• 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:
    The invention relates to a non-cariogenic hydrogenated starch for confectionery and process for preparing this hydrolysate. This hydrogenated starch hydrolysate comprises a content of polyols of DP higher than 20 which is sufficiently low for the cariogenic character of these polyols not to be troublesome and a content of low molecular weight products, which is sufficiently low for their presence not to interfere with the applicability of said hydrolysates in confectionery. The hydrogenated starch hydrolysate can be used in the manufacture of "hard candies" and chewing gums.
    公开号:SU1405706A3
    申请号:SU792857803
    申请日:1979-12-17
    公开日:1988-06-23
    发明作者:Верверд Франсуаз；Леле Жан-Бернар；Юшетт Мишель
    申请人:Рокетт Фрэр (Фирма)；
    IPC主号:
    专利说明:

    one
    The invention relates to the food industry, namely to the production of a sweet food additive, which is decayable and does not cause caries.
     The aim of the invention is to reduce the cariogenicity of the hydrogenated hydrolyzate by reducing the content of polyatomic alcohols with the degree of polymerization SP 20.
    Starch, for example, potatoes, cassava, wheat or corn, is diluted, subjected to enzymatic or acid hydrolysis to produce a pre-hydrolyzate at a dextrose equivalent value (GD) of 10-27. The pre-hydrolyzed enzymatic treatment is carried out in two stages at pH 5-6 and 50- 60 ° C. In the first stage, the treatment is carried out with amylase in the amount of 200-1000 international units (MU) per 1 kg of dry starch for 30- 72 hours until reaching DE 46-48 and the formation of maltose in the amount of 35-55%, the second stage, the treatment is carried out with (amylase in the amount of 16000-48000 m, units, per 1 kg of dry starch within 16-30 hours until reaching DE 48-51. In this case, compounds having SP 20 are converted into compounds whose SP constitutes from 8 to 6,
    The resulting hydrolyzate can be additionally hydrolyzed with amylo-1,6-glucosidase mixed with 1-amylase at pH 5-6. and 50-60 ° C for 24-48 hours, amylo-1,6-glucosidase and (3- amylase) are taken in an amount of 120-400 and 50-100 m, unit. per 1 kg of dry starch. At the same time, amylo-, 6-glucidase converts compounds that have a higher SP value, into compounds which smaller molecules can interact with p-amylase. The hydrogenation of the final hydrolyzate is carried out in the presence of a Rane nickel catalyst,
    Malt extract is used as the source containing p-amylase. The source of (o-amylases are products obtained from Bacillus subbilis or Bacillus Licheniformis. The amount of polyatomic alcohols with SP 20 in hydrogenated hydrolysis of atoms does not exceed 3%, which reduces its cariogenicity.
    Example 1, 12l of starch milk containing 33% dry matter



    0
    five
    0
    five
    diluted with acid to achieve a DF of 22.0, the mixture obtained in a twenty-liter tank at 55 ° C is adjusted to a pH value of 5.65. Malt extract resulting from acid hydrolysis is introduced into the preliminary hydrolyzate at a rate of 264 m, yd, / 3 - amylase per 1 kg of dry starch. The rate of enzymatic treatment at this stage is controlled by regular sampling to obtain the most stable value of DE 47.0, Processing time / 5-amylase for 36 hours,
    In the second stage, o-amylase at the rate of 29,500, per 1 kg of dry starch, is introduced into the hydrolyzate without changing the pH and is kept for about 28 hours with an AED of 50.7 and the number of polysaccharides having SP 20, 1.5%. The percentage ratio of polysaccharides the obtained hydrolyzate is given in, IT a l and c a 1
    Hydrogenation of the hydrolyzate is carried out in the presence of a Rane nickel catalyst,
    3 14057064
    The results of the study of such a hydrolytic ester to the cariogenicity of the resultant hydrogenated product. listed in table 2.
    Table 2
    Comparative 7.65 7.50 7.40 7.30 7.30
    Hydrogenated according to Example 1 7.65 7.45 7.30 7.05 6.70 6.55
    The difference in pH f at the beginning and end of the study corresponds to the requirements for the hydrogenated hydrolyzate. Hydrogenated hydrolysis is used to make caramel candies with aromatic additives, citric acid, and yellow dye. The mixture is heated to and cooked under vacuum at 170 ° C and a pressure not exceeding 9 bar. Then the mixture is cooled at, formed into a ribbon, molded and cut into pieces with a diameter of 2 cm and a thickness of about 0.5 cm. The resulting candy is hard, brittle, does not respond to karyogenicity, does not lose when compared to taste with candies made similarly, but using sucrose.
