• 专利附录
  • 专利说明
  • 权利要求
  • 类似技术
  • 同族专利
  • 引用文献
  • 法律状态
  • 优先权
    • 专利摘要:
    Process for the treatment of aqueous sweet juice containing a mixture of saccharides containing an aldehyde functional group, especially fructose, and saccharides containing a ketone functional group, especially glucose, with a view to separating and selecting the saccharides containing a ketone functional group. It consists (a) in making up a hydroorganic medium by mixing the sweet juice with a ketonic compound containing active methylene, a calcium-based catalyst and preferably ethanol, (b) in stirring the medium until the formation of furane-based polyol by condensation of the ketonic compound and the saccharides containing an aldehyde functional group, and (c) in allowing the furane-based polyol to precipitate and separating it off by a physical route from the liquid medium; the latter is completely freed from the saccharides containing an aldehyde functional group. The process of the invention makes it possible, in particular, to prepare pure fructose syrups.
    公开号:SU1579464A3
    申请号:SU874028809
    申请日:1987-01-16
    公开日:1990-07-15
    发明作者:Феликс Жо Луи；Элизабет Борредон Мари；Дельма Мишель；Газэ Антуан
    申请人:Энститю Насьональ Политекник Де Тулуз (Фирма)；
    IPC主号:
    专利说明:

    The invention relates to the chemistry of sugars, namely to a method for the extraction of fructose from aqueous sugar-containing juice.
    The purpose of the invention is to reduce the cost of the method for separating a mixture of fructose and glucose from a sugar-containing soot, which consists in separating glucose as a furan polyhydric alcohol in the presence of a calcium chloride catalyst and obtaining fructose as a syrup with a high content of the latter.
    Example 1. Hydrolyze 100 g of sucrose (cane sugar) on
    46 g of Amberlite E 252 cation-exchange resin in 50 ml of water and 160 ml of ethanol at 80 ° C. After separating the resin from the reaction medium and dosing the amount of glucose contained in the solution, stir 93 ml of this solution containing 18 g of glucose with 7 ml of ethanol, 55 g of calcium chloride and 26.5 ml of ethyl acetoacetate at 78 ° C (reflux temperature ) within 6 h 30 min. During the reaction, precipitation of whitish crystals is observed; at the end of the reaction, 400 ml of water is added and the crystals are filtered off.
    SP
    |
    with
    Ј O5
    -Јb

    and
    The mother liquor is settled. A new filtration of this solution is then carried out, which makes it possible to isolate ethyl 4- (D-arabino-tetroxybutyl) -2-methyl-5-furoate crystals.
    The obtained filtrate is subjected to extraction of ethanol from the medium by gentle distillation and extraction of excess ethyl acetate-acetic acid ester with ethyl acetate in order to return it to the cycle, as well as simultaneous demineralization and bleaching with the Lévovit 5P 102 / MP 64 ion exchange resin. Then, the resulting solution is dehydrated and get fructose syrup with a fructose content of more than 95% by weight without ethyl acetoacetate, salt and ethanol, fructose is crystallized by adding ethanol to the resulting syrup ..
    Example 2 100 g of cane sugar molasses, in which the saccharide content is 39-61% by weight, is added to the reactor and hydrochloric acid is added to obtain pH 2. The mixture is brought to 85 ° C over 1/2 hr. Pro-hydrolysis is controlled by liquid high-performance chromium, thermography (N.P.I.S.). Upon completion of the reaction, the mixture is neutralized by adding lime (pH 6-7).
    Then, the content of glucose in the solution is metered, 60 g of calcium chloride and 23 g of acetoc methyl ester are introduced. hydrochloric acid, and then 150 ml of ethanol. The mixture is heated to 78 ° C for 6 hours and 30 minutes; at the end of the reaction, 200 ml of water is added and the furan crystals formed are separated from the mother liquor to give methyl 4- (D-arabino-tetroxybutyl) -2-methyl-5-furoate. Subsequent processing in example 1 is obtained pure fructose syrup with a fructose content of 90 wt.%.
    EXAMPLE 3. It is processed sugar sugar molasses, in which the total content of sugars is 37 - 15 May. 7. The inversion is carried out with hydrochloric acid (8 ml at 33%), added to 100 g of beet sugar molasses.
    The mixture is heated to 80 ° C; control
    Degrees of conversion of sucrose to glucose
    and fructose was carried out by chromatography (H.P.L.C.). After neutralizing the medium, calcium chloride (12 g per 10 g of saccharides) is added, followed by ethyl acetate.
    acetoacetic acid ester (26 g per 18 g of gliukoza) and finally 150 ml of ethanol.
    The mixture is heated to 78 ° C, stirred for 4 hours and 30 minutes, then water is added and, after repeated recrystallization, ethyl 4- (D- -arabino-tetroxybutyl) -2-methyl-5-furoate is obtained.
