• 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 stable glucose isomerase concentrate, in which the glucose isomerase is dissolved in a concentrated carbohydrate water solution. The invention also relates to a process for the preparation of such a glucose isomerase concentrate, whereby a) a suitable salt is added to the ultrafiltered glucose isomerase solution obtained from fermentation, so as to crystallize the glucose isomerase, b) the solution is cooled so as to promote crystallization of the glucose isomerase, and the crystal mass formed is separated, whereupon, if desired, one or several recrystallizations are performed, and c) a carbohydrate or a concentrated water solution of same is added to the crystal mass obtained, which said mass is dissolved, whereby a stable glucose isomerase concentrate is obtained. The glucose isomerase concentrate according to the invention is used for immobilizing the glucose isomerase on a carrier material in a reactor column.
    公开号:SU1575946A3
    申请号:SU864027042
    申请日:1986-02-24
    公开日:1990-06-30
    发明作者:Юхани Висури Калеви
    申请人:Суомен Сокери Ой (Фирма)；
    IPC主号:
    专利说明:

    This invention relates to biotechnology and concerns a method for producing a glucose isomerase concentrate.
    The purpose of the invention is to increase the activity and stability of the target product,
    The method of producing glucose isomerase is carried out as follows.
    From the producing microorganisms Streptoj.yces rubiginosis ATCC 21175, by the geysis of bacterial cells, a cell-free extract is obtained. its ultrafiltration on a membrane with a permeability of 100,000 dalton., a concentrate with glucose isomerase activity of 200 about .800 IHE / ml is obtained.
    The pH value of the solution is set to B within 5, 7-8, preferably pH 7.
    Cool the solution to 16 ° C or below.
    Ammonium and / or magnesium sulphate is added to the solution in a colic from 50 to 170 g / l. The amount of ata depends on the initial concentration of the glucose isomerase, as well as on the final crystallization temperature. It is preferable that the amount of sulfate added at which the crystallization of glucose isomerase occurs occurs without the oxidation of other proteins.
    The addition of sulphate is preferable to be carried out gradually, so that
    SIL SI U1
    CO 4.
    OE
    s
    The addition of the whole salt takes 2-4 hours. The desired result can be obtained by adding the total amount of salt in one portion, but in this case the size of the isomerase crystals remains large.
    The solution is cooled for several hours to a temperature approaching the freezing point of the particular solution. With the lowest tested sulphate concentration of about + -2 ° C and at the highest concentration, the freezing temperature Delivers + 16 ° C9 cooling can be started either with simultaneous addition of sulphate or after addition of sulphate6 By gradual cooling, the crystallization-cooling effect is achieved. the size of the crystals and in TOMS that cooling reduces the solubility of u, which leads to an increase in yield
    Crystals of the glucose isomerase are separated by precipitating them at the bottom of the tank by filtration or centrifugation in continuous separators.
    A certain crystalline mass is mixed with a dry carbohydrate or its concentrated aqueous solution. At the same time, YaAl glucose isomerase is dissolved to obtain a stable concentrate.
    If desired, crystallization can be repeated and in this case the crystalline mass should be dissolved in a large amount of water with a temperature of 20-30 ° C.
    The amount of water should be such that the activity of the enzyme in the solution is 500-2000 IHE / ml, that is, the amount of water is 4-10 times the crystalline mass.
    The resulting glucose isomerase concentrates are pure, stable, easy-to-use and easily dosed preparations. Their activity can be regulated in the range from 2000 to 5000 IHE / g-preparation.
    The glucose isomerase concentrate preferably contains 30-60 wt.% Water-soluble carbohydrate, 5-17 wt.%, Glucose isomerase, not more than 15 wt.% Ammonium sulfate and / or magnesium and / or buffer pH 6-8 and water.
