• 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:
    A process for preparing a fructoside, especially a fructosyl disaccharide, comprises reacting a fructosyl saccharide such as sucrose or raffinose with an alcohol or aldose in the presence of a fructosyl-transferase, especially one derived from B. subtilis BCIB 11811, 11872 or 11873. In particular, aldose is a compound of the formula in which A represents a hydrogen atom or the group CH2X, where X represents a hydrogen atom or an alkoxy group, and the fructosyl disaccharide so formed is halogenated to provide a halosucrose or halogalactosucrose sweetener.
    公开号:SU1630617A3
    申请号:SU843757905
    申请日:1984-06-20
    公开日:1991-02-23
    发明作者:Брин Ратбоун Эльнер；Джон Хакинг Эндрю；Самуэль Джеймс Читэм Петер
    申请人:Тейт Энд Лайл Паблик Лимитед Компани (Фирма)；
    IPC主号:
    专利说明:

    This invention relates to the microbiological synthesis of substances, relates to a process for the preparation of fructosyl disaccharides suitable as sugary substances in the food industry, specifically known as TGF (the resulting fructosyl disaccharides are an intermediate product for use in the preparation of sucralose, previously known as TGS),
    The purpose of the invention is to improve the quality of the target product.
    The invention provides for the preparation of fructosyl disaccharides of the general formula by carrying out an aldose reaction of the general formula

    cm
    BUT
    -0
    ON / U, he
    (D
    BUT HE
    where A is hydrogen or CHgX group;
    X, hydrogen, aliphatic or 10 ", aromatic carboxy or alkoxy or aryl-alkoxy,
    with sucrose or raffinose in the presence of fructosyltransferase, produced by Bacillus subtilis NCIB No. 11871, 11872 or 11873, characterized by Km for sucrose of at least 0.1 M in the absence of an aldose acceptor that does not form significant polysaccharide 20 alcohol, levane from a fructose donor in the absence of an aldose acceptor, and stable to the action of surfactants, having an optimum activity at, active for at least 20 minutes at 45 ° C. The enzyme used does not exhibit invertase activity, which favorably affects the quality characteristics of the target 30 product. The Km for fructosyltransferase obtained from B. subtilis NCIB 11871 is 0.2 M for sucrose in the absence of an acceptor, in contrast to the known Km of 35 0.02 M.
    The fructosyltransferase used does not accelerate the disproportionation reaction, i.e. does not convert low molecular weight oligosaccharides into levan with high molecular weight.
    The source of fructose for the reaction can be any oligo- or disaccharide. containing, preferably, 45 unsubstituted d-fructosyl ring attached to the anomeric aldose carbon by bond (), as
    in sucrose (B-B-fructosyl-OH) -gluco-pyranoside), raffinose ((-0-galak-50 topyranosyl- (I - - - 6) -O-of-D-glucopyranosyl (1 - - , 2) - | b-B-fructofuranoside) or s.thioze. „-The reaction between the donor and acceptor of fructose is carried out at pH 5.4-6.0 and 30 ° C, the optimum values for the action of the enzyme, which Preferably used immobilized on an insoluble support.
    The B. subtilis strains produced by fructosyltransferase, according to classical tests, meet the requirements of species identification. B. subtilis NCIB 11871 is lactose negative, showing different production of acid and xylose. V.subtilis NCIB
    11872 is also lactose-negative and gives negative results with D-mannose, melibiose and trehalose in the ONPG reaction. V.subtilis NCIB
    11873 is lactose-positive and gives negative results with D-mannose and inulin.
