• 专利附录
  • 专利说明
  • 权利要求
  • 类似技术
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  • 优先权
    • 专利摘要:
    A liquid chromatography column comprising a uniform gel bed of a high packing ratio, which is produced by a process in which a column is prepared while avoiding imposing an abrupt change of flow rate or pressure on the gel bed during the column packing operation, thereby making it possible to simultaneously improve the elution speed and the durability of the column. The column comprises gels of small grain diameter, thereby exhibiting an excellent resolution. The column also ensures a direct analysis of blood serum.
    公开号:SU1471958A3
    申请号:SU823393025
    申请日:1982-02-11
    公开日:1989-04-07
    发明作者:Ногути Кохдзи；Касаи Масао
    申请人:Асахи Касеи Когио Кабусики Кайся (Фирма)；
    IPC主号:
    专利说明:

    one
    The invention relates to the field of analytical instrumentation and can be used in the chemical, medical, biological and other fields of industry for the analysis

    cm
    complex mixtures of substances by high performance liquid chromatography.
    . The purpose of the invention is to increase the speed of chromatography, the resolution of the column and provide a direct analysis of serum and other blood components.
    FIG. 1 is a graph illustrating the determination of the volume of the eluted peak (V) and the width of the peak (W) for the subsequent calculation of the equivalent height of the theoretical plate of the column; in fig. 2 - chromatogram of vinyladipate (having a purity greater than that of a commercial mixture of tiroglo-99%), 200 g of n-butyl acetate, 6.4 g
    polyvinyl acetate (having a polymerization degree of 500) and 1 g of 2,2-azobisbulin, albumin, myoglobin, and phenylalanine; in fig. 3 is a chromatogram of the separation of normal human isobutyronitrile at 70 ° C for
    which serum; on; FIG. 4 - chromate 15–20 hours in 1.2 l of water containing a gram of separation of human sym.% Polyvinyl alcohol as
    cranks for renal impairment; suspension stabilizer to obtain
    FIG. 5 is a chromatogram of the separation of polydivinyl adipate. Upon completion
    During various polymerization of human serum, the resulting granules, the flow rates of eluent. 20, are isolated by filtration, washed with water, then with methanol and dried. Loading chromate graphical column containing granules into a round bottom flask
    There is a housing with a diameter of 4-50 mm and a length of 2 liters with a capacity of 1 liter of methanol, 100-600 mm, filled with a layer of full-containing 32 g of sodium hydroxide,
    with a porous hydrophilic gel, in 25 the mixture is heated with stirring, the composition of which includes fragments of 40 ° C for 24 hours. After the completion of the reaction, the obtained granules are filtered and washed with menyl alcohol. The gel has a medium-weight granule diameter of 4–20 mm, a water retention value of 0.6–2.0 ml / g, and a concentration of hydroxyl groups of 3–15 meq / g. .
    The gel layer has a degree of homogeneity of 2.0-4.0, which is determined by the ratio of EVTT / Other, where
    Thanol and acetone.
    thirty
    Polyvinyl alcohol granules obtained in this way are loaded into a co-potone flask together with a liquid mixture containing 350 ml of dimethyl sulfoxide, 350 ml of acetone, 37 g
    ETTT 03 is equivalent to 7 heights of 35 pichlorohydrin and 16 g of hydroxide of the theoretical plate of the proposed mixture is heated with stirring in the column, and Dr is the weight-average diameter ™ of P ° for 24 hours. After the granules. The packaging ratio of the termination layer of the granules is filter 0, 66-0.78 and is determined by the formula and washed successively.
    u40 with water and then with acetone. Pop-, where V is the volume of water from the outside of the second time, the operations of the granules of the granules are repeated; V is the total volume of the skin, products and the reaction is similar
    monkey Filling of the column carried out-described by the same method.
    is as follows. Prepares-The resulting granules are heated at
    with gel suspension containing 80 ° C for 24 hours with stirring, 4.0 times the amount of gel that, together with I. n. aqueous solution, necessary for filling the column. The suspension is fed to the loading equipment and then sealed. The apparatus is connected to a column at the ends of which are fitted with filter fittings. Filling the column with a suspension is carried out with a liquid stream, which is fed at a constant rate of 0.2-1.5 m / h in
    50
    sodium oxide, after which the granules are thoroughly washed with water.
