• 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:
    Cellulose-containing material is rapidly saccharified to convert pentosans and hexosans to sugars by cooking under pressure at from 180 DEG C. to 220 DEG C. with acetone-water solvent mixture carrying from 0.05 to 0.25 weight percent of phosphoric, sulfuric or hydrochloric acids. A predominantly cellulosic material, e.g. a delignified pulp, is hydrolysed to yield relatively pure glucose recoverable from liquor which is flowed through the cellulose, then withdrawn and cooled and neutralized within an elapsed time of a minute or less. Whole wood is nearly totally dissolvable by the process, yielding mixed pentoses and hexoses. The dehydration and degradation products of sugars are formed by prolonging retention time of liquor from 20 to 45 minutes.
    公开号:SU1194282A3
    申请号:SU792760902
    申请日:1979-04-27
    公开日:1985-11-23
    发明作者:Паснер Ласло；Чан Пэй-Цин
    申请人:Бау-Унд Форшунгсгезельшафт Термоформ Аг (Фирма)；
    IPC主号:
    专利说明:

    The invention relates to an improvement in the method of decomposing lignocellulosic material from which cellulose can be obtained, avoiding contamination of air and water, and which can be used in chemical-chemical and chemical industry. The purpose of the invention is to prevent the destruction of cellulose and control the degree of hydrolysis of the starting material. Example 1. In table. 1 shows the data that compare the ability of acidified aqueous-organic solvents to dissolve the constituents of cellulose. In particular, a mixture of ethyl alcohol, water and acid and a mixture of acetone, water and acid are compared by their effect on 100 g of aspen and Douglas fir shavings. In each case, 100 g of these shavings, together with 1200 ml of a cooking liquid consisting of water and an organic solvent, taken in a ratio of 50:50, are placed in a pulping apparatus, and two charges are impregnated with a mixture containing acetone, and the other two load - a mixture containing ethyl alcohol. All liquids contain 0-, 07 wt.% HC1 as a catalyst for hydrolysis. The acid is added to a suitable amount of water to the extent that the organic solvent is mixed in, and the volume is brought to the required ratio when mixed with an aqueous solvent in the ratio of 50:50 in order to establish the necessary acid concentration. At the specified time points, samples are taken from the contents of the cooker, and the pressure in the tank is not lowered, and subjected to their analysis. Given in Table. 1 values indicate a higher dissolving capacity of the mixture consisting of acetone and HC1 water, since the complete conversion into Douglas fir pulp, one of the most difficult to process wood, requires only 20 minutes. If ethanol is used as an organic solvent in the cooking liquid then even with the increase. cooking time up to 60 minutes; pulp yield reaches at least 24%. Specified in the table. 1 cooking time includes an initial interval of 5 min, during which 82.22 impregnation and limited hydrolysis occurs, while the cooking apparatus with the contents is heated to the specified temperature on a glycerin bath at. The remaining solid is separated from the cooking liquid, then the organic solvent is distilled off at 60 ° C and the lignin obtained is filtered off from the aqueous ipacTBopa sugar by filtration. Lignin is dissolved in acetone, and it is planted in the form of a light-brown powdery substance by the addition of water. Example 2. The effect of concentration and degree of acid exposure is compared at a constant temperature for aspen using a mixture consisting of acetone and water, with a weight ratio of wood: liquid 1:10 and with a ratio of water and acetone 50:50 and 40:60. All cooking processes are carried out in a solvent mixture consisting of water and ethyl alcohol, with a wood: liquid ratio of 1:10. The amount of sugar and lignin should be understood as the percentage of the yield achieved as a result of the application of hydrolysis. All wood contains a total of 19% lignin, which can be separated, in particular 74% of the separated holocellulose, 56.3% of the cellulose obtained as glucose, and 17.9% of the separated hemicellulose, which consists of 1.9% of mannose and 16.0% of xylose. The indicated values show that increasing the acid concentration from 0.01 to 0.02 M with HC1 does not have or has only a minor effect on the reaction rate constant at a constant reaction temperature and several different ratios of organic solvent: water. With a tripled concentration (0.02-0.06 M), a significant effect is observed, and the effect of increasing acid concentration is compared with the effect of increasing temperature on the rate of hydrolysis. The test results are shown in Table. 