• 专利附录
  • 专利说明
  • 权利要求
  • 类似技术
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  • 引用文献
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    • 专利摘要:
    CHROMATOGRAFICALLY SECURITY: DISCHARGES OF POSHOLS in the chromatorphic column filled with ion-resin resin particles, in which the subsurface cidcum phase is passed through the chromatographic column, the distinct components are separated, and the distinct components are separated, and the diffuse components are periodically distributed. To improve the separation efficiency, as part of an ion-exchange resin, use is made of a cross-linked sulfonated nojra-cobalt cation-exchange resin with a content of 3.52 di inibbenzene and an average particle size of 0.24), 5 mm, with 95% of the resin particles having sizes in the range of the average particle size, water is used as the mobile phase O), and the solution of the polyols to be separated is introduced into a column with speeds of 0 15-0.6 m / h.
    公开号:SU1126203A3
    申请号:SU752199205
    申请日:1975-12-17
    公开日:1984-11-23
    发明作者:Дж.Мелая Аско；Хямяляйнен Лаури；Рантанен Лассе
    申请人:Суомен Сокери Осакейхтие (Фирма)；
    IPC主号:
    专利说明:

    Invention refers to the methods of chromatographic separation and fractionation of organic and inorganic substances on ion exchange resins.
    A known method for the chromatographic separation of substances in a chromatographic 1ChW column filled with an ion exchange resin, in which a mobile liquid phase is continuously passed through a chromatographic column and a separable mixture of substances DJ is periodically introduced
    However, the method is inefficient, as it is implemented on columns with a diameter of 0.3-1.0 cm.
    There is also known a method of chromatographic separation of polyols, in particular, the separation of sugar from the mass in a chromatographic column filled with particles of an ion exchange resin, in which a mobile liquid phase is continuously passed through the chromatographic column, a separable mixture of polyols is periodically introduced and the fractions of separated components are taken out at the column output | .
    However, the known method does not provide the necessary separation efficiency when using industrial-type columns with a diameter of up to
    3 m and more.
    The purpose of the invention is to increase the efficiency of the separation.
    This goal is achieved in that according to the method of chromatographic separation of polyols in a chromatographic column filled with particles of an ion exchange resin, in which a mobile liquid phase is continuously passed through a chromatographic column, a separable mixture of polyols is periodically introduced and the ion exchange is taken at the outlet of the column the resins use particles of a sulphurized polystyrene cation exchange resin with transverse bonds, a content of 3.5% divinylbenzene and an average of m with a particle size of 0.2-0.5 mm; moreover, 95% of the resin particles have sizes in the range of 25% of the average particle size, water is used as the mobile phase, and the solution is divided into polyols at the rate of 0.150, 6 m / h
    With a large change in the size of the resin particles in the bed, it becomes difficult to achieve a consistent fluid flow. Consequently, further classification of most resins is necessary in order to obtain resins, having particles sorted in size as evenly as practical as possible. The best results, including a good separation of the components, are achieved if 95% of the resin is within ± 25% of a medium-sized particle. The preferred range of average particle size ranges from about 0.5 m to about 0.20 mm.
    Another important factor in achieving uniform flow is the uniformity of the resin particles in the bed. In columns with material consisting of particles, particles of different sizes are classified, for example, concentrated in different zones of the column. It is important that the distribution over zones (delamination) within the spike should be minimal and that the resin particles should be distributed uniformly according to the size of the particles across the column and throughout its length. This is called uniform filling of the column. One way to accomplish this is to thoroughly and strongly backwash the resin layer.
    The mechanical strength of the resin is important, since when used in long columns of certain resins that are weak in their properties, the weight of the contents of the column causes the particles to deform in the layer, which in turn causes disturbances in the flow. If polystyrene resins are used, their strength depends on the content of divinylbenzene. Good chromatographic separation of sugars is achieved with resins containing 2-6% divipibenzene with a depth of resin layer of about 3.5 meters.
    In determining the uniformity of flow, the choice of an appropriate average particle size is also of great importance. Optimum column performance is achieved when the flow rate and temperature, as well as the dry matter content of the feed material, are chosen so that the viscosity and density gradients in the column do not cause
    whether tails and fingers are appearing, but tended to stabilize conditions in the fronts between fractions. This property changes in accordance with the coefficient of distribution of the components in the railway which is subjected to separation. The average size of the particles is chosen according to the distribution coefficient of the components, which should be separated so that the flow resistance in the column is as small as possible, and so that the diffusion of the resin particles does not become a factor controlling the speed in the separation process. If the coefficients are large, a coarse-grained resin may be used. In addition to this, it is important that the optimal permeability of the column and solution used is used. flowed through the column at a positively 1 physical speed of the system.