    The average diameter of the pellets thus obtained is determined using a Coulter Counter Model ZB (trade name of the instrument manufactured and manufactured by Cowl Electronics Inc., USA). The average diameter of the granules is 12.3 rm, and the value of W is 1.75 ml / g with a volume of 1-300 internal volumes of the co-part of the obtained gel is introduced into the reel. Then the flow rate is increased, providing an average increase in pressure from 2 to 80 kg / cm / h and max |
    an action with acetic anhydride at 90 ° C in a pyridine solvent and when calculating the concentration of hydroxy acid increase in pressure to 60 kg / cm / min.
    After filling, the column is disconnected from the loading equipment and the gel layer is fixed with a filter fitting at the upper end of the column.
    Example 1. A mixture of 80 g of diisobutyronitrile is subjected to suspension polymerization at 70 ° C for
    Thanol and acetone.
    sodium oxide, after which the granules are thoroughly washed with water.
    The average diameter of the pellets thus obtained is determined using a Coulter Counter Model ZB (trade name of the instrument manufactured and manufactured by Cowl Electronics Inc., USA). The average diameter of the reaction with acetic anhydride at 90 C in a pyridine solvent and when calculating the concentration of hydroxyl51D
    gels (Choch) gel from the number of reacted acetic antiplate find that the value of q is equal to
    Oh
    9, I mc / g.
    10 g (dry weight) of the granules thus obtained are immersed overnight in 100 ml of distilled water for swelling. The first end fitting, fitted with a filter with a pore diameter of 5 (u m, at one end of the column with an internal diameter of 7.5 mm and 500 mm length, is mounted, and the other open end of the column is connected to a loading device with an internal volume of 100 ml. The loading device is provided in its upper part with a loading hole for the gel paste and a filling hole for the filling liquid, which is connected to the loading pump with a stainless steel tube, and a pressure gauge. The loading device can be sealed after pouring into it gel pastes. The mentioned gel paste was thoroughly dispersed for 10 minutes using an ultrasonic cleaning machine (Branson B-12 type, manufactured and sold by Branson Cleaning Equipment Company, USA) and poured into the loading device through the loading hole for gel flippers. Then within 60 minutes, I pass distilled water (liquid for filling) through the loading device, and the column with a flow rate of 1.0 ml / min (LS (linear velocity. 1.36 m / h. Then increase the flow rate of distilled water with an average increase in pressure at a rate of 20 kg / cm / h in the gel layer and at a maximum rate of increase in pressure of 20 kg / cm / min. until the gauge shows 85 kg / cm. Then distilled water is passed through for 3 hours, while maintaining the pressure on the pressure gauge of 85 kg / cm% and controlling the amount of a layer of distilled water using a pump. After stopping the passage of distilled water, the column is disconnected from the loading device and a second end fitting, having the same design as the first end fitting, is attached to the open end of the column. So, the column is complete. The resulting column has an EVTT / Du value of 3.3, and a V. / V value of 1.54
    58
    and exceptional1. The molecular weight (counting per dextran) is about 2,000,000.
    An aqueous solution of commercial tyroglobulin, albumin, myoglobin and phenylanine is developed on the resulting column, and 0.05 mol / l phosphoric acid buffer (pH 6.7) is diluted, containing 0.2 mol / ml of sodium sulfate l at a flow rate of 1, 0 ml / min. Substances can be separated very efficiently (Fig. 2), washed out in molecular weight order. The analysis time is only about 20 minutes.
