WO2016005998A1 - A method for the isolation of vanillin from rice straw - Google Patents
A method for the isolation of vanillin from rice straw Download PDFInfo
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- WO2016005998A1 WO2016005998A1 PCT/IN2015/050059 IN2015050059W WO2016005998A1 WO 2016005998 A1 WO2016005998 A1 WO 2016005998A1 IN 2015050059 W IN2015050059 W IN 2015050059W WO 2016005998 A1 WO2016005998 A1 WO 2016005998A1
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- WIPO (PCT)
- Prior art keywords
- rice straw
- vanillin
- process according
- solvent
- acid
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- MWOOGOJBHIARFG-UHFFFAOYSA-N vanillin Chemical compound COC1=CC(C=O)=CC=C1O MWOOGOJBHIARFG-UHFFFAOYSA-N 0.000 title claims abstract description 64
- FGQOOHJZONJGDT-UHFFFAOYSA-N vanillin Natural products COC1=CC(O)=CC(C=O)=C1 FGQOOHJZONJGDT-UHFFFAOYSA-N 0.000 title claims abstract description 62
- 235000012141 vanillin Nutrition 0.000 title claims abstract description 62
- 238000000034 method Methods 0.000 title claims abstract description 60
- 239000010902 straw Substances 0.000 title claims abstract description 56
- 235000007164 Oryza sativa Nutrition 0.000 title claims abstract description 54
- 235000009566 rice Nutrition 0.000 title claims abstract description 54
- 238000002955 isolation Methods 0.000 title abstract description 9
- 240000007594 Oryza sativa Species 0.000 title 1
- 241000209094 Oryza Species 0.000 claims abstract description 53
- 239000003960 organic solvent Substances 0.000 claims abstract description 14
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 claims description 48
- YMWUJEATGCHHMB-UHFFFAOYSA-N Dichloromethane Chemical compound ClCCl YMWUJEATGCHHMB-UHFFFAOYSA-N 0.000 claims description 39
- XEKOWRVHYACXOJ-UHFFFAOYSA-N Ethyl acetate Chemical compound CCOC(C)=O XEKOWRVHYACXOJ-UHFFFAOYSA-N 0.000 claims description 39
- 239000002904 solvent Substances 0.000 claims description 28
- VLKZOEOYAKHREP-UHFFFAOYSA-N n-Hexane Chemical compound CCCCCC VLKZOEOYAKHREP-UHFFFAOYSA-N 0.000 claims description 27
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims description 21
- PMZURENOXWZQFD-UHFFFAOYSA-L Sodium Sulfate Chemical compound [Na+].[Na+].[O-]S([O-])(=O)=O PMZURENOXWZQFD-UHFFFAOYSA-L 0.000 claims description 20
- 229920005610 lignin Polymers 0.000 claims description 19
- 239000000706 filtrate Substances 0.000 claims description 18
- 239000000047 product Substances 0.000 claims description 18
- 239000012043 crude product Substances 0.000 claims description 17
- 239000012265 solid product Substances 0.000 claims description 16
- 238000002474 experimental method Methods 0.000 claims description 15
- 239000000463 material Substances 0.000 claims description 15
- 239000012044 organic layer Substances 0.000 claims description 15
- 238000001914 filtration Methods 0.000 claims description 14
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 12
- 238000002360 preparation method Methods 0.000 claims description 11
- 239000002253 acid Substances 0.000 claims description 10
- 239000000796 flavoring agent Substances 0.000 claims description 10
- 235000019634 flavors Nutrition 0.000 claims description 10
- 229910052938 sodium sulfate Inorganic materials 0.000 claims description 10
- 235000011152 sodium sulphate Nutrition 0.000 claims description 10
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 claims description 9
- 238000004440 column chromatography Methods 0.000 claims description 9
- 235000009508 confectionery Nutrition 0.000 claims description 9
- 239000003480 eluent Substances 0.000 claims description 9
- 238000002844 melting Methods 0.000 claims description 9
- 230000008018 melting Effects 0.000 claims description 9
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 claims description 8
- OSGAYBCDTDRGGQ-UHFFFAOYSA-L calcium sulfate Chemical compound [Ca+2].[O-]S([O-])(=O)=O OSGAYBCDTDRGGQ-UHFFFAOYSA-L 0.000 claims description 8
- 238000004040 coloring Methods 0.000 claims description 8
- 238000001035 drying Methods 0.000 claims description 8
- 239000003925 fat Substances 0.000 claims description 8
- VLTRZXGMWDSKGL-UHFFFAOYSA-N perchloric acid Chemical compound OCl(=O)(=O)=O VLTRZXGMWDSKGL-UHFFFAOYSA-N 0.000 claims description 8
- 150000003839 salts Chemical class 0.000 claims description 8
- 239000007858 starting material Substances 0.000 claims description 8
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 claims description 7
- 235000011149 sulphuric acid Nutrition 0.000 claims description 7
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 claims description 6
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 claims description 6
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 claims description 6
- 239000001117 sulphuric acid Substances 0.000 claims description 6
- 239000006228 supernatant Substances 0.000 claims description 5
- SCYULBFZEHDVBN-UHFFFAOYSA-N 1,1-Dichloroethane Chemical compound CC(Cl)Cl SCYULBFZEHDVBN-UHFFFAOYSA-N 0.000 claims description 4
- 239000001175 calcium sulphate Substances 0.000 claims description 4
- 235000011132 calcium sulphate Nutrition 0.000 claims description 4
- 229910052500 inorganic mineral Inorganic materials 0.000 claims description 4
- 239000007788 liquid Substances 0.000 claims description 4
- 239000011707 mineral Substances 0.000 claims description 4
- 239000003208 petroleum Substances 0.000 claims description 4
- 238000010992 reflux Methods 0.000 claims description 4
- 229910000029 sodium carbonate Inorganic materials 0.000 claims description 4
- AXCZMVOFGPJBDE-UHFFFAOYSA-L calcium dihydroxide Chemical compound [OH-].[OH-].[Ca+2] AXCZMVOFGPJBDE-UHFFFAOYSA-L 0.000 claims description 3
- 239000000920 calcium hydroxide Substances 0.000 claims description 3
- 229910001861 calcium hydroxide Inorganic materials 0.000 claims description 3
- 239000007787 solid Substances 0.000 claims description 3
- 238000004140 cleaning Methods 0.000 claims description 2
- 238000001816 cooling Methods 0.000 claims description 2
- 238000001704 evaporation Methods 0.000 claims description 2
- 238000002156 mixing Methods 0.000 claims description 2
- 230000020477 pH reduction Effects 0.000 claims description 2
- OTYBMLCTZGSZBG-UHFFFAOYSA-L potassium sulfate Chemical compound [K+].[K+].[O-]S([O-])(=O)=O OTYBMLCTZGSZBG-UHFFFAOYSA-L 0.000 claims description 2
- 229910052939 potassium sulfate Inorganic materials 0.000 claims description 2
- 239000001120 potassium sulphate Substances 0.000 claims description 2
- 235000011151 potassium sulphates Nutrition 0.000 claims description 2
- BDERNNFJNOPAEC-UHFFFAOYSA-N propan-1-ol Chemical compound CCCO BDERNNFJNOPAEC-UHFFFAOYSA-N 0.000 claims description 2
