• 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:
    Triglyceride oils are degummed according to a two-stage process, in which in the first step a substantially concentrated solution of an acid or an anhydride, having a pH of at least 0.5 as measured at 20 DEG C in a one molar aqueous solution, is dispersed in the oil, and in a second step 0.2 to 5 wt.% of water is dispersed in the mixture obtained and an aqueous sludge is separated from the oil after the water has been in contact with the oil-acid-mixture for at least 5 minutes at a temperature below 40 DEG C.
    公开号:SU786912A3
    申请号:SU762334806
    申请日:1976-03-10
    公开日:1980-12-07
    发明作者:Йохан Рингерс Хендрик；Корнелис Сегерс Якобус
    申请人:Юнилевер Н.В. (Фирма)；
    IPC主号:
    专利说明:

    The invention is intended for use in the oil and fat industry and relates to methods for the purification of triglyceride, preferably vegetable oils, which are liquid with. Such oils, in addition to triglycerides of fatty acids, contain minor components - impurities, for example, dyes, sugars, waxes, free fatty acids, phosFatides. Some of these impurities need to be removed from the oil, which is carried out in the process of multistage refining. One of the most important impurities of oils is phosphatides, which can be divided into two classes - hydratable and non-hydratable. A big problem is the removal of non-hydratable phos-Fatides, since the hydratable are removed by treating the oils with water, followed by separation of the precipitate. Attempts have been made to purify oils with strong mineral or edible organic acids, organic acid anhydrides, detergent solutions, salt solutions, etc. as in diluted, and in not diluted form. But these methods did not provide a sufficient degree of purification, or for various reasons were practically impractical. The most sophisticated to the proposed technical essence is the method of purification of triglyceride oils, which are liquid at 40 ° C, by successive dispersion in oil, first 0.001-0.5% by weight of acid, having a pH in a single water solution of 0.5 to 5 with, or its anhydride, and then 0.2–5 wt.% of water and extracts obtained from 5 minutes to 168 hours, followed by separation of the resulting precipitate. . The known method involves maintaining the temperature of the mixture in the process of aging in the range between 40 and 100 ° C, preferably 60-85 ° C. Under these conditions, the method does not give a satisfactory result if in oils, as is usually the case during storage and transportation, it is already partially Phosphatide content decreased. The purpose of the invention is to increase the degree of purification, reducing the loss of oil and the amount of waste ox.
    To this end, the temperature of the mixture in the process of maintenance is maintained in the range from 0 to 40 ° C.
    Under these conditions, phosphatides are much more completely deduced; the analysis shows that the phosphorus content in the oil after treatment with the method according to the invention is 2.5 ppm, while after processing in a known manner - 46 ppm.
    The treatment agent — an acid or an anhydride — under these conditions is almost completely removed with the sediment and, therefore, the oil does not require rinsing. In addition, the amount of wastewater is reduced.
    Concentrated acid or its anhydride converts the non-hydratable phosphatides into hydratable forms. After adding water at a temperature below, the phosphatides generally transfer to a semi-crystalline phase containing acid or anhydride and water, sugar, glycerol, waxes, and also magnesium or calcium ions bound to non-hydratable phosphatides. After aging, the phosphatides, together with other related components, form a precipitate, which does not adversely affect the metal of the separation equipment and is easily separated. In addition, the proposed method allows the use of smaller amounts of acid and anhydride.
    The removal of phosphatides and other above-mentioned impurities greatly simplifies the subsequent cleaning — neutralization, bleaching and deodorization; one or more of these cleaning steps can generally be omitted.
    Triglyceride oils such as soybean, rapeseed, hemp, sunflower, rice, grape seed oil, coconut, cottonseed, flaxseed, corn, palm, safflower oil, etc. can be treated using the method according to the invention.
    In the proposed method, almost all inorganic or organic acids having a pH from 0.5 to 5 at 20 in a 1 molar aqueous solution, for example, phosphoric, acetic, citric, tartaric, succinic and others, as well as a mixture of acids can be used. Preferably, avoid aggressive or toxic acids, as well as acids that have a strong corrosive effect. It is advisable to use food acids such as acetic acid, tartaric acid, lactic acid, etc., because in this case the precipitate containing this acid may be suitable for animal feed and phosphatides may be used, e.g., for the preparation of food emulsifiers. It is most advisable to use lemon.
