg). The mixture was sonicated to ensure well dispersion and then incubated at 60° C. for 3 h under N.sub.2 environment with vigorous stirring. Subsequently, the solvent was removed by evaporation and the resulting product was lyophilized to give dark grey appearance powder (denoted as Ru@HTO). The reduction of the Ru metal on the HTO was performed at 450° C. under H.sub.2 environment for 4 h to yield the reduced Ru metal hydrotalcite oxide (denoted as r-Ru@HTO). Copper loaded hydrotalcite oxide (denoted as Cu@HTO) was prepared as described above with Cu (NO.sub.3).sub.2.3H.sub.2O (38.78 mg) and the reduction was also carried out to yield reduced Cu metal hydrotalcite oxide (denoted as r-Cu@HTO).
Layered Structure Restoration of the Collapsed LDH-Based Material
[0047] The rehydration of HTO was done by putting the calcined HTO (40 mg) with 0.6 mL of deionized water per gram of sample in a capped 1.5-mL Eppendorf for 2 h, and lyophilized overnight. The given white powder was the final rehydrated hydrotalcite (HTR).
Acyclic Saccharides Trapped and Stabilized in LDH-Based Material
[0048] The derivatized saccharides, including glucose (Glcp, .sup.13C.sub.6-Glc, 1-.sup.13C Glc, and 2-.sup.13C Glc), fructose (Frup, 1-.sup.13C Fru, and 2-.sup.13C Fru), and cellobiose (Celp and 1-.sup.13C Cel) were prepared in aqueous solution (0.6 mL of the concentration of 15.0 mg/mL) and mixed with the collapsed LDH-based material (HTO, 40 mg) in a capped 1.5-mL Eppendorf tube. After the equilibration periods of 2, 12, and 24 h at room temperature, the samples were centrifugalized at 3000 rpm for 3 min to separate the HT-derived materials and saccharide solutions. The supernatant was subsequently filtered and diluted for the measurement of the final concentrations via high-performance liquid chromatography (HPLC). The HT-derived materials were lyophilized overnight for the study of the solid-state .sup.1H-.sup.13C CP/MAS and .sup.1H MAS NMR. Through nuclear magnetic resonance (NMR) analysis, stabilization of acyclic saccharides in the interlayer spaces of the LDH-based material and transformation from glucose to fructose (as shown in below Scheme I) were confirmed.
##STR00001##
[0049] Additionally, standard
[0050] Further, the stabilization of acyclic saccharides by the metal loaded hydrotalcite oxide was also carried out and investigated by .sup.13C SSNMR and PXRD.
Acetylation of Saccharides
[0051] The dried glucose-HTO (˜45 mg) was suspended and stirred in a solution of Ac.sub.2O/pyridine (1:1, v/v, 0.5 mL) at room temperature overnight. The mixture was centrifugalized with 5000 rpm for 5 min to separate the HTO-derived solid and the supernatant. The HTO-derived solid was washed by 1.0 mL ethyl acetate and then centrifugalized for 3 times. The combined solution containing acetylated saccharides was evaporated with toluene for 3 times and dried under vacuum system overnight prior to .sup.1H and .sup.13C NMR measurements.
Intermolecular Aldol Condensation
[0052] To utilize the acyclic saccharides, intermolecular aldol condensation was performed by mixing the saccharide-derived solid and acetone (below Scheme II).
##STR00002##
[0053] The dried glucose-HTO (˜80 mg) was suspended and stirred in acetone (1.2 mL) at 50° C. overnight. The mixture was centrifugalized with 5000 rpm for 5 min to separate the HTO-derived solid and the supernatant. The HTO-derived solid was washed by 1.0 mL acetone twice and dried by high-vacuum pump. The dried solid was suspended in deionized water (1.0 mL) and vortex for 10 min before centrifugalization and filtration. The filtrate was lyophilized over-night for following high resolution ESI-MS (
Apparatus
(1) High Performance Liquid Chromatography (HPLC) Analysis
[0054] HPLC analysis was performed by a Shimadzu Prominence LC-20AD liquid chromatograph equipped with a RID-20A refractive index detector and an ultra violet detector with wavelength set at 370 nm. Saccharides were quantified by these two detectors. Using syringe filters to remove impurities before liquid chromatography analysis. Samples were eluted under 50° C. with 0.01 N H.sub.2SO.sub.4 at flow rate of 0.6 mL min.sup.−1 through an ion exchange column (HPX-87H, 7.8×300 mm, Aminex).