- 238000000746 purification Methods 0.000 claims description 2
- 239000002154 agricultural waste Substances 0.000 abstract description 8
- 239000001913 cellulose Substances 0.000 abstract description 7
- 229920002678 cellulose Polymers 0.000 abstract description 7
- 238000000605 extraction Methods 0.000 abstract description 7
- DKZBBWMURDFHNE-UHFFFAOYSA-N trans-coniferylaldehyde Natural products COC1=CC(C=CC=O)=CC=C1O DKZBBWMURDFHNE-UHFFFAOYSA-N 0.000 abstract description 2
- 238000006243 chemical reaction Methods 0.000 description 17
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 13
- 229940093499 ethyl acetate Drugs 0.000 description 11
- 235000019439 ethyl acetate Nutrition 0.000 description 11
- KSEBMYQBYZTDHS-HWKANZROSA-N ferulic acid Chemical compound COC1=CC(\C=C\C(O)=O)=CC=C1O KSEBMYQBYZTDHS-HWKANZROSA-N 0.000 description 10
- KSEBMYQBYZTDHS-HWKANZROSA-M (E)-Ferulic acid Natural products COC1=CC(\C=C\C([O-])=O)=CC=C1O KSEBMYQBYZTDHS-HWKANZROSA-M 0.000 description 7
- 229940114124 ferulic acid Drugs 0.000 description 7
- KSEBMYQBYZTDHS-UHFFFAOYSA-N ferulic acid Natural products COC1=CC(C=CC(O)=O)=CC=C1O KSEBMYQBYZTDHS-UHFFFAOYSA-N 0.000 description 7
- 235000001785 ferulic acid Nutrition 0.000 description 7
- 239000011541 reaction mixture Substances 0.000 description 7
- 238000001953 recrystallisation Methods 0.000 description 7
- QURCVMIEKCOAJU-UHFFFAOYSA-N trans-isoferulic acid Natural products COC1=CC=C(C=CC(O)=O)C=C1O QURCVMIEKCOAJU-UHFFFAOYSA-N 0.000 description 7
- HEDRZPFGACZZDS-UHFFFAOYSA-N Chloroform Chemical compound ClC(Cl)Cl HEDRZPFGACZZDS-UHFFFAOYSA-N 0.000 description 6
- 239000012153 distilled water Substances 0.000 description 6
- 239000000428 dust Substances 0.000 description 6
- 239000012535 impurity Substances 0.000 description 6
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 description 4
- BJIOGJUNALELMI-ONEGZZNKSA-N Isoeugenol Natural products COC1=CC(\C=C\C)=CC=C1O BJIOGJUNALELMI-ONEGZZNKSA-N 0.000 description 4
- 239000003513 alkali Substances 0.000 description 4
- 239000002585 base Substances 0.000 description 4
- 230000015572 biosynthetic process Effects 0.000 description 4
- BJIOGJUNALELMI-ARJAWSKDSA-N cis-isoeugenol Chemical compound COC1=CC(\C=C/C)=CC=C1O BJIOGJUNALELMI-ARJAWSKDSA-N 0.000 description 4
- 239000000126 substance Substances 0.000 description 4
- 238000003786 synthesis reaction Methods 0.000 description 4
- BJIOGJUNALELMI-UHFFFAOYSA-N trans-isoeugenol Natural products COC1=CC(C=CC)=CC=C1O BJIOGJUNALELMI-UHFFFAOYSA-N 0.000 description 4
- 241000228245 Aspergillus niger Species 0.000 description 3
- 241000589517 Pseudomonas aeruginosa Species 0.000 description 3
- 230000036983 biotransformation Effects 0.000 description 3
- 229940114123 ferulate Drugs 0.000 description 3
- 238000001556 precipitation Methods 0.000 description 3
- 241000123346 Chrysosporium Species 0.000 description 2
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical class [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 2
- QAOWNCQODCNURD-UHFFFAOYSA-L Sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 description 2
- 238000013459 approach Methods 0.000 description 2
- 125000003118 aryl group Chemical group 0.000 description 2
- HUMNYLRZRPPJDN-UHFFFAOYSA-N benzaldehyde Chemical compound O=CC1=CC=CC=C1 HUMNYLRZRPPJDN-UHFFFAOYSA-N 0.000 description 2
- 239000010941 cobalt Substances 0.000 description 2
- 229910017052 cobalt Inorganic materials 0.000 description 2
- GUTLYIVDDKVIGB-UHFFFAOYSA-N cobalt atom Chemical class [Co] GUTLYIVDDKVIGB-UHFFFAOYSA-N 0.000 description 2
- RRAFCDWBNXTKKO-UHFFFAOYSA-N eugenol Chemical compound COC1=CC(CC=C)=CC=C1O RRAFCDWBNXTKKO-UHFFFAOYSA-N 0.000 description 2
- 229940071125 manganese acetate Drugs 0.000 description 2
- UOGMEBQRZBEZQT-UHFFFAOYSA-L manganese(2+);diacetate Chemical compound [Mn+2].CC([O-])=O.CC([O-])=O UOGMEBQRZBEZQT-UHFFFAOYSA-L 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 244000005700 microbiome Species 0.000 description 2
- -1 phenolic stilbenes Chemical class 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 239000002689 soil Substances 0.000 description 2
- 229910021653 sulphate ion Inorganic materials 0.000 description 2
- ZENOXNGFMSCLLL-UHFFFAOYSA-N vanillyl alcohol Chemical compound COC1=CC(CO)=CC=C1O ZENOXNGFMSCLLL-UHFFFAOYSA-N 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- 241000894006 Bacteria Species 0.000 description 1
- 239000002028 Biomass Substances 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- NPBVQXIMTZKSBA-UHFFFAOYSA-N Chavibetol Natural products COC1=CC=C(CC=C)C=C1O NPBVQXIMTZKSBA-UHFFFAOYSA-N 0.000 description 1
- 241000196324 Embryophyta Species 0.000 description 1
- 102000004190 Enzymes Human genes 0.000 description 1
- 108090000790 Enzymes Proteins 0.000 description 1
- 239000005770 Eugenol Substances 0.000 description 1
- 241000233866 Fungi Species 0.000 description 1
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 1
- UVMRYBDEERADNV-UHFFFAOYSA-N Pseudoeugenol Natural products COC1=CC(C(C)=C)=CC=C1O UVMRYBDEERADNV-UHFFFAOYSA-N 0.000 description 1
- 244000290333 Vanilla fragrans Species 0.000 description 1
- 235000009499 Vanilla fragrans Nutrition 0.000 description 1
- 238000005904 alkaline hydrolysis reaction Methods 0.000 description 1
- 235000013361 beverage Nutrition 0.000 description 1
- 238000011138 biotechnological process Methods 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 238000001311 chemical methods and process Methods 0.000 description 1
- 239000003153 chemical reaction reagent Substances 0.000 description 1
- 231100000481 chemical toxicant Toxicity 0.000 description 1
- 239000003426 co-catalyst Substances 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 239000002537 cosmetic Substances 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 229960002217 eugenol Drugs 0.000 description 1
- 238000000855 fermentation Methods 0.000 description 1
- 230000004151 fermentation Effects 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 238000009472 formulation Methods 0.000 description 1
- 239000000383 hazardous chemical Substances 0.000 description 1
- 230000007062 hydrolysis Effects 0.000 description 1
- 238000006460 hydrolysis reaction Methods 0.000 description 1
- 239000002207 metabolite Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000035772 mutation Effects 0.000 description 1
- 230000017066 negative regulation of growth Effects 0.000 description 1
- 229910052759 nickel Inorganic materials 0.000 description 1
- QNGNSVIICDLXHT-UHFFFAOYSA-N para-ethylbenzaldehyde Natural products CCC1=CC=C(C=O)C=C1 QNGNSVIICDLXHT-UHFFFAOYSA-N 0.000 description 1
- 239000002304 perfume Substances 0.000 description 1
