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CAS No. : | 67-47-0 | MDL No. : | MFCD00003234 |
Formula : | C6H6O3 | Boiling Point : | - |
Linear Structure Formula : | - | InChI Key : | NOEGNKMFWQHSLB-UHFFFAOYSA-N |
M.W : | 126.11 | Pubchem ID : | 237332 |
Synonyms : |
5-Hydroxymethylfurfural
|
Num. heavy atoms : | 9 |
Num. arom. heavy atoms : | 5 |
Fraction Csp3 : | 0.17 |
Num. rotatable bonds : | 2 |
Num. H-bond acceptors : | 3.0 |
Num. H-bond donors : | 1.0 |
Molar Refractivity : | 30.22 |
TPSA : | 50.44 Ų |
GI absorption : | High |
BBB permeant : | No |
P-gp substrate : | No |
CYP1A2 inhibitor : | No |
CYP2C19 inhibitor : | No |
CYP2C9 inhibitor : | No |
CYP2D6 inhibitor : | No |
CYP3A4 inhibitor : | No |
Log Kp (skin permeation) : | -7.48 cm/s |
Log Po/w (iLOGP) : | 0.91 |
Log Po/w (XLOGP3) : | -0.58 |
Log Po/w (WLOGP) : | 0.43 |
Log Po/w (MLOGP) : | -1.06 |
Log Po/w (SILICOS-IT) : | 1.24 |
Consensus Log Po/w : | 0.19 |
Lipinski : | 0.0 |
Ghose : | None |
Veber : | 0.0 |
Egan : | 0.0 |
Muegge : | 1.0 |
Bioavailability Score : | 0.55 |
Log S (ESOL) : | -0.54 |
Solubility : | 36.7 mg/ml ; 0.291 mol/l |
Class : | Very soluble |
Log S (Ali) : | -0.01 |
Solubility : | 124.0 mg/ml ; 0.98 mol/l |
Class : | Very soluble |
Log S (SILICOS-IT) : | -1.35 |
Solubility : | 5.67 mg/ml ; 0.045 mol/l |
Class : | Soluble |
PAINS : | 0.0 alert |
Brenk : | 1.0 alert |
Leadlikeness : | 1.0 |
Synthetic accessibility : | 2.25 |
Signal Word: | Warning | Class: | N/A |
Precautionary Statements: | P261-P280-P305+P351+P338 | UN#: | N/A |
Hazard Statements: | H302-H315-H319-H332-H335 | Packing Group: | N/A |
GHS Pictogram: |
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* All experimental methods are cited from the reference, please refer to the original source for details. We do not guarantee the accuracy of the content in the reference.
Yield | Reaction Conditions | Operation in experiment |
---|---|---|
72 %Spectr. | at 100℃; for 10 h; | 1.8 g of sucrose,0.271 g of GeCl4, 0.091 g of BBr3, and 20 mL of n-propanol were added to 50 mL of a polyTetrafluoroethylene-lined stainless steel reactor,Heated to l00 ° C,The reaction was carried out at that temperature for 10 h. Filtration,To remove unreacted sucrose and other insoluble impurities,The solvent was removed by rotary evaporation,2 mL H20 was added and the organic phase was extracted with methyl isobutyl ketone,The resulting organic phase was rotary evaporated to a high purity furan derivative,The isolated yield was 83percent. The qualitative analysis of the reaction products was carried out by gas chromatography-mass spectrometry (GC-MS)And with the standard material (HMF,5-propoxymethylfurfural and propyl propionate) in gas chromatography (GC) were compared and confirmed. Quantitative analysis of the yield distribution of different furan derivatives was confirmed by 1H NMR,The product distribution results are:5-propoxymethylfurfural was 72percent, HMF was 9percentPropyl propionate was 19percent |
Yield | Reaction Conditions | Operation in experiment |
---|---|---|
100% | With nicotinamide adenine dinucleotide; sodium hydroxide; In aq. phosphate buffer; at 35℃; for 0.5h;pH 8.5;Enzymatic reaction; | ALD-003 (5mg), NOX-009 or NOX-001 (5mg) and NAD or NADP (2Omol% based upon the amount of ALD-003) was added to 0.5mL 0.25M KPi (pH 8.5). The pH was adjusted to pH 8.5 with 1M NaOH. 10mM DFF or HMF was added and the reaction was left in ashaking incubator at 35C. After a specified time the reaction was quenched with 1 M HCI, centrifuged and analysed by RP-HPLC. The results are found in Tables 5, 6, and 7A. Reaction Conditions: 0.SmL KPi 0.25M pH 8.5, 5mg CFE, 2Omol% cofactor, 5mg NOX,10mM Substrate, 35C, reaction time 30 minutes. |
99% | With oxygen; sodium hydroxide; In water; at 20℃; | 0.2g of 5-hydroxymethylfurfural,0.05g Ag-PVP/ZrO2 catalyst (Ag:PVP=1:0.5 (molar ratio), 2.5% load),0.126g NaOH, 50mL water was added to a 150mL three-necked flask,And oxygen is introduced, the oxygen flow rate is 60 mL/min, and the reaction is carried out at a temperature of 20 C.Real-time sampling,The product was determined by high performance liquid chromatography for the content of 5-hydroxymethylfurfural and 5-hydroxymethylnonanoic acid.When the reaction is 12h,The conversion rate of 5-hydroxymethylfurfural is 99%.Yield of 5-hydroxymethyl-furoic acid 99%The selectivity is 100%. |
92% | With oxygen; sodium hydroxide; In water; at 80℃; under 3750.38 Torr; for 12h;Autoclave; Green chemistry; | Take 0.317 g of HMF, 2 g of NaOH (20%) and 3 ml of water into the autoclave. The reaction vessel was charged with 10 ml of polytetrafluoroethylene lined autoclave with 0.30 g Pt / NaY (Pt lwt% As the catalyst, the program temperature to 80 C, filled with 0.5MPa oxygen, the reaction 12 hours, the reaction process continue to add oxygen to ensure that the reaction at constant temperature and constant pressure. The reaction product was centrifuged and the supernatant was removed and analyzed using HPLC. The results showed that the conversion rate of HMF was 100% and the yield of HMFA was 92%. The reaction results are shown in Table 1. |
With oxygen; sodium carbonate; In water; at 20 - 50℃; for 2h; | Catalytic Reaction Of HMF To FDCA For this reaction, Na2C03 was used as the base. 1 g of extracted HMF was first dissolved in 5 g of water. The Na2C03 was separately prepared by dissolving Na2C03 in water. The oxidation catalyst was then added follow by the HMF solution at ambient room temperature. With oxygen gas bubbling, the solution was first heated to 50C for 2 hours, and HMF was fully converted to HFCA. After that, the reaction was heat to 95C and kept for 7 hour. The pH of the aqueous solution was then adjusted to 1 and FDCA was precipitated from the solution. The precipitate was filtered and washed with ethanol. | |
2.74 g | With 4% Au/TiO2; oxygen; sodium hydroxide; In water; at 70℃; for 7h;pH 10; | 10 g of HMF, 150 g of water, and 1 g of catalyst (4% Au/TiO2) were added into a round bottom bottle (250 mL) and then heated to 70 C. Air under atmosphere pressure was introduced into the liquid in the flask. The pH value of the above reaction was controlled to 10 by adding a sodium hydroxide aqueous solution into the flask. The reaction was continued for 7 hours to obtain a crude aqueous solution. The crude aqueous solution was extracted by 200 mL of ethyl acetate two times, and the aqueous phase of the extractions was collected by a separatory funnel. The collected aqueous phase was titrated by concentrated hydrochloric acid (HCl) until its pH value reached 3. The acidified aqueous phase was extracted by 200 mL of ethyl acetate two times, and the organic phase of the extractions was collected. The collected organic phase was vacuumed concentrated to obtain 2.74 g of solid, which was 5-hydroxymethyl-2-furoic acid (HMFCA). The above reaction is shown in Formula 8. The product of Formula 8 had NMR spectra as below: 1H NMR (400 MHz, d-DMSO): 13.08 (br, 1H), 7.14 (d, 1H, J=3.4 Hz), 6.45 (d, 1H, J=3.4 Hz), 5.59 (s, 1H), 4.44 (s, 2H); 13C NMR (100 M Hz, d-DMSO): 160.1, 159.8, 144.4, 119.0, 109.4, 56.2. |
2.74g | With gold on titanium oxide; oxygen; sodium hydroxide; In water; at 70℃; under 760.051 Torr; for 7h;pH 10; | 10 g of HMF,150 g of water,And 1 g of 4% Au / TiO2 catalyst250 mL of a round bottom flask,Heated to 70 C,And air was introduced under normal pressure.The pH of the reaction was then controlled to 10 with the addition of aqueous sodium hydroxide,After 7 hours of continuous reaction, an aqueous solution of the crude product was obtained.The crude aqueous solution was added to 200 mL of ethyl acetate for extraction twice,The water layer was taken in a separatory funnel.The aqueous layer was titrated with concentrated hydrochloric acid (HCl) until the pH was 3.After extraction twice with 200 mL of ethyl acetate, the organic layer was taken.The organic layer was concentrated under reduced pressure to give 2.74 g of a solid,5-hydroxymethyl-2-furoic acid (HMFCA).The above reaction is shown in Formula 8 below. |
With sodium hydroxide; In water; at 30℃; under 2250.23 Torr; for 5h; | The Au / MgO (Au0.5 wt%) catalyst, 1 mmol of 5-hydroxymethylfurfural, NaOH, 10 ml of water was charged to a stainless steel autoclave with a Teflon-lined internal metal, 5-hydroxymethylfurfural: NaOH = 0.015: 1: 4 (mol: mol: mol).Using automatic temperature control program temperature to the reaction temperature of 30 C, adding 0.3MPa oxygen, reaction 5 hours, the reaction process to maintain the same pressure.The reaction product was analyzed by HPLC. | |
95%Chromat. | With recombinant Escherichia coli cells expressing 3-succinoylsemialdehyde-pyridine dehydrogenase from Comamonastestosteroni SC1588; In aq. phosphate buffer; at 30℃; for 5h;pH 7;Enzymatic reaction; | General procedure: Typically, 4 mL of phosphate buffer (0.2 M, pH 7) containing 50mMFF and 50 mg (cell wet weight) per mL microbial cells was incubated at30 C and 160 r/min. Aliquots were withdrawn from the reaction mixturesat specified time intervals and diluted with the correspondingmobile phase prior to HPLC analysis. The conversion was defined as theratio of the consumed substrate amount to the initial substrate amount(in mol). The yield was defined as the ratio of the formed productamount to the theoretical value based on the initial substrate amount(in mol). The selectivity was defined as the ratio of the formed productamount to the total amount of all products (in mol). All the experimentswere conducted at least in duplicate, and the values were expressed asthe means ± standard deviations. |
Yield | Reaction Conditions | Operation in experiment |
---|---|---|
99.6% | With copper(II) nitrate trihydrate; In water; toluene; acetonitrile; at 80℃; for 8.0h; | Article 0.2g raw materials 5-hydroxymethyl-furfural, 0.36g oxydizers cu (NO3)2· 3H2O in 2.5 ml acetonitrile and 5 ml of water in the mixed solution, stir, add 5 ml toluene, at a temperature of 80 C, agitation speed 1200rpm reaction under the conditions of 8h, after the reaction is ended split-phase, non-polar solvent phase after concentrating under reduced pressure to obtain 2,5-furan-phthalaldehyde crude product, obtained after re-crystallization with methylene chloride 2,5-furan-phthalaldehyde of excellence.By the detection, 2,5-furan-phthalaldehyde in the yield of 99.6%, 5-hydroxymethyl-furfural conversion is 99.6%. |
> 99% | With oxygen; In aq. phosphate buffer; acetonitrile; at 37℃;pH 7.6;Enzymatic reaction; | GOase M35 (3.3 mg/mL; 103 pL), catalase (3.3 mg/mL; 33 pL), HMF (3 pL of a solution defined in Table 2 in MeCN), potassium phosphate buffer (concentration as per Table 2, pH 7.6) were combined and made up to 300 pL. After full conversion of HMF to DFF, PaoABC (13.3 mg/mL; 5 pL) was added. Formation of DFF was monitored via RP-HPLC using a Thermofisher Hypurity 018 column with flow rate 0.6mLlmin using 85% water + 0.1% Acetic acid and 15% MeCN. Formation of 2,5-FDCA was monitored via RP-HPLC using a Thermofisher Hypurity 018 column with flow rate 1 mL/min using a 98% 10 mM phosphate buffer (pH 6.5) and 2% MeCN mobile phase. The results can be found inTable 2. |
98% | With Immobilization of vanadyl (VO2+) and cupric (Cu2+) ions on sulfonated carbon; air; In acetonitrile; at 140℃; under 30003.0 Torr; for 4.0h;Autoclave; | General procedure: The general scheme of aerobic oxidation of HMF into DFF isdepicted in Scheme 2. In a typical reaction, 300 mg catalyst, 300 mgHMF and 30 mL acetonitrile were charged in the high pressurestainless steel reactor and air (40 bar) was introduced at 140C.After 4 h of reaction, the reactor was cooled, the pressure wasreleased and the catalyst was separated by centrifugation. The sep-arated catalyst was washed with acetonitrile and re-used withoutany further treatment. The product analysis was performed usingHPLC system equipped with BIO-RAD Aminex HPX-87H ion exclu-sion column (300 mm × 7.8 mm), the eluent 0.1% H3PO4, flow rate0.5 mL/min, column temperature 60C, UV-Vis (254 nm) detec-tor. To prepare samples for HPLC analyses, the liquid product wasdiluted 10 times with eluent. All major products were identified bycomparing their retention time with those of authentic compounds(15.1 min, 20.8 min, 21.6 min, 32.7 min and 39.8 min for FDCA, FFCA,HMFCA, HMF and DFF, respectively). |
