• 专利附录
  • 专利说明
  • 权利要求
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    • 专利摘要:
    This invention relates to biotechnology, the continuous conversion of sucrose to isomaltulose, and may be used in the food industry as a sweetener. The purpose of the invention is to increase the yield and purity of the target product. The method involves the enzymatic isomerization of 45-75% sucrose solution by passing it through a reactor with immobilized cells PROTAMINOBACTER RUBRUM CBS 57477 or SERCATIA PLYMUTHICA ATCC 15928 or S.MARCESCENS NCIB 8285 at a temperature of from 40 to 65 ° C. Basically, all cell immobility techniques are suitable for immobilizing cells. Due to the two-step crystallization, up to 91.5% of the isomaltulose present in the solution is obtained in crystalline form. 7 hp f-ly.
    公开号:SU1512489A3
    申请号:SU813335150
    申请日:1981-09-10
    公开日:1989-09-30
    发明作者:Мунир Мохаммад
    申请人:Зюддойче Цукер-Акциенгезельшафт (Фирма)；
    IPC主号:
    专利说明:

    This invention relates to biotechnology and is concerned with the continuous conversion of sucrose to isomaltulose (palatinose, B70-B-glucopyranoside-D-fructose) using immobile bacterial cells.
    Isonaltulose is an intermediate to produce glucopyranoside-1,6-manitol and glucopyranoside-1,6-sorbitol (isomaltite), which are sugar substitutes.
    The purpose of the invention is to increase the yield and purity of the target product.
    In order to implement the method in order to obtain immobilized cells, optimal cell multiplication is carried out in a nutrient medium containing only 5 wt. dry matter.
    The nutrient medium contains a thick syrup (intermediate product of the sugar industry, maize water for swelling and (However, it is preferable to use a cheaper nutrient substrate, which consists only of fodder beet molasses and (III)
    To prepare such a nutrient solution, molasses is diluted with distilled water to a 5% dry matter content. As an additional source of nitrogen and phosphate per 100 kg of this solution, 0.1 kg (No. 4) 4 PRO is added. The pH is adjusted to 7.2 with sodium hydroxide, potassium hydroxide solution or hydrochloric acid.

    CM
    Vaccination of a microorganism, for example, Protaminobacter rubrum CBS 57.77 forming an isomaltulose, is carried out by washing with 10 ml of a sterile nutrient solution of the specified composition and fermentation is carried out in suction flasks filled with 200 ml of this nutrient medium at 29 ° C. When the number of microorganisms in the culture loaded reaches 5x10 microorganisms / ml, the culture is transferred to a small fermentor with the nutrient medium of the specified coagula and further cultivated with the highest possible degree of aeration and mixing speed at 29 ° C. The reproduction control is carried out in the same way. as well as controlling reproduction in shaker flasks, by determining the number of microorganisms. As soon as the number of microorganisms reaches 5x10 microorganisms / ml, the fermenter is released.
    All immobilization methods of I.CUIBATA cells (Immobilized Enzymes, John Wiley and sons, New Jork, London, 1978) are generally suitable for obtaining immobilized cells.
    The following methods are recognized as preferred.
    a) Fermentation contents are added to either the fermenter itself or
    in another vessel with a 1% solution of cationic coagulant. The amount of coagulum required should be determined in preliminary experience. The cell mass subjected to coagulation is asserted, freed from excess water, and then the precipitate is washed twice with phosphate buffer 0.1 N, pH 7.0. After that, the cell mixture is dehydrated to obtain a paste-like appearance, pressed into the cavity, dried, ground and sieved.
    b) O, 5-2, l O, 2-chitosan solution, are added to a 10 l fermentation broth while slowly stirring (the coagulated cell mass is washed with phosphate buffer O, 1 M,
     pH 7.0, dehydrated in a centrifuge. for example, with a chemical principle or in a settling tank, pressed into strips, dried, ground and sieved. wow.
    c) In the centrifuge, the cell mass is separated from the fermentation broth 5-20 g of this cell suspension (dry matter content 10%) is suspended
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    45-60 ml of alginate solution (8 g in 100 ml) are injected and, using a syringe (needle diameter 0.55 mm), are added dropwise to the CaC solution. Appearing granules are mixed for approximately 15 minutes in CaC solution and then washed with water. The granules are dried at room temperature for approximately 20 hours.
    d) In a centrifuge, the cell mass is separated from the fermentation broth, washed with phosphate buffer (0.1 M, pH 7.0) and freeze-dried.