- 239000011591 potassium Substances 0.000 description 1
- 229910052700 potassium Inorganic materials 0.000 description 1
- YQUVCSBJEUQKSH-UHFFFAOYSA-N protochatechuic acid Natural products OC(=O)C1=CC=C(O)C(O)=C1 YQUVCSBJEUQKSH-UHFFFAOYSA-N 0.000 description 1
- 239000011734 sodium Substances 0.000 description 1
- 229910052708 sodium Inorganic materials 0.000 description 1
- 235000021286 stilbenes Nutrition 0.000 description 1
- 239000000758 substrate Substances 0.000 description 1
- 239000003440 toxic substance Substances 0.000 description 1
- WKOLLVMJNQIZCI-UHFFFAOYSA-N vanillic acid Chemical compound COC1=CC(C(O)=O)=CC=C1O WKOLLVMJNQIZCI-UHFFFAOYSA-N 0.000 description 1
- TUUBOHWZSQXCSW-UHFFFAOYSA-N vanillic acid Natural products COC1=CC(O)=CC(C(O)=O)=C1 TUUBOHWZSQXCSW-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C45/00—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds
- C07C45/78—Separation; Purification; Stabilisation; Use of additives
- C07C45/80—Separation; Purification; Stabilisation; Use of additives by liquid-liquid treatment
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C45/00—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds
- C07C45/78—Separation; Purification; Stabilisation; Use of additives
- C07C45/81—Separation; Purification; Stabilisation; Use of additives by change in the physical state, e.g. crystallisation
-
- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11B—PRODUCING, e.g. BY PRESSING RAW MATERIALS OR BY EXTRACTION FROM WASTE MATERIALS, REFINING OR PRESERVING FATS, FATTY SUBSTANCES, e.g. LANOLIN, FATTY OILS OR WAXES; ESSENTIAL OILS; PERFUMES
- C11B9/00—Essential oils; Perfumes
- C11B9/02—Recovery or refining of essential oils from raw materials
- C11B9/025—Recovery by solvent extraction
Definitions
- the present invention relates to a process for the isolation of Vanillin (4-hydroxy- 3-methoxy benzaldehyde) by modified convenient process (extraction with organic solvent) of pretreated cellulose from rice straw, a renewable agricultural waste.
- This invention is also relates to the extraction of vanillin using organic solvents (reusable) in a very cheap and convenient method from a renewable agriculture resource, rice straw. The process does not involve any costly or hazardous chemicals.
- Vanillin is one of the most important and popular aromatic flavor materials used extensively in foods, beverages, perfumes, cosmetic and pharmaceuticals industries. More than 10 thousand tons per year had been produced by the industries all over the world through chemical synthesis. Demands increasing extensively and existing is not sufficient for the demands. Natural vanillin is mainly obtained from Vanilla planifolia pods which is very much expensive compared to synthetic vanillin derived from various compounds. This 'natural' vanillin, can cover only 1 % of the global demand and the cost is (US $ 4,00.00-500.00 per kilogram) [Virginia Commonwealth University News, 14.04.2003, vcunews@vcu.edu].
- ferulic acid is first isolated from its source, which is converted to vanillin and vanillic acid using microbes [Synthesis of vanillin from a carbon source; John W. frost, U.S. Pat. No. 6,372,461].
- the drawback of the method is that the extraction of ferulic acid from paddy straw was carried out via alkaline hydrolysis and was optimized through Central Composite Design (CCD) to give 4.092 g/l corresponding to 0.818% of ferulic acid. Ferulic acid was further utilized as a substrate for the biotransformation of vanillin and resulting in multiple steps.
- CCD Central Composite Design
- Vanillin from isoeugenol by using soil stains like Pseudomonas aeruginosa [Use of growing cells of Pseudomonas aeruginosa for synthesis of the natural vanillin via conversion of isoeugenol; Iraj Nahvi et al, Egyptian J.Phar.Res., 10(4), 749-757, 2011]
- vanillin is prepared from isoeugenol by using soil stains like Pseudomonas aeruginosa.
- Vanillin from Oryzae sativa by biotransformation method using Aspergillus niger and Phanorochaete [Aromatic benzaldehyde from oryzae sativa; Noor Hasyierah Md. Salleh et al, IPCBEE, 9, 140-144, 201 1]
- vanillin is Vanillin from Oryzae sativa by biotransformation method using Aspergillus niger and Phanorochaete chrysosporium through two steps of bioengineering.
- ferulate is extracted from rice straw and that ferulate is oxidized by hydrogen peroxide in the presence of manganese acetate etc. with co-catalyst from salts of cobalt, nickel etc. for conversion of vanillin.
- the drawback of the method is that it uses ferulate from rice straw, hydrogen peroxide, manganese acetate, salt of cobalt etc. to get vanillin with multi steps reactions and vanillyl alcohol and furfurel present with the vanillin. Also, the yield of the vanillin was 0.012%.
- biotechnological processes require multi-steps, heavy investment and stringent control to dictate the specific enzymes to work, and have high risk of mutation or inhibition of growth of microorganisms in presence of metabolites and are slow.
- This invention shows a new method aimed to preparation of vanillin today must concern itself for use of renewable resources and cheap and easily available chemicals.
- the ideal raw material is the supernatant obtained from the precipitation of lignin from alkali solution (1-3.5%) containing agro-wastes such as rice straw, which is cheap and abundant.
- the main objective of the present invention is to provide a handy method for the isolation of vanillin from pretreated cellulose of rice straw which obviates the drawbacks of the previously reported methods known prior art as detailed above.
- Yet another objective of the present invention is to provide a process for the isolation of vanillin by directly from the supernatant of the alkali solution after precipitation of lignin of pretreated cellulose from rice straw thereby reducing the cost of the chemicals to the minimal and avoiding the release of the toxic chemicals to the environment.
- the present invention provides a method for the preparation of vanillin from rice straw which comprises a. mixing the rice straw with base solution under reflux conditions for a period of 3-10 hours for pretreatment, then cooling to a temperature of about 25- 30° C and separating the solid mass by filtration, collecting the filtrate, b. acidification of the said filtrate to pH 2-3 using mineral acid to separate the lignin part from the liquid by further filtration, c. after filtration extracting the supernatant with an organic solvent followed by removing the moister with anhydrous salts, d. separating the salts from the liquid by filtration, and drying the resultant organic layer to obtain the desired crude product, e.