    PRI mme R 2. Load a liquid mixture of 100 g of vinyl acetate, 32.2 g of triallyl isocyanurate (X is a number: 0 0.25), 100 g of n-butyl acetate and 3.3 g of 2.2-azobisisobutyronitrile into a cylindrical flask with a capacity of 2 liters, together with 0.8 liters of water containing 1% by weight of polyvinyl alcohol as a suspension stabilizer, the mixture is stirred until a stable suspension is formed. Then the suspension is heated at 65 ° C for. 18 hours and then at 75 ° C for 5 hours while stirring to conduct slurry polymerization. After completion of the polymerization, the formed granules are filtered off, filled with water and then with methanol and dried. Pellets 35 are loaded into a 3-liter round-bottomed flask together with 2 liters of methanol containing 47 g of sodium hydroxide, and the mixture is heated with stirring at 15 s for 20 hours and 40 to carry out the transesterification reaction (ixation. After this, the classification is carried out in water, gels are obtained (D | .. 9.8 mm, Other / Dp. The obtained gels have a concentration of 45 hydroxyl groups of 7.3 meq / g and a value of W (f 1.58 b / g.
    Then three portions of 7 g (dry weight) are weighed out of the gel. Each of the three portions is immersed overnight in a 0.2 mol / l sodium sulfate aqueous solution and dispersed for 5 minutes using an ultrasonic homogenizer (type US-300, manufactured and sold by Nippon Seiki Saysakupo K. K., Japan). Each of the obtained pastes of the gels was poured into the loading device, which is connected to a forcolon with an internal diameter of 7.5 mm and a length of 100 mm, connected at one end to a main column made of stainless steel with an internal diameter of 7.5 mm and a length of 250 mm, having at the other end, the first end fitting, fitted with a filter, as used in example 1, the forcolon and main column are filled with an aqueous 0.2 mol / l sodium sulfate solution. After sealing the loading device, an aqueous 0.2 mol / l sodium sulfate solution (filling liquid) is passed through the loading device and the column and the main column at a flow rate of 0.5 rii / MHH (LS 0.68 m / h) for 60 minutes using a pump. During this time, the gel paste moves into the main column, while an aqueous 0.2 mol / l sodium sulfate solution is discharged, entraining the gel paste, this solution is used as a filling fluid, through the first end fitting at the bottom end of the main column. thus forming a gel layer in the main column. Thereafter, the flow rate of an aqueous 0.2 mol / l sodium sulfate solution is increased at an average rate of pressure increase of 5 kg / cm / h in the gel layer and at a maximum rate of pressure increase of 5 kg / cm min in the gel layer. until the gauge mentioned in example 1 shows 26, 46 or. 57 kg / cm. While maintaining the indicated pressure reached, the liquid is continued to flow through the column for another 2 hours. After this, the loading device and the forcolon are disconnected, and the second terminal 4 tipping is attached to each column to fix the gel layer.
    The filled columns are tested in relation to both the characteristic properties and practical application with obtaining favorable results. The characteristic properties of the proposed MiK columns are presented in the table.
    , Yu 15 20 25 30 35 40
    5 Q
    five
    All of these columns have an exceptional molecular weight limit (counting on dextran) of about 30,000.
    In column 1, a mixture of commercial y-globulin, albumin from bovine serum, albumin from egg protein and myoglobin is separated, eluted with an aqueous solution with pH 7.0, 0.3 mol / l sodium chloride and 0.1 mol / l sodium phosphate. Each component is allocated approximately 100%. All of these proteins are washed out in molecular weight order.
    In column 2, 100 ml (1 mg) of aqueous 1% by weight ethylene glycol is separated, eluted with distilled water at and at a flow rate of 1.0 ml / min. From the resulting chromatogram, the ESTR is determined. This procedure is repeated 800 times. EVTT values are in the range of 24.5-25.6 mm. The stability of the ECTT can be considered as a demonstration of the long life of the column and the absence of any destruction to it.
    A 0.2 mol / l aqueous solution of sodium sulfate is continuously passed through column 3 at a flow rate of 1.2 ml / min for 240 h, after which the EVEET value is determined to show a positive value of 32.9 mm (EVTT / Other 3 , 36). No column degradation was observed.