    Example 1. Getting 6-acetate-sucrose,
    a) Obtaining the enzyme. Fructosil transferase is obtained by cultivating Bacillus subtilis, strain NCIB 11871. The enzyme is induced with sucrose during cell growth in shake flasks (capacity 250 ml, 4 flasks) containing minimal sucrose medium (100 ml per flask). The culture is incubated until the last exponential phase of the microorganisms, shaking with, then the contents of the four flasks are combined and the culture medium is separated from the cells by centrifugation (5000 g for 15 min), 20-30% of the total amount of enzyme remains in association with the cells. The resulting supernatant was adjusted to 65% saturation by adding solid ammonium sulfate and allowed to stand for 45 minutes at. As a result, most of the unwanted invertase and other protein constituents are precipitated, and most of the enzyme remains in solution. Then the sample is re-centrifuged (20,000 g for 30 min) and the sediment containing invertae is unloaded. More ammonium sulfate was added to the solution to bring it to 95% saturation and left to stand for another 45 minutes at 0 ° C. A second precipitate formed, mainly fructosyltransferase, which was collected by centrifugation (40,000 g for 45 minutes) and re-solution 12 ml of 50 mM osfat buffer, pH 6.0. The result of two precipitations and the dissolution of a second precipitate is the purification and concentration of the enzyme, such that with the aid of polyacrylamide gel electrophoresis, only an ode protein band is detected. The remaining ammonium sulfate is removed from the enzyme enzyme system by dialysis (0 ° C for 4 hours) in the presence of 50 mM phosphate buffer.
    The dialyzed enzyme is examined before and after the addition of n-hydroxybenzoate, which suppresses invertase, but has no effect on fructosyltransferase. Usually, this method determines that fructosyltransferase preparations are free from invertase. The protein content of the preparations is estimated to be about 0.45 mg / ml by determining the absorption of proteins at a wavelength of 280 nm. Black pigment is often present even in purified enzyme preparations, but it does not affect their activity.
    b) Preparation of sucrose 6-acetate 6-glucose acetate (80 g dried under vacuum to constant weight) and granulated sucrose (160 g) are dissolved at room temperature in 100 ml of MacIlvaine buffer solution at pH 5.4 and diluted to 600 ml (i.e. 40% by weight of deionization with water. This solution is then filtered and 28 ml of the enzyme solution is added. The reaction mixture is incubated at 30 ° C. Samples are taken at certain time intervals until it is determined that Sucrose 6-acetate is no longer formed and maxi is reached. The average concentration of sucrose 6-acetate is 120 g / l. The enzyme is removed by filtering the reaction mixture through a column of DEAE cellulose, which adsorbs the enzyme. Another way was to denature it by heating at 65 ° C for 1 hour. it can promote the slow hydrolysis of sucrose 6-acetate and release fructose.
    The product is then isolated using preparative HPLC and at least 65% sucrose 6-acetate is obtained with a total yield of 50%. The initial fermentation reaction rate is 244.5 mg of sucrose 6-acetate per 1 mg of enzyme per hour. The yield at the fermentation stage was 58% based on the consumption of glucose 6-acetate or 48% based on the sucrose 6-acetate formed.
    Example 2. Preparation of 6-deoxysaccharose.
    Isolation, purification and crystallization. 6-Deoxy-O-glucose (D-quinose, 20 g) and sucrose are subjected to a reaction similar to that described in Example 1, and a mixture of 6-deoxysaccharose, D-chinose, sucrose
    and glucose, total volume 140 ml. 6-dehydroxacarose is separated from the mixture by preparative HPLC using a reverse-phase waters column prepak 500-C1.8 and water as
    5 elgaent. There is a surprisingly large difference in the retention time of 6-deoxy sucrose and the retention time of the other components of the mixture. D-chinovoz, sucrose and D-glucose
    0 is eluted 4–9 minutes after administration, and 6-deoxy-sucrose only after 29 minutes (maximum peak height), —Long release time allows a large amount of
    5 substances per injection than would otherwise be possible. The eluate containing 6-deoxy sucrose is evaporated to dryness under reduced pressure (bath temperature) and receive
    0 transparent syrup (16.7 g, 42%), which crystallizes at room temperature ... The product is recrystallized from ethanol and it had a melting point of 180-181 ° C, X; L + 57.6 ° (c 2 , 5, water).