    The amount of added acid or anhydride is practically independent of the amount of phosphatides in the oil. It will be almost the same for pre-refined oil containing 0.5 wt.% Of phosphatides and for crude oil containing 2.5 wt.% Of them. The acid is preferably concentrated. Citric acid is usually added in the form of a saturated or close to saturation solution with a concentration of up to 50 wt.%. But less concentrated solutions can also be used, with an acid content of about 10-50% by weight, preferably 30-50% by weight.
    Acid can be introduced into the oil at a temperature of the latter from 20 to higher temperatures do not give a noticeable effect, although temperatures up to 100 ° C and higher can also be used. At low temperatures, more time is required for homogeneous mixing of the acid with the oil with the same degree of purification. After the addition of acid, hold the mixture for the time required for the reaction.
    Normally enough contact for 120 minutes, but if necessary, you can increase the holding time.
    If the acid is added at a higher temperature, the oil should be cooled to a temperature, for example, by passing through a cooler. Low temperatures (up to 0 ° C) can be used if the oil remains liquid at this temperature.
    After cooling the mixture, a small amount of water, preferably distilled or demineralized, is added.
    However, water can be added before cooling. The amount of water is determined based on the need to hydrate the acacides of the phosphatides present in the oil. This amount should not be too large, since a third phase may form, which can lead to difficulties in the subsequent centrifugal separation of the precipitate. Typically, the amount of water content is 0.2-5 wt.%, Preferably 1-2 wt.% Based on oil.
    After mixing water with oil
    the resulting mixture again over the course of time, oscillating
     from 5 minutes to a week (168 hours). Such a long contact time is required when processing pre-refined oil. For crude oils, 5–20 minutes are usually sufficient to form a precipitate.
    It is only necessary that the temperature of the mixture of oil / water / acid be as low as 40 ° C, preferably 25-35 ° C, and the same temperature is separated,
    sediment, preferably by centrifugation.
    At temperatures of high, especially Btaue 50 ° C, the phosphatides transLormify to the mesomorphic lamellum, a phase that is more difficult to separate from the oil. However, to facilitate the separation of the precipitate, it is possible to heat the oil directly before separation to 60-90 ° C, provided that this heating is carried out for a sufficiently short time, for example, not more than 5 minutes, in order to avoid the transfer of phosphatides into the said phase.
    The precipitate of phospholipids also contains many sugar-like substances, glycerin, magnesium and calcium ions, and other minor components originally present in the oil. Acid in the sediment acts as a preservative to prevent biological degradation.
    Further, the oil can be subjected to known purification techniques, during which traces of phosphorus compounds are removed.
    At the same time, the processing of the oil according to the invention provides the following advantages: less amount of alkali during neutralization, cleaner raw materials
    for soap, cleansing water after soap splitting, less need for bleaching earth at the bleaching stage, etc.
    In addition, the treated oils can be stored for a longer time without decomposition and without sedimentation.
    Flushing the oil after processing is not necessary.
    The process may be considered as
    0 intermittently and continuously.
    For example. 1. To the pre-cleaned by washing with water at 70 ° C soybean oil with a temperature of 7.0 C, add 0.3 wt.% Solution
    5 pimonic acid with a concentration of 50%, after a time of contact (20 minutes), the oil is cooled to 20-25 seconds, mixed with water, held in a storage tank for 1 hour and centrifuged. In the first experiment, the oil is added, washed with water and centrifuged again.
    In experiments i and 3, the oil is not washed, then in all three experiments the oil is heated to neutralize 1-2N
    5 night, washed and dried.
    The results of the experiments are given in table.1.
    Table 1
    Additional washing in experiment 1 does not give effect.
    The phosphorus content of the original oil varies to some extent depending on the origin, quality and time of storage of the oil.
    EXAMPLE 2 Lemon-acid is added to pre-fresh, Kiy soybean oil at. Then the oil is cooled to 2O-25 C and mixed with water. After over 168 hours, the oil is centrifuged, then neutralized at 2N or 4N.
    alkali, taken with an excess of 20%, washed and dried.