    Example 2. 12 l of starch milk containing 33% of dry substances is subjected to enzymatic fy hydrolysis (/ -amylase produced by Bacillus subbilie to reach DE 18.0. The pH value is adjusted to 5.5 and the temperature to 55 C. at the first stage of the enzymatic treatment, the preliminary hydrolyzate is injected (J-amylase) at the rate of 440 ppm for 1 kg of dry starch and incubated for 40 hours until DB reaches 48.0. Then 22100 ppm is introduced for 1 kg of dry starch. (-amshtase, which interacts at 55 ° C for 24 hours. The amount of polysaccharides with SP 20, determined by molecular ita, 2%.
    For additional hydrolysis of the obtained hydrolyzate, amylo-1,6-glucosidase and -amylase are introduced in the amount of 220 and 80 m units, respectively, per 1 kg of dry starch at pH 5.5 and. After 24 h DE 50, and
    7.30
    the number of products with SP 20, 0.5.
    The carbohydrate distribution of the hydrolyzate obtained in example 2 is given in table 3.
    Table3
    55
    Hydrogenation of the hydrolyzate is carried out according to Example 1. Hydrogenated hydrolyzate is used to make chewing gum instead of glucose. With this, grinding and rolling of the chewing gum is facilitated. When testing for accelerated aging by hot treatment with alternation of low and low humidity, surface recrystallization is not observed. Gum has a pleasant taste and texture,
    EXAMPLE 3, The method is carried out as in example 1, but with the enzymatic treatment of the pre-hydrolyzate, pH 5, temperature. At the first stage, the treatment is 200 m. -amylases within 30 hours before reaching DE 46. In step two, the amount of o (-amylases is 16000, time 16 hours and DE 48. The results are similar to example 1 "
    Example 4. The method is carried out as in Example 1, but when processing a pH of 6, a temperature of 60 ° C, / -amylases take 1000 ppm, its exposure time is 72 hours to EUT 48, 48000 are introduced with / -amylases honey. The treatment is carried out within 30 hours before DE 51. The results are similar to example 1,
    EXAMPLE 5 The method is carried out with PS as described in Example 2, but additional processing is carried out at pH 5 and 50 ° C for 24 hours. Amylo-1,6-glucosidases and α-amylases take 120 and 50 mU. correspondingly, naturally. Results are the same as for example 2.
    Example 6. The method was carried out as in Example 2, but at pH 6 and for 48 hours, with 400 and 100 ppm, amylo-1,6-glucosidase and -amylase, respectively. When changing the parameters downwards for the proposed -. The limits of the content of polyhydric alcohols increase and the cariogenicity of the hydrogenated starch hydrolysis increases. Exceeding the specified parameters is impractical due to the cost of the process.
    0
    Thus, the invention allows to reduce the cariogenicity of the hydrolyzate by reducing the content of polyhydric alcohols with SP 20,
    权利要求:
    Claims (1)
    [1]
    1. A method of producing hydrogenated starch hydrolyzate, which involves acidic or enzymatic hydrolysis of starch to DE 10-27 to produce a preliminary hydrolyzate, its enzymatic treatment using s-amylase and amylase, and subsequent hydrogenation of the resulting hydrolyzate, characterized in that reducing the karyogenicity of the hydrolyzate by reducing the content of polyhydric alcohols c, the enzymatic treatment of the pre-hydrolyzate is carried out at pH 5-6 to a temperature of 50-60 ° C in two stages, and processing the first of which are born in amylase for 30-72 h to achieve. DE 46-48, and on the second - I-amylase for 16-30 hours until reaching DE 48-515, i-amylase is taken in an amount of 200-1000 and (/ -amylase in an amount of 16000-48000 international units (my ,) per 1 kg of dry starch, and hydrogenation is carried out in the presence of a Rene nickel catalyst.