    5 Mass spectrum, t / e: 293 (M-SNUK)). C-NMR spectrum (DgO solution, relative to molecular DSS at Om.d .: Carbon atom Chemical shift
    ppm
    0, 32
    1 94.70
    3 3 5
    5 4f 3 2 4
    6f P 6
    0
    84.01 79.04 77.74 76.73 74.93 73.95 71.09 65.02 63.77 19.36
    Example 3. The procedure described in Example 1 is repeated, but instead of 6-acetate, b-benzoate and g of lucose are used in step b. A similar result is obtained.
    1 Example 4. The method described in example 1 is modified using the enzyme obtained by cultivating Marburg 168 strain, NCIB 11872 or 11873 strain in step b. The reaction proceeds in the same manner, but at a slower rate.
    Example 5. Immobilization and purification of fructosyltransferase of NCIR 11871 strain using ion-exchange DEAE cellulose and obtaining xylochosis.
    The ion-exchange DEDE cellulose (DE52) was intensively washed with 50 mM McIlvaine pH 5.4 buffer and then with a buffered substrate (sucrose-xylose 2: 1, 40 wt.%, Total sugars). After filtering off almost dry through a Buchner DEAE funnel, the cellulose (10 g) is mixed with 8 ml of the fructosyltransferase preparation obtained by cultivating B. subtilis, as in Example 2, Re 1, for 15 minutes at 306 C with stirring. The resulting mixture of DEAE (Cellulose and enzyme is loaded onto a 110-millimeter column with a water jacket (19x1 cm and maintained at 2–30 ° C using a Churchill thermal circulator. The DEAE cellulose is drained by its own gravity and these drains are collected. Substrate is pumped upwards using a Watson-Marlow pump at a speed of 3 1.0 ml / h, the eluate is collected at regular intervals and examined for fructosyltransferase activity. Absorption 3 is also determined for a solne length of 280 nm (F ngp). 1 ml of liquid sample or O, 1 g of immobilized enzyme (on DE 52) is incubated with 2 ml of substrate at 30 ° C for 4 hours.
    Using the xylose-sax-rose substrate to prepare xyxaccharose, the concentration and activity of the depleted solution remaining after the completion of the immobilization procedure is compared to the concentration and activity of the original enzyme preparation. It was found that 68.5% of the initially present tg enzyme in the cell extract was immobilized together with 83% of the original protein present. Immobilized enzyme has an initial activity of 80.2% of the activity of an equivalent amount of free ferment; the activity of both drugs is respectively equal to 0.38 g of xylsaccharose / g of immobilized enzyme0
    with p 5 0 5
    0
    5 tg -
    that per hour and 0.865 g of xylsaccharose / ml of enzyme extract for an hour.
    The immobilized enzyme (10 g) is continuously fed to the column at 30 ° C for 2 weeks at a constant pH of the eluate, microbiological contamination is excluded. During the first three days, small amounts of protein and enzyme were desorbed (approximately 24% of the initially adsorbed protein and 2.3% of the initially adsorbed enzyme). The activity of the immobilized enzyme falls with a half-life of 95 hours, and there is an inverse relationship between the degree of conversion of substrates into products and the flow rate along the column. At the lowest flow rate, 0.086 column volumes without packing (eq.) And 80% conversion to xystat-sucrose, an eluate containing 2) g / l xylaharose is obtained. This yield is higher than the yields obtained in periodic reactions, probably because the kinetics of flow with the structural core of the column contributes to the formation of xylsacrose, since the products are continuously discharged from the column and, thus, they do not accumulate and do not slow down the reaction, In general, during these operations, 20–25 g of xylsacrose are formed in a state from which it is easy to obtain pure xylsacrose.
    In contrast to the initially used soluble enzyme, the immobilized enzyme caused the formation of side products during the reaction. A small amount of fructose was formed — less than that produced by the initial extract of the enzyme used for immobilization — probably because the invertase that contaminates the extract is only partially adsorbed by DE 52. were eluted at the last stage of the QEDD with a retention time of 13 and 20 min, although they were not detected when analyzing the reaction products with soluble enzymes. These are probably oligosaccharides formed from common reagents with the help of an enzyme. It is assumed that the retention of reagent molecules by an immobilized enzyme increases
    the time of their contact with the enzyme in such a way that there is a possibility of polymerization.
