• 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:
    Ash-containing solids are separated from coal liquid by mixing alcohol with said coal liquid, followed by a solids-liquid separation step.
    公开号:SU791256A3
    申请号:SU782605853
    申请日:1978-04-03
    公开日:1980-12-23
    发明作者:Л.Карр Норман；Л.Макджиннис Эдгар
    申请人:Галф Рисерч Энд Дивелопмент Компани (Фирма)；
    IPC主号:
    专利说明:

    (54) METHOD FOR CLEANING COIL LIQUID PRODUCT
    one
    The invention relates to methods for purifying products obtained from coal liquefaction, and can be used in the chemical industry.
    A known method of purification of coal liquefaction products 5 obtained by hydrogenation from solid particles by mechanical separation
    one.
    However, suspended particles 10
    The ashes are very small, some have submicron dimensions, and therefore it is very difficult to remove them from liquid products.
    Closest to the present invention is a method for cleaning coal liquefaction products 5 from solid particles by mechanically separating the latter. As a result, the liquid hydrogenation products are divided into desired products and a stream containing a concentrate of solid particles 2j.
    However, the speed of cleaning products is insufficient. .
    The purpose of the invention is to increase the speed of cleaning products.
    The goal is achieved by the fact that in the method of cleaning coal liquefaction products from solid particles by mechanically separating the latter into the raw material before separation of the particulate matter
    Particles are added portionwise 0.0515.0% by weight of aliphatic alcohol, which forms a homogeneous mixture with the feedstock, with intervals between portions 0, min.
    Preferably, isopropyl, primary, secondary, tertiary butyl alcohol is used as the alcohol. In addition, the interval between the last portion of alcohol and the separation of solids is 0.5-180 minutes.
    The rate of extraction of solids increases significantly with batch addition of alcohol than with a single addition. Before adding alcohol, the temperature of the feedstock should be 38371 ° C, preferably 6-316 ° C and 204-288 ° C. After adding each portion of alcohol, the feedstock is thoroughly mixed to obtain a homogeneous composition in the liquid phase. With additives of portions of mouth, the raw materials to be cleaned are kept at a mixing temperature of 30 seconds to 3 hours, preferably from 1 minute to 1 hour, or from 2-5 to 30 minutes. The same time intervals are used as the stency time between the addition of the last portion of alcohol and the step of separating the solids from the liquid. With the introduction of an excess amount of alcohol in one portion, the effect worsens. However, if the same amount of alcohol is added in portions with fixed intervals between additives, a much greater effect is achieved. Part of the alcohol can be recycled. It is possible to use a mixture of several alcohols.
    In the event that the alcohol is added in portions to a hot, unfiltered suspension of dissolved coal, the resulting mixture is stirred and aged between portions and after the last portion. The mixture is then passed through a filter, onto which a coating of diatomaceous earth is previously applied. The alcohol-containing filtrate is distilled to recover the alcohol. Alcohol is recycled and mixed with the filter feed stream along with the required amount of fresh alcohol.
    Filtration data is processed according to a mathematical filtering model.
    T / W -, where 1 - filtration time, min,
    W - the weight of the collected filtrate per
    time T,
    K - filter cake resistance coefficient, min / g С - preliminary coating resistance coefficient,
    T / W - (speed), g / min.
    The amount of filtrate extracted W is automatically recorded as a function of time T. W and T are basic experimental data.
    Parameters such as temperature, pressure drop across the filter, the nature of the precoat and the method of its application, the thickness of the precoat and the cross-sectional area of the filter to maintain comparable results are kept constant.
    . In filtering experiments, a 90-mesh sieve is used. The sieve is pre-coated with diatomaceous earth. The thickness of the layer is 1.27 cm. The filter element has an internal diameter of 1.9 cm, a height of 3.5 cm, and a surface area of 2.84 cm. To prevent deformation, the screen rests on a strong frame. The precoating operation is carried out by spraying on it with 5% by weight of a spal of dicalite material in light oil using nitrogen at a pressure of 2.8 kg / cm. The precoating is carried out at a temperature close to that of the subsequent filtering operation. The resulting porous layer of pre-coating material weighs 1.2 g. After applying the pre-coating material through the filter for -1-2 seconds, nitrogen is blown under a pressure of 0.35 kg / cm to remove traces of light oil. Then, a sample of a coal liquefaction product — an unfiltered oil (NOM) in the amount of 750 g is introduced into a separate autoclave. The product temperature is maintained at 38-54 ° C. The product is continuously stirred. Mixing is carried out using two turbines with a diameter of 5 cm. The speed of the shaft is. 2000 rpm
    Filtration begins at pressure. Nitrogen in an autoclave 2.8-5.6 kg / cm NOM flowing out of the autoclave is passed through a preheater coil, the residence time in which is controlled by means of valves. The temperature of the raw material is kept constant. NOM from the preheater is fed to the filter. The filter element and the filter heater, as well as the preheating spiral, are equipped with thermocouples. The weight of the filtrate is automatically recorded every five seconds.