2 (initial wood - aspen,%: lignin 19; glucose 56.3; mannose 1.97; xylose 16.0). The breaking strength of the pulp is strongly affected by residual viscosity, i.e. degree 3 polymerization of cellulose after fiber separation. Strong acids, even at a lower concentration, are not specific to Their anti-nodal effect, since they hydrolyze all glucoside compounds in lignocellula, including those that are in the higher order, i.e. they hydrolyze amorphous, mea-morphic and crystalline cellulose. It has been established that when using oxalic acid by a glass or using a strong acid with a neutral salt of this acid in a water-ethanol mixture, the effect of an aqueous organic solvent mixture, which also occurs almost quickly, is achieved as with a mixture of strong acid and solvent, however, cellulose fibers are found in the free state with a significantly better P-value of the degree of polymerization (DP). A significantly higher DP value of cellulosic fiber can be achieved by treatment to remove lignin, over a reduced period of time when an aqueous-organic solvent mixture catalyzed by oxalic acid is used. In addition, the DP-value of the selected fiber is close to the DP-value of the practically non-destructed natural fiber. After the pulp is separated, the pulp is treated as in Example 1. Example 3. Several 5 g loads of crushed and dried aspen and spruce wood in a furnace are heated in a stainless steel cooking apparatus, each with 60 ml of water mixture and ethyl alcohol, taken in a 40:60 ratio. A specific amount of HC1 or oxalic acid is added to each load. The yield and pH of the remaining cellulose are presented in table. 3. The degree of polymerization is determined using iron, tartaric acid and sodium complexes. The ratio of the amounts of wood and liquid is 1:12 when using aspen wood and 1: 8 when using spruce wood, with the exception of cooking 2 spruce wood with HC1, at which ratio the wood: liquid is 1:10. These values show a very large increase in the strength of the plant fibers of these types in comparison with the fibers that are obtained as a result of chemical or bacterial and fungal effects. The strength of paper tapes, laminates, filters, threads, ropes, and accessories from all plants containing fiber is greatly increased as a result of applying the proposed method for separating such fibers. Semi-mechanical or semi-chemical pulps represent a compromise between a high yield in the case of a mechanical pulp, for example. wood pulp, and a very hard chemical pulp, since pulp of better quality with less damaged fibers is obtained when part of the bonding fiber material, namely lignin and hemicellulose, is removed, and the fibrous network is chemically softened to such an extent that only a small breaking load is required to loosen the fibers. An improved pulp of this type is obtained with a smaller yield, but with a higher sheet strength and in a much shorter period of time than necessary. the case of pulping, only as a result of chemical exposure. pulp of very high strength, with low costs and in a very short time, and when using a solvent mixture, which is then made of water, ethyl alcohol and oxalic acid, cooking is carried out separately or continuously. Ltsignin removal and hydrolysis, on. For example, shredded wood, straw, sugarcane or gogassa is carried out at a cellose boiling temperature of approximately 180 ° C, usually in 3-5. min. At this point, the lignocellulose residue, although softened, however, still retains its original structural form, and yet, when mixed in a liquid, the material can easily be processed into fiber dispersion, i.e. into the pulp after it has been passed through one or more high pressure grinders, as a result of which thermomechanical pulp is formed. The lignin content can be as high as 5-6%, while pulp having an extremely high strength is formed. The cooking fluid is treated as in Example 1. To slurry the pulps upon receipt of regenerated cellulose. vines are required, for example, the DP value of bleached pulp is above 800 and the minimum alpha cellulose content is 85%. These requirements are sufficient in the implementation of the proposed method. Example 4. Carrying out several loads of 20 g each from air-dried aspen, spruce and birch wood chips i with a chip size of 2x6x0.8 cm 1, 5 mm, sugar, cane fibers 3x3 mm x 10 cm and wheat straw 10 cm long Each load with an amount of solvent mixture at which the weight ratio of the load and solvent mixture is 1:10 is placed in a stainless steel cooking autoclave. The mixture of solvents contains 60 parts of ethyl alcohol and 40 parts of water and oxalic acid. concentration of 0.05 M, (pH 2.5). In about 7 minutes, the temperature in the cooker is brought to 200 ° C and heated at the specified temperature for a certain period of time. The resulting pulp is then analyzed and its yield, residual lignin content, DP, and the amount of alpha-cellulose are determined. The values obtained are presented in Table. 