• 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:
    1. A method for producing granules of carbamide, including the transmission of falling drops of urea melt towards the cooling air flow through the cooling zone and supplying urea seed particles to this zone, in order to increase the impact strength of the granules, the carbamide particles size 2-10 microns in an amount of 8 - 25 mg per 1 m of air. i joint venture with
    公开号:SU1145924A3
    申请号:SU813360406
    申请日:1981-11-27
    公开日:1985-03-15
    发明作者:Хендрик Виллемс Михаэль；Виллем Клок Ян
    申请人:Уни Ван Кунстместфабрикен Б.В.(Фирма)；
    IPC主号:
    专利说明:

    2. A method according to claim 1, characterized in that the carbamide particles are obtained at least partially by grinding the crystalline carbamide.
    3. A method according to claim 1, characterized in that the carbamide particles are supplied to the cooling zone at such a place that under all local atmospheric conditions the water pressure of the cooling air is less than or equal to the water pressure of the particles at the temperature of the cooling air.
    The invention relates to a method for producing carbamide granules, which are formed when passing falling droplets of urea melt, which is practically free of water, in a countercurrent flow of cooling gas through a cooling zone in which the material that creates the seed crystals is distributed. A method is known for producing carbamide granules by spraying a melt of urea containing no water against a flow of cooling gas in a cooling zone containing solid particles of carbamide or particles of another material that creates seed crystals, preferably in a calloid state or in the form of mist. l. However, with this method, the droplets during cooling from the outer surface inward turn into large crystals, oriented almost in the same direction in which the outer shell, having flowed from the first one, is drawn partially inward during cooling and solidification of the rest of the granule. what is formed in the granules, cavities. As a result, the granules have a slight toughness and are sprayed during transport and processing. The aim of the invention is to increase the impact strength of the granules. The goal is achieved by the fact that according to the method of obtaining carbamide granules, including passing the falling droplets of urea melt towards the flow of cooling air through the cooling zone and supplying urea seed particles to this zone, the content of urea particles with sizes of 2-10 microns is maintained in the cooling zone. in the amount of 8-25 mg per 1 m of air. At the same time, urea particles are obtained at least partially by grinding crystalline urea, they are fed into the cooling zone in such a place that under all local atmospheric conditions the vapor pressure of the cooling air is less than or equal to the water vapor pressure of the particles at the temperature of the cooling air. FIG. 1 shows a granule obtained in a known manner; in fig. 2 granules obtained by the proposed method; in fig. 3 is a graph of impact strength versus number of crystallization centers per granule (number of collisions). According to the invention, granules with randomly oriented crystals and without cavities can be obtained if dispersion of crystalline particles having a size of 2-10 microns in an amount of 8-25 mg per 1 m of cooling gas is created in the cooling zone. Particles with a size of less than 2 microns {are ineffective in using as a material to form the seed crystals, since they are carried by the cooling gas past the drops and, therefore, do not collide with them. Particles with sizes greater than 10 microns can be used, but they create the same effect as particles with sizes of 4-8 microns. In order to obtain samples consisting of small crystals with disordered orientation, it is necessary that before the start of crystallization in the drop between the falling droplet and the seed material, there are at least 20, preferably about 25, collisions. To obtain 25 collisions, it is necessary to use about 5 kg / h of seed material with an average diameter of 4-5 μm, if the average diameter of a part is 10 μm, 40 kg / h is needed, and with a diameter of 100 μm, 4000 kg / h of seed material. Thus, the number of collisions is determined by the size of the crystals, the orientation and strength of the sample, more than the amount of seed material. The tests carried out in the laboratory at the experimental facility showed that using the proposed method, granules with impact strength of more than 90% are obtained (over 90% of the granules are not destroyed during the impact test), and 25 sludge more seed centers are contained in the granules, resulting in the granules have a mesh structure of small crystals with a random orientation. In tab. Figure 1 shows the impact strength of carbamide granules obtained by spraying a carbamide melt in an air stream (600000 m / h) in which 10 kg of urea are dispersed (at 16 mg / m in the form of particles of various sizes. Table From Table 1 it is clear that