    Example 1, Streptomyces rubiginosis ATCC 21175 Sowing Culture
    Q
    five
    0
    five
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    five
    0
    fermented in a known manner in a 40cc fermenter. The cell mass is lysed, the cell residue is removed by filtration through conventional silica gel drum filters5 to give 12 tons of filtrate containing gzzhopzoprezomerezu, the filtrate obtained is subjected to ultrafiltration through a PCI ultrafilter PCI (Patterson - Candy Inc) with a permeability of 100,000 daltons to obtain 3000 kg a glucose isomerase concentrate with an activity of 960,000,000 IHE; the filtrate that has passed through the membrane is removed,
    To the concentrate obtained, 120 kg of magnesium sulfate and 300 kg of ammonium sulfate are added. To accelerate the crystallization, the mixture is cooled to 10 ° C. The crystals formed are separated by decantation and the crystallization is repeated by adding 411 kg of water, as well as 17 kg of magnesium sulfate and 1 kg of ammonium sulfate. The crystals are again separated by decanting. By adding 452 kg of water, the crystal mass is dissolved and by adding 1 M ammonia solution the pH of the solution is adjusted to 6.5. The solution is filtered through a plate filter and the crystallization is repeated again by adding 16 kg of magnesium sulfate and 40 kg of ammonium sulfate.
    90 kg of crystalline mass containing 20 kg of enzyme, 3.7 kg of salts, the rest is water, 45 kg of glucose and 45 kg of fructose are added to the crystalline mass, and 20 kg of inverted sugar having a dry matter content of 70 wt.%. As a result receive 200 kg of an enzyme preparation having a composition, wt.% g water 29.2, sugar 52 glucose isomers 1495, magnesium sulfate and ammonium salt 4, 3 „
    Glucose activity in concentrate 4500 IHE / g.
    Example 2. According to the procedure of Example 1, an ultrafiltered enzyme was prepared. To 4000 kg it was added 244 kg of crystalline ammonium sulfate, and then a solution of ammonium sulfate containing 600 kg of salt in 900 liters of water. The solution is cooled to 13 ° C and kept at this temperature for 20 hours. The crystalline mass formed is separated in a Westfalia-Na- separator. The crystals are dissolved in water and the resulting solution is filtered. 51575946
    This gives a 20 L liter filtrate. The crystallization is repeated using 122 kg of crystalline ammonium sulfate in an ammonium sulfate solution containing 300 kg of ammonium sulfate in 460 l of water. The resulting crystalline mass is again separated in the separator. To the 525 kg crystalline mass, the same amount of fructose is added crystalline, then the resulting mass is dissolved with partial isomerization of fructose to glucose. Get concentrate containing
    m
    ten
    wt.%: sugar 50; enzyme 11,2; ammonium sulfate 3, 5; water 35.3. The activity of the glucose isomerase in the concentrate is 3000 IHE / g.
    PRI me R 3. According to the method of Example 1, 4000 l of ultrafiltered enzyme with an activity of 240,000,000 IHE is prepared. The pH was adjusted to 7.0 with a 5% NaOH solution, the temperature was set to 12 ° C.
    To crystallize the glucose omerase in 750 l of water, 500 kg of ammonium sulfate is dissolved and the resulting solution is added over 2 hours at a uniform rate of addition. The resulting solution is cooled to -2 ° C and stirred for 24 hours. In the Westphali separator a-7, glucose isomerase crystals are separated. The yield of crystalline mass is 290 kg with a content of 23.6% by weight of dry matter and an activity of 23,000,000 IHE. 30 kg of sodium chloride and 180 kg of glucose are added to the crystalline mass, the pH of the resulting enzyme concentrate is adjusted to 7.0 by adding a 5% aOH solution, and the glucose is partially insulated.
    Get 600 kg of a stable concentrate of the enzyme, containing, wt.%: Ode 49,7; sugar 30; enzyme 12.8; ammonium ulfate 2, 5 and potassium chloride. The concentration of glucose isomerase in the concentrate is 3400 IHE / g.