4. From table. 4 it follows that all the pulps obtained by this method have an alpha cellulose content of more than 85% and can be subjected to three stage bleaching, including chlorination, extraction and treatment with hypochlorite, after which the whiteness of the bleached pulp reaches 88%. The alpha cellulose content is 95-99%. “Example 5. Removing most of the lignin from lignocellular materials such as straw, herbs, sugarcane residues and various hard and soft woods is also useful for increasing digestibility their ruminant animals. However, the costs of lignin removal are so high that such materials cannot compete with conventional livestock feed. In addition, when some known methods of removing lignin are carried out, the residual lignin content changes to such an extent that the residue of lignocellulose is finished in cattle. When using the present invention, the costs of lignin removal are significantly reduced and after boiling for a short period of time, the residual lignin content in the material is less than 5%. The experiments were carried out using in each case 100 g of air-dried aspen, Douglas fir, spruce, bagasse and wheat straw. Each load, together with a mixture of solvents consisting of acetone and water in a ratio of 60:40 and hydrochloric acid with a concentration of 0.02 M, is placed in a stainless steel pulping apparatus. The cooking temperature after heating for 6-7 minutes is different, and the cooking time is different in different cases. Output, residual lignin content and digestibility of dry material are presented in table. 5. From table. 5, it follows that using the proposed method, good cattle feeds from plant materials which cannot be used are obtained, are only limitedly applicable for this purpose. By obtaining such by-products from the cooking liquid as lignin, sugar, and the regenerated solvent, the costs of implementing the Method and the necessary instrumentation are further reduced. The device used is a single stage cooker, and an open vessel is used for impregnating the mixture of solvents at room temperature. The installation consists of a pressure-loaded loading device for Wood Particles, a baffle that is able to maintain a pressure of 35 bar, a heating system, a system for heating under pressure and a system for supplying liquid, a discharge pipe, a cooling and flushing device to the bottom of the centrifuge with a washing device. an evaporator for the regeneration of solvents; a mixer for loading; and a granulating device for pulp. Example 6. A cooking liquor consisting of a mixture of water, ethanol and oxalic acid, promotes fiber separation and has a particular advantage. At elevated cooking temperatures, oxalic acid decomposes to form carbon dioxide and water. In this case, rapid hydrolysis is observed with 0.05 M oxalic acid, which slows down to the extent that it is decomposed so that the fibers are exposed to acid. A series of experiments without lignocellulose are carried out, and oxalic acid is heated used as a catalyst at 200 ° C in a mixture of ethyl alcohol and water, taken in a ratio of 60:40, at an acid concentration of 0.05 M. At intervals of 30 minutes, the pH is measured, samples are taken, the liquid is titrated and residual amount of acids is also determined by a number of other experiments, the applied liquid not containing an organic solvent and in a number of other experiments applied liquid of equal parts acetone and water. Presented in table. 6 values show a progressive and rapidly decreasing acidity of the mixture of solvents over time, and this reduction occurs most quickly in ethyl alcohol and water, and most slowly when using only water. A series of experiments were carried out, during which aspen, spruce and birch wood flakes were heated at 200 ° C in a solvent mixture consisting of ethyl alcohol and water in the ratio of 60:40 and acidified by adding oxalic acid to a concentration of 0.05 M. In tab. 7 shows the pulp yield residual lignin content and DP fiber. I The wood matter loss rate is about 2-8 2.5% over 5 minutes of cooking time after the initial heating time of 7 minutes. Aspen fibers were boiled after boiling for 7.5 minutes, and were eaten after boiling for 8.59 minutes. Small losses during cooking suggest that acid decomposition helps to maintain a high DP-fiber value. Separated cooking liquid is treated analogously to example 1. Example 7. First stage. 