- step e purifying, drying and further recrystallizing the crude product by using solvent to get the white crystalline solid product as vanillin
- step e solvent used in step e is recovered and reused for further experiments
- g. vanillin obtained from the said process has melting point 82-85 °C, with a yield in the range of 0.1 to 0.2% and has sweet flavor.
- rice straw is obtained by Cleaning and drying and is cut and milled, which is extracted with ethanol in a soxhlet apparatus to remove fats and coloring materials to obtain the starting material for pretreatment of rice straw.
- base solution used for pretreatment of the rice straw is selected from the group consisting of potassium hydroxide, sodium hydroxide, calcium hydroxide and sodium carbonate and in the range of 1 % in 200 ml-3.5% in 200 ml per 10 gm of rice straw used.
- the organic solvent used is selected from the group consisting of dichloromethane, dichloroethane, methanol, ethyl acetate, particularly dichloromethane in the range of 40-80 ml for 10-20 gm of pretreated rice straw used.
- the mineral acid used is selected from the group consisting of sulphuric acid, hydrochloric acid or perchloric acid etc, particularly sulphuric acid and in the range of 10-20 ml per 10 gm of pretreated rice straw used.
- temperature used is refluxing condition is in the range of 90-100 °C.
- anhydrous salt used is anhydrous sodium sulphate, potassium sulphate, calcium sulphate etc.
- drying is done by evaporating the solvent under reduced pressure.
- solvent used in step e of claim 1 is selected from dichloromethane, ethanol, methanol, propanol or acetic acid.
- the renewable agrowaste used is rice straw.
- Rice straw a renewable resource, which on treatment under mild reaction conditions- sodium base/ potassium base /calcium hydroxide /sodium carbonate, sulphuric acid/ hydrochloric acid/perchloric acid, extracted with ethyl acetate/chloroform/ dichloromethane/ dichloroethane etc and on refluxing produces vanillin in a easiest method particularly extraction with dichloromethane.
- This is the new method where vanillin is produced from pretreated cellulose of rice straw a renewable resource which is convenient and cost effective.
- This method reported in the invention is novel and non-obvious.
- the filtrate obtained after filtration of lignin was extracted with dichloromethane (40 ml) and washed the organic layer with water for 2-3 times. After that treated with anhydrous sodium sulphate to absorb the moisture content present the organic layer and filtered to separate sodium sulphate.
- the organic solvent was evaporated under reduced pressure to get the crude product.
- the solvent used in the method is recovered and reused for further experiments.
- the crude product was purified by column chromatography technique using hexane : ethyl acetate :: 10:1 as eluent, and evaporated the solvent to get the desired product under reduced pressure. For recrystallization of the product using methanol to give the white crystalline solid product with sweet flavor, melting point 82-85 °C (Reported 81-83 °C).
- the vanillin was estimated 10 mg (0.1 %).
- Dry rice straw 500 grams was extensively washed with distilled water in order to remove impurities (mainly dust).
- the materials were first dried in sunlight and cut into smaller pieces and milled to pass through a 1-2 mm mesh and extracted with methanol in a soxhlet apparatus to remove fats and coloring materials. This rice straw was preserved and used in subsequent experiments.
- the filtrate obtained after filtration of lignin was extracted with dichloromethane (40 ml) and washed the organic layer with water for 2-3 times. After that treated with anhydrous sodium sulphate to absorb the moisture content present the organic layer and filtered to separate sodium sulphate.
- the organic solvent was evaporated under reduced pressure to get the crude product.
- the solvent used in the method is recovered and reused for further experiments.
- the crude product was purified by column chromatography technique using hexane : ethyl acetate :: 10:1 as eluent, and evaporated the solvent to get the desired product under reduced pressure. For recrystallization of the product using methanol to give the white crystalline solid product with sweet flavor, melting point 82-85 °C (Reported 81-83 °C).
- the vanillin was estimated 14 mg (0.14%).
- Dry rice straw 500 grams was extensively washed with distilled water in order to remove impurities (mainly dust).
- the materials were first dried in sunlight and cut into smaller pieces and milled to pass through a 1-2 mm mesh and extracted with petroleum ether (60-80 °C) in a soxhlet apparatus to remove fats and coloring materials. This rice straw was preserved and used in subsequent experiments.
- the filtrate obtained after filtration of lignin was extracted with dichloromethane (40 ml) and washed the organic layer with water for 2-3 times. After that treated with anhydrous sodium sulphate to absorb the moisture content present the organic layer and filtered to separate sodium sulphate.
- the organic solvent was evaporated under reduced pressure to get the crude product.
- the solvent used in the method is recovered and reused for further experiments.
- the crude product was purified by column chromatography technique using hexane : ethyl acetate :: 10:1 as eluent, and evaporated the solvent to get the desired product under reduced pressure. For recrystallization of the product using methanol to give the white crystalline solid product with sweet flavor, melting point 82-85 °C (Reported 81-83 °C).
- the vanillin was estimated 20 mg (0.2%).
- Dry rice straw 500 grams was extensively washed with distilled water in order to remove impurities (mainly dust).
- the materials were first dried in sunlight and cut into smaller pieces and milled to pass through a 1-2 mm mesh and extracted with petroleum ether (60-80 °C) in a soxhlet apparatus to remove fats and coloring materials. This rice straw was preserved and used in subsequent experiments.
- Dry rice straw 500 grams was extensively washed with distilled water in order to remove impurities (mainly dust).
- the materials were first dried in sunlight and cut into smaller pieces and milled to pass through a 1-2 mm mesh and extracted with methanol in a soxhlet apparatus to remove fats and coloring materials. This rice straw was preserved and used in subsequent experiments.
- the filtrate obtained after filtration of lignin was extracted with chloroform (40 ml) and washed the organic layer with water for 2-3 times. After that treated with anhydrous pottasium sulphate to absorb the moisture content present the organic layer and filtered to separate pottasium sulphate.
- the organic solvent was evaporated under reduced pressure to get the crude product.
- the solvent used in the method is recovered and reused for further experiments.
- the crude product was purified by column chromatography technique using hexane : ethyl acetate :: 10:1 as eluent, and evaporated the solvent to get the desired product under reduced pressure. For recrystallization of the product using methanol to give the white crystalline solid product with sweet flavor of melting point 82-85 °C (Reported 81-83 °C).
- the vanillin was estimated 13 mg (0.13%).
- the filtrate obtained after filtration of lignin was extracted with methanol (80 ml) and washed the organic layer with water for 2-3 times. After that treated with anhydrous calcium sulphate to absorb the moisture content present the organic layer and filtered to separate calcium sulphate.
- the organic solvent was evaporated under reduced pressure to get the crude product.
- the solvent used in the method is recovered and reused for further experiments.
- the crude product was purified by column chromatography technique using hexane : ethyl acetate :: 10:1 as eluent, and evaporated the solvent to get the desired product under reduced pressure. For recrystallization of the product using methanol to give the white crystalline solid product with sweet flavor of melting point 82-85 °C (Reported 81-83 °C).