    At 90 ° C under reflux, 15 g of cellulose acetate are dissolved in 100 ml of a mixture of dimethyl sulfoxide and acetone (b:). After cooling to 30 ° C, 3-30 g of sublimated cells are added. This suspension is injected into the water using an injection syringe (0.8 mm needle) as drops. The resulting granules are dried,
    e) In a centrifuge, the cell mass is separated from the fermentation broth. 5 g of this cell mass is suspended in .5 ml of physiological saline solution at 5-50 ° C. 1.7 g of K-carrageenan (soluble sulfuric acid polysaccharide ester) is dissolved in 3 ml of physiological saline at 45-60 ° C. Both solutions are mixed and this mixture is maintained at 10 ° C for 30 minutes. the gel is fixed in a cold 0.3 M solution of KC1 and then split into pieces of about 3 mm.
    f) the fermentation broth is mixed first with a 1% solution of a cationic coagulant and then with an aqueous solution of an anionic coagulant either in the fermenter itself or
    in another vessel. The required amount of coagulants must be determined in preliminary experience. The coagulated cell mass is settled, washed with 0.1 M phosphate buffer, pH 7.0, pressed into strips, milled dried, and sieved.
    Microbial cells obtained by the described methods are subjected to immobilization by stitching. Bifunctional drugs, such as glutaraldehyde, are used for crosslinking. The usual concentration of glutaraldehyde, 2.5-5.0, with a contact duration of min, in the case of the use of isomaltulose microorganisms, may not be observed. It was found that all non-mobile preparations under these conditions are fully immobilized. Glutaraldehyde concentration is taken as the optimal conditions for crosslinking according to the proposed method to 0.1 with a treatment time of 10 minutes.
    The fixed crosslinked cells obtained by the above methods are fed to the reactor column. In this reactor, a uniform temperature is maintained, and the ratio of diameter and height is 1: 1 to 1:20, preferably 1: 1 to 1:10, preferably 1: 1.5 to 1: 5. A pure sucrose solution (concentration of 5-75%) at 40-65 ° C is heated through the column, either from top to bottom or bottom to top. The flow rate is set so that the contact time is 1 - 10 hours, mostly h (this corresponds to 0.2-0.8 g, sucrose, mostly 0.4-0.6 g, per 1 g of immobile (dry) cells at 1 h). When this is completely converted, sucrose is converted, and
    ten
    the cells are washed with 10 ml of a nutrient sterile substrate consisting of 8 kg of sugar syrup, thick, concentration B5%, 2 kg of maize water for swelling, 0.1 kg (NH) ,. and kg of distilled water (if necessary, set the pH value to 7.2). This suspension serves as a seed substance for preculture in a flask with a volume of 1, with 200 ml of the nutrient solution of the indicated composition, which is in the shaking mechanism.
    After a 30-hour incubation at 59 ° C, 16 liters of the nutrient solution of the indicated composition are poured into 20 flasks (4 liters), dispersed in a small 30-liter fermenter and fermented 20 at 29 ° C with aeration of 20 liters per minute and a stirring speed of 350 rpm Increasing cell number is determined by a microscopic method. After the cell number reaches 5x10 cells / ml j the contents of the fermenter are transferred to another vessel in which it is mixed with cationic coagulant (for example, Rohtn Haas PRIMAFLOC C7V,
    )five
    25
    glucose, 4% fructose, B2% isomal-, "Philadelphi, USA). Coagulated
    ln of 4 l. PMJ L /
    tulosis and 13 l-O-oi-D-glucopyranoside-. D-fructose.