    In chromatographic (4 separations, the resolution of the 1 "1, which must be separated, depends on the linear flow rate through the column and mainly decreases with increasing speed. The permeability of the system increases with increasing particle size of the resin. It is desirable to achieve as high permeability as possible. in order to achieve industrial production speeds. On the other hand, the flow rates should be Ga / fb low enough to provide a reasonable resolution or separation of the components of the solution. The resolution sets the upper limit of permeability and flow rate through the system. The column syringe ability can be determined from the permeability coefficient and should be determined emtgarically for each system. Permeability coefficient: can be determined using. Equation

    where dP is the pressure drop in the bed
    resin, V - linear flow rate
    solution, m / s; L is the height of the resin bed, m; (U is the viscosity of the solution, K is the permeability coefficient
    1 / M2.
    62034
    Formula (1) is a modification of the so-called Darcy law for flow in a porous medium, where the Reynolds number is below 1. 5 The formation of tails and fingers, which occurs even in fairly uniformly compacted layers and which causes a difference in density and viscosity in solution is avoided or reduced to 1 "minimum if the flow rate is the critical speed (CW) or 0.52 critical speed which depends on the parameters of the system
    5 1 tic speed must be found empirically for a chromatographic system; it depends on the difference in density and viscosity in solution and can be determined by the formula
    0 V g () / 2)
     K ((U, r- {a.) V
    where Vg is the critical speed, m / s S is the specific gravity, t kg / m
    f) - viscosity,
    k - coefficient 1 phony
    layer, g - constant force of tin,
    9.81 m / s.
    The assumption that the viscosity p and the density of the fluid 8 are replaced by the viscosity jlt and density Sf as the flow moves downwards, indices 1 and 2 volts. (2) refer to the upper and lower fluid layer, respectively. 5 In the concentration zones, / which are usually found in large-scale separations of sugars and polyatomic alcohols, the density and viscosity are approximately linearly correlated with respect to concentration. Thus, the following equations are obtained.
    (3)
    Emergency (4)
    | u PC
    where 0 and and are empirical constants;
    C — solution concentration, wt.%; d - the density of water
    jUo is the viscosity of water. Substituting equations (3) and (4) into equation 2, we obtain for the critical speed
    v - (5)
    (Kft
    For separations using large-scale chromatography of sugars and MULTI-VOLUME alcohols in columns having a diameter of more than 1 m and a height of more than 3 m, which are filled with polystyrene dinvine benolic resin with an alkaline-earth form, the coefficient of permeability K is range from liio / to 4x10 1 / m. The permeability coefficient depends on the system parameters, the cross section and height of the resin layer, the size of the resin particle, the distribution of the size of the resin and the type of resin. In addition, when monosaccharides or polyhydric alcohols are separated at 50 ° C, the constants of σ and 3 3 are 4 kg / m in f, 3. n / m2. Thus, the critical speed for separations can be calculated V. 0.5 m / h; 0.3 m / h. The drop in pressure in the drum column is R / t 2000 N / m per meter height of the resin bed. The critical velocity and permeability coefficient relate to stabilization. chromatographic systems. After the backwash operation, the column should be able to stabilize; This is achieved by supplying water to the column until the layer reaches a stable state. The feed intervals are selected by the capacity of malo, but so that the fractionated components do not overlap from one feed to the next. The solids content of the supplied material is improved so that optimal conditions are achieved, taking into account separation performance and quality, as well as the cost of shrinkage and design. The proposed method makes it possible to carry out large chromatographic separations with the same good separation efficiency as in small Laboratory columns. This is achieved using simple and relatively inexpensive devices that are easier to fill with resin, easier to reverse wash and There is little flow resistance, and there are also no significant problems associated with swelling or shrinkage of the resin during the separation cycle or during regeneration. Compared to a battery of small speakers that provide (the same performance, the proposed equipment is less expensive in terms of design and maintenance, requires a reduced amount of accessories, such as pipelines, valves and pumps, and has a significantly reduced setup cost. the method is carried out as a simple chromatographic separation of the material supplied by gravity in the form of a downward flow, in which the feed solution and ale The NTs are fed sequentially to the top of the column. The examples below show the large-scale performance of the column. In each example, only one separation cycle is described. It is clear, however, that in practical use behind the eluent used in the separation, the solution to be treated is followed by KOTO1JL1 eluent follows again. In Example 1, the separation step is 120 minutes, after which the next porous feed is added to the top of the column. In examples 2 and 3, each separation step lasts 160 minutes. In addition, each of the examples was carried out in a column in which the resin was held on a thin mesh screen at the bottom of the column, which in turn was held using a uniformly perforated steel bar. Under the slab was a free zone for collecting the solution that passed through the column. For turbulence free ot-. water solution by gravity at the bottom of the column provides additional funds. Example 1. Ganic (sugar) and inorganic (non-sugar) components were separated from birch wood hydro-lisate by means of xF 4athographic separation techniques, using the