- the vanillin was estimated 11 mg (0.11 %).
- the used solvent was recovered by using rotating-evaporator to get the crude (solid) product as well as distilled solvent (36-78 ml) which was used for our further reaction systems. This way we were using the recycled solvents in our reaction systems.
- the crude product was purified by column chromatography technique using hexane : ethyl acetate :: 10:1 as eluent, and evaporated the solvent to get the desired product under reduced pressure.
- the vanillin was estimated 20 mg (0.2%).
- Pretreated cellulose of Agro-waste such as rice straw produces vanillin in a convenient and handy method.
- the solvent used for the reaction system can be recycled, hence cost effective.
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Abstract
The present invention relates to a process for the isolation of Vanillin (4-hydroxy- 3-methoxy benzaldehyde) by a convenient process (extraction with organic solvent) of pretreated cellulose from rice straw, a renewable agricultural waste. This invention relates to the extraction of vanillin using organic solvents (reusable) in a very cheap and convenient way from a renewable agriculture resource, rice straw.
Description
A METHOD FOR THE ISOLATION OF VANILLIN FROM RICE STRAW FIELD OF THE INVENTION
The present invention relates to a process for the isolation of Vanillin (4-hydroxy- 3-methoxy benzaldehyde) by modified convenient process (extraction with organic solvent) of pretreated cellulose from rice straw, a renewable agricultural waste. This invention is also relates to the extraction of vanillin using organic solvents (reusable) in a very cheap and convenient method from a renewable agriculture resource, rice straw. The process does not involve any costly or hazardous chemicals.
BACKGROUND AND PRIOR ART OF THE INVENTION
Vanillin is one of the most important and popular aromatic flavor materials used extensively in foods, beverages, perfumes, cosmetic and pharmaceuticals industries. More than 10 thousand tons per year had been produced by the industries all over the world through chemical synthesis. Demands increasing extensively and existing is not sufficient for the demands. Natural vanillin is mainly obtained from Vanilla planifolia pods which is very much expensive compared to synthetic vanillin derived from various compounds. This 'natural' vanillin, can cover only 1 % of the global demand and the cost is (US $ 4,00.00-500.00 per kilogram) [Virginia Commonwealth University News, 14.04.2003, vcunews@vcu.edu]. Alternative biotechnology-based approaches for the production are based on bioconversion of lignin, phenolic stilbenes, isoeugenol, eugenol, ferulic acid, or aromatic amino acids, and on de novo biosynthesis, applying fungi, bacteria, plant cells, or genetically engineered microorganisms. The recent focus on vanillin production is centered on isolation of ferulic acid from agro-waste lignocellosic biomass and its subsequent conversion to vanillin. Recently, biotechnological approaches have been initiated to achieve this target. Some progress is being made in developed countries to prepare vanillin through a biotechnological route from feru late-moiety containing agricultural waste. Where, ferulic acid is first isolated from its source, which is converted to vanillin and vanillic acid using microbes [Synthesis of vanillin from a carbon source; John W. frost, U.S. Pat. No. 6,372,461].
[Formulation of vanillin from paddy straw; Noor Hasyierah, M. S.; Mohamed Zulkali, M. D.; Dachyar Arbain, JIRCAS, 73, 160-165, 2012]
In this method ferulic acid is converted to vanillin by using Aspergillus niger and Phanorochaete chrysosporium through two steps of fermentation.
The drawback of the method is that the extraction of ferulic acid from paddy straw was carried out via alkaline hydrolysis and was optimized through Central Composite Design (CCD) to give 4.092 g/l corresponding to 0.818% of ferulic acid. Ferulic acid was further utilized as a substrate for the biotransformation of vanillin and resulting in multiple steps.
Yet another reference may be made to Vanillin from isoeugenol by using soil stains like Pseudomonas aeruginosa [Use of growing cells of Pseudomonas aeruginosa for synthesis of the natural vanillin via conversion of isoeugenol; Iraj Nahvi et al, Iranian J.Phar.Res., 10(4), 749-757, 2011]
In this method vanillin is prepared from isoeugenol by using soil stains like Pseudomonas aeruginosa.
The drawback of the method is that this biotechnological route is not very economical, take long time, in multiple steps.
Yet another reference may be made to Vanillin from Oryzae sativa by biotransformation method using Aspergillus niger and Phanorochaete [Aromatic benzaldehyde from oryzae sativa; Noor Hasyierah Md. Salleh et al, IPCBEE, 9, 140-144, 201 1] In this method vanillin is Vanillin from Oryzae sativa by biotransformation method using Aspergillus niger and Phanorochaete chrysosporium through two steps of bioengineering.
The drawback of the method is that this biotechnological route is not very economical, take more time, in multiple steps.
Yet another reference may be made to Vanillin from agriculture waste [Process for the preparation of vanillin from agriculture waste; Naleen Borthakur; US patent No. US 7,399,889 B2, 2008]
In this method ferulate is extracted from rice straw and that ferulate is oxidized by hydrogen peroxide in the presence of manganese acetate etc. with co-catalyst from salts of cobalt, nickel etc. for conversion of vanillin.
The drawback of the method is that it uses ferulate from rice straw, hydrogen peroxide, manganese acetate, salt of cobalt etc. to get vanillin with multi steps
reactions and vanillyl alcohol and furfurel present with the vanillin. Also, the yield of the vanillin was 0.012%.
The biotechnological processes require multi-steps, heavy investment and stringent control to dictate the specific enzymes to work, and have high risk of mutation or inhibition of growth of microorganisms in presence of metabolites and are slow.
Considering the environment-polluting non-renewable petroleum crude based chemicals employed in the existing methods there is a great scope for inventing handy chemical processes that can use renewable raw materials for the synthesis of vanillin in a very convenient and cost effective method.
This invention shows a new method aimed to preparation of vanillin today must concern itself for use of renewable resources and cheap and easily available chemicals. In this invention, the ideal raw material is the supernatant obtained from the precipitation of lignin from alkali solution (1-3.5%) containing agro-wastes such as rice straw, which is cheap and abundant.
OBJECTS OF THE INVENTION
The main objective of the present invention is to provide a handy method for the isolation of vanillin from pretreated cellulose of rice straw which obviates the drawbacks of the previously reported methods known prior art as detailed above.
Another objective of the present invention is to provide a new method for the isolation of vanillin directly from the supernatant of the alkali solution after precipitation of lignin of pretreated cellulose from rice straw, a renewable agricultural waste. Yet another objective of the present invention is to provide a new method for the isolation of vanillin by using mild reaction conditions, reagents and solvent that makes the method convenient and easiest.
Yet another objective of the present invention is to provide a process for the isolation of vanillin by directly from the supernatant of the alkali solution after precipitation of lignin of pretreated cellulose from rice straw thereby reducing the cost of the chemicals to the minimal and avoiding the release of the toxic chemicals to the environment.