    By simply cooling the solution, isomaltulose is partially crystallized. When evaporated and cooled from ma. The additional solution is crystallized with 5 additional amounts of isomalous tulose, thus, in general, the crypt can be removed from the resulting isomaltulose, rounded, washed with phosphate buffer (0.1 M, pH 7.0), and dried in a centrifuge. Next, the mass is extruded into strips, dried in air and ground.
    The sifted fraction of 0.3-0.8 mm from the obtained preparation is stirred for 10 minutes in 0, glutaraldehyde solution, washed with phosphate buffer (0.1 M, pH 7.0) and
    The sieved fraction of 0.3-0.8 mm from the obtained preparation is stirred for 10 minutes in 0, glutaraldehyde solution, washed with phosphate buffer (0.1 M, pH 7.0) and
    91.5% thallize i. . ..., In a preferred embodiment, a solution of sucrose is used to free it from the supernatant of the process by decanting. The definition of the enzyme is allowed through the column to more rapidly the tative activity immobilized so that only the cells are transformed to give a specific activity of .75-80 sucrose. Part of the isomalt-1 60 u / g of dry matter. In thermostaloses, it can be obtained in the crystallized column so much in an immune form by cooling the flow of bilized cells so that the volume of the product layer and the residue after adding the cell mass is 1 bO, see.
    This amount corresponds to 60. g dry matter. The column is then heated with a fresh sucrose solution once again passed through the column. The advantage of this process is that the formation of 1 -O.-c-B-glucopyranoside-Gfructose is suppressed due to the shorter one. contact time and as a result, a greater yield of isomaltulose can be achieved.
     Example. From infecting the strain of Erotaminobacter. rubrum CBS 57.77


    ten
    124896
    the cells are washed with 10 ml of a nutrient sterile substrate consisting of 8 kg of sugar syrup, thick, concentration B5%, 2 kg maize water for swelling, 0.1 kg (NH) ,. and kg of distilled water (if necessary, the pH value is set to 7.2). This suspension serves as a seed substance for preculture in a flask with a volume of 1 L - with 200 ml of the nutrient solution of the indicated composition contained in the shaking mechanism.
    After a 30-hour incubation at 59 ° C, 16 liters of the nutrient solution of the composition indicated are poured into 20 flasks (4 liters), dispersed in a small 30-liter fermenter, and 20 are fermented at 29 ° C with aeration of 20 liters per minute and a stirring speed of 350 rpm The increasing number of cells is determined by a microscopic method. After the number of cells reaches 5x10 cells / ml j, the contents of the fermenter are transferred to another vessel, in which it is mixed with cationic coagulant (for example, PRIMAFLOC C7V from Rohtn Haas,
    )five
    25
    , "Philadelphia, USA). Coagulated

    the cells are decanted, rounded, washed with phosphate buffer (0.1 M, pH 7.0) and dehydrated in a centrifuge. Next, the mass is extruded into strips, dried in air and ground.
    The sieved fraction of 0.3-0.8 mm from the obtained preparation is stirred for 10 minutes in 0, glutaraldehyde solution, washed with phosphate buffer (0.1 M, pH 7.0) and
    . . ... free from supernatant by decanting. The determination of the enzymatic activity of immobilized cells gives a specific activity of 60 units / g of dry matter. So much immobilized cells are introduced into the heat-stabilized column so that the volume of the cell mass layer is 1 bO cm.
     freed from the supernatant by decanting. The determination of the enzymatic activity of immobilized cells gives a specific activity of 60 units / g of dry matter. So much immobilized cells are introduced into the heat-stabilized column so that the volume of the cell mass layer is 1 bO cm.
    50
    This amount corresponds to 60. g dry matter. The column is then heated to 50 ° C and the sucrose solution is continuously passed through it at a flow rate of 20 .. The effluent of the product stream has the following composition, g / 10O g dry substance 55
    Glucose1
    Fructose 4
    Sucrose. ABOUT
    Isomaltulose 82-1-O-O-B-glucopyra-: noisid-B-fructose 13 The resulting isomaltulose solution is fed to a crystallizer for cooling to 20 ° C and the crystallized isomorphulose is separated from the mother liquor by centrifuging on a sieve
    15
    20
    atom drum. The mother liquor is evaporated at 0 ° C to a dry content of 80% and cooled again to 0 ° C in a crystallizer for cooling. The crystallized isomalt-ose is separated from the second masterbatch, solution (molasses) on a centrifuge with a mesh drum. Due to this crystallization step, 1.5% of the crystalline isomaltulose present in the azurer is obtained.