98% | With 2,2,6,6-Tetramethyl-1-piperidinyloxy free radical; oxygen; In acetic acid; at 50℃; under 760.051 Torr; for 5.0h; | The experiments were carried out in test tubes equipped with a balloon containing pure O2, using O2 as the oxidant. In a general procedure, HMF (125 mg, 1 mmol), ECS-IL-Al(NO3)3 (90 mg), TEMPO (8.5 mg, 0.05 mmol) and glacial acetic acid (2 mL) were added to a 10 mL test tube. The reaction mixture was stirred magnetically at 50 C for 5 h. After completion of the reaction, the mixture was cooled down to room temperature and filtered, and the remaining solid was washed with acetonitrile and acetone to separate the catalyst. Then, the recovered catalyst was dried and used in several runs in the same manner as reported for the first run. Samples were collected and analyzed via HPLC. |
96.6% | With manganese(IV) oxide; In toluene;Dean-Stark; Inert atmosphere; Heating; | To a single necked (24/40) round bottomed flask was added, toluene (400 mL), 5-hydroxymethylfurfural (11.46 g, 0.0909 mol), and a PTFE coated magnetic spinning egg. The mixture was stirred vigorously pure-crystalline HMF did not fully dissolve. To that stirring mixture was added 88% active electrolytically precipitated manganese dioxide (Alfa Aesar, 11.51 g, 0.2498 mol). The black slurry was stirred vigorously, and a Dean-Stark trap was installed above the flask (topped with a Dimroth condenser plumbed with a stream of cold water). The headspace of the flask was purged with argon and the mixture was brought up to a fast boil. The flask was wrapped in aluminum foil and distillate began to collect. As the reaction proceeded, water separated to the bottom of the trap while dry toluene was allowed to return. This azeotropic distillation proceeded for six hours. The mixture was suction filtered through qualitative paper in a ceramic Buchner funnel. The residue was packed into a Soxhlet extractor and the filtrate was installed below. The Soxhlet extractor was charged from the top with enough acetone to flush the extractor five times. The mixture was brought up to boiling temperature with a heating mantle and a variable controller. The residue was continuously extracted with acetone in that manner overnight. (0148) The heat was killed, the acetone/toluene solution was suction filtered through a bed of Celite packed into a medium porosity fitted Buchner funnel. The filtrated was a light yellow color and was concentrated by rotary evaporation under a vacuum induced by a water aspirator. The light yellow crystalline solid was scraped into a free flowing flakey solid and dried on the high vacuum line to constant mass which afforded 2,5-diformyl furan (10.89 g, 0.0878 mol, 96.6% yield). 1H NMR (CDCl3, 400 MHz) delta: 7.35 (s, 2H), 9.87 (s, 2H) (0150) 13C NMR (CDCl3 100 MHz) delta: 119.3, 154.2, 179.2 |
95.3% | With oxygen; In dimethyl sulfoxide; at 120℃; under 7500.75 Torr; for 6.0h; | In atypical experiment, the high-pressure hastelloy reactor(Microreactor, Yanzheng Instrument Ltd. Shanghai) was charged with HMF (126 mg, 1 mmol), HPMoVsurf(n)/CeO2 (80 mg), and 5 mLDMSO. The reaction was conducted at 120 C and initiated by vigorous stirring with a magnetic stirrer under 1.0 MPa of oxygen pressure for 6 h. After the reaction was finished, the reactor was cooling down toroom temperature and the oxygen pressure was released. The catalyst was separated by centrifugation. The analysis of the recovered solutions was monitored by using high-performance liquid chromatography(HPLC). Samples were separated by a reversed-phase C18 column and detected by UV detector at the wavelength of 280 nm. The mobile phase was constituted of acetonitrile and 0.1 wt % acetic acid aqueous solution(10: 90, v/v) at 0.9 mL min-1 [18]. |
95% | With 3-(tert-butoxycarbonyl amino)-9-azabicyclo[3.3.1]nonane N-oxyl; oxygen; sodium nitrite; In acetic acid; at 25℃; for 1.0h; | General procedure: A 25-mL tube equipped with a magnetic stirrer bar was added p-methylbenzyl alcohol (0.122 g, 1 mmol), sodium nitrite (5.5 mg, 8 mol%) and 3-(tert-butoxycarbonyl amino)-9-azabicyclo[3.3.1]nonane N-oxyl (3-BocNH-ABNO) (7.7 mg, 3 mol%). After the air in the tube was replaced with O2, 1 mL of acetic acid was added with syringe. Then the mixture was stirred under dioxygen atmosphere (balloon) at room temperature until the reaction was completed. After the reaction was finished, to the reaction mixture was added 8 mL of diethyl ether. Then the mixture was transferred into a separation funnel, and washed with saturated sodium bicarbonate solution (10 mL×3). The aqueous phase was extracted with 8 mL of ether. The combined organic phases was concentrated on a rotary evaporator and the residue was purified by column chromatography on silica gel using petroleumether/diethyl ether as eluent to afford p-methyl benzaldehyde as a colorless liquid; yield: 0.108 g (90%). |
94.7% | With 4-acetylamino-2,2,6,6-tetramethyl-1-piperidinoxy; oxygen; nitric acid; In toluene; at 85℃; under 7500.75 Torr; for 2.5h;Autoclave; | Add 5-hydroxymethylfurfural (5-HMF, 2.5 g) to toluene (47.5 g) to a concentration of 5% by mass in an autoclave with an internal volume of 100 mL,Furthermore 4-acetamide-2,2,6,6-Tetramethylpiperidine 1-oxyl(4AA-TEMPO, 0.106 g, 2.5 mol% relative to 5-HMF) and 1N nitric acid (2.07 g) were added and sealed. Using a back pressure valve at the outlet of the autoclave while passing a mixed gas of 5% by volume oxygen gas and 95% by volume nitrogen gas as the oxygen-containing gas at a rate of 100 mL / min, the pressure in the autoclave is 1.0 MPa Adjusted to The reaction solution was reacted at 85 C. for 2.5 hours while being stirred at 500 rpm. The outlet oxygen concentration was measured with an oximeter manufactured by Itinenjiko Co., Ltd., and the point at which the consumption of oxygen was not confirmed was taken as the end point of the reaction.After the reaction, the reaction solution is analyzed using a gas chromatograph (column: DB-1701, detector: FID) manufactured by Agilent, and the raw material conversion ratio, the yield of diformylfuran (DFF), the selectivity, the DFF production rate The catalyst rotation number (TON) was calculated. Since the ratio of the amount of nitric acid to toluene, which is an organic solvent, is small, the reaction solution was diluted and analyzed without separating the aqueous layer and the organic layer. In addition, the DFF formation rate represents the number of moles of DFF produced per hour by oxidation of 5-HMF by 1 mole of 4AA-TEMPO, and the catalyst rotation number is 5-HMF of 1 mole of 4AA-TEMPO. Represents the number of moles of DFF produced by oxidizing. The results are shown in Table 1.The reaction solution was also cooled in an ice bath for about 1 hour. After cooling, the reaction solution was treated with ADVANTEC No. The crystals were collected by vacuum filtration using 5 C filter paper and a Buchner funnel. The obtained crystals were analyzed by gas chromatography, which confirmed that the DFF had a purity of over 98%. In addition, the recovery rate of DFF was 72.4%. |
93% | With 2,4,6-trimethyl-pyridine; 4-acetylamino-2,2,6,6-tetramethyl-1-piperidinoxy; iodine; sodium hydrogencarbonate; In dichloromethane; water; at 20 - 22℃; for 1.0h;Catalytic behavior; | A solution of 5-hydroxylmethylfurfural 1c (10.08 g, 80 mmol), nitroxide 4a (0.85 g, 4.0 mmol) and collidine 6d (0.97 g, 8 mmol) in CH2Cl2 (100 mL) was added to a vigorously stirred solution of NaHCO3 (20.16 g, 240 mmol) in water (100 mL) at 20 C. Then I2 (40.6 g, 160 mmol) powder was added portionwise within 10 min to the formed reaction mixture at vigorous stirring and temperature 20-22 C. The reaction mixture was stirred at 20-22 C for 1 h, then powdered crystalline sodium thiosulfate was added portionwise to discoloration. Organic and aqueous phases were separated and the aqueous phase was then extracted with CH2Cl2 (3×20 mL). Organic phase and the extracts were combined, dried with anhydrous Na2SO4 and evaporated to dryness to give 9.22 g of crude 2c of 97% purity according to HPLC analysis (93% yield). This product was recrystallized from water to give 8.37 g (88% yield) of pure compound 2c, mp 109-110 C (lit.1 109-110 C). 1H NMR (CDCl3) delta 7.33 (s, 2H, 2CH), 9.83 (s, 2H, 2CHO). 13C NMR (CDCl3) delta 119.4, 154.3, 179.3. |
93% | With phosphoric acid; sodium nitrite; at 25℃; for 1.0h; | Sodium nitrite was added with vigorous stirring (magnetic stirrer) to a solutionof 0.310 g (2.46 mmol) of 5-(hydroxymethyl)-furfural in 4 mL of phosphoric acid (85 wt %). Themixture was stirred for 1 h at 25C in a flask equippedwith a reflux condenser, 10 mL of distilled water wasadded, and the mixture was extracted with chloroform(5 × 5 mL). The combined extracts were washed withwater until neutral washings, dried over anhydroussodium sulfate, filtered, and evaporated to dryness.The residue was recrystallized from hexane containing2 vol % of chloroform. Colorless crystals, mp 108-110C [9]. 1H NMR spectrum, delta, ppm: 7.33 s (2H,=CH), 9.83 s (2H, CHO). 13C-{1H} NMR spectrum,deltaC, ppm: 119.4 (=CH), 154.2 (=C), 179.2 (CHO). |
90% | With Iron(III) nitrate nonahydrate; 2,2,6,6-Tetramethyl-1-piperidinyloxy free radical; sodium chloride; In 1,2-dichloro-ethane; at 20℃; for 4.0h; | A, 5-HMF (63 mg, 0.5 mmol) was added to 2 mL of dichloroethane and then TEMPO (7.8 mg, 0.025 mmol, 5 mol%), Fe (NO3)3· 9H2(10.1 mg, 0.025 mmol, 5 mol%) and NaCl (1.5 mg, 0.025 mol, 5 mol%) were added and stirred at room temperature for 4 h to give a reaction mixture containing 2,5-furanaldehyde. The results of the GC detection are shown in Fig. 1. It can be seen from Fig. 1 that the product 2,5-furanaldehyde (internal standard: 5-methylfurfural) was successfully obtained. |
88% | With Iron(III) nitrate nonahydrate; 2,2,6,6-Tetramethyl-1-piperidinyloxy free radical; sodium chloride; In 1,2-dichloro-ethane; at 20℃; for 4.0h;Catalytic behavior; | 5-HMF (63 mg, 0.5 mmol), Fe(NO3)3·9H2O (10.1 mg, 0.025 mmol, 5 mol%), TEMPO (7.8 mg, 0.025 mmol, 5 mol%), NaCl (1.5 mg, 0.025 mol, 5 mol%) were charged into a tube, and then 2 mL of DCE was added. The reaction mixture was stirred at room temperature for 4 h in open air. Then, the reaction was monitored by GC analysis using 5-methyl-2-furaldehyde as an internal standard. Separation of 2,5-DFF from reaction solution: after the epinephelos solution was filtered and washed with ethyl acetate for three times, the organic solvents were evaporated and the crude product was purified by flash column chromatography (PE:EA=3:1) to give the desired product in 88 % yield (detected by 1H NMR). 1H NMR (400 MHz, CDCl3): delta 9.84 (s, 2H), 7.33 (s, 2H). 13C NMR (100 MHz, CDCl3): delta 179.34, 154.30, 119.43. |
84% | With oxygen; In toluene; at 110℃; under 760.051 Torr; for 6.0h; | 5-HMF is reacted in presence of several catalysts to produce DFF, in presence of organic solvents for 6 hours with 1 atm 02. Results are mentioned in Table 3. Table 3 It appears then that good yield and conversion are obtained with the process of the present invention with several variations regarding to the surfactant compounds used to produce the mesostructured VPO catalysts. |
84% | With oxygen; In toluene; at 110℃; under 760.051 Torr; for 6.0h; | 5-HMF is reacted in presence of several catalysts to produce DFF, in presence of organic solvents for 6 hours with 1 atm 02. Results are mentioned in Table 3. Table 3 It appears then that good yield and conversion are obtained with the process of the present invention with several variations regarding to the surfactant compounds used to produce the mesostructured VPO catalysts. |
83% | With 2,2,6,6-Tetramethyl-1-piperidinyloxy free radical; copper(l) chloride; In acetonitrile; at 20℃; under 750.075 Torr; for 24.0h; | All experiments were carried out in one-necked flasks equipped with a condenser. The condenser was left open in experiments using air as the oxidant and equipped with a balloon containing pure O2 in experiments using O2 as the oxidant. In a general procedure, HMF (125 mg, 1 mmol), CuCl (10 mg, 0.1 mmol) and TEMPO (17 mg, 0.1 mmol) were dissolved in solvent (5 mL). The reaction mixture was stirred magnetically (450 rpm) for 24 h and the reaction volume subsequently adjusted. Samples were collected periodically and analyzed via HPLC. More details about the instrument setup and HPLC analysis are found in the Supporting information. |
78% | With [bis(acetoxy)iodo]benzene; oxygen; acetic acid; In ethyl acetate; at 40℃; under 760.051 Torr; for 1.0h; | All experiments were carried out in two-necked round bottomflasks initially purged with O2 and then fastened with an O2-filled balloon (1 atm). The flasks were placed in a temperature-controlledoil bath with magnetic stirring. Typically, appropriate amounts of the reactants 5-HMF, TEMPO-SBA-15, BAIB, and acetic acid (if used) were allowed to react in ethyl acetate solvent (10-15 mL). The reaction mixture was magnetically stirred for a certain reaction time,at a controlled temperature. After each run, the reaction mixture was filtered to separate the solid catalyst. The filtrate was dried under reduced pressure, dissolved in deionized (DI) water and then analyzed in high pressure liquid chromatography (HPLC). |