10.8 g of air-dry aspen wood chips, freed from extractive substances (humidity 8%), together with a solvent in an amount of 120 ml, made up of acetone and water in a ratio of 60:40, acidified to 0.02 n., Placed s bomb from stainless steel. After sealing, the bomb is quickly heated in a preheated oil bath to 190 C. The preheating time. is 9 minutes, during which the temperature is maintained at the same level. After reaction time, the bomb is rapidly cooled to room temperature and uncorked, then the contents of 4 are lit through filter paper on a Buchner funnel. The undissolved precipitate of the canal is washed with a solvent in potassium (e 30 ml each time. After drying in an oven, 4.31 g of residue is obtained (43.1% of the initial weight). The reaction and rinsing liquids are mixed, the acetone is evaporated under vacuum at. The membrane is dried and dried with a dry dryer, and 1.275 g of light brown powdered lignin is obtained. 100 mg of myosinosaccharide is added to the aqueous filtrate, then sulfuric acid is added to a concentration of 3, then the mixture is boiled for 30 min. reverse flow. The solution is cooled to room temperature, neutralized with a saturated barium hydroxide solution, and the precipitate is filtered off. The bright solution is treated with NaBH overnight and evaporated to dry. The sugar residue is converted to aldiacetate and analyzed by gas chromatography. The total sugar content is It is 3.332 g, of which 31% (1.03 g) is xylose. The second stage is 4.31 g (weight after kiln-dried) of the undried residue from the first stage with 50 np of the same hydrolysis liquid / as. and in the first stage, placed in a bomb made of stainless steel, which is quickly heated in an oil bath to (7 min) and then heated for 15 more minutes. The bomb is then rapidly cooled down to room temperature and its contents analyzed in the same manner as in the first stage. : Get the second stage final products, g:
    Table 1 2 10 Solid residue 0.15 LigninO, 38 Recoverable sugar .2,985 Total balance of trace. The non-hydrolysable residue in the second stage is 0.15 g, 1.50%; lignin in the first stage - 1.257 g, in the second - 0.380 g, 1.637 g, 96.3%; the reduced sugar in the first stage is 3.332 g, in the second 2,985 g, 6.317 g, 76.11%. Total: 8.104 g, 81.04%.
    47.9
    7 10 45.4
    00
    Ethanol
    31.2
    20 28.6
    30 43.5
    7 34.2
    10 15 20 30 15.1
    00
    Acetone 10.4 3.7
    2.4 47.5 7 1.8 42.0 5.85
    and
    o o m
    About SP
    s
    well
    ": about
    at

    SP
    Raw wood
     Kapp number
    15 Note.
    16 Table 5 Use a sample of 25 ml of cooking liquid. OXA - Oxalic acid.
    Birch tree
    权利要求:
    Claims (2)
    [1]
    1. METHOD FOR DECOMPOSITION OF LIGNOCELLULOSE MATERIAL by hydrolysis in an acidified cooking liquid containing 60-40 parts of water and 40-60 parts of an organic solvent - ethanol or acetone and acid as a catalyst, at a temperature of 180-210 ° C and a pressure of c. for 10-60 min, followed by separation of cellulose from the cooking liquid, washing it, distilling off the organic solvent and volatile decomposition products from the cooking liquid, with lignin being precipitated out, condensing the distillation products and obtaining sugars in the residual solution, The reason is that, in order to prevent cellulose degradation and control the degree of hydrolysis of the starting material, the hydrolysis process is carried out while maintaining the pH of the cooking liquid 3.51.7, and if acetone is used, hydrochloric or sulfuric acid is used as the acid, and if ethanol, then oxalic acid is used as the acid.
    [2]
    2. The method according to claim 1, characterized in that the process of hydrolysis of lignocellulosic material is carried out in two stages: on the first, boiling is carried out at 180-210 ° C with a mixture of water - acetone - HC1 or acetone - | £
    Hjso | having a pH of 3.5–2.2, for β 10 min with the separation of cellulose, and | B on the second — boiling. isolated pulp in a solution of water - acetone - with HCl or water - acetone - HjSO |, having a pH of 2 , 2-1.7, for 30 min before the transition of cellulose into solution, followed by distillation from the mother liquors of both stages of the solvent and boiling compounds with the precipitation of lignin and obtaining sugar in the residual solution. ·
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    法律状态:
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    申请号 | 申请日 | 专利标题
    CA285,821A|CA1100266A|1977-08-31|1977-08-31|Organosolv delignification and saccharification process for lignocellulosic plant materials|
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