    100 kg of isomaltulose isomaltulose leaving the reactor. It contains 0 kg of water and 70 kg of dry matter, of which S7, kg (82%) is somaltulose. At the first stage of crystallization, 32, kg isomally separated. About 1 kg of wash water is added by centrifuging. 68.6 kg of the stock solution of 37.6 kg of dry matter and 31 kg of the vessel are obtained. In order to concentrate this uterine solution from a content of 5.8% dry matter to a content of 80% dry matter to the second stage of crystallization, 21.6 kg of water must be evaporated, with the amount decreasing by 47.0 kg; end up.
    In the second stage of crystallization, 20.1 kg of isomaltulose is obtained, thus the total yield is 52.5 kg or 91.5% from the α-isomaltulose reactor (corresponding to 75% of sucrose used). Isomaltulose from the first crystallization stage has a purity greater than 99.5% and can be directly used further. Isomaltulose with a second degree of crystallization (20.1 kg) has a purity of more than 96.0% and must be recrystallized. To do this, it is first dissolved in - 13 kg of water and then crystallized out by evaporation and cooling.
    The evaporating amount of water COCY supplies 21.6 + 13 kg to produce 52.5 kg of isomaltulose or 0.67 kg / kg of isomaltulose,
    Example 2, a) 0T of infection of the strain Protaminobacter rubrum CBS .77 cells are washed with 10, ml of sterile 5th nutrient from 6 sy concentrates and 93) 65 kg to ensure that the suspension of the suspension is up to 30 ml hours 29 ° С 1b l of the pyrolysis content (1 l), by fermenting it at 29 ° С the speed of the first
    . Further about example 1 „
    An example of the strain Prota 51,11 is a cell mixture of 1 b5% and 2 parts in a 0.5 g / z zyazhnyh serves in the material for a capacity of 1 l of the solution of the specified 20
    40
    cultivar
    30 The thief is indicated on each 20 flasks hoisted in the farm, and they are altered at speed / min.
    The growing grating capacity of the solution is 300 (see and water from 25%, pure substance at ae rate at 30 ° C and s / min.
    After. l are never going
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    55 laziness 0.2 h
    equal to the quantitative cumulative distance
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    20

    25 so; end up.

    A nutritional solution consisting of 6.25 kg of beet molasses with a concentration of 80%, 0.1 kg (NH) and 93) 65 kg of distilled water (if necessary, the pH value is set to 7.2 using HC1). This slurry serves as a seed for preculture in a 1 L flask with 200 ml of the nutrient solution of the indicated composition contained in the shaking mechanism. After a 30-hour incubation at 29 ° C, a 1-liter nutrient solution of this composition, poured into 20 flasks (1 l), is dispersed in a 30-liter fermenter, and fermented at 29 ° C with aeration of 20 l / min and a stirring speed of 350 rpm
    . The process is then carried out as in Example 1.
    Example From the subculture of the strain Protaminobacter rubrum CBS 51, 11 cells are washed off with 10 ml of a sterile mixture of 1 part syrup concentration b5% and 2 parts of tap water containing 0.5 g / l (NH). This suspension serves as an inoculum for preculture in 1 l flasks with 200 ml of a nutrient solution of a specified composition, sterilized for 20 minutes at 121 ° C, contained in vibrating machines. After 30 hours at
    40
    cultivation
    30 C preliminary cultivation of 6 liters of the nutrient solution of the indicated composition, poured into 20 flasks (total volume t l), is dispersed in a 30-liter fermenter. Fermented at 30 ° C with aeration of 12 l / min and at a stirring speed of 350 rpm.
    The 20 l nutrient solution grown in the fermenter serves as a graft material for a fermenter with a capacity of 300 l with l80 l of nutrient solution (a mixture of syrup with sucrose and water with a dry matter content of 25%, a purity of 9b% calculated on the dry matter), the fermenter operates at a rate aeration 200 l of air / min at 30 ° C and a rotation speed of 200 rev / min.