66% | With 2,2,6,6-Tetramethyl-1-piperidinyloxy free radical; [bis(acetoxy)iodo]benzene; acetic acid; In ethyl acetate; at 30℃; for 0.75h;Green chemistry;Catalytic behavior; | As described above, because BAIB play the TEMPO radical, the amount of TEMPO can be significantly reduced catalytically at stoichiometric levels (stoichiometric) level. As it is shown in Table 1, the 5-HMF, by using the case where a small amount of TEMPO and BAIB chemical stoichiometric amount of 4 hours at room temperature to obtain the 2,5-DFF of 34% (Entry 2). The results indicate that under a mild condition with addition BAIB, TEMPO or even promote the 5-HMF oxide in limited circumstances. This indicates that TEMPO radical that is being played by the BAIB. Referring to Figure 2 of the (B) HPLC chromatogram, CH-2,5 DFF with a product 3 is COOH is observed. These results are consistent with the reaction mechanism (see Fig. 3) described above. The CH 3 COOH may be due to the ligand exchange reaction of the by-product that is released during playback or TEMPO radical (see above reaction mechanism 2 (B)), BAIB (see reaction mechanism 2 (A)). The results described in the above means that the amount of TEMPO in the presence of BAIB will be significantly reduced. |
58% | In 1,3,5-trimethyl-benzene; at 150℃; for 12.0h;Autoclave; Inert atmosphere; | Add 5-hydroxymethylfurfural (5mmol), mesitylene (15mL), and reduced 6.6wt% Cu/gamma-Al2O3 catalyst (1.0g) to the autoclave. Pass N2 to exhaust the air in the empty reactor, stop the reaction after mechanically stirring the reaction at 150 C for 12h. The reaction was cooled to room temperature, the supernatant was centrifuged, and the catalyst was settled at the bottom. The supernatant was directly analyzed by gas chromatography. The reaction result was that the conversion of 5-hydroxymethylfurfural was 58.0%, The yield of formaldehyde was 36.6%. Wherein the detection of the product: After completion of the reaction, the reaction solution was centrifuged, the upper layer is a colored supernatant, the lower layer is a metal catalyst.The supernatant was centrifuged, filtered and analyzed by gas chromatography. |
46.7% | With vanadium phosphate; In dimethyl sulfoxide; at 150℃; for 5.0h; | Example 61 mmol glucose and 0.3 mmol AlCl3 were placed in a round bottom flask. It was added 5mL of dimethyl sulfoxide. After stirring at room temperature for 10 minutes, heat to 120 deg. C. It is reacted at this temperature for 3h. Then,cool to room temperature. Thereto was added 0.1mmol VOPO4. After stirring evenly, heat to 150 deg.C. At this temperature, react for 5h. After completion of the reaction, 20mL of water and 30mL of methylene chloride was added, separated, the solvent was removed by distillation under reduced pressure, the product was purified by sublimation. The first step after the completion of the reaction part of the purified product was determined to HMF yield was 84.9%, the final DFF yield(based on glucose) of 46.7%. |
37.5% | With oxygen; In N,N-dimethyl-formamide; under 760.051 Torr; for 4.0h;Heating; Green chemistry; | The aerobic oxidation of HMF under atmospheric pressure wascarried out in a 25 mL round bottom flask, which was coupledwith a reflux condenser and capped with a balloon. Typically,HMF (1 mmol, 126 mg) was firstly dissolved into DMF (7 mL) witha magnetic stirrer. Then, the catalyst Fe3O4/Mn3O4was addedinto the reaction mixture and flushed with pure oxygen at a rateof 20 mL min-1. The reaction was carried out at 110C for thedesired reaction time. Time zero was taken when the oxygenwas flushed into the reaction mixture. After reaction, the cata-lyst Fe3O4/Mn3O4was separated from the reaction mixture bya permanent magnet, and the products were analyzed by HPLCmethod. |
7.9% | With oxygen; In 1,4-dioxane; water; at 120℃; under 10343.2 Torr;Sealed tube; Inert atmosphere; | [0235] Catalyst testing was conducted within 1 mL glass vials housed in a 96- well insert situated in a high pressure high throughput reactor. See Diamond, G. M., Murphy, V., Boussie, T. R., in Modern Applications of High Throughput R&D in Heterogeneous Catalysis, (eds, Hagemeyer, A. and Volpe, A. Jr. Bentham Science Publishers 2014, Chapter 8, 299-309); see also US 8,669,397, both of which are herein expressly incorporated by reference in their entireties. 10 mg of each powder catalyst was placed into a reactor along with 0.25 mL of a solution prepared in a 3:2 (wt/wt) dioxane:H20 mixture containing 0.5 M 5-hydroxymethylfurfural (HMF) (6.0 wt%). The 1 mL reaction vials within the insert were each covered with a Teflon sheet, a silicon mat and a steel gas diffusion plate each containing pin-holes to enable gas entry. The insert was placed within a pressure vessel which was leak tested under nitrogen pressure. The atmosphere within the reactor was then replaced by oxygen at a target pressure of 200 psig and the reactor was heated to a target temperature of 120C, and then shaken at 800 rpm for 120 min. After the reaction was completed, the shaking was stopped and the reactor was cooled down to room temperature. Samples were prepared for HPLC analysis by sampling from each reactor after diluting the sample with dimethyl sulfoxide (DMSO) and H2O. Reaction products were 5-hydroxymethylfurancarboxylic acid (HMFCA), 2,5- furandicarboxaldehyde (DFF), 5-formylfuran-3-carboxylic acid (FFCA) and 2,5- furandicarboxylic acid (FDCA). Each of the above products as well as remaining HMF were quantified through a calibration curve for each analyte by plotting the relative concentration against the relative detector response for calibration standards, and performing a fit to a parabolic expression. The mass balance (MB) is the sum of remaining HMF (not shown in Table 3), FFCA, and FDCA pathway products. The results are shown in Table 3. |
86%Chromat. | With oxygen; acetic acid;cobalt(II) acetate; manganese(II) acetate; In butanone; at 120℃; under 51716.2 Torr; for 3.5h;Product distribution / selectivity; | SELECTIVE OXIDATION OF HMF TO DFF USING Co/Mn CATALYSTS IN THE PRESENCE OF METHYL ETHYL KETONEExample 1[0032] A reaction mixture containing 97% purity HMF (5.0 g), acetic acid (50 mL), cobalt acetate (0.97 g), manganese acetate (0.98 g), and methyl ethyl ketone (1.90 mL) was placed in a 100 mL reactor and subjected to 1000 psi oxygen at 12O0C for 3.5 hours. The sample was spotted on TLC plates (K5F Whatman) and developed in 1 :1 EtOAc/hexane and visualized under UV light. Visual analysis indicated that after 3.5 hours, substantially all of the HMF was converted. The reaction mixture (58.58 g) was found to contain 46,356g/kg DFF (86%), 2,908 g/kg FFCA (5%), 4,201 g/kg HMF (8%) and 62 g/kg FDCA (1%) for a DFF selectivity of 86%. Subsequent GC/MS data revealed the conversion of HMF to DFF m/z = 124. Thus, after 3.5 hours, the conversion of HMF to DFF was essentially complete.. |
12.4%Chromat. | With ammonium cerium (IV) nitrate; 2,2,6,6-Tetramethyl-1-piperidinyloxy free radical; tetraethylammonium bromide; oxygen; sodium nitrite; In water; at 80℃; under 2250.23 Torr; for 3.0h;Autoclave; Sealed tube; | General procedure: All oxidation experiments are performed in a 120mL autoclave equipped with the magnetic stirring and temperature control. A typical procedure for the oxidation of benzyl alcohol is as follows: 1.08g (10.0mmol) of benzyl alcohol, 0.0156g (0.1mmol) of TEMPO, 0.274g (0.5mmol) of CAN, 0.0690g (1.0mmol) of NaNO2, additive in suitable amount and 10mL of H2O were charged into the reactor, and the atmosphere inside is replaced with oxygen after the reactor is sealed. Then, pure oxygen is charged to 0.3MPa at room temperature. In the following, the autoclave is heated to 80C under stirring, and then kept for 2h. After reaction, the autoclave was cooled to room temperature and excess gas was purged. The mixture was transferred into a flask, in which the reactor was washed with CH2Cl2 for 3-5 times in order to transfer completely. Next, the products are extracted with 6mL CH2Cl2 three times. The obtained products were analyzed with internal standard technique by GC with a flame ionization detector (all products were determined on GC-MS with an Agilent 6890N GC/5973 MS detector). |
With vanadium(IV) oxide sulfate hydrate; copper(II) nitrate trihydrate; oxygen; In acetonitrile; at 80℃; under 750.075 Torr; for 1.5h;Autoclave;Activation energy; | The aerobic oxidation of HMF was carried out in a 50-mL stain-less steel autoclave equipped with a magnetic stirrer, a pressure gauge and automatic temperature control apparatus. Typically, VOSO4(0.2 mmol, 34.3 mg), Cu(NO3)2·3H2O (0.2 mmol, 48.3 mg) and HMF (10 mmol, 1.26 g) were put into the autoclave with Teflon lining, followed by 5 mL acetonitrile. After the autoclave was closed, oxygen was added (0.1 MPa). The autoclave was then heated to 80 C within ca. 20 min. The reaction temperature was maintained at 80 C for 1.5 h. Oxygen was recharged if consumed during the oxidation. The autoclave was cooled to room temperature and depressurized carefully. A sample of the reaction mixture was taken for GC analysis, which were conducted on Agilent GC 7890D equipped with 19095J-323 capillary column(30 m × 530 m × 1.5 m) and a flame ionization detector. The quantitative results were based on the internal standard method using mesitylene as internal standard. The results reported as conversion and selectivity are expressed in mol% based on the total HMF intake. | |
With (x)H2O*KMn8O16; In N,N-dimethyl-formamide; at 109.84℃; for 1.0h;Autoclave; High pressure; | General procedure: HMF oxidation reactions were carried out in a Teflon-lined stainless steel autoclave (50 mL). Typically, 1 mmol HMF (98%, Alfa Aesar) and 50 mg catalysts were introduced to 10 mL DMF (J.T.Baker, 60.02% H2O) in the autoclave and were stirred at ca.700 rpm. The reactants and products were analyzed by HPLC (ShimadzuLC-20A) using a UV detector and an Alltech OA-1000 organic acid column (0.005 M H2SO4 mobile phase, 0.7 mL/minflow rate, and 353 K oven temperature). HMF reaction activities were reported as molar HMF conversion rates per gram (or m2) of catalysts per hour (i.e., mmol HMF/(gcat h) or mmol HMF/(m2cat h)) and selectivities on a carbon basis. For catalyst recycling tests, if not specially stated, the retrieved catalysts were washed thoroughly with deionized water and then dried in vacuum oven before being recycled. | |
With 4-acetylamino-2,2,6,6-tetramethyl-1-piperidinoxy; nitric acid; acetic acid;Autoclave;Catalytic behavior; | 10 g (79 mmol) of 5-(hydroxymethyl)furfural (referred to herein as 5-HMF, purity of 98%), 0.213 g (1 mmol) of 4-acetoamino(2,2,6,6-tetramethylpiperid-1-yl)oxyl (referred to herein as 4AA Tempo), 100 g (1.67 mol) of acetic acid and 4.35 g of nitric acid at 0.91 mol/1 (4 mmol) are placed in a stainless-steel autoclave with an internal volume of 600 ml, sold by the company Parr (model No. 4346), equipped with a variable-speed stirrer and a double-paddle system in the form of an impeller, a gas inlet tube connected to a pressurized bottle equipped with a pressure regulator, a gas evacuation tube, a cooling coil and a system for measuring and regulating the temperature. The ratios are established so as to have 2.1% by weight of 4AA Tempo, 5 mol % of nitric acid relative to the 5-HMF. The HNO3/4AA Tempo ratio is thus 4. Once all the reagents have been placed in the autoclave, it is purged once at 0.3 MPa with oxygen and then heated under 0.1 MPa of oxygen. The stirring speed is then adjusted to 1600 rpm. When the reactor reaches 70 C., the oxygen pressure is adjusted to 0.3 MPa. The consumption of oxygen starts at 80 C. The temperature is regulated at 85 C. for 1 hour. After one hour of contact time, the autoclave is cooled by simply switching off the heating, with removal of the heating mantle, without circulation of water in the cooling loop (which avoids crystallization of the DFF on the coil). The stirring is lowered to 250 rpm during the cooling. When the reactor reaches 60 C., the stirring is stopped and the pressure is reduced to atmospheric pressure. The autoclave is opened at 60 C., all the components are in solution, and there are neither any crystals nor any precipitates. A sample of the crude reaction product is taken and analyzed by gas chromatography (GC) and the results are expressed as a percentage of the area distribution. The composition of the crude reaction product is presented in Table 1. | |