    Since the xylose content in the substrate is 133 g / l, the maximum possible concentration of xylo-sucrose is 266 g / l. The maximum concentration at 0.086 eq / h is 80% of this value, i.e. JQ 210 g / l, and the calculated data based on xylase consumption during the reaction is 69.5%. The yield is higher than in periodic reactions, since the nature of the flow process with a structural core is such that it causes a constant outflow of the product, and since the product is relatively non-polar compared to the substrate and therefore selectively diverts from the positive of the immobilized substrate, both of these effects contribute to the formation of xylsacrose.
    The same method is used to teach sucrose 6-acetate from 6-aceticate-25 tat glucose, 6-0-methylsaccharose from 6-0-methylglucose, and 6-0-benzylsacarose from 6-0-benzylglucose.
    The enzyme obtained by the method described in Example 1 (0.1 ml) is mixed with 2 ml of a 40% (May / vol) f solution of sucrose and xylose (1: 1), buffered at pH 5.5 at 30 ° C. Xylsaccharose is determined by HPLC. The formation of Levan is defined by 5, visually. Below are the results comparing the effects of various enzymes
    These enzymes according to the invention convert at least 10 times to more xylsaccharose than the enzyme obtained using the Marburg strain, and at least 100 times more when using the enzyme obtained using the NCIB strain J1871. Moreover, the competing education of Levan is much less.
    Use raffinose as a donor.
    Example 6. The formation of xylsaccharose.
    Rafinoza and sucrose are dissolved in McIlvaine buffer (pH 5.4) and incubated with fructasyl transferase from example 1 at 30 ° C until the ph / c analysis shows that xylaxarose and melibiose are no longer formed (approximately 100 hours), then the enzyme 50
    55
    naturing by heating (or alternatively, it can be removed by adsorption to DEAE cellulose). Both the amounts of xylose and raffinose are measured at a total sugar concentration of 30% by weight, and the absolute concentration of sugars at a ratio of refined sugar: xylose 2: 1 (May / May). The highest xylsacarose concentrations obtained during these experiments were 9.5 g / 100 ml with a substrate concentration of 65 g / 100 ml. Then, xylsaccharool is isolated by preparation hp / c, which is the last peak to be eluted, with a time of 15.5 minutes (xylose about 3 minutes, refining and melibiose for about 7 minutes each).
    Example 7. Formation of 6-deoxysucrosis.
    The raffinose and 6-deoxyglucose are reacted as described using the raffinose: 6-deoxyglucose ratio 2: 1 and the total sugar concentration is 30%. After an incubation time of about 40 hours, 4 g of 6-deoxysaccharose per 100 ml of substrate are obtained.
    The results of the studies in examples 1-7 are shown in table,
    权利要求:
    Claims (1)
    [1]
    1. A process for the preparation of fructosyldi-saccharides of the general formula .-
    ASNOON
    NIGHT (CH2OH
    but he but he
     - (i)
    where A is hydrogen or the group CH @ X, X is hydrogen, aliphatic or
    an aromatic carboxy group, or an alkoxy group, or an aryl alkoxy group
    by conducting an aldose reaction of the general formula
    BUT
     V-O
    . he-/
    but he is 1D) I
    1116
    where A has the indicated value defined for formula (II) with sucrose or raffinose in the presence of a glycosyltransferrizing enzyme produced by Bacillus subtilis under optimal conditions of the enzyme, in order to improve the quality of the target product as The glycosyltransfering enzyme enzyme uses fructosyltransferau produced by Bacillus subtilis NCIB No. 11871, 11872 or 1 1873, having a Km for sucrose of at least O, 1 M in the absence of an aldose acceptor that does not form significant amounts of precipitates direct alcohol levan from fructose donor in the absence of an aldose acceptor, and stable to the action of surface-active substances having optimum activity at a temperature of 30 ° C, an active and not less than 20 min at temperatures up to 45 ° C,
    712
    2, the method according to p. 1, about tl and h a tout and with the fact that they use immobilized enzyme.