    Example 4. According to the method of Example 1, 4000 l of fermentate is obtained with an alcohol content of 240,000,000 IHE. The pH of the solution is adjusted to 7.0, the temperature is 12 ° C by adding the% solution. To fix the glucose isomerase, 50 kg of mmonium sulfate is dissolved in 50 l of water and the resulting solution is added within 2 hours with a uniform feed rate. Crystals of glucose omerase are decanted.
    15
    20
    25
    thirty
    35
    40
    45
    u
    1 t s in e in 5
    tse
    1 tse 0, but su on the wah of the va ei ki 97
    Ta to Wed Wa pr de pr de pr
    the main thing
    50 her pr with ma with
    55 in pr
    what is it
    Get 230 kg of crystalline mass containing 40 wt.% Dry
    five
    0
    five
    0
    five
    0
    five
    substances with an activity of IGU 2300000000.
    115 kg of glucose and 115 kg of fructose are added to the crystalline mass, as well as 50 kg of inverted sugar with a content of 70% by weight of dry matter. Get it. 510 kg of gluco-eisomerase concentrate with content, wt.%: Water 30; sugar (glucose, fructose) 52; enzyme 15.1; ammonium sulfate 2.9.
    Glucose isomerase activity in concentrate is 4500 IHE / g.
    Example 5 According to the procedure of Example 1, an ultrafiltered glucose concentrate is obtained. At 25 ° C to a 0.95 L end of the waste of an isomerase with an activity of 600 IHE / ml, 50 g of ammonium sulfate are added. No precipitate formation is observed at this stage. The solution is cooled for 16 hours at 0 ° C and maintained at this temperature with gentle constant stirring. After two days the crystals begin to precipitate. form and only 2.5 wt.% all further in dissolved form, in the mother liquor. Using a laboratory centrifuge, the crystals are separated from the solution, yielding 56 g of a wet crystalline mass.
    As can be seen from the example, it is possible to crystallize the isomerase at a very low concentration of ammonium sulphate in comparison with the amounts recommended by the literature. At the same time, this example is an example of crystallization only under the action of cooling. In the light of this example, it is easy to understand that if the precipitation under the action of ammonium sulfate is carried out quickly and thereafter immediately, for example after 15 minutes, the
    sediment in the centrifuge, the isomerase remains completely in solution when using a low concentration of ammonium sulphate, but even if the isomerase is precipitated,
    its crystallization is not observed and the benefits of crystallization remain unused. The crystalline mass prepared in accordance with the present example can be dissolved in the same manner as in the other examples.
    The glucose isomerase concentrate produced according to the invention is used to immobilize glucose isomerase on the carrier material of the reactor.
    1575946
    IN THE COLUMN
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    权利要求:
    Claims (2)
    [1]
    Invention Formula
    H
    one . A method for producing a glucose isomerase concentrate comprising a culture | stimulation of the glucose-producing m. of the microorganism Streptomyces rubiginosis ATCCY27575 on a nutrient medium until the maximum activity has been reached, the separation of biomass, the lysis of the cell mass with the production of a cell-free extract, purification and concentration of the extract, about a liter and a fora; and with the fact that, in order to increase the activity and stability of the target product, ultra-
    filtering on a membrane with a permeability of 100,000 daltons to produce a concentrate with an activity of 200–800 IHE / ml. The enzyme is isolated by precipitation with a water soluble salt of magnesium and / or ammonium sulfate in an amount of 50–170 g / l of the concentrate, the mixture is cooled to minus 2 up to plus 13 C, which promotes crystallization, the crystalline mass obtained is separated by decanting, the crystals are dissolved in water and recrystallized one or more times; carbon is added to the crystalline mass
    about
    0
    eight
    [2]
    2. Pop-up method 1, characterized in that the enzyme is isolated from the concentrate by first adding crystalline ammonium sulfate and then a solution of ammonium sulfate as a separator followed by cooling, the resulting crystalline mass is separated and recrystallized by dissolving in water, the resulting solution is filtered and crystalline ammonium sulfate is added and its solution, the resulting crystalline mass is separated and mixed with Lructose,
    The method according to claim 1, wherein the enzyme is extracted from the concentrate by adding magnesium sulfate, ammonium sulfate and cooling, the resulting crystals are separated by decanting and recrystallized by adding water, magnesium sulfate and ammonium sulfate, the pH is adjusted to: 6 , 5 by adding diluted ammonia
    -.