With oxygen; In N,N-dimethyl-formamide; at 120℃; under 760.051 Torr; for 8.0h;Catalytic behavior; | 2.4. General procedure for the oxidation of HMF HMF (1 mmol), DMF (3 mL), and catalyst (20 mg) were mixed in athree-neck ask. Then the mixture was heated to 120 C and stirredunder O2 atmosphere for 8 h at atmospheric pressure. O2 was chargedfrom a balloon. After the reaction was completed, the catalyst was l-tered to be used in the next cycle. The conversion and selectivity are de-termined by HPLC analysis. | |
With ruthenium-carbon composite; oxygen; In toluene; at 110℃; under 14997.7 Torr; for 1.0h; | [0035] In a second process, a mixture of 5-hydroxymethylfurfural (1 equivalent), ruthenium on activated carbon catalyst (0.01 equivalent metal) and toluene as solvent is treated with oxygen gas (about 290 psi) while heating at about 110 C for about 1 hour. After filtration to remove the catalyst the toluene is removed by evaporation under reduced pressure to yield 2,5-diformylfuran. A mixture of 2,5-diformylfuran (1 equivalent), hydroxylamine hydrochloride (2 equivalents), potassium acetate (2 equivalents) and 50% aqueous ethanol is heated at about 50 C for about 1 hour. The precipitate is filtered, washed with water and dried under reduced pressure to yield 2,5-diformylfuran dioxime. A mixture of 2,5-diformylfuran dioxime (1 equivalent), Raney nickel (about 5 grams per mmol of dioxime) and tetrahydrofuran as solvent is treated with hydrogen gas (about 50 bar) in an autoclave. When no more hydrogen is absorbed, the catalyst is removed by filtration under argon gas and rinsed with tetrahydrofuran. The combined filtrates are concentrated under reduced pressure to yield 2,5-bis(aminomethyl)furan that is purified by recrystallization of its dihydrobromide salt. |
Yield | Reaction Conditions | Operation in experiment |
---|---|---|
9%; 60%; 7% | With iron(II) phthalocyanine; In aq. phosphate buffer; at 37 - 80℃; for 16.0833h;pH 7; | HMF (100 mM) was added to KPi buffer (500 mM pH 7.0). GOase M35 (103p1 of3.3mg/mL), PaoABC (ipI of 28.9mg/mL) and a metal complex (see Table 4) were added at 37 00 and the pH was continuously adjusted with NaHCO3 for a period of 16 hours. The reaction was heated to 80 00 for 5 minutes and left to cool. The solution containing denatured protein was centrifuged and the supernatant removed and analysed by RP20 HPLC. |
Yield | Reaction Conditions | Operation in experiment |
---|---|---|
With potassium hydroxide; mesitylenesulfonylhydroxylamine; | EXAMPLE 66 [5-(5-Amino-7-bromo-[1,2,4]triazolo[1,5-a]pyridin-2-yl)-furan-2-yl]-methanol The title compound, MS m/e (%): 311 (M30 +2, 100), was prepared in accordance with the general method of example 63 from <strong>[329974-09-6]4-bromo-pyridine-2,6-diamine</strong>, O-mesitylene-sulfonylhydroxylamine, and 5-hydroxymethyl-furfural. The purification was performed with reversed phase HPLC eluting with an acetonitrile/water gradient. |
Yield | Reaction Conditions | Operation in experiment |
---|---|---|
With water;phosphoric acid; at 50 - 95℃; for 0.25 - 0.75h;pH 1.75 - 3.75; | Figure 4, from a second laboratorial work, is a TLC - Thin Layer Chromatography on silicagel 60 (Merck) developed with the mixture isopropanol : ethyl acetate : water 5:1 :2 as mobile phase and with partial runs of 1/3, 2/3, and 3/3 of the front line and developed with orcinol : sulfuric acid : methanol at 1000C for 5 minutes. This figure illustrates the profile of FOS - Fructooligosaccharides when one hydrolyzes purified inulin from dahlia roots (5g%) with phosphoric acid at pH = 2.5 at 850C during 15 minutes (15), 30 minutes (30), and 45 minutes (45), indicating that the modulation of a single kinetic parameter - time of hydrolysis - already allows to govern the quantitative relation of FOS > fructose (cases 15 and 30) or the opposite (FOS < fructose; 45). A similar strategy for FOS > fructose may also be governed by the other parameters (pH itself or temperature of hydrolysis), as shown for hydrolysis of inulin with phosphoric or citric acids at pHs from 1.75 to 3.75 in the range of 5O0C to 95oC (as better explained in Figure 5). In Figure 4, (f) and (g) denotes for free fructose and glucose, respectively. GP refers to the Degree of Polymerization. It is remarkable that phosphoric or citric hydrolyses of inulin may be effectively addressed <n="27"/>to the preferential preparation of FOS - Fructooligosaccharides since when addressed to a higher fructose content (lane 45), some amount of the co-product HMF - hydroxymethylfurfural turns clearly visible in the front zone of the chromatogram. Its companion spot most probably is a DFA (difructose anhydride).; Figure 5 is a bar graphic comparing the effect of the kinetic parameters such as temperature and time of hydrolysis once fixed the hidrogenionic potential at pH = 2.5 and their respective capacities for the modulation on the qualitative nature of the products from the hydrolyses of dahlia inulin with phosphoric or citric acids when the substrate is used at a concentration of 5g%. According to the intended innovation in this patent request - the preferential production of FOS or FrutoOligoSaccharides - is obviously that, for each range of temperature, namely, 750C, 850C ou 950C, either in the phosphoric or in the citric hydrolyses, the formation of FOS is preferential in (8x2 =) 16 assays, except for those two - at 950C and during 25 minutes - where fructose shows predominance with respect to FOS. Incidentally, those two exceptional conditions - which are not the scope of this patent request - also led to the formation of some HMF - hydroxymethylfurfural - undesirable in a inulin hydrolysis, with the attenuating condition that a less expensive practice as activated charcoal is able to remove the contaminant HMF. Concerning the reaction yield reported to the initial inulin input, the diluted phosphoric acid guarantees in the times of 25 min at 850C and of 15 min at 950C percentages of hydrolyses up to 80%, being the most of the products - 76% and 63%, respectively - FOS or frutooligosaccharides and being the remaining fructose since HMF is no longer detected under these conditions of hydrolysis. The same approach is attained with citric acid although with somewhat reduced yields - 64% or 76%, but even so FOS correspond to 78% and 74% of the hydrolysis products.; Figure 6 derives from another practical example of laboratory work, namely a high performance liquid chromatography or HPLC in a column of 10 micra microparticles of silica gel derivatized with amino groups and provided by Spectraphysics. Twenty microliters of a citric hydrolyzate of inulin at 10% obtained at pH 2.5 during 5 or 15 minutes at 850C were applied to the column and elution proceeded with 70% acetonitrile at a 1 mL/min flow rate and the monitoring was carried out with DRI- differential refraction index. It is shown that in both conditions <n="28"/>- 5 and 15 minutes - inulin is converted, by citric acid, into a family of FOS - FructoOligoSaccharides with DP - Degree of Polymerization - 3 to 18 or more (considering the analytical capacity of the referred column), still emphazing that fructose, with respect to FOS concentration, contributes with a maximum of 25% and a minimum of 5%.; Figure 7, resulting from another practical laboratory work, is also - like Figure 6 - a HPLC but carried out with samples arising from phosphoric acid hydrolyses under the same conditions of those described in Figure 6. The qualitative profiles for FOS are quite similar in both figures. In 8 of 9 assays, FOS predominates. In the nineth - 25 minutes of hydrolysis at higher temperature - FOS and fructose contents are more or less equivalent. |
Yield | Reaction Conditions | Operation in experiment |
---|---|---|
With water;citric acid; at 50 - 95℃; for 0.25 - 0.75h;pH 1.75 - 3.75; | Figure 4, from a second laboratorial work, is a TLC - Thin Layer Chromatography on silicagel 60 (Merck) developed with the mixture isopropanol : ethyl acetate : water 5:1 :2 as mobile phase and with partial runs of 1/3, 2/3, and 3/3 of the front line and developed with orcinol : sulfuric acid : methanol at 1000C for 5 minutes. This figure illustrates the profile of FOS - Fructooligosaccharides when one hydrolyzes purified inulin from dahlia roots (5g%) with phosphoric acid at pH = 2.5 at 850C during 15 minutes (15), 30 minutes (30), and 45 minutes (45), indicating that the modulation of a single kinetic parameter - time of hydrolysis - already allows to govern the quantitative relation of FOS > fructose (cases 15 and 30) or the opposite (FOS < fructose; 45). A similar strategy for FOS > fructose may also be governed by the other parameters (pH itself or temperature of hydrolysis), as shown for hydrolysis of inulin with phosphoric or citric acids at pHs from 1.75 to 3.75 in the range of 5O0C to 95oC (as better explained in Figure 5). In Figure 4, (f) and (g) denotes for free fructose and glucose, respectively. GP refers to the Degree of Polymerization. It is remarkable that phosphoric or citric hydrolyses of inulin may be effectively addressed <n="27"/>to the preferential preparation of FOS - Fructooligosaccharides since when addressed to a higher fructose content (lane 45), some amount of the co-product HMF - hydroxymethylfurfural turns clearly visible in the front zone of the chromatogram. Its companion spot most probably is a DFA (difructose anhydride).; Figure 5 is a bar graphic comparing the effect of the kinetic parameters such as temperature and time of hydrolysis once fixed the hidrogenionic potential at pH = 2.5 and their respective capacities for the modulation on the qualitative nature of the products from the hydrolyses of dahlia inulin with phosphoric or citric acids when the substrate is used at a concentration of 5g%. According to the intended innovation in this patent request - the preferential production of FOS or FrutoOligoSaccharides - is obviously that, for each range of temperature, namely, 750C, 850C ou 950C, either in the phosphoric or in the citric hydrolyses, the formation of FOS is preferential in (8x2 =) 16 assays, except for those two - at 950C and during 25 minutes - where fructose shows predominance with respect to FOS. Incidentally, those two exceptional conditions - which are not the scope of this patent request - also led to the formation of some HMF - hydroxymethylfurfural - undesirable in a inulin hydrolysis, with the attenuating condition that a less expensive practice as activated charcoal is able to remove the contaminant HMF. Concerning the reaction yield reported to the initial inulin input, the diluted phosphoric acid guarantees in the times of 25 min at 850C and of 15 min at 950C percentages of hydrolyses up to 80%, being the most of the products - 76% and 63%, respectively - FOS or frutooligosaccharides and being the remaining fructose since HMF is no longer detected under these conditions of hydrolysis. The same approach is attained with citric acid although with somewhat reduced yields - 64% or 76%, but even so FOS correspond to 78% and 74% of the hydrolysis products.; Figure 6 derives from another practical example of laboratory work, namely a high performance liquid chromatography or HPLC in a column of 10 micra microparticles of silica gel derivatized with amino groups and provided by Spectraphysics. Twenty microliters of a citric hydrolyzate of inulin at 10% obtained at pH 2.5 during 5 or 15 minutes at 850C were applied to the column and elution proceeded with 70% acetonitrile at a 1 mL/min flow rate and the monitoring was carried out with DRI- differential refraction index. It is shown that in both conditions <n="28"/>- 5 and 15 minutes - inulin is converted, by citric acid, into a family of FOS - FructoOligoSaccharides with DP - Degree of Polymerization - 3 to 18 or more (considering the analytical capacity of the referred column), still emphazing that fructose, with respect to FOS concentration, contributes with a maximum of 25% and a minimum of 5%. |
Yield | Reaction Conditions | Operation in experiment |
---|---|---|
8%; 90% | With oxygen; at 80℃; under 1500.15 Torr; for 4h;Autoclave; | General procedure: To a 20 mL autoclave were added 0.03 g of 5-hydroxymethylfurfural and 3 g of methanol (1 wt%),Then add 0.04g Co7K3-N-C, Co7Fe3-N-C, Co7Mri3-N-C,Co7Cu3-N-C, Co7Bi3-N-C, Co7Cs3-N-C, Co7Sr3-N-C,Co7Mg3-N-C, Co7Ca3-N-C, Co7Ni3-N-C,Co7Ce3-N-C (where the metal loading is 2.4% by weight and the molar ratio of the two metals is 7: 3) as a catalyst, the reactor is sealed, 2 bar of oxygen is passed through, and vigorous stirring (500 rpm),Heat to 80 C and hold for 4 hours. After finishing the reaction, cool to room temperature and take a sample.GC-MS (Shimadzu) and GC (Agilent) were used for qualitative and quantitative detection. The test results are listed in Table 1 with serial numbers 1-11. |
Yield | Reaction Conditions | Operation in experiment |
---|---|---|