    After the .7 hour growth phase, add continuously at a dilution rate of 50
    55 laziness 0.2 hour nutrient solution
    and
    an equal amount of the transformed nutrient solution with the cells is continuously removed from the fermenter.
    915
    500 l of this converted solution contains 2 l of cells (wet), which are separated by centrifugation; The concentration of the remaining solution is 23.8% compared with 25% in the initial solution (loss due to blowing out a portion of the dry matter). The amount of solution is 498x1,1001, 8 kg with a dry matter content of 130, + kg with 101.7 kg of isomaltosis. After evaporation to a dry content of 8% at 70 ° C, the solution is cooled to 20 ° C in a crystallizer for cooling. The isomaltulose that crystallizes out is separated by centrifugation from the mother liquor.
    Output. 55.9 kg of isomaltulose with a purity of about 99.0% i
    Evaporation of water in the second stage of crystallization 20, k kg. All isomalt vine (88.3 kg) is recrystallized to increase the purity to a value above 99.5%. For this purpose, it is dissolved in 58.9 kg of water. When reinstallation, then this water needs to be evaporated again.
    Output: 85.5 kg of isomaltulose with a purity of more than 99.5%.,
    Evaporation of water: 385+ -..., 20.4 + 58,, 3, 43 kg per 1 kg of Isomaltulose.
    500 l of the initial solution contains 138.2 kg of dry matter (corresponding to 132.7 kg of sucrose). Thus, the yield of isomaltulose is 64.4% of the sucrose used.
    PRI me R 4. A sifting fraction of 0.3–0.8 mm from the preparation prepared in Example 1 was stirred in a 0.1% solution of glutaraldehyde for 10 minutes, washed with 0.1 M phosphate buffer, pH 7.0, and by decanting free from liquid. The determination of the enzymatic activity of the treated immobilized cells shows a specific activity of 60 units / g of dry matter. The thermostatic column is filled with immobilized cells so that the volume of the cell mass is 16 liters. This amount corresponds to 6 kg of dry matter, Serve the column; heated to 50 ° C and through it continuously pass 50% sucrose solution with a consumption rate of 10 l / h. The product leaving the column has the following composition, g / 100 g dry matter:
    Glucose
    1.4

    248910
    Fructose 4,5
    Sucrose About
    Isomaltulose 81.1 1-0-o (.- B-glucopyranoside-D fructose 13.0
     The resulting solution of isomaltulose is evaporated to a concentration of 80% Q, fed into a cooling crystallizer, cooled before and crystallized isomaltulose on a filter basket centrifuge and detach. poured from the mother liquor. Uterus at 70 ° C
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    5 fall to a concentration of 80% and in a cooled crystallizer again cooled to 20 ° C. The crystallized isomaltulose is separated from the secondary mother liquor (molasses) in a similar centrifuge.
    100 kg of isomaltulose solution leaving the reactor contains 50 kg of dry matter, of which 4Q, 55 kg (81.1%) is isomaltulose. 37.5 kg of water is evaporated to increase the concentration to 80%. At the 1st crystallization stage, 22.9 kg of isomaltulose precipitates and about 0.5 kg of washing water is added during centrifugation. The resulting 40.1 kg of the mother liquor with 27.1 kg of dry matter and 13 kg of water. In order to blast the concentration of the mother liquor from 67.6 to 80% before the 2nd crystallization, 6.2 kg of water must be evaporated.
    At the 2nd crystallization stage, 14 kg of isomaltulose are obtained, so that the total yield is 3b, 9 kg, or 91% of the isomal vine in the reactor (corresponding to 73.8% of sucrose used). Isomaltulose from the 1st crystallization stage has a purity of more than 99.5%, and it can be directly applied further. Isomaltulose from the 2nd crystallization stage (14 kg) has a purity of more than 9b% and needs to be recrystallized. To do this, it is first dissolved in 9.5 kg of water and then crystallized out by evaporation and cooling.