    5 2, the method according to claim 1, about tl and h and yu and the fact that before hydrogenation the hydr olysate is additionally hydrolyzed with amylo-1,6-glucosidase mixed with 0-amylase at pH 5-6 and temperature 50-60 C for 24-48 h,
    moreover, amylo-1,6-glucosidase and-amylase are taken in the amount of 120-400 and 50-100 m. units, per I kg of dry starch.
    five
    0
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    同族专利:
    公开号 | 公开日
    ES486744A1|1980-06-16|
    US4279931A|1981-07-21|
    FI66111C|1984-09-10|
    AU5364479A|1980-06-19|
    ZA796660B|1981-06-24|
    IE792322L|1980-06-11|
    DK153892B|1988-09-19|
    ATA781079A|1982-12-15|
    NO150161B|1984-05-21|
    CH643119A5|1984-05-30|
    NZ192337A|1981-12-15|
    CA1142108A|1983-03-01|
    AU526729B2|1983-01-27|
    AT371835B|1983-08-10|
    JPS626580B2|1987-02-12|
    DE2949783A1|1980-06-19|
    BE880500A|1980-06-10|
    NL7908900A|1980-06-13|
    NL190932B|1994-06-01|
    IT1194899B|1988-09-28|
    GB2038832B|1983-05-11|
    MX6371E|1985-05-22|
    NL190932C|1994-11-01|
    JPS5586802A|1980-07-01|
    FR2444080B1|1983-07-22|
    SE450076B|1987-06-09|
    IT7941663D0|1979-12-11|
    DK526379A|1980-06-12|
    DE2949783C2|1988-11-17|
    GR69881B|1982-07-20|
    HU185610B|1985-03-28|
    FR2444080A1|1980-07-11|
    SE7910191L|1980-06-12|
    FI66111B|1984-05-31|
    GB2038832A|1980-07-30|
    NO794035L|1980-06-12|
    FI793877A|1980-06-12|
    IE48712B1|1985-05-01|
    引用文献:
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    RU2671467C2|2013-10-02|2018-10-31|Юнайтед Стейтс Джипсэм Компани|Method of preparing pregelatinised, partially hydrolysed starch and related methods and products|
    US10399899B2|2012-10-23|2019-09-03|United States Gypsum Company|Pregelatinized starch with mid-range viscosity, and product, slurry and methods related thereto|
    US10464847B2|2012-10-23|2019-11-05|United States Gypsum Company|Pregelatinized starch with mid-range viscosity, and product, slurry and methods related thereto|
    US10875935B2|2012-10-23|2020-12-29|United States Gypsum Company|Method of preparing pregelatinized, partially hydrolyzed starch and related methods and products|US26959A|1860-01-24|Zachariah walsh |
    US2891869A|1953-06-03|1959-06-23|Staley Mfg Co A E|Process for preparing starch syrups|
    US2822303A|1956-06-08|1958-02-04|Anheuser Busch|High d. e. syrup and method of making same|
    US3067066A|1958-11-03|1962-12-04|Anheuser Busch|High fermentable non-crystallizing syrup and the process of making same|
    US3137639A|1962-04-30|1964-06-16|Staley Mfg Co A E|Method of producing starch conversion syrups|
    NL137813C|1963-05-06|1900-01-01|
    US3492203A|1965-07-08|1970-01-27|Hayashibara Co|Extraction of beta-amylase from wheat bran|
    US3708396A|1968-01-23|1973-01-02|Hayashibara Co|Process for producing maltitol|
    JPS567665B1|1969-01-24|1981-02-19|
    US3644126A|1969-05-26|1972-02-22|Standard Brands Inc|Method of making a starch conversion syrup|
    CA973492A|1970-10-27|1975-08-26|Jiro Ito|Production of new amylases by cultivation of streptomyces and uses of these new amylases|
    JPS5853948B2|1979-06-30|1983-12-02|Eidai Co Ltd|US4405600A|1979-06-07|1983-09-20|University Patents, Inc.|Methods and materials for prevention of carious degradation of teeth|
    FR2459002B1|1979-06-15|1983-04-15|Roquette Freres|
    GB2079129B|1979-09-24|1984-08-30|Life Savers Inc|Sugarless coating for comestibles and method|
    US4448778A|1981-08-03|1984-05-15|Ici Americas Inc.|Maltitol containing gel base systems|
    US4357314A|1981-01-05|1982-11-02|Ici Americas Inc.|Maltitol containing toothpaste|
    US4471001A|1981-08-03|1984-09-11|Ici Americas Inc.|Edible maltitol containing gel base systems|
    US4381318A|1981-01-05|1983-04-26|Ici Americas Inc.|Maltitol containing gel base systems|