(2) Nuclear Magnetic Resonance (NMR) Analysis
[0055] The dried HT-derived material was finely powdered and packed into a 4 mm zirconium MAS rotor for .sup.13C and .sup.1H NMR and 2.5 mm rotor for .sup.1H NMR. .sup.1H-.sup.13C cross polarization magic angle spinning (CP/MAS) NMR spectra were obtained using a Bruker AV 300 MHz instrument, equipped with a 4 mm double resonance probe operating at .sup.1H and .sup.13C Larmor frequencies of 300.13 and 75.47 MHz, respectively. The contact time was 1 ms and radio-frequency (rf) field strength was 41.0 kHz for both the .sup.1H and .sup.13C channels for the CP experiments. .sup.13C spectra were acquired with a sample spinning frequency of 10 kHz and at ambient temperature. Chemical shift was referenced to the carboxyl carbon signal of glycine at 176.4 ppm for .sup.13C. .sup.1H MAS spectra were collected by a Bruker AVIII-800 MHz instrument with a sample spinning frequency of 30 kHz. Chemical shift was referenced to tetramethylsilane (TMS) at 0 ppm for .sup.1H. Proton (.sup.1H) NMR analysis was performed by Bruker AV500. Samples were prepared in deuterium oxide (6=4.79 ppm). Pyridine was added to the samples in fixed concentration as internal calibration standard for quantification.
(3) Powder X-Ray Diffraction (PXRD) Analysis
[0056] PXRD analysis of sample diffraction patterns were obtained using a Bruker D8 Advance x-ray diffractometer (Brucker, USA), with a Copper K.sub.α radiation source (λ=1.5418 Å) operating at 40 kV and 40 mA. Samples were analyzed through a 0.6 mm slit. The diffraction results was scanned over a 2θ range of 5-90° and scanning rate was 0.5 s per step with the monitor air scattering knife fixed at 3 mm above the sample.
(4) Gas Chromatograph (GC) Analysis
[0057] GC analysis was performed by a Shimadzu GC-2014 gas chromatograph equipped with a flame ionization detector (FID). The column length is 30 m with film thickness of 0.25 μm and the radius is 0.32 mm. The syringe filters are used to remove the impurities prior to the analysis. Chromatography conditions: for each measurement, 0.5 μL sample was injected and heated to 200° C. for vaporization. The carrier gas (helium, 99.9992%) pressure is set at 90.8 kPa with total flow rate of 67.5 mL/min. The purge flow rate is 3.0 mL min.sup.−1 and the split ratio is 40:1. The sample flows into the column at the rate of 1.57 mL min.sup.−1 The samples were separated through the specific temperature control program (
Results Section
.SUP.13.C SSNMR Results
[0058] In the .sup.13C NMR spectrum, an extra peak at downfield area was found after .sup.13C-labelled glucose .sup.13C.sub.6-Glc treated by HTO (
[0059] To verify the acyclic glucose, 1-.sup.13C labelled glucose 1-.sup.13C Glc (
[0060] To further confirm the aldehyde carbon from ring opening of saccharides at reducing end, sorbitol, maltose and cellobiose were used for the same treatment condition and .sup.13C CP/MAS NMR measurements (
[0061] Moreover, aldehyde protons of fructose, glucose and cellobiose were found 9 ppm in .sup.1H MAS NMR (
[0062] The present invention further proposed the mechanism involving in acyclic saccharide stabilization of HT (
[0063] In conclusion, an extra characteristic peak at 170 ppm appeared after treatment of .sup.13C.sub.6 glucose by HTO. It indicates the conformational change from glucopyranose to acyclic glucose. The intercalation of .sup.13C.sub.6 glucose, 1-.sup.13C glucose and 2-.sup.13C glucose in rehydrated HT was carried out with various treatment times individually. The 170-ppm peak was therefore verified from C1 of glucose. The other carbonate peak at 183 ppm appeared later after a longer treatment time and was confirmed from C2 of fructose. The acyclic saccharides were considered to form a carbonate-like complex with rehydrated HT based on the resulting chemical shifts. The related .sup.1H MAS NMR spectra also supported the explanation. Moreover, the glucose-fructose transformation through acyclic glucose was observed when the freeze-dried sample powder kept in a rotor. It implies the transformation can occur with the trace amount of water. It is believed that the acyclic saccharides trapped and stabilized by rehydrated HT give an opportunity for direct functionalization of these reactive species to other valuable molecules.
PXRD Results
[0064] The PXRD patterns of the as-synthesized hydrotalcite (HT), calcined hydrotalcite (HTO), and rehydrated hydrotalcite (HTR) are given in
[0065] Most of the HT-derived materials, obtained by treating saccharides with HTO, gave the similar PXRD patterns indicating the recovery of layered structure, as shown in
[0066] Furthermore, the better layer reformation from disaccharides solution may elucidate the roles of OH group in forming hydrogen bonding with HTO surface. As more hydroxyl group is available from the disaccharides, the layers are more likely to be pulled together through intercalating and/or forming hydrogen bonding with the sugar molecules, therefore, rebuild the layered structure of LDH-based materials.
[0067] Additionally, the metal loaded hydrotalcite also exhibits the “memory effect” that the layer structure could be restored after introducing appropriate anionic species. The PXRD pattern suggests that the layer structure of Cu@HTO has better structural recovery ability (
Saccharides Adsorbed Quantification
[0068] After HPLC analysis, the amount of saccharides adsorbed on HTO and Metal-HTO was quantified, as shown in Tables 2 and 3. The higher quantity of saccharides is adsorbed (%), the better adsorption ability the material possesses. Some of these saccharides was degraded due to the mobile phase (0.01N sulfuric acid) used in HPLC, so liquid .sup.1H NMR or GC was used for quantification.