    To determine the effectiveness of the additives, comparative experiments were carried out using the same batch of the initial NOM. B experiments use the product of coal liquefaction (oil), having the following characteristics
    Specific weight at
    15,
    1.15
    Kinematic viscosity at 98.9-c 24.1 sC-T Density at
    15.6 ° С1.092
    Ash4.49 wt.%
    Insoluble pyridines 6, 34 wt.%
    Data on distillation is given in Table. one.
    Example 1. Filtration of the carbon liquefaction product is carried out with the addition of various alcohols and phenol at a pressure drop on the filter of 2.8 kg / cm.
    The effect on the filtration of alcohols and phenol is presented in Table. 2
    Filtration resistance coefficient k is the best indicator of the effect of an additive on filtration. Since this coefficient excludes all effects on filtration from the side of the filtering system and precoating. On the other hand, the value of C illustrates the effect of the filtering system and pre-coating, regardless of whether the additives are alcohol or phenol.
    Given in Table. 2, the data show that the coefficient of filtration maturation with the introduction of alcohols decreases, however, to varying degrees, with the greatest effect and a decrease in the resistance coefficient
    renders secondary butyl alcohol. On the contrary, phenol increases the resistance coefficient, showing that it is a dispersed medium, not an agglomerate. Therefore, the presence of phenol has the opposite effect on the filtration of coal liquefaction products.
    T t and m e p 2. Filtration was carried out with the introduction of methyl and ethyl alcohols at a pressure drop across the filter of 5.6 kg / cm.
    The effect on the filtration of methyl and ethyl alcohols is shown in Table. 3
    As can be seen from the above data, methyl alcohol increases the filtration resistance coefficient K, while ethyl alcohol reduces it.
    Example 3. The filtration of the liquefaction product is carried out with the addition of organic acids, aldehydes and ketones at 2 ° C and a pressure drop of 5.6 kg / cm.
    The effect on the filtration of these additives is presented in Table. four.
    Filtration is carried out with the addition of methyl ethyl ketone at 210 ° C and a pressure drop of 5.6 kg / cm.
    The effect on filtration of methyl ethyl ketone is shown in Table 5.
    As can be seen from the above data, butyl aldehyde, methyl ethyl ketone and acetic acid have little effect on the filtration resistance coefficient K. The introduction of acetone slightly increases the coefficient. In industry, the use of acids is undesirable because of their aggressiveness.
    Example 4. Filtration is carried out with the addition of isopropanol at 260 ° C and a pressure drop of 2.8 kg / cm.
    The dependence of the filtration resistance coefficient and reaction rate on the amount of isopropanol introduced is presented in Table. 6
    These data show that as the amount of isopropanol increases from 0 to 1-2 wt.%, The filter resistance coefficient K gradually decreases. However, the advantages of adding 2.7% by weight of alcohol are lower than those of 2%, which indicates a decrease in the beneficial effect with an increase in the amount of alcohol above the critical one.
    Example 5. Filtration is carried out with batch addition of secondary and tertiary butyl alcohol at a pressure drop of 5.6 kg / cm and a holding time of 2 minutes at. Alcohol is added to the starting product to be purified at a temperature.
    The dependence of the coefficient K of filtration resistance on the exposure time for batch addition of alcohols is given in Table. 7
    The data show that the exposure time between the introduction of secondary butyl alcohol into the feed to the filter and the filtration effect has an effect on the filter resistance coefficient K. Within 80 minutes of adding a portion of secondary butyl alcohol, the effect of the alcohol increases to a peak and then decreases, so that the apparent advantage of the additive is more than 40 minutes than after 1 or 80 minutes. After adding a second portion of secondary butyl alcohol, the effect of the additive is higher after 5 minutes than after 55 minutes. The same applies to the addition of tertiary butyl alcohol. In addition, the effect of adding the first two percent of secondary butyl alcohol increases and decreases as a result, the effect of the second additive
    Butyl butyl alcohol similarly increases and decreases with exposure; the second peak occurs at a lower filtration resistance than the first peak. This indicates that the batch addition of secondary butoyl alcohol makes it possible to achieve an increased advantage from the addition of alcohol.