    JPS632439B2|1981-02-12|1988-01-19|Hayashibara Seibutsu Kagaku Kenkyusho Kk|
    US4508713A|1981-03-27|1985-04-02|Nabisco Brands, Inc.|Method of reducing dental caries|
    US4457921A|1981-03-27|1984-07-03|Nabisco Brands, Inc.|Method of reducing dental caries|
    FR2504783B1|1981-05-04|1983-07-22|Roquette Freres|
    AT379292B|1982-03-12|1985-12-10|Nabisco Brands Inc|METHOD FOR PRODUCING A NEW FOAMED SUESSWARE|
    EP0161244A4|1983-11-04|1987-11-30|Gen Foods Corp|Sweetener composition, process for making the same, and comestibles comprising said sweetener composition.|
    US4528206A|1983-12-20|1985-07-09|Howard Kastin|Hard candy composition|
    US4597981A|1983-12-20|1986-07-01|Howard Kastin|Soft candy composition|
    FR2559033B1|1984-02-07|1987-03-27|Roquette Freres|SUGAR-FREE ICE CREAM AND ITS PREPARATION METHOD|
    US4671961A|1984-05-18|1987-06-09|Wm. Wrigley Jr. Company|Chewing gum compositions and methods of preparation|
    US4671967A|1984-05-18|1987-06-09|Wm. Wrigley Jr. Company|Carbohydrate syrups and methods of preparation|
    US4816445A|1984-06-21|1989-03-28|Kabushiki Kaisha Hayashibara Seibutsu Kagaku Kenkyujo|Crystalline alpha-maltose|
    GB2166637A|1984-10-04|1986-05-14|Powell & Scholefield Limited|Drink concentrate|
    FR2575180B1|1984-12-20|1987-02-06|Roquette Freres|HIGH MALTITOL CONTENT, USES THEREOF AND PROCESS FOR PRODUCING THE SAME|
    FR2575038B1|1984-12-21|1990-03-16|Roquette Freres|SUGAR-FREE CHEWING GUM AND MANUFACTURING METHOD THEREOF|
    US4774094A|1985-03-29|1988-09-27|Nabisco Brands, Inc.|Stabilized APM in comestibles|
    US4840807A|1987-08-24|1989-06-20|Sanmatsu Kogyo Kabushiki Kaisha|Branched dextrin production and compositions containing same|
    JP2556718B2|1987-12-24|1996-11-20|明治製菓株式会社|Method for producing high-pressure gas-filled candy|
    US4959225A|1988-10-28|1990-09-25|Warner-Lambert Company|Synergistic sweetening compositions containing chlorodeoxysugars and maltitol and methods for preparing same|
    US4935243A|1988-12-19|1990-06-19|Pharmacaps, Inc.|Chewable, edible soft gelatin capsule|
    US4963359A|1989-01-30|1990-10-16|Plough, Inc.|Non-cariogenic confections|
    AT145407T|1991-02-20|1996-12-15|Pfizer|REDUCED POLYDEXTROSE|
    GB9117617D0|1991-08-15|1991-10-02|Cerestar Holding Bv|Process for the production of hard candy|
    FR2688792B1|1992-03-19|1994-06-10|Roquette Freres|HYDROLYSATE OF STARCH HYDROGEN HYPOCARIOGENE, PROCESS FOR THE PREPARATION AND APPLICATION OF THIS HYDROLYSAT.|
    DE69403356T2|1993-02-16|1997-11-20|Roquette Freres|Sweet syrup based on maltitol, sweets made with the help of this syrup and the use of an agent for regulating the crystallization process in the manufacture of these products|
    US5637313A|1994-12-16|1997-06-10|Watson Laboratories, Inc.|Chewable dosage forms|
    US6919446B1|1998-01-20|2005-07-19|Grain Processing Corp.|Reduced malto-oligosaccharides|
    WO1999036442A1|1998-01-20|1999-07-22|Grain Processing Corporation|Reduced malto-oligosaccharides|
    US6780990B1|1998-03-26|2004-08-24|Spi Polyols, Inc.|Hydrogenated starch hydrolysate|
    US6380379B1|1999-08-20|2002-04-30|Grain Processing Corporation|Derivatized reduced malto-oligosaccharides|
    CA2352269A1|1999-10-20|2001-04-26|Grain Processing Corporation|Reduced malto-oligosaccharide cleansing compositions|
    WO2001028325A2|1999-10-20|2001-04-26|Grain Processing Corporation|Compositions including reduced malto-oligosaccharide preserving agents|
    US7026008B2|2001-09-13|2006-04-11|Spi Polyols Inc.|Stable sugar-based hard candy having high index of whiteness|
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    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    FR7834830A|FR2444080B1|1978-12-11|1978-12-11|
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