    Accordingly, the amount of water to be evaporated is 37j5 + 6.2 + 3,, 2 kg to obtain Zb, 9 kg of isomaltulose or 1.44 kg / kg of isomaltulose,
    EXAMPLE 5 A sifting fraction of 0.3-0.8 mm from the preparation prepared in Example 1 is stirred in a 0.1% solution of glutaraldehyde in te5.
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    10 min., washed with 1.0 M phosphate buffer, pH 7.0, and freed from water by zincing. Determination of the enzymatic activity of the treated, secret immobilized cells to shows the specific activity of 60 units / g of dry matter. The temperature-controlled column is filled with immobilized cells, so that the volume of the cell mass is 1bl. This amount corresponds to 6 kg of dry matter. Then the column is heated to kQ ° C and 50% sucrose solution is continuously passed through it with a consumption rate of 10 l / h. The product leaving the column has the following composition, g / 100 g dry matter:
    Glucose 2.5 Fructose A, 5 Sucrose 0.6 Isomaltulose 82.5 1 -O-ui-D-glucopyranoside-1) -fruct9.9
    The resulting solution of isomaltulose is crystallized as described in the example scheme.
    From 100 kg of isomaltulose solution, 37, t kg of isomaltulose are obtained (corresponding to a yield of 7.8% based on the amount of sucrose used). The amount of water to be evaporated is 53.2 kg to obtain 37, kg of isomaltulose or 1.2 kg / kg of isomaltulose,
    Example 6: Inoculation of the Serratia plymuthica ATCC 15928 strain was used to wash the cells with 10 ml of sterile nutrient medium consisting of 8 kg of syrup from a sugar plant, 65, 2 kg of water from swelling of corn, 0.1 kg (N1-14) 2НРО and 89.9 kg of distilled water (if necessary, the pH is set at 7.2). This suspension serves as a seed material for preculture in 1 liter shake flasks with 200 ml of the specified nutrient solution. a.
    After incubation for 30 hours with inoculation using 20 flasks (l) of 1 liter of nutrient medium of the indicated composition in a 30 liter fermenter, and fermented with aeration of 20 liters of air / min and at a stirring speed of 350 rpm. An increased number of microorganisms are detected by microscopic
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    chesky method. After at least 5x10 microorganisms have been reached / ml, the fermentation is completed.
    The contents of the fermenter are transferred to another tank (vessel), where they are mixed with cationic coagulant (such as PRIMAFLOC® C7: .. from Rohm and Haas, Philadelphia, USA). The coagulated cells are removed by decanting the supernatant, washed with 0.1 M phosphate buffer pH 7.0 and dehydrated in a centrifuge. The mass is then extruded to form strands, air dry, and grind.
    60 g of the fraction obtained from the obtained preparation, sifted through a sieve of 0.3-0.8 mm in size, are stirred for 10 minutes in a 0.1% solution of glutaraldehyde, washed with 0.1 M phosphate buffer, pH 7.0, and decanted free from supernatant. Determination of the enzyme activity of the thus treated immobilized cells shows a specific activity of 40 units / g of dry matter. The immobilized cells are introduced into a column which is Thermostatically controlled at 5 ° C. The volume of the cell mass layer is approximately 1bO cm. The sucrose solution continuously flows through the columns at a flow rate of 70. The product stream exiting the column has the following composition, g / 100 g dry matter:
    Glucose3,4,
    Fructose5,7
    Sucrose; 1,3
    Isomaltulose 74,4 1-0-p6-B-glucopyranoside-B-fructose 15.2 The resulting solution of isomaltulose is crystallized according to the scheme described in Example 4. From 50 kg of isomaltulose solution, 17.3 kg of isomaltulose are obtained (corresponding to the yield of B9.2 based on the amount of sucrose used).