96% | With oxygen; at 80℃; under 1500.15 Torr; for 4h;Autoclave; | General procedure: To a 20 mL autoclave were added 0.03 g of 5-hydroxymethylfurfural and 3 g of methanol (1 wt%),Then add 0.04g Co7K3-N-C, Co7Fe3-N-C, Co7Mri3-N-C,Co7Cu3-N-C, Co7Bi3-N-C, Co7Cs3-N-C, Co7Sr3-N-C,Co7Mg3-N-C, Co7Ca3-N-C, Co7Ni3-N-C,Co7Ce3-N-C (where the metal loading is 2.4% by weight and the molar ratio of the two metals is 7: 3) as a catalyst, the reactor is sealed, 2 bar of oxygen is passed through, and vigorous stirring (500 rpm),Heat to 80 C and hold for 4 hours. After finishing the reaction, cool to room temperature and take a sample.GC-MS (Shimadzu) and GC (Agilent) were used for qualitative and quantitative detection. The test results are listed in Table 1 with serial numbers 1-11. |
95% | With oxygen; sodium carbonate; at 100℃; under 15001.5 Torr; for 12h; | 0.05 g of 5-hydroxymethylfurfural, 0.1 g of ZIF-67C (800), 5 mL of methanol and 0.015 g of anhydrous sodium carbonate were added to a stainless steel closed reactor. Filled with 2 Mpa O2 and heated to 100 C at 600 rpm for 12 h. After the reaction was completed, it was cooled to room temperature. The catalyst is separated by a magnetic rotor, The reaction solution was tested. After gas chromatography analysis, The molar yield of dimethyl 2,5-furandicarboxylate was calculated to be 95%. |
71% | A mixture of HMF (0.6 mmol) and 1,2-diethoxyethylane (3.6 mmol) was added to a 25 mL reaction tube with an O2 balloon at room temperature. Then the contents were stirred at 115 C for 24 hours. The contents were cooled to room temperature, methanol (0.8 mmol) and CH2Cl2 (5 ml) was added under N2 atmosphere, DCC (0.9 mmol), DMAP (0.3 mmol) was slowly added and stirred for 8 hours at room temperature. The reaction was quenched by adding water and extracted with EtOAc. The organic layer was washed with water and brine, dried over MgSO4, filtered and evaporated under reduced pressure to afford the crude product which was further purified by silica gel column chromatography with petroleum ether/ethyl acetate as eluent. The overall yield was 71 %. |
With oxygen; at 130℃; under 750.075 Torr; for 3h;Autoclave;Catalytic behavior; | General procedure: Furfural or HMF oxidative esterifications with oxygen or air were investigated without NaCH3O addition, using a mechanical stirred autoclave fitted with an external jacket [14]. Catalyst (100 mg), substrate (300 mul furfural or 200 mg HMF, Sigma-Aldrich 99%) and n-octane (150 mul), used as internal standard, were added to the solvent (150 ml of methanol or ethanol). The reactor was charged with the oxidant (0.5-6 bar of relative pressure), stirred at 1000 rpm and heated at a proper temperature in the range 60-140 oC. The progress of the reaction was determined typically after 90 min (if not specified otherwise) by gas chromatographic analysis of the converted mixture (capillary column HP-5, FID detector). Preliminary experiments showed that the system works in a strictly kinetic regime [14]. | |
6%Chromat. | With oxygen; sodium carbonate; at 120℃; under 3800.26 Torr; for 15h; | The reaction was carried out under the conditions described in Example 1, except that HMF (manufactured by Sigma-Aldrich) was used instead of PD-HMF. After the reaction, the pressure vessel was rapidly cooled to room temperature, and then the substrate and the product were qualitatively and quantitatively determined by 1 H NMR.The yield of the objective product, furandicarboxylic acid methyl ester was as low as 6%, and a large amount of solid by-products were produced in the reaction solution after completion of the reaction. |
95.6%Chromat. | With manganese(IV) oxide; oxygen; at 100℃; under 4500.45 Torr; for 12h;Autoclave; | CoOx-N/C-phen (Co 3.0 wt%) catalyst, 40 mg MnO20.5mmol 5-hydroxymethylfurfural and 10Million liters of methanol is added to the stainless steel autoclave,PTFE inner liner, of which Co: 5-hydroxymethylfurfural:=0.13:1 (mol: mol). The temperature was raised to 100 C by an automatic temperature controller, and 0.6 MPa of oxygen was added.Reaction for 12 hours,Keep the pressure constant during the reaction. The reaction product was analyzed using GC |
With oxygen; at 110℃; under 22502.3 Torr; for 2h;Sealed tube; Inert atmosphere; | General procedure: 5ml 5-hydroxymethylfurfural and methanol in the reactor is thoroughly mixed, 2g of gold-based catalyst is added to the reaction mixture; the reactor is sealed, stirring is started, pure oxygen and inert gas are introduced into the bottom of the reactor, and reacted for 2 hours;The molar ratio of methanol to 5-hydroxymethylfurfural in the reaction mixture is 15:1,The reaction temperature is controlled at 110 C, and the reaction pressure is controlled at 3 MPa.The product in the reaction system is subjected to gas chromatography analysis.Conversion of 5-hydroxymethylfurfural conversion C (HMF) and furan-2,5-dicarboxylic acid dimethyl selectivity S (FDMC) was carried out, and the results are shown in Table 1.As can be seen from the results in the table, the catalyst having Au as the active center exhibits excellent catalytic activity.The conversion rate and selectivity are higher than that of the non-gold-based catalyst, and the activity of the gold-based catalyst is greatly improved after the addition of the lanthanide metal. |
Yield | Reaction Conditions | Operation in experiment |
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19%; 10%; 35%; 20%; 8% | With dihydrogen peroxide;methyltrioxorhenium(VII); In dichloromethane; water; acetonitrile; at 20℃; | Comparative examples 1 to 3: Oxidation of 5-hydroxymethyl furfural in homogeneous conditions; 5-hydroxymethyl furfural (HMF) was oxidized with 10 equivalents of hydrogen peroxide (35percent by weight in aqueous solution) in the presence of methyltrioxo rhenium in an amount of 5percent by weight of HMF, at a temperature about 200C during 24 to 48 hours, until the conversion of furfural was complete, in various solvents. The results of the reactions are summarized in Table 1 below. |
Yield | Reaction Conditions | Operation in experiment |
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23%; 6%; 11%; 16%; 29% | With dihydrogen peroxide;methyltrioxorhenium(VII); In ethanol; water; at 20℃; | Comparative examples 1 to 3: Oxidation of 5-hydroxymethyl furfural in homogeneous conditions; 5-hydroxymethyl furfural (HMF) was oxidized with 10 equivalents of hydrogen peroxide (35percent by weight in aqueous solution) in the presence of methyltrioxo rhenium in an amount of 5percent by weight of HMF, at a temperature about 200C during 24 to 48 hours, until the conversion of furfural was complete, in various solvents. The results of the reactions are summarized in Table 1 below. |
Yield | Reaction Conditions | Operation in experiment |
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62% | With PEDOT(1+)*OTf(1-); In n-heptane; for 20h;Inert atmosphere; Reflux; | The reaction of d-<strong>[87-79-6]sorbose</strong> (18, 180 mg, 1 mmol) and 2 (570.0 mg, 0.5 mmol) under identical conditions gave 78.1 mg (0.6 mmol, 62%) of 17.refPreviewPlaceHolder25 |
53.3% | With sodium bromide; In tetrahydrofuran; water; at 130℃; for 0.333333h; | The reaction vessels were loaded with 0.25 g sugar, 0.25 g Amberlyst 70, and 1 wt% NaBr, in 90% THE in water. The samples were heated up to 130C for 20minutes as described in the General Methods. After the samples were cooled to room temperature, the reaction mixtures were analyzed using HPLC as described in the General Methods. As shown in Table 12, it can be seen that different sources of C6 sugars provide a higher HME yield in the presence of NaBr in aqueous THE. |
Yield | Reaction Conditions | Operation in experiment |
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7%; 90% | With bis-acetylacetonyl vanadium (II); In aq. phosphate buffer; at 37 - 80℃; for 16.0833h;pH 7; | HMF (100 mM) was added to KPi buffer (500 mM pH 7.0). GOase M35 (103p1 of3.3mg/mL), PaoABC (ipI of 28.9mg/mL) and a metal complex (see Table 4) were added at 37 00 and the pH was continuously adjusted with NaHCO3 for a period of 16 hours. The reaction was heated to 80 00 for 5 minutes and left to cool. The solution containing denatured protein was centrifuged and the supernatant removed and analysed by RP20 HPLC. |
With sodium carbonate; at 100℃; under 30003 Torr; for 0.1h;pH 10.12; | Experimental Conditions The HMF having 95% purity was supplied by Interchim. The method of the invention was implemented in a discontinuous reactor under pressure in a 300 mL autoclave equipped with magnetically driven gas-inducing agitator. Heating was ensured by a heating collar connected to a PID controller (proportional integral derivative). A sampling gate allowed the taking of a sample from the reaction medium via an immersed tube, allowing the monitoring of the progress of the reaction over time. The samples were analysed by HPLC chromatography with two RID detectors (Refractive Index Detector) and PDA (Photodiode array) (ICE-Coragel 107H column, eluting with 10 mM H2SO4). Total Organic Carbon (TOC) in solution was also analysed using a TOC analyser and the value measured was compared with the mass balance (MB) calculated by HPLC. The reactor was charged with 150 mL of 100 mM aqueous HMF solution (2 g), a weight of catalyst corresponding to a HMF/Pt molar ratio of 100, and the desired amount of base in the form of NaOH (comparative example), NaHCO3, KHCO3, Na2CO3 or K2CO3 expressed as base/HMF molar ratio. Air was added at a pressure of 40 bar and the reactor heated to 100 C. The influence of the Bi/Pt ratio was also examined in the presence of Na2CO3 (Na2CO3/HMF=2). The same trend was observed when comparing a series of bimetallic catalysts having molar ratios varying between 0.07 and 1. The results are grouped together in Tables 11 to 15. |
Yield | Reaction Conditions | Operation in experiment |
---|---|---|
86%; 6.6%; 7.3% | With bis-acetylacetonyl vanadium (II); In aq. phosphate buffer; at 37 - 80℃; for 16.0833h;pH 7; | HMF (100 mM) was added to KPi buffer (500 mM pH 7.0). GOase M35 (103p1 of3.3mg/mL), PaoABC (ipI of 28.9mg/mL) and a metal complex (see Table 4) were added at 37 00 and the pH was continuously adjusted with NaHCO3 for a period of 16 hours. The reaction was heated to 80 00 for 5 minutes and left to cool. The solution containing denatured protein was centrifuged and the supernatant removed and analysed by RP20 HPLC. |
With platinum on carbon; water-d2; oxygen; at 100℃; under 75007.5 Torr; for 4h;Autoclave; | l-b Catalyst screening experiments: Catalyst screening was carried out in a series of single experiments designated "Screen 1 " to "Screen 7". In each single experiment "Screen 1 " to "Screen 7" the organic reactant compound HMF (compound of Formula (II)) was in parts catalytically converted by means of at least one heterogeneous platinum catalyst (see Tables 1 and 2, below) into FDCA (compound of formula (I)). The general experimental procedure for each screening experiment of "Screen 1 " to "Screen 7" was as follows: In a first step, an aqueous reactant mixture was prepared by filling a specific amount of deuterated water (D20, 99,9 atom%, Sigma Aldrich (151882)) and a specific amount of HMF (99+%, Sigma Aldrich (W501808)) into a steel autoclave reactor (inner volume 60 ml or 90 ml, respectively, for exact information see Table 2, below). In case a steel autoclave reactor with an inner volume of 60 ml was used the amounts of HMF and D20 were as follows: D20: 18,0 g, HMF: 2,0 g (corresponding to 15,9 mmol as starting amount of HMF). In case a steel autoclave reactor with an inner volume of 90 ml was used the amounts of HMF and D20 were as follows: D20: 27,0 g, HMF: 3,0 g (corresponding to 23,8 mmol as starting amount of HMF). The starting concentration C0[HMF] of HMF in each aqueous reactant mixture was 10 % by weight, based on the total mass of the aqueous reactant mixture (total mass of deuterated water and HMF). The respective amount of solid heterogeneous catalyst as stated in Table 2 was added to the respective aqueous reactant mixture and, thus, a reaction mixture comprising deuterated water, HMF, and the heterogeneous catalyst was obtained. After adding the specific amount of heterogeneous catalyst the obtained reaction mixture appeared as a deep black slurry, the black color apparently caused by the black solid particles of the heterogeneous catalyst. The molar ratio of substrate to metal of the heterogeneous catalyst (HMF : Pt) was approximately 100 : 1. In a second step, the filled reactor was tightly sealed and pressurized with synthetic air (total pressure 100 bar, Oxygen (as part of the synthetic air) : HMF ratio is approximately 2,25 : 1 ) to obtain conditions for catalytic conversion. The present reaction mixture was heated to a temperature of 100C while stirring at 2000 rpm. After reaching 100C this temperature was maintained for 4 or 20 hours, respectively, (see Table 2 "Reaction time" for exact information) while continuing stirring the heated and pressurized reaction mixture during the reaction time. As a result, a first product suspension comprising FDCA in solid form and the heterogeneous catalyst in solid form was formed. | |