SUMMARY OF THE INVENTION
Accordingly the present invention provides a method for the preparation of vanillin from rice straw which comprises a. mixing the rice straw with base solution under reflux conditions for a period of 3-10 hours for pretreatment, then cooling to a temperature of about 25- 30° C and separating the solid mass by filtration, collecting the filtrate, b. acidification of the said filtrate to pH 2-3 using mineral acid to separate the lignin part from the liquid by further filtration, c. after filtration extracting the supernatant with an organic solvent followed by removing the moister with anhydrous salts, d. separating the salts from the liquid by filtration, and drying the resultant organic layer to obtain the desired crude product, e. purifying, drying and further recrystallizing the crude product by using solvent to get the white crystalline solid product as vanillin, f. solvent used in step e is recovered and reused for further experiments, g. vanillin obtained from the said process has melting point 82-85 °C, with a yield in the range of 0.1 to 0.2% and has sweet flavor.
In another embodiment, rice straw is obtained by Cleaning and drying and is cut and milled, which is extracted with ethanol in a soxhlet apparatus to remove fats and coloring materials to obtain the starting material for pretreatment of rice straw.
In yet another embodiment, base solution used for pretreatment of the rice straw is selected from the group consisting of potassium hydroxide, sodium hydroxide, calcium hydroxide and sodium carbonate and in the range of 1 % in 200 ml-3.5% in 200 ml per 10 gm of rice straw used.
In yet another embodiment, the organic solvent used is selected from the group consisting of dichloromethane, dichloroethane, methanol, ethyl acetate, particularly dichloromethane in the range of 40-80 ml for 10-20 gm of pretreated rice straw used.
In yet another embodiment, the mineral acid used is selected from the group consisting of sulphuric acid, hydrochloric acid or perchloric acid etc, particularly
sulphuric acid and in the range of 10-20 ml per 10 gm of pretreated rice straw used.
In yet another embodiment, temperature used is refluxing condition is in the range of 90-100 °C. In yet another embodiment, anhydrous salt used is anhydrous sodium sulphate, potassium sulphate, calcium sulphate etc.
In yet another embodiment, drying is done by evaporating the solvent under reduced pressure.
In yet another embodiment, column chromatography using Hexane: ethyl acetate:: 10:1 as eluent for the purification of the product is used.
In yet another embodiment, solvent used in step e of claim 1 is selected from dichloromethane, ethanol, methanol, propanol or acetic acid.
In yet another embodiment of the present invention, the renewable agrowaste used is rice straw. DETAILED DESCRIPTION OF THE INVENTION
Rice straw a renewable resource, which on treatment under mild reaction conditions- sodium base/ potassium base /calcium hydroxide /sodium carbonate, sulphuric acid/ hydrochloric acid/perchloric acid, extracted with ethyl acetate/chloroform/ dichloromethane/ dichloroethane etc and on refluxing produces vanillin in a easiest method particularly extraction with dichloromethane. This is the new method where vanillin is produced from pretreated cellulose of rice straw a renewable resource which is convenient and cost effective. This method reported in the invention is novel and non-obvious.
The following specific examples are given by way of illustration of the invention in actual practice and therefore should not be construed to limit the scope of the present invention.
Rice straw were obtained from Mr Ramen Saikia of Bhathmora Gaon, P.O. RRL, Jorhat, P.S. Pulibor, Pin-785006, Assam India. (Please see Annexure-1)
EXAMPLE 1
Preparation of starting materials:
Dry rice straw 500 grams was extensively washed with distilled water in order to remove impurities (mainly dust). The materials were first dried in sunlight and cut into smaller pieces and milled to pass through a 1-2 mm mesh and extracted with methanol in a soxhlet apparatus to remove fats and coloring materials. This rice straw was preserved and used in subsequent experiments.
Pretreatment of Rice Straw
Rice straw (10 grams) was mixed with NaOH solution (1.5% in 200 ml) in a 500 ml round bottomed flask and refluxed for 5 hrs. in a oil bath. The reaction mixture was cooled, filtered to separate the solid products. The filtrate was acidified with H2S04 acid (10 ml) to maintain the pH 2-3 of the solution. Precipitated lignin was filtered and collected.
Conversion of pretreated Rice Straw to Vanillin:
The filtrate obtained after filtration of lignin was extracted with dichloromethane (40 ml) and washed the organic layer with water for 2-3 times. After that treated with anhydrous sodium sulphate to absorb the moisture content present the organic layer and filtered to separate sodium sulphate. The organic solvent was evaporated under reduced pressure to get the crude product. The solvent used in the method is recovered and reused for further experiments. The crude product was purified by column chromatography technique using hexane : ethyl acetate :: 10:1 as eluent, and evaporated the solvent to get the desired product under reduced pressure. For recrystallization of the product using methanol to give the white crystalline solid product with sweet flavor, melting point 82-85 °C (Reported 81-83 °C). The vanillin was estimated 10 mg (0.1 %).
EXAMPLE 2
Preparation of starting materials:
Dry rice straw 500 grams was extensively washed with distilled water in order to remove impurities (mainly dust). The materials were first dried in sunlight and cut into smaller pieces and milled to pass through a 1-2 mm mesh and extracted with methanol in a soxhlet apparatus to remove fats and coloring materials. This rice straw was preserved and used in subsequent experiments.
Pretreatment of Rice Straw
Rice straw (10 grams) was mixed with NaOH solution (2.0% in 200 ml) in a 500 ml round bottomed flask and refluxed for 5 hrs. in a oil bath. The reaction mixture was cooled, filtered to separate the solid products. The filtrate was acidified with H2S04 acid (10 ml) to maintain the pH 2-3 of the solution. Precipitated lignin was filtered and collected.
Conversion of pretreated Rice Straw to Vanillin:
The filtrate obtained after filtration of lignin was extracted with dichloromethane (40 ml) and washed the organic layer with water for 2-3 times. After that treated with anhydrous sodium sulphate to absorb the moisture content present the organic layer and filtered to separate sodium sulphate. The organic solvent was evaporated under reduced pressure to get the crude product. The solvent used in the method is recovered and reused for further experiments. The crude product was purified by column chromatography technique using hexane : ethyl acetate :: 10:1 as eluent, and evaporated the solvent to get the desired product under reduced pressure. For recrystallization of the product using methanol to give the white crystalline solid product with sweet flavor, melting point 82-85 °C (Reported 81-83 °C). The vanillin was estimated 14 mg (0.14%).
EXAMPLE 3 Preparation of starting materials:
Dry rice straw 500 grams was extensively washed with distilled water in order to remove impurities (mainly dust). The materials were first dried in sunlight and cut into smaller pieces and milled to pass through a 1-2 mm mesh and extracted with petroleum ether (60-80 °C) in a soxhlet apparatus to remove fats and coloring materials. This rice straw was preserved and used in subsequent experiments.
Pretreatment of Rice Straw
Rice straw (10 grams) was mixed with NaOH solution (2.5% in 200 ml) in a 500 ml round bottomed flask and refluxed for 5 hrs. in a oil bath. The reaction mixture was cooled, filtered to separate the solid products. The filtrate was acidified with H2SO4 acid (10 ml) to maintain the pH 2-3 of the solution. Precipitated lignin was filtered and collected.