    And p). 3. The human serum was separated on the combined columns 1 and 2, which were prepared according to Example 2, eluted at pH 7.0 with an aqueous solution of 0.3 mol / l sodium chloride and O, 1 mol / l sodium phosphate at a flow rate of 1.0 ml / min, using an ultraviolet spectrophotometer at 250 nm (wavelength) as a detector. FIG. 3 shows the chromatogram of normal human serum obtained in accordance with the above procedure, and FIG. 4 shows the serum chromatogram in renal failure. In the same diagram, two chromatograms that were obtained with different sensitivity of the detector are given to show together the main and minimum components of the serum. From these chromatograms it can be concluded that the liquid chromatographic column
    9 14
    According to the present invention, it has excellent resolution (it is capable of substances and that it is particularly useful for the fractionation of mixtures containing many types of dissolved substances, such as blood.
    PRI me R 4. A mixture of 100 g of vinyl acetate, 41.4 g of triphenyl isocyanurate, 70 g of n-butyl acetate, and 3.3 g of 2.2-azobisisobutyronitrile are loaded into the flask, and suspension polymerization is carried out, the re-sterication and classification according to the method of example 2, receive a gel having a value of Other 9.4 mm The gel has a concentration of hydroxyl groups of 7.1 meq / g and a value of W, 1.20 ml / g. 13 g are weighed from this gel and they fill a stainless steel column with an internal diameter of 7.5 mm and a length of 500 mm according to the method of Example 1, a filled column is obtained which has an EVTT / A value. 2.75 and the value of V, - / U „1.55.
    Chromatography was performed on this serum column of a patient suffering from renal insufficiency according to the procedure of Example 2. with the exception that the analysis was carried out at a higher eluent flow rate. FIG. 5 shows a chromatogram obtained at an eluent flow rate of 1.0 ml / min and a chromatogram obtained at an eluent flow rate of 2.0 ml / min. A chromatogram obtained at such a high flow rate of eluent as 2.0 ml / min, which corresponds to 2.72 m / h in drug values, clearly shows the same high resolution as in FIG. 5, i.e. on the chromatogram I obtained at a flow rate of eluent of 1.0 ml / min. Therefore, a column filled in accordance with the pre-invention by the invention provides high-speed high resolution chromatography. In addition, even after using for chromatography 150 serum samples at a flow rate of 2.0 ml / min, the column retains its original resolution and efficiency, which it showed in its preparation. This proves the durability of the columns filled in accordance with the invention.
    Example 5: Suspension polymerization of a mixture of 100 g of vinyl acetate, 32.2 g of triallyl isocyanu is carried out. 10
    rata (degree of crosslinking of 0.25), 40 g of i-butyl acetate and 3.3 g of 2,2-azobisisobutyronitrile, filtered, extracted, transesterified, and classified according to the method of example 2, a gel is obtained having a peel size D 13 mm, Dr / DR 1.32, the concentration of hydroxyl groups of 8.2 meq / g and the value of W
    1.05 ml / g. A gel column thus prepared with an internal diameter of 7.5 mm and a length of 500 mm was filled in by the procedure of Example 1, and a filled column with EBTT / A was obtained. 3.4 and
    , Chromatography is carried out on this filled column with an aqueous mixture of N, N-dimethyl-4,4 -bi chloride. pyridipi (NQ), H-methyl-4- (4-pyridyl) -pyridinium (MQ) and 4-methylpyridinium (MS), this mixture is obtained during the preparation of the agricultural chemical, eluted with aqueous 0.3 mol / l chloride sodium at a flow rate of 1.0 ml / min. Received
    the chromatogram is shown in FIG. 6, where the fractions of the mixture are clearly shown. From this we can conclude that the column, filled in accordance with the proposed 1m invention, also
    effectively applicable to the fractionation and identification of electrolytes of low molecular weight.
    权利要求:
    Claims (9)
    [1]
    1. A liquid chromatography column containing a cylindrical body and a layer of a fully porous hydrophilic gel containing fragments of vinyl alcohol.
    different from that.
    that, in order to increase the speed of chromatro grapho in ani, the resolution of the column and ensure the direct
    analysis of serum and other blood components, the gel has a medium-weight granule diameter of 4–20 mm, a moisture retention value of 0.6–2.0 ml / g, and a concentration of hydroxyl groups of 315 mac / g, and the gel layer has a degree of homogeneity of 2.0 -4.0, determined by the ratio of the equivalent height of the theoretical plate of the column to the weight-average diameter of the granules, and
    packing ratio 0 / 66-0.78, defined by the formula
    where V is the volume of water from the outside of the granules; Vj. - total column volume.