    Example 6. The filtration is carried out using isopropanol and
    The amount of time between the addition of isopropanol to the feedstock and the start of filtration at 260s and a pressure drop of 5.6 kg / cm.
    Effect on increase filtering
    5 time exposure is presented in Table. eight.
    These data show a positive effect on the coefficient K of filtration increase resistance.
    0 time between the addition of isopropanol and the start of filtration. These data illustrate the effect of the interaction of alcohol and feedstock.
    Example 7. Four experiments were carried out on filtration with a time delay between the introduction of isopropanol into the feedstock and the start of filtration at 260 ° C and a pressure drop of 5.6 kg / cm -.
    The drawing shows a graph of the dependence of the value of W on the value of T / W, which is the inverse of the reaction rate.
    The slope of each curve is K, and their intersection with the vertical axis
    5 corresponds to C. Curves 1-4 illustrate PE Ovodi e experiments 1-4, respectively.
    In the first experiment, isopropanol was not added to the feedstock. In experiments 2,3 and 4, 2 wt.% Were added to the feedstock.
    0 alcohol, the exposure time is 2.4 and b min, respectively.
    Parameter C is, first of all, the characteristics of the precoat, since it is
    five
    is the reciprocal of the filtration rate at the beginning of the experiment before a significant amount of the filtered substance is deposited on the surface of the precoat. G on the other hand, the slope of the Y curve is a pair of MSMS filter cake deposited on the precoat during filtration, and therefore characterizes the filtration itself, without precoating. The relatively low slope of the K curve (a low value of the filter resistance coefficient K) fairly low filter resistance. The upper curve has the greatest slope (the largest K value), while the lower curve has the smallest slope (the lowest k value).
    After one minute of filtration on the upper curve, the amount of filtrate is less than on the lower curve. Although each curve is characterized by a lower filtration rate, i.e. more, by a high value (speed), a slight slope of the curve at the end of the experiment indicates that the filtration rate decreases slightly during the experiment.
    The time values marked along each curve are the drip%
    71 (All are distilled
    volatile components) 496
    the time elapsed from the start of the filtering experiment to the moment of obtaining the experimental data. The use of isopropanol reduces filtration resistance in all cases. A gradual increase in the time between the addition of isopropanol and the start of the filtration experiment leads to a gradual decrease in filtration resistance.
    Example 8. Conduct a series of additional experiments on filtration using a portion of the supply of alcohol. Isopropanol is added to the feedstock having a temperature of 43-54 seconds. The exposure time between the last batch of alcohol and the start of filtration is 5 minutes at a temperature. Filtration was carried out at 260 ° C and a pressure drop of 5.6 kg / cm.
    The results of a comparative analysis of the effect on filtration of single and portioned additions of alcohol are given in Table. 9.
    These data suggest that the addition of 4 wt.% Isopropanol in one portion leads to a slight improvement (resistance coefficient compared to the addition of one porpy 2 wt.% Isopropanol. However, the addition of wt.% Isopropanol in two separate portions leads to a significant improvement in resistance
    Table
    I Temperature at 1 atm, С
    T a b l and c a 2
    Additive weight%
    Secondary butyl alcohol, 2
    Tertiary butyl alcohol, 2
    Isoamyl alcohol, 2 Phenol, 2
    Additive
    None MethloBy alcohol None Ethyl alcohol
    Additive, wt.% K, min / g C, mnn / g, g / min
    None0,0247
    Butyl aldehyde 20.0258
    None0,063
    0 0245 0.352.5
    Ут 0,0239 0,263,0
    20.0372 0.232.9 Additive jk:, min / g JC, min / g, g / min
    No
    et0.0235 0.154.1
    Methyl ethyl ketone 0 0256 0.173.9
    Additive, I K, min / g YYMg / min
    weight.% .