Conversion of pretreated Rice Straw to Vanillin:
The filtrate obtained after filtration of lignin was extracted with dichloromethane (40 ml) and washed the organic layer with water for 2-3 times. After that treated with anhydrous sodium sulphate to absorb the moisture content present the organic layer and filtered to separate sodium sulphate. The organic solvent was evaporated under reduced pressure to get the crude product. The solvent used in the method is recovered and reused for further experiments. The crude product was purified by column chromatography technique using hexane : ethyl acetate :: 10:1 as eluent, and evaporated the solvent to get the desired product under reduced pressure. For recrystallization of the product using methanol to give the white crystalline solid product with sweet flavor, melting point 82-85 °C (Reported 81-83 °C). The vanillin was estimated 20 mg (0.2%).
EXAMPLE 4 Preparation of starting materials:
Dry rice straw 500 grams was extensively washed with distilled water in order to remove impurities (mainly dust). The materials were first dried in sunlight and cut into smaller pieces and milled to pass through a 1-2 mm mesh and extracted with petroleum ether (60-80 °C) in a soxhlet apparatus to remove fats and coloring materials. This rice straw was preserved and used in subsequent experiments.
Pretreatment of Rice Straw
Rice straw (10 grams) was mixed with NaOH solution (3% in 200 ml) in a 500 ml round bottomed flask and refluxed for 5 hrs. in a oil bath. The reaction mixture was cooled, filtered to separate the solid products. The filtrate was acidified with H2S04 acid (10 ml) to maintain the pH 2-3 of the solution. Precipitated lignin was filtered and collected.
Conversion of pretreated Rice Straw to Vanillin:
The filtrate obtained after filtration of lignin was extracted with dichloromethane (40 ml) and washed the organic layer with water for 2-3 times. After that treated with anhydrous sodium sulphate to absorb the moisture content present the
organic layer and filtered to separate sodium sulphate. The organic solvent was evaporated under reduced pressure to get the crude product. The solvent used in the method is recovered and reused for further experiments. The crude product was purified by column chromatography technique using hexane : ethyl acetate :: 10:1 as eluent, and evaporated the solvent to get the desired product under reduced pressure. For recrystallization of the product using methanol to give the white crystalline solid product with sweet flavor, melting point 82-85 °C (Reported 81-83 °C). The vanillin was estimated 12 mg (0.12%). EXAMPLE 5
Preparation of starting materials:
Dry rice straw 500 grams was extensively washed with distilled water in order to remove impurities (mainly dust). The materials were first dried in sunlight and cut into smaller pieces and milled to pass through a 1-2 mm mesh and extracted with methanol in a soxhlet apparatus to remove fats and coloring materials. This rice straw was preserved and used in subsequent experiments.
Pretreatment of Rice Straw
Conversion of pretreated Rice straw to vanillin we were using the standard optimum condition 4 got from the experiments 1-7 for variation of alkalies.
Rice straw (10 grams) was mixed with KOH solution (2.5% in 200 ml) in a 500 ml round bottomed flask and refluxed for 7 hrs. in a oil bath. The reaction mixture was cooled, filtered to separate the solid products. The filtrate was acidified with HCI acid (5 ml) to maintain the pH 2-3 of the solution. Precipitated lignin was filtered and collected.
Conversion of pretreated Rice Straw to Vanillin:
The filtrate obtained after filtration of lignin was extracted with chloroform (40 ml) and washed the organic layer with water for 2-3 times. After that treated with anhydrous pottasium sulphate to absorb the moisture content present the organic layer and filtered to separate pottasium sulphate. The organic solvent was evaporated under reduced pressure to get the crude product. The solvent used in
the method is recovered and reused for further experiments. The crude product was purified by column chromatography technique using hexane : ethyl acetate :: 10:1 as eluent, and evaporated the solvent to get the desired product under reduced pressure. For recrystallization of the product using methanol to give the white crystalline solid product with sweet flavor of melting point 82-85 °C (Reported 81-83 °C). The vanillin was estimated 13 mg (0.13%).
EXAMPLE 6
Preparation of starting materials: Dry rice straw 500 grams was extensively washed with distilled water in order to remove impurities (mainly dust). The materials were first dried in sunlight and cut into smaller pieces and milled to pass through a 1-2 mm mesh and extracted with ethanol in a soxhlet apparatus to remove fats and coloring materials. This rice straw was preserved and used in subsequent experiments. Pretreatment of Rice Straw
Rice straw (10 grams) was mixed with Na2C03 solution (2.5% in 200 ml) in a 500 ml round bottomed flask and refluxed for 9 hrs. in a oil bath. The reaction mixture was cooled, filtered to separate the solid products. The filtrate was acidified with H2S04 acid (10 ml) to maintain the pH 2-3 of the solution. Precipitated lignin was filtered and collected.
Conversion of pretreated Rice Straw to Vanillin:
The filtrate obtained after filtration of lignin was extracted with methanol (80 ml) and washed the organic layer with water for 2-3 times. After that treated with anhydrous calcium sulphate to absorb the moisture content present the organic layer and filtered to separate calcium sulphate. The organic solvent was evaporated under reduced pressure to get the crude product. The solvent used in the method is recovered and reused for further experiments. The crude product was purified by column chromatography technique using hexane : ethyl acetate :: 10:1 as eluent, and evaporated the solvent to get the desired product under reduced pressure. For recrystallization of the product using methanol to give the
white crystalline solid product with sweet flavor of melting point 82-85 °C (Reported 81-83 °C). The vanillin was estimated 11 mg (0.11 %).
EXAMPLE 7 Recycle of the used solvents:
For using the recycled solvent in the conversion of pretreated rice straw to vanillin we were using the standard optimum condition 4 by following method.
Rice straw (10 grams) was mixed with NaOH solution (2.5% in 200 ml) in a 500 ml round bottomed flask and refluxed for 8 hrs. in a oil bath. The reaction mixture was cooled, filtered to separate the solid products. The filtrate was acidified with sulphuric acid/hydrochloric acid/perchloric acid (5 ml) to maintain the pH 2-3 of the solution. Precipitated lignin was filtered and collected. The filtrate was extracted with dichloromethane/ethylacetate/chloroform/ dichloroethan (40-80 ml) and washed the organic layer with water for 2-3 times. The used solvent was recovered by using rotating-evaporator to get the crude (solid) product as well as distilled solvent (36-78 ml) which was used for our further reaction systems. This way we were using the recycled solvents in our reaction systems. The crude product was purified by column chromatography technique using hexane : ethyl acetate :: 10:1 as eluent, and evaporated the solvent to get the desired product under reduced pressure. For recrystallization of the product using methanol to give the white crystalline solid product with sweet flavor, melting point 82-85 °C (Reported 81-83 °C). The vanillin was estimated 20 mg (0.2%).
ADVANTAGES OF THE INVENTION
1. Pretreated cellulose of Agro-waste such as rice straw produces vanillin in a convenient and handy method.
2. In the present invention no further steps are required for vanillin preparation. After hydrolysis it gives the desired product directly.