    After crystallization and filtration, the preceding filtrate is purified as described in Example 1 to obtain pure fructose syrup with a fructose content of 93% by weight.
    Example4. To a mixture of fructose and glucose, containing 18 g of glucose per 20 ml of water, 80 ml of ethanol, 55.5 g of calcium chloride and 31.64 g of acetoacetic acid butyl ester are added.
    The reaction medium is brought to reflux with an azeotropic mixture of water and ethanol (78 ° C) for 6 hours and 30 minutes and ethyl 4- (D-arabino-tetroxybutyl) -2-propyl-5-furoate is obtained.
    Next, similarly to example 1, receive fructose syrup containing 90 wt% fructose.
    Thus, the proposed method allows fructose to be isolated from a mixture of glucose and fructose and to produce a high fructose syrup.
    权利要求:
    Claims (1)
    [1]
    1. A method of extracting fructose from a mixture of fructose and glucose from aqueous sugar-containing juice, characterized in that, in order to reduce the cost of the process, sugar syrup with lower alkyl ester of acetoacetic acid is mixed in water-ethanol or water-methanol medium in excess of the stoichiometric amount of glucose, in the presence of calcium chloride as a catalyst, taken in a molar ratio of 1-6 relative to glucose, the reaction mass is heated at 40–78 ° C for 4–8 h with the formation of furan polyatom th alcohol which is precipitated by cooling the reaction mixture, if necessary with the prior addition of water and the separated aqueous phase containing fructose.
    2o The method according to claim 1, characterized in that the quality of the bottom is 155794646
    Aceous acetoacetate alkyl ester3. The method according to claim 1, about tl and h of the acid, use methyl or ethylic acid and with this, before the termination of the methyl ester. Add water.
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    同族专利:
    公开号 | 公开日
    AU6755087A|1987-07-23|
    EP0234065A3|1988-03-30|
    FR2593182A1|1987-07-24|
    JPS62252797A|1987-11-04|
    OA08461A|1988-07-29|
    CN87100590A|1987-09-02|
    BR8700134A|1987-12-01|
    IN166690B|1990-06-30|
    US4785794A|1988-11-22|
    AT47885T|1989-11-15|
    EP0234065B1|1989-11-08|
    EP0234065A2|1987-09-02|
    FR2593182B1|1990-03-16|
    DE3666841D1|1989-12-14|
    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    US3290263A|1962-08-02|1966-12-06|Colonial Sugar Refining Co|Process of reacting sugars with reagents wherein the sugar is dissolved in monohydric alcohols containing grouping|
    US3533839A|1966-02-16|1970-10-13|Kazuo Hara|Process for separating fructose from glucose|
    AT263660B|1966-03-30|1968-07-25|Laevosan Gmbh & Co Kg|Process for the technical separation of sugar mixtures|
    NL166723C|1970-06-26|1981-09-15|Cpc International Inc|METHOD FOR REMOVING GLUCOSE FROM A SOLUTION CONTAINING GLUCOSE AND FRUCTOSE.|
    EP0109203B1|1982-11-16|1987-09-16|Imperial Chemical Industries Plc|Process for effecting aldose to ketose conversion|
    JPH1174A|1997-06-13|1999-01-06|Wakuda Planning Le-Mu:Kk|Dog walking rope having extensible mechanism|
    JPH119964A|1997-06-19|1999-01-19|Nippon Sanso Kk|Method for detoxicating ammonia-containing waste gas|FR2634210B1|1988-07-13|1990-10-12|Furchim|PROCESS FOR THE SEPARATION OF ARABINOSIS CONTAINED IN A SUGAR SACCHARIDE JUICE|
    US6656287B2|2002-04-15|2003-12-02|Co2 Solutions, Llc|System to produce sugar from plant materials|
    DE60332289D1|2003-08-14|2010-06-02|Korea Basic Science Inst|METHOD FOR MOORING AN ACTIVE METHYLENE COMPOUND TO CARBOHYDRATE|
    FR2932815B1|2008-06-23|2015-10-30|Cie Ind De La Matiere Vegetale Cimv|PROCESS FOR PRETREATING PLANT RAW MATERIAL FOR PRODUCING SACCHARIFEROUS AND LIGNOCELLULOSIC RESOURCES, BIOETHANOL AND / OR SUGAR, AND.|
    WO2018116272A1|2016-12-23|2018-06-28|Petiva Private Ltd.|Process for separating ketoses|
    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    FR8601123A|FR2593182B1|1986-01-17|1986-01-17|PROCESS FOR TREATING AQUEOUS SUGAR JUICE FOR SEPARATING AND SELECTING KETONIC SACCHARIDES|
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