    The results are shown in table 2.
    table 2
    Lemon solution
    acids (1: 1),
    wt.% by oil 0.3 0.15 0.3
    Water, wt.%
    oil1.0 0.5 .1.0
    Continued table. 2
    20 10 10 60 30 60 Content (phosphorus in the original oil, hours / million 124-99 99 Content of phosphorus in oil,% treated with acid and water, hours / million 22 54 51 Content of phosphorus in neutralized oil, hours / million 3 12 9 The phosphorus content in the neutralized and washed oil, parts / mln. O16 3 Soap lye from the neutralization and water washing stages were combined and decomposed with sulfuric acid. An analysis of acidic water showed that chemical oxygen demand and glycerol content were lower than in acidic water obtained by ordinary cleaning Example 3. In this example, the study The effect on purification of the differences in cooling temperature and the amount of water added is noted .. In all experiments, 0.3 wt.% citric acid solution (1: 1) was added to the previously purified soybean oil at 10 minutes. The oil was cooled to 35 ° C. - 25 ° C and water is added. The mixture is kept for 1 hour and centrifuged. The results are shown in Table 3. Ta.
    Continued table. 3
    holding time after cooling did not affect cleaning. The best results are obtained when KonOpyt 3 time, where 1 wt.% Of water was added to an oil with a temperature of 30 ° C, gave the best result. Example 4. To a crude soybean oil, obtained by extracting soy with hexane and containing 537 ppm of phosphorus, was added 0.3 wt.% Citric acid solution (1: 1) at a temperature, after 15 minutes, the oil was cooled to 20 ° C for 30 min-, then incubated for 45 min or 2 h 45 min; thereafter, 1.5 or 2.5% by weight of water is added to the oil. After the contact time has expired (15 minutes or 1 hour), the oil is centrifuged and the phosphorus content is determined. The results are summarized in table 4. Table 4
    The stroke of water with oil is about 1 hour.
    The amount of water added is also not affected. The phosphorus content in all experiments is obtained.
    The resulting phosphatidic precipitate contains about 5% citric acid.
    Example 5. Experiments were carried out to study the required quantities of citric acid, when an acid solution (1: 1) was added to the extracted soybean oil in different quantities at an oil temperature. After 15 minutes, the oil is cooled to, which takes about 30 minutes. After 2 h, water is added and after the time of contact of the water with the oil (15 or 75 minutes), the centrifugal oil is then washed with water. The results are summarized in table 5.
    Table 5
    When using 0.003 wt.% Solution. Acid, the time of contact of water with oil does not have any effect on the removal of phosphatides; when using 0.01 wt.% acid solution, the best results are obtained with a contact time of 2 hours. From the table Continuation of the table. five
    When 5% by weight of water is used, the amount of phosphatides removed largely depends on the amount of acid added, however at; using 1.5 wt.% water even a 0.03 wt.% acid solution gives an excellent cleaning effect.
    Etc. Measure 6. To the extracted soybean oil with a phosphorus content of 700 ppm, various amounts of citric acid solution (1: 1) are added at. After 15 min, the oil is cooled to 23 ° C. Immediately after cooling, 1.5% by weight of water is added and after soaking for various periods, the oil is centrifuged. The results are summarized in Table 6.
    | Table6
    These also show that calcium and iO ions are consumed together with phosphatides.
    Example 7. To 700 g of grape seed oil is added 0.3 wt.% 65 citric acid solution (1: 1) with
    at an oil temperature, after which the oil is stirred for 15 minutes, 5% by weight of water is added and left for 15 minutes. Oil center and. Sutiat.

    As a result, the initial oil contains ppm: phosphorus 24, wax 8170. The purified oil contains ppm: phosphorus 8, wax 175.
    The example shows that the proposed method also removes most of the waxes from oils with a high content of wax.
    Example 9. 500 g of sunflower oil is mixed with a 0.15% 50% solution of citric sclerothione at or. Stirring is continued for 15 minutes, and then the mixture is cooled to 30 (if
    Example 8. 700 g of sunflower oil are heated to 70 s, a 0.3 wt.% Solution of citric acid (1: 1) is added and stirred. With the aid of a mechanical stirrer at a speed of 600 rpm. The oil is cooled to 5% by weight of water and kept for 1 hour. Then the oil is centrifuged, neutralized and bleached with 1% active clay, after which the wax is removed by cooling the oil to 15 ° C and slowly stirring at this temperature for 4 hours. subsequent filtration. The results are summarized in Table 7.
    Table 7
    the initial temperature was) Launch / add 5% w / w of water with; ;; following stirring for 1 hour and centrifuging.
    The results are given in Table 8. Table 8
    Example 10. Example 9 was repeated, but rapeseed oil containing 131 ppm of phosphorus was used instead of sunflower seed. Results are shown in Table 9.
    Table 9
    Example 11. Example 9 was repeated, but flaxseed oil containing 160 ppm was used instead of sunflower oil. phosphorus. The results are summarized in table 10.