3. The chemicals used are cheap and commercially available.
4. The extraction of vanillin from rice straw, described in the invention is a new method reported for the first time.
5. The solvent used for the reaction system, can be recycled, hence cost effective.
Claims
A method for the preparation of vanillin from rice straw which comprises a. mixing the rice straw with base solution under reflux conditions for a period of 3-10 hours at temperature in the range of 90-100°C for pretreatment, then cooling to a temperature of about 25-30°C and separating the solid mass by filtration, collecting the filtrate, b. acidification of the said filtrate to pH 2-3 using mineral acid to separate the lignin part from the liquid by further filtration, c. after filtration extracting the supernatant with an organic solvent followed by removing the moister with anhydrous salts, d. separating the salts from the liquid by filtration, and drying the resultant organic layer to obtain the desired crude product, e. purifying, drying and further recrystallizing the crude product by using solvent to get the white crystalline solid product as vanillin, f. solvent used in step e is recovered and reused for further experiments.
The process according to claim 1 , wherein rice straw is obtained by cleaning and drying and is cut and milled, which is extracted with ethanol or methanol or by petroleum ether in a soxhlet apparatus to remove fats and coloring materials to obtain the starting material for pretreatment of rice straw.
The process according to claim 1 , wherein the base solution used for pretreatment of the rice straw is selected from the group consisting of potassium hydroxide, sodium hydroxide, calcium hydroxide and sodium carbonate and in the range of 1 % in 200 ml-3.5% in 200 ml per 10 gm of rice straw used.
The process according to claim 1 , wherein the organic solvent used is selected from the group consisting of dichloromethane, dichloroethane, methanol, ethyl acetate, particularly dichloromethane in the range of 40-80 ml for 10-20 gm of pretreated rice straw used.
5. The process according to claim 1 , wherein the mineral acid used is selected from the group consisting of sulphuric acid, hydrochloric acid or perchloric acid etc, particularly sulphuric acid and in the range of 10-20 ml per 10 gm of pretreated rice straw used.
6. The process according to claim 1 , wherein vanillin obtained from the said process has melting point 82-85 °C, with a yield in the range of 0.1 to 0.2% and has sweet flavor.
7. The process according to claim 1 , wherein the anhydrous salt used is anhydrous sodium sulphate, potassium sulphate, calcium sulphate etc.
8. The process according to claim 1 , wherein drying is done by evaporating the solvent under reduced pressure.
9. The process according to claim 1 , wherein column chromatography with Hexane: ethyl acetate :: 10:1 as eluent for the purification of the product is used.
10. The process according to claim 1 , wherein solvent used in step e of claim 1 is selected from dichloromethane, ethanol, methanol, propanol or acetic acid.
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2017170549A1 (en) * | 2016-03-29 | 2017-10-05 | 東レ株式会社 | Method for producing hydroxycinnamic acid |
EP4308535A1 (en) * | 2021-03-15 | 2024-01-24 | Specialty Operations France | Process for the purification of vanillin or a vanillin derivative obtained by a biotechnological process |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6372461B1 (en) | 1998-09-18 | 2002-04-16 | Board Of Directors Operating Michigan State University | Synthesis of vanillin from a carbon source |
WO2007094013A1 (en) * | 2006-02-13 | 2007-08-23 | Council Of Scientific & Industrial Research | Process for the preparation of vanillin from agricultural plant waste by manganese salt catalyzed oxidation employing hydrogen peroxide |
-
2015
- 2015-07-03 WO PCT/IN2015/050059 patent/WO2016005998A1/en active Application Filing
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6372461B1 (en) | 1998-09-18 | 2002-04-16 | Board Of Directors Operating Michigan State University | Synthesis of vanillin from a carbon source |
WO2007094013A1 (en) * | 2006-02-13 | 2007-08-23 | Council Of Scientific & Industrial Research | Process for the preparation of vanillin from agricultural plant waste by manganese salt catalyzed oxidation employing hydrogen peroxide |
US7399889B2 (en) | 2006-02-13 | 2008-07-15 | Council Of Scientific And Industrial Research | Process for the preparation of vanillin from agricultural waste |
Non-Patent Citations (8)
Title |
---|
EKHE, J.D. ET AL.: "ISOLATION AND CHARACTERIZATION OF LIGNIN DEGRADATION PRODUCTS FROM BAGASSE AND RICE STRAW", IPPTA, INDIAN PULP AND PAPER TECHNICAL ASS., vol. 9, no. 2, 1997, pages 21 - 28, XP008079325, ISSN: 0379-5462 * |
HERRMANN, W.A. ET AL.: "Methyltrioxorhenium: oxidative cleavage of CC-double bonds and its application in a highly efficient synthesis of vanillin from biological waste", JOURNAL OF MOLECULAR CATALYSIS A: CHEMICAL, vol. 153, no. 1-2, 2000, pages 49 - 52, XP002435577, ISSN: 1381-1169, DOI: 10.1016/S1381-1169(99)00370-2 * |
IRAJ NAHVI ET AL.: "Use of growing cells of Pseudomonas aeruginosa for synthesis of the natural vanillin via conversion of isoeugenol", IRANIAN J. PHAR. RES., vol. 10, no. 4, 2011, pages 749 - 757 |
NOOR HASYIERAH MOHD SALLEH ET AL.: "Optimization of alkaline hydrolysis of paddy straw for ferulic acid extraction", INDUSTRIAL CROPS AND PRODUCTS, ELSEVIER, NL, vol. 34, no. 3, 7 June 2011 (2011-06-07), pages 1635 - 1640, XP028381749, ISSN: 0926-6690, [retrieved on 20110613], DOI: 10.1016/J.INDCROP.2011.06.010 * |
NOOR HASYIERAH, M. S.; MOHAMED ZULKALI, M. D.; DACHYAR ARBAIN, JIRCAS, vol. 73, 2012, pages 160 - 165 |
NOOR HASYIERAH, M.S. ET AL.: "Formulation of vanillin derived from paddy straw", JIRCAS WORKING REPORT, MINISTRY OF AGRICULTURE, FORESTRY AND FISHERIES, TSUKUBA, JP, vol. 73, 2012, pages 160 - 165, XP009187147, ISSN: 1341-710X * |
SALLEH ET AL.: "Aromatic benzaldehyde from oryzae sativa", IPCBEE, vol. 9, 2011, pages 140 - 144 |
VIRGINIA COMMONWEALTH UNIVERSITY NEWS, 14 April 2003 (2003-04-14), Retrieved from the Internet <URL:vcunews@vcu.edu> |
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WO2017170549A1 (en) * | 2016-03-29 | 2017-10-05 | 東レ株式会社 | Method for producing hydroxycinnamic acid |
JP6278163B1 (en) * | 2016-03-29 | 2018-02-14 | 東レ株式会社 | Method for producing hydroxycinnamic acid |
US10519093B2 (en) | 2016-03-29 | 2019-12-31 | Toray Industries, Inc. | Method of producing hydroxycinnamic acids |
AU2017244704B2 (en) * | 2016-03-29 | 2021-07-08 | Toray Industries, Inc. | Method for producing hydroxycinnamic acid |
EP4308535A1 (en) * | 2021-03-15 | 2024-01-24 | Specialty Operations France | Process for the purification of vanillin or a vanillin derivative obtained by a biotechnological process |
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