    [2]
    2. Column as claimed in claim 1, characterized in that the gel is made of a viniparboxylate homopolymer or copolymer.
    [3]
    3. A column according to claim 2, characterized in that the copolymer is a copolymer of vinylcarboxylate and the crosslinking monomer contains isocyanurate rings.
    [4]
    A, the column of claim 2, wherein the copolymer is a vinyl carboxylate copolymer and the crosslinking monomer contains a cyanurate ring,
    [5]
    5. Column as claimed in claim 3, characterized in that the crosslinking monomer containing the isocyanurate ring is triallyl isocyanate;
    [6]
    6. A column according to claim 2, wherein the vinylcarboxylate homopolymer or copolymer is made of a monomer containing at least two ester groups of the vinylcarboxylate.
    [7]
    7. The column according to claim 6, characterized in that the monomer containing at least two complex
    five
    the group of vinylcarboxylate, is divinyl adipate.
    [8]
    8. Column PP. 1–7, about which it has a diameter of 4–50 mm and a length of 100–600 mm.
    [9]
    9. A method for filling a column for liquid chromatography, comprising preparing a gel suspension in a solvent containing 1.1-4.0 times the gel needed to fill the column, feeding the gel suspension to the loading equipment, then sealing it, connecting the equipment to the column, at the ends of which are installed fittings with filters, passing the flow of fluid through the loading equipment and the bottom filter of the column to promote the suspension, changing the flow rate of the fluid to regulate the UPA ovochnogo ratio, disconnecting the column from the feed apparatus and fixing, fitting with a gel layer
    5 with a filter at the upper end of the column, characterized in that the fluid flow in the volume of 1-300 internal volumes of the column is passed at a constant speed of 0.2-1.5 m / h, after which the flow rate is increased to ensure an average pressure increase 2 -80 kg / cm / h and maximum pressure increase up to 60 kg / cm / min.
    0
    0
    Ve
    1
    Ve
    FIG. 2
    Fig.Z
    FIG.
    Phi1.5
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    同族专利:
    公开号 | 公开日
    CA1177047A|1984-10-30|
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    DD202626A5|1983-09-28|
    DE3268906D1|1986-03-20|
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    US4416783A|1983-11-22|
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    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    NL6702806A|1966-03-31|1967-10-02|
    US4016149A|1973-09-10|1977-04-05|Research Corporation|Selective removal of albumin from blood fluid and compositions therefore|
    JPS5519243B2|1975-11-27|1980-05-24|
    SE420838B|1975-12-12|1981-11-02|Pharmacia Fine Chemicals Ab|Particle Form Dextrand Derivative Gel for Separation Endam|
    JPS5731925B2|1976-03-09|1982-07-07|
    FR2435284B1|1978-09-09|1984-10-19|Asahi Chemical Ind|
    US4314032A|1978-10-26|1982-02-02|Kureha Kagaku Kogyo Kabushiki Kaisha|Crosslinked polyvinyl alcohol gel|
    DE2926872A1|1979-07-03|1981-01-22|Biotechnolog Forschung Gmbh|System for packing chromatograph columns - using viscous liq. suspension in feed tube to charge column with sintered pad at base and sprung outlet pipe|
    JPS6150256B2|1979-10-06|1986-11-04|Hitachi Chemical Co Ltd|
    JPS648304B2|1979-11-01|1989-02-13|Asahi Chemical Ind|
    US4368275A|1980-06-25|1983-01-11|Asahi Kasei Kogyo Kabushiki Kaisha|Isocyanurate-vinyl alcohol-vinyl ester chromatographic packing|JPH0144725B2|1981-05-18|1989-09-29|Asahi Chemical Ind|
    GB2128099B|1982-10-04|1986-07-02|Varian Associates|Narrow bore microparticle column packing process and product|
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    US5597485A|1988-05-13|1997-01-28|Vilmax S.A.|Process for separating proteins|
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    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    JP56017985A|JPH0140953B2|1981-02-12|1981-02-12|
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