    and recrystallization is carried out by adding magnesium sulfate and ammonium sulfate, and then glucose, fructose and water are added to the crystalline mass to form the desired product.
    Priority points and features:
    06.25.84 pp. 1-3
    06.06.85po n, 1
    06/25/84 - the enzyme is precipitated out
    crystal water and / or Concentration with a water soluble sulfate salt
    solution in an amount that ensures its content in the target product is from 30 to 60 wt.%
    magnesium and / or ammonium in the amount of 50 to 170 g / l, and the mixture is cooled from -2 to
    m3 ° s
    water soluble sulphate salt
    magnesium and / or ammonium in the amount of 50-170 g / l, and the mixture is cooled from -2 to
    m3 ° s
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    同族专利:
    公开号 | 公开日
    FI78117B|1989-02-28|
    FI852270A0|1985-06-06|
    FI78117C|1989-06-12|
    HUT40463A|1986-12-28|
    HU194937B|1988-03-28|
    FI852270L|1985-12-26|
    WO1986000336A1|1986-01-16|
    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    US2773002A|1955-03-31|1956-12-04|Nat Dairy Res Lab Inc|Purification of lactase enzyme and spray-drying with sucrose|
    GB1076750A|1964-09-16|1967-07-19|Takeda Chemical Industries Ltd|Enzyme preparations in liquid form|
    US3413198A|1966-06-30|1968-11-26|Calbiochem|Reagents and method for assaying biological samples|
    DE2038103A1|1970-07-31|1972-02-10|Henkel & Cie Gmbh|Dish-washing concentrates - contg enzymes, stabilised with sugar alcohols, monosaccharides or disaccharides|
    US4077842A|1976-03-19|1978-03-07|Cory Robert Paul|Stabilized glucose isomerase enzyme concentrate|
    US4152211A|1977-08-23|1979-05-01|Novo Industri A/S|Iron containing cell mass glucose isomerase preparation|
    US4237231A|1979-11-13|1980-12-02|Uop Inc.|Method of purifying glucose isomerase and a composition for storing same|
    GB2090599B|1981-01-05|1984-06-13|Novo Industri As|Stabilized plasmin compositions and method for preparation thereof|USRE39497E1|1989-02-16|2007-02-27|Nektar Therapeutics|Storage of materials|
    GB8903593D0|1989-02-16|1989-04-05|Pafra Ltd|Storage of materials|
    US5801022A|1990-08-03|1998-09-01|Vertex Pharmaceuticals, Incorporated|Method of producing a product with crosslinked crystals of thermolysin|
    AU659645B2|1991-06-26|1995-05-25|Inhale Therapeutic Systems|Storage of materials|
    US6309671B1|1995-04-14|2001-10-30|Inhale Therapeutic Systems|Stable glassy state powder formulations|
    US5565318A|1994-09-02|1996-10-15|Pharmacia Biotech, Inc.|Room temperature stable reagent semi-spheres|
    US5593824A|1994-09-02|1997-01-14|Pharmacia Biotech, Inc.|Biological reagent spheres|
    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    FI842549A|FI842549A|1984-06-25|1984-06-25|STABILT GLUCOSISOMERASKONCENTRAT OCH FOERFARANDE FOER DESS FRAMSTAELLNING.|
    FI852270A|FI78117C|1984-06-25|1985-06-06|Process for preparing a stable glucose isomerase concentrate|
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