With sodium carbonate; at 100℃; under 30003 Torr; for 0.33h;pH 9.10; | Experimental Conditions The HMF having 95% purity was supplied by Interchim. The method of the invention was implemented in a discontinuous reactor under pressure in a 300 mL autoclave equipped with magnetically driven gas-inducing agitator. Heating was ensured by a heating collar connected to a PID controller (proportional integral derivative). A sampling gate allowed the taking of a sample from the reaction medium via an immersed tube, allowing the monitoring of the progress of the reaction over time. The samples were analysed by HPLC chromatography with two RID detectors (Refractive Index Detector) and PDA (Photodiode array) (ICE-Coragel 107H column, eluting with 10 mM H2SO4). Total Organic Carbon (TOC) in solution was also analysed using a TOC analyser and the value measured was compared with the mass balance (MB) calculated by HPLC. The reactor was charged with 150 mL of 100 mM aqueous HMF solution (2 g), a weight of catalyst corresponding to a HMF/Pt molar ratio of 100, and the desired amount of base in the form of NaOH (comparative example), NaHCO3, KHCO3, Na2CO3 or K2CO3 expressed as base/HMF molar ratio. Air was added at a pressure of 40 bar and the reactor heated to 100 C. The influence of the Bi/Pt ratio was also examined in the presence of Na2CO3 (Na2CO3/HMF=2). The same trend was observed when comparing a series of bimetallic catalysts having molar ratios varying between 0.07 and 1. The results are grouped together in Tables 11 to 15. |
With nicotinamide adenine dinucleotide phosphate; In aq. phosphate buffer; at 37℃; for 2h;pH 7;Enzymatic reaction; | Reaction Conditions: HMF (10mM), KRED (089) (7.5mg), 0.SmL KPi Buffer (pH x), and NOX-1 and NADP as defined in Table 7B were reacted at 37C for 2 hours. A sample was quenched with 1 M HCI, centrifuged and analysed by RP-HPLC. The results from thereaction can be seen in Table 7B.Using lOmol% of NADP (relative to the amount of HMF used) and 5mg NOX-1 provided the highest conversion of HMF to 2,5-FDCA. Reducing the amount of NADP and NOX-1 lead to a lower conversion of HMF to HMFCA. | |
With nicotinamide adenine dinucleotide phosphate; In aq. phosphate buffer; at 37℃; for 2h;pH 7;Enzymatic reaction; | Reaction Conditions: HMF (10mM), KRED (089) (7.5mg), 0.SmL KPi Buffer (pH x), and NOX-1 and NADP as defined in Table 7B were reacted at 37C for 2 hours. A sample was quenched with 1 M HCI, centrifuged and analysed by RP-HPLC. The results from thereaction can be seen in Table 7B.Using lOmol% of NADP (relative to the amount of HMF used) and 5mg NOX-1 provided the highest conversion of HMF to 2,5-FDCA. Reducing the amount of NADP and NOX-1 lead to a lower conversion of HMF to HMFCA. | |
With nicotinamide adenine dinucleotide phosphate; In aq. phosphate buffer; at 37℃; for 2h;pH 7;Enzymatic reaction; | Reaction Conditions: HMF (10mM), KRED (089) (7.5mg), 0.SmL KPi Buffer (pH x), and NOX-1 and NADP as defined in Table 7B were reacted at 37C for 2 hours. A sample was quenched with 1 M HCI, centrifuged and analysed by RP-HPLC. The results from thereaction can be seen in Table 7B.Using lOmol% of NADP (relative to the amount of HMF used) and 5mg NOX-1 provided the highest conversion of HMF to 2,5-FDCA. Reducing the amount of NADP and NOX-1 lead to a lower conversion of HMF to HMFCA. | |
7.67%Chromat.; 18.1%Chromat.; 73.67%Chromat. | With platinum on activated charcoal; sodium hydroxide; In 1-methyl-pyrrolidin-2-one; water; at 80℃; under 16501.7 Torr; for 0.5h;Flow reactor; | 1.) NMP/NaOH/Pt-C/air/22bar/90Ci) Oxidation 1 - inNMP, Pt-c, 17 bar and 80C, NaOHThe starting solution A is prepared by dissolving 5-Hydroxymethylfurfural (99%) in 95gNMP (99,5%, Sigma Aldrich) and 5g deionized water. The starting solution B is a 15%NaOH solution, prepared from 150.41 g NaOH and 850.1 8g deionized water.In a continuous flow plant, solution A and solution B are contacted in a 1/16? t-piece. The flow rate for solution A is 0.08 ml/min, and for solution B 0.06 ml/min. The mixture obtained is directly contacted with 125 ml/min air flow, before the mixture enters the actual reactor. In this case the reactor was a trickle bed reactor using platinum on activated carbon as catalyst. The double jacketed reactor is heated to 80C and provides a residence time of 30 minutes for the given flow rates. The whole system is pressurized to 22 bar with a pressure maintaining valve.The reaction mixture obtained in this step contains no HMF. The oxidation product mixture contains, according to HPLC analysis, FDCA: 73.67%, HMFCA: 18.10%, FFCA: 7.67%, DFF: 0.41% and 0.15% unknown oxidation products. Additionally, a small amount of dark, solid material is yielded using this procedure, leading to a reduced lifetime cycle of the catalyst fixed bed.ii.) Extraction with ethyl acetateThe reaction mixture (20.4m1) collected from the first oxidation step was extracted six times using 20 ml ethyl acetate per cycle to remove NMP. The HPLC chromatogram showed noloss of the acids in the aqueous phase after this procedure. The DFF was transferred completely to the organic phase. |
Yield | Reaction Conditions | Operation in experiment |
---|---|---|
89%; 5% | With sodium hydroxide; In water; at 30℃; under 7500.75 Torr; for 4h; | The Au / Mg (OH)2(1 wt%) catalyst, 2 mmol of 5-hydroxymethylfurfural, NaOH and 10 mL of water were charged into a stainless steel autoclave equipped with a polytetrafluoroethylene liner containing 5-hydroxymethylfurfural: NaOH = 0.01: 1 : 4 (mol: mol: mol).Using automatic temperature control program temperature to the reaction temperature of 30 C, adding 1MPa oxygen, reaction for 4 hours, the reaction process to maintain the same pressure.The reaction product was analyzed by HPLC. |
76%; 12% | With oxygen; potassium hydroxide; In water; at 60℃; under 2250.23 Torr; for 6h;Autoclave; Green chemistry; | Take 0.317 grams of HMF, 2.8 grams of Kappa0Eta (20%), 3 ml of water into the reactor, the reaction vessel containing 10 ml of poly Tetrafluoroethylene-lined high-pressure reactor, take 0.30 g Au / HY (Au2wt%) as a catalyst, the program heated to 60 C, filling 0.3MPa oxygen, the reaction 6 hours, the reaction process continue to add oxygen to ensure that the reaction at constant temperature and constant pressure. reaction product After centrifugation, go to the supernatant and analyze with HPLC. The HMF conversion was 100%, the yield of HMFA was 76% FDA yield of 12%, the reaction results in Table 1. |
26%; 73% | With vanadium(V) oxide; In aq. phosphate buffer; at 37 - 80℃; for 16.0833h;pH 7; | HMF (100 mM) was added to KPi buffer (500 mM pH 7.0). GOase M35 (103p1 of3.3mg/mL), PaoABC (ipI of 28.9mg/mL) and a metal complex (see Table 4) were added at 37 00 and the pH was continuously adjusted with NaHCO3 for a period of 16 hours. The reaction was heated to 80 00 for 5 minutes and left to cool. The solution containing denatured protein was centrifuged and the supernatant removed and analysed by RP20 HPLC. |
60%; 33% | With bis-acetylacetonyl vanadium (II); In aq. phosphate buffer; at 37 - 80℃; for 16.0833h;pH 7; | HMF (100 mM) was added to KPi buffer (500 mM pH 7.0). GOase M35 (103p1 of3.3mg/mL), PaoABC (ipI of 28.9mg/mL) and a metal complex (see Table 4) were added at 37 00 and the pH was continuously adjusted with NaHCO3 for a period of 16 hours. The reaction was heated to 80 00 for 5 minutes and left to cool. The solution containing denatured protein was centrifuged and the supernatant removed and analysed by RP20 HPLC. |
59.4%; 40.6% | With oxygen; sodium hydroxide; In water; at 24.84℃; for 6h; | The HMF oxidation reaction was carried out in a three-neck flask with an attached glass reflux condenser under oxygen flow (Figure 2). In each experiment, the reactor was filled with 1.0mmol of HMF and 5.0mmol of NaOH in 10mL of water. Then, 0.1 g of M/RGO (M = Pd, Rh, Ru, or Pt) was added to the reactor, and oxygen was introduced at a flow rate of 50mL min-1 with stirring under atmosphere pressure. After reaction, the catalyst was filtered off before the high-performance liquid chromatography (HPLC) measurement (AnimexHPX-87H column from Bio-Rad Laboratories Co., Ltd., 0.5mL min-1 flow rate, 10nM H2SO4 solvent, 323 K). The products were analyzed using a refractive index (RI) detector. |
39%; 45% | With oxygen; sodium hydroxide; In water; at 60℃; under 2250.23 Torr; for 6h;Autoclave; Green chemistry; | Take 0.317 grams of HMF, 2 grams of NaOH (20%), 3 ml of water into the reactor, the reaction vessel was equipped with a 10 ml polytetrafluoroethylene lined high pressure reactor, 0.30 g Au / H x Na 1-x Y (Au 2 wt%) as a catalyst, after the program is warmed to 60 C, filled with 0.3MPa oxygen, reaction for 6 hours, during the reaction, oxygen is continuously added, ensure that the reaction is carried out at constant temperature and pressure. The reaction product was centrifuged to the supernatant, analytical using HPLC. after testing, HMF conversion rate of raw materials is 100% HMFA yield of 39%, FDA yield of 45%, the reaction results in Table 1. |
With oxygen; sodium hydroxide; In water; at 60℃; under 7500.75 Torr; for 4h;Autoclave; | The oxidation of 5-hydroxymethyl-2-furfural (HMF) was carriedout using an autoclave (Parr Instruments) reactor of 300 mLcapacity and equipped with a mechanical stirrer (0-1200 rpm) andprovision for measurement of temperature and pressure. The reactorwas charged with an aqueous solution (25 mL distilled water)containing the appropriate amount of 5-hydroxymethyl-2-furfural,base (NaOH) and catalyst (HMF/metal molar ratio = 100). The autoclavewas purged 3 times with O2 (5 bar) and then pressurized at10 bar. If not differently indicated, the temperature was increasedto 60 C and the reaction mixture was stirred at ca. 1000 rpm for4 h. At the end of the reaction, the reactor was cooled to room temperatureand the solution was filtered. Then, 4 mL of water wasadded to an aliquot of the reaction solution (1 mL) before analysiswith an Agilent Infinity 1200 liquid chromatograph equippedwith a Aminex HPX 87-H 300 mm×7.8 mm column using a0.005 M H2SO4 solution as the mobile phase. Identification of compoundswas achieved by calibration using reference commercialsamples. | |
86.39%Chromat.; 9.2%Chromat. | With disodium hydrogenphosphate; copper oxides/alumina; at 90℃; under 13501.4 Torr; for 0.166667h; | i) Oxidation 1 - inNMP, Pt-C, 17 bar and 80C, Na2HPO4The process was carried out in a comparable, scaled up continouos lab-plant setup as used inthe examples above. Starting solution A was prepared by mixing 65.6g HMF and 400.OgNMP; solution B was a 15% solution of sodium phosphate, prepared by mixing 150.OgNa2HPO4 and 850.Og of deionized water.The flow rates used in this trial were 2.86m1/min solution A, 2.14m1/min solution B and 250.Onml/min for air. Further processing parameters were 10 minutes residence time at 90C and 18 bar. The catalyst used was copper oxide on aluminium oxide.The oxidation product mixture obtained from this trial contains, according to HPLC analysis, FDCA: 9.20%, HMFCA: 86.39%, FFCA: 0.13%, DFF: 0.36% and 2.82% of HMF. About 1% are unidentified side products.ii.) Extraction with ethyl acetateNMP extraction was carried out with ethylacetate. 50m1 reaction mixture was extracted six times with 40m1 ethyl acetate in each cycle.FDCA, HMFCA and FFCA remained completely in the water phase. Also a small amount of HMF was found in the water phase (0.5% according to HPLC). DFF completely went into the organic phase and was discarded. |
21%Chromat.; 74%Chromat. | With oxygen; sodium hydrogencarbonate; In water; under 7500.75 Torr;Autoclave; Heating; | HMF (0.2 mmol), NaHCO3 (0.4 mmol), and the catalyst (25 mg) were added to a 12 mL stainless steel autoclave containing 8 mL of deionized water. The autoclave was heated to 80 C and pressurized with O2 (10 bar) under vigorous stirring (900 rpm). During the reaction, 0.1 mL sample was taken at regular intervals of about 0.5-1 hours, filtered with 0.2 mum PTFE filters, diluted with water and analyzed using a high-performance liquid chromatograph (Shimadzu LC-20AD equipped a Bio-Rad Aminex HPX-87H column). Sulfuric acid (5 mM) at 333 Kwith a flow rate of 0.55 mL min-1 was used as an eluent. Each catalyst was tested at least twice to verify the reproducibility. The reproducibility of conversion levels and yields were within 5%. |