following equipment and conditions: column with a diameter of 250 cm, resin layer 350 cm in height; resin - strong sulphurized polystyrene cation exchange resin with 3.5% divinylbenzene, average resin particle size 0.43 mm; the form of Na of all 95% resin particles was within i 25% of the average particle size. Linear feed materials speed of 1 m / h, temperature. Material: 540 kg of dry matter in the form of an 18% aqueous solution. The content of the material is 59% of sugars by dry weight. The column is filled with resin up to a height of 350 cm and the resin is thoroughly backed down to ensure uniform sorting of the resin particles throughout the column. An average resin particle size of 0.43 mn was chosen after evaluating the resin particle size range. Shlbrayin resin particle size provided minimal resistance to the flow of the supplied birch wood hydrolyzate. Both the solution supply and the eluent (water) supply were carried out to the top of the column by spraying fine splashes over the liquid-permeable plate-shaped unit, above the resin bed. Equal to the FLOW was installed throughout the column and maintained throughout the process. "Fractions were withdrawn from the lower part of the column without disturbing the flow uniformity." Column washed with water. Table 1 shows the separation of components. Ilpmiep 2. Glucose and -fructose were separated from an aqueous solution containing both substances using chromatographic methods that use the following equipment and conditions: a column with a diameter of 260 cm, a resin layer 350 cm in height, a resin — sulfated polystyrene is a strong cation-exchange resin with the content of 3.5% divinylbenzene, the average particle size is 0.38 mm Ca form from all the resin particles. 95% was within ± 25% of the average particle size. Linear feed: speed 0.42 m / h temperature. Material: 750 kg of dry matter in the form of a 37.5% military solution. Content of 60.5% fructose and 39.5% glucose dry 8 Permeability coefficient critical rate 0.5. The column is filled with a cream to a height of 350 cm and thoroughly rinsed with a back-flow to ensure uniformity of the resin particle size throughout the column. An average particle size of 0.38 mm is selected after evaluating the range of average particle sizes. The selected particle size of the resin provided minimal resistance to the flow of the feed solution. The solution of the material to be treated and the eluent (water) were fed to the top of the column by spraying fine sprays over the liquid-permeable plate-like unit that overlaps the resin layer. Flow uniformity was established throughout the column and maintained throughout the process. 4 fractions were removed from the bottom of the column without disturbing the flow uniformity. Column washed with water. Table 2 shows the separation of sugar. Example 3: Separate multidimensional alcohols are separated from an aqueous solution containing a mixture of multidimensional alcohols using the equipment described in examples 1 and 2. Assure the following: Permeability coefficient. K 2,6 10. critical speed Vg 0.3 m / h. Resin: Sulfurized polystyrene cationic resin containing 3.5% divinylbenzene, average particle size 0.27 mm, Sr form from all resin particles 95% within 125% average particle size. 1 & 1 line feed: speed 0.50 m / h, temperature +55 C. Source material: 420 kg of dry matter in the form of a 28% aqueous solution. Composition,%: arabinite 4.5, xylitol 77.9, mannitol 3.7, galactitol 3.6,. Sorbitol 8.1, and others 2.2. The column is filled with resin to a height of 350 cm, the resin is thoroughly backwashed to ensure uniform resin particle size throughout the column. The average particle size was 0.27 mm and was selected after evaluating the range of average particle size. The resin of the selected particle size provided minimal resistance to the flow of the feed solution. 9 The treated solution and eluent (water) were fed to the top of the column by spraying small sprays over the liquid-permeable platelets M4 node to the overlapping resin layer. A uniform flow was established across the entire column and maintained throughout the process. Fractions were removed from the bottom of the column without disturbing the uniformity of the 3 stream. The column was filled with water. Table 3 shows the separation of components (given the concentration of the components separated from one fraction, g / ml). The results obtained with the use of a large column are also effective and even better than those obtained with the use of small laboratory columns. Table 1
    one
    2
    3
    four
    five
    6
    7
    eight
    9
    ten
    eleven
    12
    0.3
    0.7
    1, t
    2.3
    3.2
    4.2
    5.2
    1.4
    2.9 7.9 0.1 13.3 6.8
    0.7
    Table 2
    7.5
    10.8
    15.6
    18.6
    19.3
    18.0
    12.9
    7.0
    2.5
    Continued Table 2
    A, 5 2.1 0.9 0.3
    Table 3
    13
    1126203
    14 Continuation of table.
    权利要求:
    Claims (1)
    [1]
    METHOD FOR CHROMATOGRAPHIC SEPARATION OF POLIOLS in a chromatographic column filled with ion-exchange resin particles, in which a mobile liquid phase is continuously passed through a chromatographic column, a separable mixture of polyols is introduced periodically and fractions of separated components are selected at the column outlet, characterized in that, in order to increase the efficiency separation, as the ion exchange resin using particles of sulfonated polystyrene cation exchange resin with cross-links, the content of 3.5% divi nilbenzene and an average particle size of 0.2-0.5 mm, with 95% of the resin particles having sizes in the range of 3.5Z of the average particle size, water is used as the mobile phase, and the solution of separable polyols' is introduced into the column at a rate of .0 15-0.6 m / h
    SU W, 1126203
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    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    US550026A|US3928193A|1975-02-14|1975-02-14|Process for large scale chromatography|
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