Langmuir Isotherm
[0069] The Langmuir constants of glycosyl substrate were tabulated as below Table 1.
TABLE-US-00001 TABLE 1 .sup.aLangmuir constants Saccharides Q.sub.m (mg .Math. g.sup.−1) b (L .Math. mg.sup.−1) R.sup.2
[0070] Among all monosaccharides, glucose achieved highest maximum adsorption amount (Q.sub.m) of 87 mg per gram of HTO while its stereoisomers and derivatives obtained lower adsorption amount. Regarding the b value, galactose (2.673 L.Math.mg.sup.−1) is expected to be adsorbed preferentially as opposed to glucose (0.546 L.Math.mg.sup.−1). However, it does not accord to the corresponding adsorption result. Taking the stereo-configuration of the saccharides into consideration, galactose is an epimer of glucose with axial hydroxyl group (OH group) at C4 position. The low adsorptive capacity may be attributed to the orientation of the axial OH group on the saccharides as the out-of-plane OH group could create the steric obstacle and/or other reaction, which prevented the saccharides sorption from the ambient to the interlayer/surface of the metal oxides. In terms of the dimer of glucose, the better adsorptive activity of β-1,4 linkage cellobiose (Q.sub.m=103.36 mg g.sup.−1) was observed in comparison with glucose and α-1,4 linkage maltose (Q.sub.m=75.42 mg g.sup.−1). It could also be explained by the direction of glycosylic bond. The two D-glucopyranose units of cellobiose are found in the same plane, but with one twisted relative to the other; whereas the D-glucopyranose units are twisted in the opposite direction in maltose. The α-1,4 linkage within maltose causes a bend in the molecule so that monomers do not lie in the same plane; therefore, it is harder for maltose to intercalate into the hydrotalcite layer due to its spatial arrangement. This is positively correlated to b value where that for cellobiose is 1.574 L mg.sup.−1 and 0.955 L mg.sup.−1 for maltose.
[0071] As to the glucopyranose derivatives, the deoxy sugars (fucose and 2-deoxy-glucose) also appeared to possess lower Q.sub.m (80 and 69 mg g.sup.−1, respectively) compared to glucose. A possible reason for this outcome could be the lower number of OH groups available within the saccharide for interacting with HTO surface functional groups. It is noted that the position where the hydroxyl group is replaced by the hydrogen atom, C5 for fucose and C2 for 2-deoxy-glucose, does not matter as much with respect to the adsorption behavior. Additionally, the adsorption of glucose was also performed using the calcined commercial hydrotalcite (Sigma-Aldrich, USA) as the adsorbent and the result indicated the commercial hydrotalcite derived oxide hardly adsorbs saccharide molecule.
Saccharides Adsorption
[0072] Saccharide adsorption were tabulated as below Table 2 (HTO) and 3 (metal-HTO).
TABLE-US-00002 TABLE 2 Quantity Q.sub.e adsorbed Saccharides structure (mg/g) (%) Xylose.sup.a
Metal-HTO
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TABLE-US-00003 TABLE 3 Q.sub.e HTO materials (mg/g) % removed 2Ru.sup.1 44.92 20.77 2-r-Ru.sup.2 63.56 28.94 2Ru@.sup.3 84.96 39.01 5Ru.sup.1 40.3 18.5 5-r-Ru.sup.2 67.00 31.07 10Ru.sup.1 36.13 17.18 10-r-Ru.sup.2 100.76 45.28 1Cu.sup.1 27.41 12.53 5Cu.sup.1 80 36.69 Adsorption condition: HTO ≅ 20 mg, glucose concentration ≅ 15 mg/mL, quantified by HPLC-Refractive index detector. .sup.1(1)Al ion is partially replaced by Ru or Cu ion with different weight percentage that display the value at the front. (2)The material was prepared by co-precipitation method followed by calcination. .sup.2Like.sup.1,but reduced by hydrogen at 450° C. for 4 hr. .sup.3Post synthesis; metal loaded hydrotalcite oxide was synthesized by the wet impregnation method with HTO.
[0074] In the above embodiments, the adsorption of various saccharides by HTO and metal-HTO (having loaded metal in an amount of greater than 0 to about 10 wt. %) has been verified. Accordingly, another aspect of the present invention is to provide a saccharide-adsorbed composite, including LDH-based material and saccharides (such as those listed in Tables 1-3) adsorbed on the LDH-based material. As mentioned above, the saccharide-adsorbed composite can be obtained by equilibration of the collapsed LDH-based material and the saccharides in a solvent (e.g. water).
[0075] The above examples are intended for illustrating the embodiments of the subject invention and the technical features thereof, but not for restricting the scope of protection of the subject invention. Many other possible modifications and variations can be made without departing from the spirit and scope of the invention as hereinafter claimed. The scope of the subject invention is based on the claims as appended.