Yield | Reaction Conditions | Operation in experiment |
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With sodium hydroxide; 1-ethyl-3-methylimidazolium bis(trifluoromethylsulfonyl)imide; at 0 - 20℃; | With reference to Scheme 1 below, 1 ml of 1-ethyl-3-methylimidazolium bis(trifluoromethanesulfonyl)imide ([EMIm]TFSI, available from Merck) newly serving as an ionic liquid was placed in a round-bottom flask, 0.126 g (1 mmol) of 5-hydroxymethylfurfural (HMF, Compound I) was dissolved, the reaction temperature was adjusted to 0° C., and then sodium hydroxide powder (0.200 g, 5 mmol) was added thereto. Subsequently, the reaction temperature was increased to room temperature so that the reaction took place. After completion of the reaction, 20 ml of dichloromethane was added, after which the filtrate obtained via filtration, namely, the dichloromethane layer was distilled under reduced pressure, thus recovering the ionic liquid. [0057] The lump of filtered particles resulting from recovering the ionic liquid was dissolved in 2 ml of water, and then neutralized with 1 N HCl, so that the pH of the solution was adjusted to about 78. Extraction using ethyl acetate (3×50 ml) and then concentration under reduced pressure were conducted, yielding 2,5-dihydroxymethylfuran (DHMF, Compound II) as a white solid. [0058] The pH of the remaining water layer was adjusted to about 3, followed by performing extraction using ethyl acetate and then concentration under reduced pressure, yielding 5-hydroxymethylfuranoic acid (HMFA, Compound III) as a light yellow solid. The yields of the products are shown in Table 1 below. [0059] The melting point of the light yellow crystals was 239.5° C., and the light yellow crystals were analyzed to be a target compound using 1H-NMR, 13C-NMR. The analytic data was as follows. [0060] HMFA: 1H NMR (300 MHz, acetone-d6): delta 7.16 (d, J=3.4, 1H), 6.47 (d, J=3.4, 1H), 4.59 (s, 2H) ; 13C NMR (75 MHz, acetone-d6): delta 160.9, 159.5, 144.9, 119.6, 109.6, 57.3. [0061] DHMF: 1H NMR (300 MHz, acetone-d6): delta 6.18 (s, 2H), 4.48 (d, J=5.8, 4H), 4.18 (t, J=5.8, 2H) ; 13C NMR (75 MHz, acetone-d6): delta 155.8, 108.22, 57.2. | |
With 1-butyl-3-methylimidazolium Tetrafluoroborate; sodium hydroxide; at 0 - 20℃; | DHMF and HMFA were prepared in the same manner as in Example 1, with the exception that 1-butyl-3-methylimidazolium tetrafluoroborate ([BMIm]BF4, available from C-TRI) was used as the ionic liquid instead of 1-ethyl-3-methylimidazolium bis(trifluoromethanesulfonyl)imide ([EMIm]TFSI). [0075] The melting point of the light yellow crystals was 239.5° C., and the light yellow crystals were analyzed to be the target compound using 1H-NMR, 13C-NMR. The analytic data was as follows. [0076] HMFA: 1H NMR (300 MHz, acetone-d6): delta 7.16 (d, J=3.4, 1H), 6.47 (d, J=3.4, 1H), 4.59 (s, 2H) ; 13C NMR (75 MHz, acetone-d6): delta 160.9, 159.5, 144.9, 119.6, 109.6, 57.3. [0077] DHMF: 1H NMR (300 MHz, acetone-d6): delta 6.18 (s, 2H), 4.48 (d, J=5.8, 4H), 4.18 (t, J=5.8, 2H) ; 13C NMR (75 MHz, acetone-d6): delta 155.8, 108.22, 57.2. |
Yield | Reaction Conditions | Operation in experiment |
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With oxygen; In water; at 90℃; under 6000.6 Torr; for 24h;Autoclave;Catalytic behavior; | General procedure: As a general procedure, the oxidation of HMF was performed under a vigorous stirring in a stainless steel autoclave in the presence of molecular O2 (8 bars), 1 mmole of substrate (HMF), 10 mLsolvent, 0.05 g of catalyst and a temperature of 90C for 24 h. All the changes of reaction parameters: temperature, pressure, solvent, amount of the catalysts or reaction time were notified inthe text. After ending the HMF oxidation and filtering off the catalyst, the mother liquor was diluted 5 times and the products were analyzed by high performance liquid chromatography (HPLC), ona Thermo Scientific Accela 600 device equipped with a UV-vis detector and a Rezex-ROA H+column. 5-Hydroxymethyl furfural(HMF), diformyl furan (DFF), 5-hydroxymethyl-2-furancarboxylicacid (HMFCA), 5-formyl-2-furancarboxylic acid (FFCA) and 2,5-furandicarboxylic acid (FDCA) from Sigma-Aldrich were used as standards. The maximum of absorption for FDCA and HMFCA corresponded to = 260 nm while for HMF, FFCA and DFF to = 285 nm. The mobile phase consisted of 0.05 N H2SO4, at a flow rate of 0.5 mL/min, and the analysis was carried out at 40C, using a two channels detection (260 nm and 285 nm) and an injection volume of 3 L. A carbon mass balance of 98-99% was obtained for all the performed reactions. |
Yield | Reaction Conditions | Operation in experiment |
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In dimethylsulfoxide-d6; at 22℃; for 24h;Sealed tube; | The catalyst in this carbene catalysis is l-ethyl-3-methylimidazolin-2-ylidene carbene I (Figure 3), present in the [EMIMJOAc equilibrium that favors the ion pair form. The early steps of the proposed elementary reactions involved in the catalysis deviate somewhat from those put forth for the NHC-catalyzed umpolung of aldehydes and a, ?-unsaturated esters, due to the important role of HO Ac, which co-exists with carbene I in the [EMIMJOAc equilibrium. Specifically, nucleophilic addition of the carbene I to the carbonyl group of HMF generates a zwitterionic tetrahedral intermediate, which is protonated by HO Ac to afford a 2-(5-hydroxymethyl-2-a-hydroxyfuranyl) imidazolium acetate salt, the resting intermediate II.; Third, we obtained direct evidence for the formation of the resting intermediate II through NMR monitoring of the HMF reaction with [EMIMJOAc (1: 1 molar ratio) in DMSO-i4 at RT (-22 C) and 80 C with hexamethylbenzene as the internal standard. At RT, 17% HMF was consumed immediately upon mixing HMF with [EMIMJOAc, which approximately corresponds to the amount of the NHC catalyst accessible in [EMIMJOAc at this temperature for its reaction with HMF to form intermediate II. This intermediate is not converted into DHMF at RT, even after 24 h. With this valuable information, next we carried out the same reaction at RT but with a 1 :5 molar ratio of HMF: [EMIM]OAc to form the intermediate exclusively (i.e., devoid of HMF and DHMF), plus excess [EMIMJOAc; the reaction in this ratio at RT enabled conclusive spectroscopic characterization of intermediate II (Figures 4 and 5). Identification of Intermediate II from the Reaction of HMF with [EMIM]OAc. The 1:1 reaction of HMF with [EMIMJOAc at RT was monitored by NMR (DMSO-rf6) in a J. Young-type NMR tube using hexamethylbenzene as the internal standard. This study showed that 17% HMF was consumed immediately upon mixing HMF with [EMIMJOAc at RT, which approximately corresponds to the amount of the NHC catalyst accessible in [EMIMJOAc at this temperature for its reaction with HMF to form intermediate II. This intermediate is not converted into DHMF at RT, even after 24 hours, and the ]H NMR remained the same from the beginning of the reaction up to 24 hours at RT. To aid analysis of the spectra of the in situ reactions, the chemical shifts of the four species involved in the reaction of HMF with [EMIMJOAc were summarized as follows. All chemical shifts were reported in DMSO-i, and the NMR solvent residual signal was referenced at 2.54 ppm (not 2.50 ppm), based on the chemical shift of the hexamethylbenzene internal standard set at 2.15 ppm. ]H NMR for HMF (known compound): delta 9.56 (s, 1H, CHO), 7.51, 6.59 (d, 2Eta, furan ring Eta), 4.54 (s, 2Eta, CH2OH). ]H NMR for [EMIM]OAc (known compound): delta 9.60 (s, 1H, NCHN), 7.84, 7.76 (d, 2Eta, imidazolium ring Eta), 4.24 (q, 2Eta, NCH2CH3), 3.89 (s, 3H, NC), 1.65 (s, 3H, OAc), 1.44 (t, 3H, NCH2G).; ]H NMR for Intermediate II (new compound, see Figures 4 and 5): delta 7.98 (d, /H-H = 2.1 Hz, imidazol ring H), 7.93 (d, /H-H = 1-8 Hz, 1H, imidazol ring proton), 6.74 (s, 1H, CHOH), 6.38 (d, /H-H = 3.3, 1H, furan ring H), 6.24 (d, /H-H = 3.0 Hz, 1H, furan ring H), 4.41 (m, 2H, NCH2CH3), 4.36 (s, 2H, CH2OH), 3.96 (s, 3H, NC), 1.64 (s, 3H, OAc), 1.31 (t, /H-H = 7.2 Hz, 3H, NCH2C). 13C NMR: delta 175 (C=0), 158 (NCN), 151, 146, 109, 108 (4 resonances for the furan ring), 125, 122 (2 resonances for the imidazol ring), 60.4 (CH-OH), 56.3 (CH2OH), 44.2 (NCH2CH3), 36.2 (NCH3), 26.5 (0=C-CT), 16.3 (NCH2CH3). |
Yield | Reaction Conditions | Operation in experiment |
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With dihydrogen peroxide; In water; at 25℃; under 760.051 Torr; for 24h;Green chemistry; | The catalytic activity performance of the metal Salen complexessupported on SBA-15 (Co/SBA-15, Fe/SBA-15 and Cu Salen/SBA-15) inthe oxidation of HMF were evaluated. The HMF oxidation reaction wascarried out in an aqueous system at neutral pH (the pH was not adjusted)using H2O2 as oxidant agent. The reaction was performed undermild conditions (aqueous media, neutral pH, atmospheric temperatureand pressure). The system consisted of a 125 mL round-bottom flaskwith a refrigerant column to avoid the HMF volatilization. All testswere performed with an initial substrate HMF 0.4 mM [8], 50 mL reactionvolume, H2O2 30 w/Vpercent (100 muL) as oxidant agent and using0.05 g of catalyst. Aliquots of 500 muL were taken during 24 h, fromwhich 75 muL were injected in the chromatograph for their analysis. Thesamples were taken in short periods of time at the early minutes of thereaction, and in a longer period as the reaction advanced in order tohave enough information for the kinetic study. The reaction mixturewas stirred at a constant 500 rpm. Tests were done at low temperatures25, 30 and 40 °C to know how the temperature affects the reaction.Although the catalyst can be used at higher moderate temperatures,40 °C level was selected as the maximum temperature to avoid H2O2degradation. Temperature levels were recorded with thermocouplespreviously connected to a temperature monitoring program using theLabview System Design Software. |
Yield | Reaction Conditions | Operation in experiment |
---|---|---|
60.26%; 5.9%; 25.45% | With 10% Pt/activated carbon; oxygen; sodium carbonate; In water; at 100℃; under 7500.75 Torr; | General procedure: Oxidation of HMF to obtain FFCA Reactant HMF (5 mg/mL) in wateEach CatCart (70x4 mm) was filled first with 20 mg Celite 545 and then 280 mg 10% Pt/C were added. Fresh CatCart was used every time, when the system pressure was changed. Before each screening series, the entire reaction line was purged with H20 (HPLC Grade), the Teflon frit of the system valve was replaced and ThalesNano X-Cube System Self-Test was performed. The initial system stabilization was always achieved using H20 (HPLC Grade) and when the reaction parameters remained constant, the pumping of the reaction solution began, then the system was allowed to stabilize and equilibrate at the new conditions for 10 min and two samples of 1 mL each were then collected. Then the temperature was increased and the system was again allowed to stabilize (the same procedure was applied for all temperatures within the experimental series). In all the cases 40 bar difference between the system pressure and the external gas pressure was provided for good system stability. At a temperature of 100C, an ideal compromise between substrate conversion and product selectivity regarding the product FFCA was achieved. r.Base additive Na2C03 (2 equiv. based on HMF, premixed with HMF solution) Catalyst 10% Pt/C (280 mg 10% Pt/C + 20 mg Celite 545) Oxidant synthetic air. Reactor System ThalesNano X-Cube, pump flow rate: 0.5mL/min, residence time: 2 min Table 6 below there is set out a summary of the results from HMF-FFCA oxidation screening in flow using the following parameters: 1 mL HMF (5 mg/mL), 2 equiv. Na2C03, H20, 10% Pt/C, 80 bar Air, 60-160C, 0.5 mL/min, 2 min. Table 6 it is evident that under the given conditions a high FFCA yield and a high FFCA selectivity may be achieved. The yield in average is increasing with increasing temperature up to approx. 120C. A temperature yielding FFCA in a range of approx. 45 to 60% related to the starting material HMF is in the range from 60C to 160C, in particular from 80 to 140C, e.g. 100 to 120C. |
Yield | Reaction Conditions | Operation in experiment |
---|---|---|