    Xylsarose, g / ml enzyme per hour
    Levan's education
    8.6 O
    2.9 Visible
    1.4 +
    0.08 ++
    0.19 ++
    - 0.87 ++
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    同族专利:
    公开号 | 公开日
    ES8603577A1|1985-12-16|
    US4617269A|1986-10-14|
    NO842496L|1984-12-27|
    ES533607A0|1985-12-16|
    GB8415877D0|1984-07-25|
    ZA844655B|1986-02-26|
    EP0130054A2|1985-01-02|
    GB2145080B|1987-07-15|
    DK297784A|1984-12-22|
    AT50774T|1990-03-15|
    IE841551L|1984-12-21|
    DE3481514D1|1990-04-12|
    NO162080B|1989-07-24|
    IE58153B1|1993-07-14|
    FI842513A0|1984-06-20|
    DK172955B1|1999-10-18|
    MX7714E|1990-10-09|
    EP0130054B1|1990-03-07|
    PH20732A|1987-04-02|
    AU2957784A|1985-01-03|
    NZ208606A|1988-05-30|
    CA1225348A|1987-08-11|
    PT78770B|1986-06-26|
    EP0130054A3|1987-04-22|
    FI85160B|1991-11-29|
    GB2145080A|1985-03-20|
    FI85160C|1992-03-10|
    NO162080C|1989-11-01|
    JPS6037993A|1985-02-27|
    KR850000434A|1985-02-27|
    PT78770A|1984-07-01|
    DK297784D0|1984-06-18|
    AU578418B2|1988-10-27|
    JPH0777559B2|1995-08-23|
    FI842513A|1984-12-22|
    IL72176A|1989-12-15|
    IL72176D0|1984-10-31|
    GB8316790D0|1983-07-27|
    引用文献:
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    US4309505A|1980-05-19|1982-01-05|Cpc International Inc.|Process for the production of fructose transferase enzyme|
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    NL8701616A|1987-07-09|1989-02-01|Stamicarbon|FRUCTOSYL TRANSFERASE AND PREPARATION OF FRUCTOSE OLIGOMERS THEREOF.|
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    US6518051B1|1991-04-11|2003-02-11|The Trustees Of The University Of Pennsylvania|Saccharide compositions, methods and apparatus for their synthesis|
    US5180674A|1990-04-16|1993-01-19|The Trustees Of The University Of Pennsylvania|Saccharide compositions, methods and apparatus for their synthesis|
    AT225402T|1990-04-16|2002-10-15|Univ Pennsylvania|SACCHARID COMPOSITIONS, METHODS AND APPARATUS FOR THEIR SYNTHESIS|
    US5334524A|1992-05-18|1994-08-02|Solvay Enzymes, Inc.|Process for producing levan sucrase using Bacillus licheniformis|
    JPH07274990A|1994-04-15|1995-10-24|Mitsubishi Kasei Eng Co|Method for purifying cyclic inulooligosaccharide|
    AU759465B2|1998-05-05|2003-04-17|Mcneil Specialty Products Company Division Of Mcneil-Ppc, Inc.|Functional sugar polymers from inexpensive sugar sources and apparatus for preparing same|
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    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    GB838316790A|GB8316790D0|1983-06-21|1983-06-21|Chemical process|LV920525A| LV5135A3|1983-06-21|1992-12-29|Fractionation of fructosylisaccharide|
    LTRP675A| LT2149B|1983-06-21|1993-06-22|FRUCTZILDISACHARIDA RECEIVING BUDGET|
    MD94-0114A| MD127C2|1983-06-21|1994-03-23|Method of obtaining of fructosyldisauharide|
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