    0.01925.6 is missing
    Isopropanol, 1 0,01197.3
    Nzopropanol, 2 0,00658,6
    Mzopropanol
    ; 70,0086 8.2
    Continued table. 2
    K, min / G I s, min / g
    1g / min 1
    5.0
    0.13
    5.6
    0.05 3.1 0.28 2.8 0.27
    Table
    : i
    , -f
    g / min
    s, min / g
    min / g
    5.0
    0.07 4.5 0.07 4.4 0.6 4.6 0.10
    Table 4
    3.5
    3.5 2.5
    Table 5
    Table 6
    0.0534
    t
    butyl 0,0309
    butyl 0.0301
    butyl 0,6309
    butyl 0,019 ()
    butyl
    0.0265
    butyl
    0.0236
    butyl 0,0247 Includes the original 2 wt. % plus t BO min.
    Missing 0.0510
    Isopropanol, 2 (entered in one portion) .0,0239
    Table 7
    3.8 2.8 4D
    40 2.8
    80
    85 (5 mi 4.2 after the first portion)
    135 (55min
    3.7 after the first portion)
    5.6
    45 4.1
    0.07
    3.8
    0.09
    4.9 additional 2 wt.%, Added down. Table B
    Continued table. 9
    权利要求:
    Claims (3)
    [1]
    Claim
    1. The method of purification of coal liquefaction products from solid particles by mechanical separation of the latter, characterized in that, in order to increase the purification rate, 0.05-15.0 wt.% Of aliphatic alcohol C <2_ is added portionwise to the feedstock before separation of solid particles. -C ^ o , forming a homogeneous mixture with the feedstock, with intervals between porpies of 0.5-180 minutes.
    [2]
    2. The method according to π. 1, characterized in that, as an aliphatic alcohol, isopropyl, primary, secondary, tre2Q .’s butyl alcohol is used.
    [3]
    3. The method according to π. 1, distinguished by the fact that the gap between. the last portion of alcohol and the separation of solid particles is 0.5 to 180 minutes.
    25
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    同族专利:
    公开号 | 公开日
    PL111725B1|1980-09-30|
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    CA1111795A|1981-11-03|
    AU510347B2|1980-06-19|
    US4102774A|1978-07-25|
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    DD136396A5|1979-07-04|
    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    US2133280A|1935-04-26|1938-10-18|Standard Oil Co|Preparation of mineral oil products and the like|
    US3598718A|1969-08-18|1971-08-10|Universal Oil Prod Co|Solvent extraction of coal|
    US4029567A|1976-04-20|1977-06-14|Canadian Patents And Development Limited|Solids recovery from coal liquefaction slurry|
    US4030893A|1976-05-20|1977-06-21|The Keller Corporation|Method of preparing low-sulfur, low-ash fuel|US4260485A|1979-05-07|1981-04-07|Gulf Research & Development Company|Filtration of a coal liquid slurry using polyisobutylene and an alcohol|
    US4252646A|1979-05-07|1981-02-24|Gulf Research & Development Company|Filtration of a coal liquid slurry using an ethylene vinyl acetate copolymer and an alcohol|
    US4255258A|1979-05-07|1981-03-10|Gulf Research & Development Company|Filtration of a coal liquid slurry using an alkylmethacrylate copolymer and an alcohol|
    US4252647A|1979-05-07|1981-02-24|Gulf Research & Development Company|Filtration of a coal liquid slurry using an ethylene vinyl acetate copolymer|
    US4251364A|1979-05-07|1981-02-17|Gulf Research & Development Company|Filtration of a coal liquid slurry using polyisobutylene|
    US4252648A|1979-05-07|1981-02-24|Gulf Research & Development Company|Filtration of a coal liquid slurry using an alkylmethacrylate copolymer|
    US4298451A|1980-02-25|1981-11-03|The United States Of America As Represented By The United States Department Of Energy|Two stage liquefaction of coal|
    NL8101061A|1981-03-05|1982-10-01|Shell Int Research|METHOD FOR SEPARATING CRYSTALLINE SILICATES|
    US4428820A|1981-12-14|1984-01-31|Chevron Research Company|Coal liquefaction process with controlled recycle of ethyl acetate-insolubles|
    US4434043A|1982-06-01|1984-02-28|Exxon Research And Engineering Co.|Recovery of catalyst from coal liquefaction residues|
    US4617105A|1985-09-26|1986-10-14|Air Products And Chemicals, Inc.|Coal liquefaction process using pretreatment with a binary solvent mixture|
    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    US05/784,047|US4102774A|1977-04-04|1977-04-04|Separation of solids from coal liquids using an additive|
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