    PRI me R 7. The sieve fraction of 0.3-0.8 mm from the preparation obtained according to Example 1 is stirred for 30 minutes in 0, cyanuric chloride solution (2,4,6-trichloro-symmm, - triazine), washed phosphate buffer 0.1 M, pH 7.0 and by decanting. release from the supernatant. Determination of the enzyme activity of the immobilized cells thus treated shows a specific activity of 55 units / g of dry matter. The column so incubated at 40 ° C is filled with so many immobilized cells so that the volume of the cell mass layer is 1 B O. This number corresponds to 60 g of dry matter. A 50% sucrose solution is then continuously passed through the column at a flow rate of 30. The product stream leaving the column has the following composition, g / 10O g dry matter:
    ; Glucose2,7
    Fructose3,9
    Sucrose0,7
    Isomaltulose 79.9 1-O-oi-D-glucopyranoside-D-fructose 12.8
    The isomaltulose solution thus obtained is crystallized according to the scheme described in Example 4.
    From 50 g of isomaltulose solution get 17.8 kg of isomaltulose. This corresponds to a yield of 71.2% based on the amount of sucrose used,
    Example 8, From the enzyme solution prepared according to Example 6, a cell mass is obtained using a centrifuge. This cell mass is mixed in 8% sodium alginate solution in a ratio of 1 h, cell mass per 10 h, alginate solution. The suspension thus obtained is passed through dies with a diameter of 0.8 mm in a slowly stirred 2% solution of calcium chloride. When this occurs, calcium alginate granules (pellets) are formed which contain the incorporated bacteria cells. Measurement of the enzyme activity of the granules (balls) shows a specific activity of 87 units / dry matter. In a column heated at 40 ° C, 1 bO cm of granules (balls) is introduced. This amount corresponds to 45 g of dry matter. A 50% sucrose solution is passed through the column continuously at a flow rate of 50. The product stream exiting the column has the following composition, g / 100 g dry, substance: Glucose2.1
    Fructose4,3
    Sakharova2.0
    Isomaltulose 78.3. 1-0-O6-B-glucopyranoside-B-fructose 13.3
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    The resulting solution of isomaltulose.: Crystallized according to the scheme described in example 4,
    14z 50 kg of isomaltulose solution get 17.6 kg of isomaltulose. This corresponds to a yield of 70.4%, based on the amount of sucrose used,
    PRI me R 9. Protaminobacter rubrum CBS 574.77 strain was fermented as in Example 6, the contents of the fermenter were mixed with 2% chitosan solution, while the cell mass was coagulated while being centrifuged, extruded before the strands were obtained. and sit down. Then the mass is ground and sieved. The sieve fraction of 0.3-0.8 mm is stirred for 30 minutes in 0, the solution of cyanuric chloride (2,4,6-tri-chloro-symm, -triazine) is washed with 0.1 M phosphate buffer, pH 7.0, and separated from the supernatant by decantation. The determination of the enzyme activity of the immobilized cells treated in this way shows the specific activity of B5 units / g of dry matter. The column heated to temperature at 40 ° C is filled with so many immobilized cells so that the volume of the cell mass layer is 1bO cm3. This number is equivalent. It produces 50 g of dry matter. The sucrose solution is then continuously passed through the column at a flow rate of 60 cm / h. The product stream leaving the column has the following composition, g / OO g dry matter: Glucose1.3
    Fructose3,2
    Sucrose1,2
    Isomaltulose 80.6 1-0-sh1-b-glucopyranoside-b-fctose 13.7 The resulting isomaltulose solution is crystallized according to the scheme described in example 4.
    From 50 g of isomaltulose solution get 18.1 kg of isomaltulose. It . corresponds to a yield of 72.4% based on the amount of sucrose used,
    PRI me R 10, Overwrite strain Protaminobacter rubrum CBS 574,77 fermented analogously to example 6,,
    The contents of the fermenter are transferred to another vessel, mixed with a coagulant aqueous solution consisting of. cationic coagulant PRIMAFLOCS C7 from Rohm and Haas, Philadelphia;
    15
    USA) and anionic coagulant PRIMAFLOC AIO from Rohm and Haas, Philadelphia CUJA, Coagulated cells are precipitated, decanted, washed with 0.1 N phosphate buffer, pH 7.0, and dehydrated on a centrifugal fuge. The mass is then extruded. In bundles, dried at 30 ° C and milled. 100 g of sieve fraction 0, 8 mm of the obtained preparation is mixed. for 10 minutes in a solution of glutaraldehyde, washed with phosphate buffer (0.1 K, pH 7.0) and free from supernatant by decanting. The treated cells have a specific activity of b5 units / g dry matter.