80.65%; 20.15% | With 10% Pt/activated carbon; oxygen; sodium hydroxide; In water; at 120℃; under 60006 Torr; | General procedure: Oxidation of HMF to obtain HMFCA Reactant HMF (5 mg/mL) in water .Catalyst K-OMS-2 (263.4 mg K-OMS-2 + 50 mg Celite 545) prepared according to Angew. Chem. Int. Ed. 2012, 51, 544-547. Oxidant oxygen or synthetic air, Reactor System ThalesNano X-Cube, pump flow rate: 0.5 mL/min, residence time:2/4 min (0108) Each CatCart (70x4 mm) was filled first with 50 mg Celite 545 and then 263.4 mg K-OMS-2 were added. Fresh CatCart was used every time, when the system pressure was changed. Before each screening series, the entire reaction line was purged with H2O (HPLC Grade), the Teflon frit of the system valve was replaced and ThalesNano X-Cube System Self-Test was performed. The initial system stabilization was always achieved using H2O (HPLC Grade) and when the reaction parameters remained constant, the pumping of the reaction solution began, then the system was allowed to stabilize and equilibrate at the new conditions for 10 min and two samples of 1 mL each were then collected. Then the temperature was increased and the system was again allowed to stabilize (the same procedure was applied for all temperatures within the experimental series). In all the cases 40 bar difference between the system pressure and the external gas pressure was provided for good system stability. The experiments were carried out using one or two catalyst cartridges offering ideal reaction conditions to produce DFF in good yield (-70%) requiring only 10 bar of oxygen partial pressure.To reduce the hazardous potential of pure oxygen, the reactions were also performed substituting oxygen with synthetic air. However, to reach similar yields, the pressure had to be increased to 80 bar of compressed air. In Table 2 below there is set out a summary of the results from HMF-DFF oxidation screening in flow using the following parameters:1 mL HMF (5 mg/mL), H20, K-OMS-2/Celite, 10 bar 02, 100-160C, 0.5 mL/min, 2 (using one catalyst cartridge). |
Yield | Reaction Conditions | Operation in experiment |
---|---|---|
With 1-methylimidazole hydrogen sulfate; In water; dimethyl sulfoxide; at 180℃; for 6h;High pressure; Autoclave; | General procedure: GlcNAc (100 mg, 0.452 mmol) was added into a mixed solvent composed of DMSO (8 g) and deionized water (12 g) in a 50 mL stainless steel vessel with a Teflon lining and sealed by a screw cap.Different amounts of ILs with different structures, used as catalysts,were loaded into the reactor. Then, the reactor was then immersed into a preheated oil bath, and the reaction mixture stirred for a given time. Time zero was recorded when the reactor was immersed in to the preheated oil bath. The clear solution darkened gradually overtime. After the scheduled time, the reactor was taken out from the oil bath and immediately submerged in an ice-water bath to quench the reaction. Then, the reaction mixture was taken out and filtered with filter paper to remove insoluble humin polymer. Afterwards,1mL of this reaction mixture was diluted with 5mL of methanol in a volumetric flask. This diluted solution was then taken out, filteredthrough a 0.22 mm PTFE filter, and injected into a glass tube. The 5-HMF yield was determined by high performance liquid chromatography(HPLC) of these aqueous solutions, using a standard curve(Fig. S1, Supplementary material) in order to quantify the amount. |
Yield | Reaction Conditions | Operation in experiment |
---|---|---|
With oxygen; at 140℃; under 2250.23 Torr; for 5h;Autoclave; | General procedure: All oxidation experiments are performed in a 120 mL autoclaveequipped with the magnetic stirring and automatic temperature control.A typical procedure for the oxidation of HMF is as follows: a methanol(15mL) solution ofHMF (0.252 g, 2.0mmol) and Cu-MnO2 catalyst(0.05 g) is charged into the reactor, and the atmosphere inside is replacedwith the pure oxygen after the reactor is sealed. Under stirring,oxygen is charged to 0.3 MPa at room temperature and the autoclaveis preheated to 140 C, and then kept for 5 h. After reaction, the autoclavewas cooled and the obtained mixture is analyzed by HPLC andGC-MS instruments after the excess gas is purged (the detection ofproduct is presented in 1.2 and Fig. S1 of Supporting information). |
Yield | Reaction Conditions | Operation in experiment |
---|---|---|
With manganese(IV) oxide; oxygen; at 140℃; under 2250.23 Torr; for 5h;Autoclave; | General procedure: All oxidation experiments are performed in a 120 mL autoclaveequipped with the magnetic stirring and automatic temperature control.A typical procedure for the oxidation of HMF is as follows: a methanol(15mL) solution ofHMF (0.252 g, 2.0mmol) and Cu-MnO2 catalyst(0.05 g) is charged into the reactor, and the atmosphere inside is replacedwith the pure oxygen after the reactor is sealed. Under stirring,oxygen is charged to 0.3 MPa at room temperature and the autoclaveis preheated to 140 C, and then kept for 5 h. After reaction, the autoclavewas cooled and the obtained mixture is analyzed by HPLC andGC-MS instruments after the excess gas is purged (the detection ofproduct is presented in 1.2 and Fig. S1 of Supporting information). |
Yield | Reaction Conditions | Operation in experiment |
---|---|---|
95% | With ammonium sulfate; oxygen; In butan-1-ol; at 130℃; under 12001.2 Torr; for 0.2h; | will be 0.5mmol 5 - hydroxymethyl furfural, 0.10 mmol OMS - 2, 8 mmol ammonium sulfate,2 mL of n-butanol was added20 mL stainless steel reactor with Teflon lining, Charged with 1.6 MPa O2, Heating to 130 C, at this temperature the reaction 5h. Filtering, the solvent is removed by rotary evaporation, adding 5 ml H2 O,Extracted with ether,A high purity of 2,5-dicyanofuran,The isolated yield was 95%. |
Yield | Reaction Conditions | Operation in experiment |
---|---|---|
54.9% | With 1-methylimidazole hydrogen sulfate; In water; dimethyl sulfoxide; at 180℃; for 6h;High pressure; Autoclave; | General procedure: GlcNAc (100 mg, 0.452 mmol) was added into a mixed solvent composed of DMSO (8 g) and deionized water (12 g) in a 50 mL stainless steel vessel with a Teflon lining and sealed by a screw cap.Different amounts of ILs with different structures, used as catalysts,were loaded into the reactor. Then, the reactor was then immersed into a preheated oil bath, and the reaction mixture stirred for a given time. Time zero was recorded when the reactor was immersed in to the preheated oil bath. The clear solution darkened gradually overtime. After the scheduled time, the reactor was taken out from the oil bath and immediately submerged in an ice-water bath to quench the reaction. Then, the reaction mixture was taken out and filtered with filter paper to remove insoluble humin polymer. Afterwards,1mL of this reaction mixture was diluted with 5mL of methanol in a volumetric flask. This diluted solution was then taken out, filteredthrough a 0.22 mm PTFE filter, and injected into a glass tube. The 5-HMF yield was determined by high performance liquid chromatography(HPLC) of these aqueous solutions, using a standard curve(Fig. S1, Supplementary material) in order to quantify the amount. |
Yield | Reaction Conditions | Operation in experiment |
---|---|---|
With potassium hydroxide; In methanol; at 60℃; for 0.5h;Microwave irradiation; | A representative procedure for synthesis of thioaurones is as follows. To a solution of 150 nig (1.00 mmol) of 1-thiobenzofuranone and the required aldehyde (1 mmol) in 2 mL of methanol was added 2 mL of a 50% by weight solution of potassium hydroxide in methanol. This mixture was heated to 60 C in a CEM microwave reactor for 30 minutes. After cooling, the reaction was acidified with 1-N HC1 and partitioned between ethyl acetate and water. The organic layer was directly concentrated in vacuo and then purified via column chromatography on silica using ethyl acetate/hexanes mixtures to afford the desired thioaurone product as a solid in 20-50% yield. These products displayed spectroscopic data consistent with the assigned structure. |
Yield | Reaction Conditions | Operation in experiment |
---|---|---|
46.1%Chromat.; 8.5%Chromat. | With manganese(IV) oxide; oxygen; at 100℃; under 4500.45 Torr; for 12h;Autoclave; | CoOx-N/C-bpya (Co 3.0 wt%) catalyst, 40 mg MnO2, 0.5 mmol 5-hydroxymethylfurfural and 10 m The methanol was added to a stainless steel autoclave with a polytetrafluoroethylene liner, wherein Co: 5-hydroxymethylfurfural = 0.13:1 (mol: mol). The temperature was raised to 100 C by an automatic temperature controller, and 0.6 MPa of oxygen was added.The reaction was carried out for 12 hours, and the pressure was maintained during the reaction. The reaction product was analyzed using GC, and the results are shown in Table 1. |
Yield | Reaction Conditions | Operation in experiment |
---|---|---|
With oxygen; In ethanol; at 129.84℃; under 7500.75 Torr; for 4h; | 8% sodium methoxide was used as the base, Aldrich (Sigma-Aldrich) HMF 2 mM,400 mg of bimetallic nanoparticles (2% AuPd (0.5: 1) -IRA743) prepared according to preparation Example 2 as a catalyst was added to 25 ml of ethanol to prepare a mixed solution, oxygen gas at 10 bar pressure was injected as an oxidizing agent, 403K (129.85 C). The reaction was carried out at a temperature for 4 hours to remove HMF 2,5-furan dimethylcarboxylate (FDMC) was prepared by oxidative methylation. |
Yield | Reaction Conditions | Operation in experiment |
---|---|---|
40% | With bis(1,5-cyclooctadiene)rhodium(I) tetrafluoroborate; 1,3-bis-(diphenylphosphino)propane; sodium carbonate; In 2-methyltetrahydrofuran; at 135℃; for 24h;Molecular sieve; Inert atmosphere; Sealed tube; | General procedure: Rh(cod)2BF4(6 mol%), DPPP (0.09 mmol), Na2CO3 (1 mmol) and 4A MS (SiO2,powder, 150 mg) were transferred into an oven-dried tube (15 mL), which was evacuated and backfilled with N2 (5x). 2-Methyltetrahydrofuran (2.5 mL), alkyl or aryl iodide (1 mmol),HMF (1.2 mmol) were added into the tube via syringe and sealed with Teflon plug. The reaction mixture was stirred at 125 C for24 h. After the reaction was complete, the mixture was concentrated by rotary evaporation. The crude product was purified by column chromatography (EA/PE = 1/20) on a silica gel to afford the desired product. |
Yield | Reaction Conditions | Operation in experiment |
---|---|---|
40% | With bis(1,5-cyclooctadiene)rhodium(I) tetrafluoroborate; 1,3-bis-(diphenylphosphino)propane; sodium carbonate; In 2-methyltetrahydrofuran; at 125℃; for 24h;Molecular sieve; Inert atmosphere; Sealed tube; | General procedure: Rh(cod)2BF4(6 mol%), DPPP (0.09 mmol), Na2CO3 (1 mmol) and 4A MS (SiO2,powder, 150 mg) were transferred into an oven-dried tube (15 mL), which was evacuated and backfilled with N2 (5x). 2-Methyltetrahydrofuran (2.5 mL), alkyl or aryl iodide (1 mmol),HMF (1.2 mmol) were added into the tube via syringe and sealed with Teflon plug. The reaction mixture was stirred at 125 C for24 h. After the reaction was complete, the mixture was concentrated by rotary evaporation. The crude product was purified by column chromatography (EA/PE = 1/20) on a silica gel to afford the desired product. |
Yield | Reaction Conditions | Operation in experiment |
---|---|---|
35% | With bis(1,5-cyclooctadiene)rhodium(I) tetrafluoroborate; 1,3-bis-(diphenylphosphino)propane; sodium carbonate; In 2-methyltetrahydrofuran; at 135℃; for 24h;Molecular sieve; Inert atmosphere; Sealed tube; | General procedure: Rh(cod)2BF4(6 mol%), DPPP (0.09 mmol), Na2CO3 (1 mmol) and 4A MS (SiO2,powder, 150 mg) were transferred into an oven-dried tube (15 mL), which was evacuated and backfilled with N2 (5x). 2-Methyltetrahydrofuran (2.5 mL), alkyl or aryl iodide (1 mmol),HMF (1.2 mmol) were added into the tube via syringe and sealed with Teflon plug. The reaction mixture was stirred at 125 C for24 h. After the reaction was complete, the mixture was concentrated by rotary evaporation. The crude product was purified by column chromatography (EA/PE = 1/20) on a silica gel to afford the desired product. |
Yield | Reaction Conditions | Operation in experiment |
---|---|---|
88%; 10% | With oxygen; at 80℃; under 1500.15 Torr; for 4h;Autoclave; | General procedure: Add 0.03g of 5-hydroxymethylfurfural to a 20mL autoclave,Then add 3g ethanol and propanol (1wt%), and then add 0.04g Co7Cu3-N-C (where the metal loading is 2.4wt% and the molar ratio of the two metals is 7: 3) as catalystSeal the reaction kettle, pass in 2bar of oxygen, and stir vigorously (500rpm),Heat to 80 C and hold for 4 hours. After finishing the reaction, cool to room temperature and take a sample.Qualitative and quantitative detection using GC-MS (Shimadzu) and GC (Agilent),The test results are listed in Tables 2 and 3, respectively. |
Tags: 67-47-0 synthesis path| 67-47-0 SDS| 67-47-0 COA| 67-47-0 purity| 67-47-0 application| 67-47-0 NMR| 67-47-0 COA| 67-47-0 structure
A1267824[ 1219193-98-2 ]
5-Hydroxymethyl-2-furaldehyde-13C6
Reason: Stable Isotope
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