    Table 10
    Example 12. In order to investigate the effect of temperature on the course of the purification process, the following experiments were carried out. To 500 g of crude extracted soybean oil, 0.07 wt.% Citric acid solution (, 1: 1) is added at an oil temperature. After stirring for 15 minutes, 2.5 wt.% Of water is added and
    incubated for 2 hours. The precipitate is removed by centrifugation.
    The results are shown in Table 5.1.
    Table 11
    the whole process at, prices15 trifugation at
    90
    75
    The temperature drops until after adding acid, centrifuging at 30 ° C.
    nineteen
    18
    70
    58
    The temperature is reduced from 70 ° C to after adding water-, centrifuging at 30 ° C 22
    20
    The temperature is reduced from 70 ° C to 30 ° C after the addition of water, centrifugation at 70 ° C 55
    52
    in experiments 3 and 5, before centrifugation, the temperature was increased to 70 ° within 30 minutes, during which time the phosphatides passed into the high-temperature phase, as a result of which they were poorly removed. The phosphorus content in the original oil A was 768 ppm, in oil B - 804 ppm.
    Example 13. To a crude rapeseed oil with a phosphorus content of 201 ppm, 0.1% by volume of an 85% phosphoric acid solution is added,
    ; the oil is then cooled to, G is added, 5% by weight of water and after aging
    . Centrifuge for 1 h. In the purified oil, the phosphorus content is reduced to 62 ppm. After neutral V P.
    t
    .- Ttt ..f h f,
     - 786912
    etion 4 K sodium hydroxide solution, the phosphorus content is reduced to 2 ppm.
    Example 14. To 500 g of crude soybean oil with a phosphorus content of 489 ppm, 0.1 weight is added. acetic anhydride in the form of a solution with a concentration of 97.5%. After stirring for 15 minutes at a stirrer speed of 600 rpm, the mixture is cooled to and 2.5 weight percent is added. water. Then kept under stirring (200 rpm) for another 2 h and centrifuged. The phosphorus content in the oil after purification 46 ppm
    权利要求:
    Claims (1)
    [1]
    1. Paten of Germany No. 1058184, class 23 a.Z, published. 1970 (prototype).
    类似技术:
    公开号 | 公开日 | 专利标题
    SU786912A3|1980-12-07|Method of purifying triglycerine oils liquid at 40 c
    US4280962A|1981-07-28|Methods for refining oils and fats
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    Antoniassi et al.1998|Pretreatment of corn oil for physical refining
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    同族专利:
    公开号 | 公开日
    IN145068B|1978-08-19|
    DE2609705C3|1982-01-28|
    IT1057708B|1982-03-30|
    NO146435C|1982-09-29|
    BE839399A|1976-09-10|
    JPS5949278B2|1984-12-01|
    DK153228B|1988-06-27|
    GB1541017A|1979-02-21|
    US4049686A|1977-09-20|
    NO760789L|1976-09-13|
    DK101076A|1976-09-11|
    DD123892A5|1977-01-19|
    IE42651B1|1980-09-24|
    JPS51112810A|1976-10-05|
    BR7601409A|1976-09-14|
    FI63438C|1983-06-10|
    AU1188476A|1977-08-11|
    LU74523A1|1977-01-11|
    NL168876B|1981-12-16|
    FI760598A|1976-09-11|
    FR2303849B1|1979-04-20|
    ATA168176A|1979-09-15|
    CH617455A5|1980-05-30|
    ZA761405B|1977-10-26|
    YU37357B|1984-08-31|
    IE42651L|1976-09-10|
    FI63438B|1983-02-28|
    CS197206B2|1980-04-30|
    NL7602488A|1976-09-14|
    MX3253E|1980-08-08|
    NL168876C|1982-05-17|
    SE429346B|1983-08-29|
    CA1060041A|1979-08-07|
    SE7603132L|1976-12-17|
    DE2609705A1|1976-09-23|
    PT64880A|1976-04-01|
    DK153228C|1988-11-07|
    DE2609705B2|1980-12-04|
    YU61476A|1983-04-27|
    NO146435B|1982-06-21|
    FR2303849A1|1976-10-08|
    TR19480A|1979-01-22|
    ES445951A1|1977-05-16|
    PT64880B|1978-02-06|
    AT356229B|1980-04-10|
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    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    GB9862/75A|GB1541017A|1975-03-10|1975-03-10|Degumming process for triglyceride oils|
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