    Immobilized cells are filled with a column reactor heated to 30 ° C. The volume of the cell mdss layer is approximately 300 cm. The sucrose solution is continuously passed through the reactor at a flow rate of 180. The product stream exiting the reactor has the following composition, g / 100 g dry matter:
    Glucose3, .1
    Fructose 9
    Sucrose 0.8.
    Isomaltulose 81.5
    权利要求:
    Claims (1)
    [1]
    1-0-1, -B-glucopier
    nosido-1) fructose 9,7
    The resulting solution of isomaltulose is crystallized according to the scheme described in Example k.
    From 50 kg of isomaltulose solution get 18.3 kg of isomaltulose. This corresponds to a yield of 73.2% per rose quantity used. ,
    The invention provides the following advantages: a solution containing isomaltulose can be crystallized: 45 thallization without prior evaporation, due to which significant energy savings are achieved; the use of immobilized cells increases the yield of isomaltulose, since caxa-jjo y and also by using immobilized cells included in K-carrageenan gel.
    7. The method according to claim 1, characterized in that immobilized cells are used, which are included in
    fibers of diacetate or tseglulose triacetate.
    rose is not consumed for bacterial mass metabolism; the yield of isomaltulose is further increased due to the fact that pure sucrose solutions are introduced and therefore extensive formation of molasses is avoided; Since sucrose solutions with concentrations above 65% are microbiologically stable, sterilization can be excluded8. The method according to claim 1, characterized in that use immo
    sixteen
    substrate; higher concentration
    -
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    five
    five
    Radios of the substrate can be entered in less. smaller volume and, thus, it is possible to use smaller equipment; an increase in bacterial mass to obtain immobile cells occurs under optimal conditions for development; A cheap nutrient substrate, such as a dilute molasses solution, can be used to prepare the bacterial mass.
    Invention Formula
    1. A method for producing isomaltulose, which involves enzymatic isomerization of a sucrose solution with Protamtnobacter rubrum CBS 574.77 or Serratia plymuthica cells, followed by isolation and crystallization of the target product, characterized in that, to increase the yield and purity of the target product, isomerization is carried out using immobilized cells of cultures of Protaminobacter rubrum CBS, 574.77 or Serratia plymuthica ATCC 15928, or S. maycescens NCIB 8285 by continuously passing a kS 75% sucrose solution through an immobilized cell reactor at itO-65 ° C,
    2 Method of. Section 1, which is distinguished by the fact that immobilized cells obtained by coagulation with glutaraldehyde or cyanur chloride are used.
    3. The method according to claim 1, wherein the immobilized cells obtained by coagulation with cationic coagulant are used.
    4. The method according to PP LZ, I distinguish u and i, that chitosan is used as a coagulant.
    5. Method of pop. 1, different from and using the immobilized cells included in the alginate-calcium matrix.
    6. Method pop.1, differ 8. The method according to claim 1, characterized in that they use immo17151248918
    bilized cells obtained by co-active coagulant or their combination of CT with her anionic or cationic ..
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    同族专利:
    公开号 | 公开日
    DK434981A|1982-04-10|
    AT16406T|1985-11-15|
    US4640894A|1987-02-03|
    DK150310B|1987-02-02|
    DK150310C|1987-09-28|
    IE51455B1|1986-12-24|
    IE811670L|1982-04-09|
    DE3038219A1|1982-04-15|
    ES505364A0|1982-08-16|
    DE3038219C2|1988-05-11|
    ES8206623A1|1982-08-16|
    FI70926C|1986-10-27|
    JPS5794298A|1982-06-11|
    DD201695A5|1983-08-03|
    DE3172822D1|1985-12-12|
    EP0049742B1|1985-11-06|
    EP0049742A1|1982-04-21|
    FI812560L|1982-04-10|
    FI70926B|1986-07-18|
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    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    DE3038219A|DE3038219C2|1980-10-09|1980-10-09|
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