high only a sample obtained using a seed material, the average particle size of which is 4 microns, is only 4,4 which is a result of the dogt’s frequency of collisions between a capol of a urea melt and a seed particle. particle sizes less than 2 microns, most of the seed particles are carried away along with the air flow and bypass the urea drops, which they touch.The use of particles larger than 10 microns leads to an uneconomical increase in the consumption of seed material.The number of seed centers of 25 or more can also be obtained when the use of more than the above amount of seed material. However, the use of more than 25 mg of seed material per 1 m of cooling air is uneconomical. The number of seed centers from 20 to 25 can be obtained by using approximately 8 mg of booster material per 1 m of cooling air, as a result, the carbamide resistance is sufficiently hardened. When using a seed material of less than 8 mg / m, the number of seed centers is less 20, which leads to a sharp decrease in the impact strength of carbamide granules. In addition, the amount of material required to create seed crystals depends, albeit to a much smaller degree, on the size of droplets of melted urea melt. In the preparation of carbamide granules with a diameter of 1–3 mm, good results are achieved if in 1 m of cooling gas there is 8–25 mg of material, t creating seed crystals, with a particle size of 2–10 µm. The number of particles with a diameter of 10 microns in 1 m of cooling gas 0.01 x 10 a with a diameter of 2 microns is 4.5 x Yu. It is preferable to use urea particles as a material that creates seed crystals. These particles can be obtained by grinding granules or carbamide crystals. To ensure good grinding and reliable movement in pipelines, a substance that prevents sticking, such as salt, can be added to the crystalline urea.
    Calcium, magnesium, zinc and aluminum fatty acids, clay, talcum calcite, preferably calcium stearite.
    In order to investigate the ability of priming urea particles with respect to their mass, a number of experiments have been carried out. During these experiments, an uninterrupted flow of crystalline urea is supplied to the metal plate, it is heated to a dark red color by electricity at approximately EPA. Urea is completely evaporated, forming a thick cloud of extremely small particles (diameter less than 2 microns). This cloud is then introduced into the air, which is used to cool the curable molten urea droplets in the pilot curing plant. The formation of dust particles of urea in the bottom of this column is suppressed so that only the seed particles get together with the air. Even at low relative humidity of air, the particles of urea thus formed differ in a plate-like crystal structure. Since such particles were formed in the absence of seed material, they have a fuzzy configuration (see Fig. 1). The urea particles with such a plate-like structure have an impact strength of about 5-15%. The concentration of urea mist in the cooling air is not measured, however, an increasing amount is introduced until visibility inside the column after the addition is limited to less than 2 m (this is more than 100 mg / m). In addition to ineffective seeding of urea droplets, the use of such urea mists as a seed material leads to a significant increase in fluff from the curing column.
    In addition, in experiments on a pilot plant, the effect of the size and concentration of gravity particles introduced into the cooling air on the impact strength of the obtained urea particles is studied.
    It has been found that when crystalline urea particles are present in the cooling air, the impact strength of particles is significantly increased.
    moreover, the urea crystal particles have an effective diameter of 2-10 microns, their amount is approximately 8-25 mg / m of cooling air. The urea particles obtained in this way have impact strength up to 90% (about 90% of the particles remain intact or intact in the shooting test), 25 or more seed points and a needle-like crystal structure (see Fig. 2). The crystal structure of such particles does not show a general orientation, and the orientation of elongated crystals, apparently, leads to increased impact strength.
    These experiments are repeated in the factory setting, where devices are installed for introducing 15 mg / m of urea fine particles (2-10 µm) into the cooling air. 93 samples of urea pieces obtained with this are taken on random days from the Donn part of the curing column for 6 months.
    Determine the impact strength of the granules,%:
    Observation
    268-72
    373-77
    478-82
    583-87
    688-92 Average impact strength for
    this set of samples is 83.5% with a spread of only 4.5%.
    The method for determining the impact strength of the Granules includes pneumatic firing of the granules into steel platinum at a speed of 20 m / s at an angle of 45 °. The amount (%) of the remaining values is. In this test, the granules are taken as the impact strength value.
    Melt, subject to raspery,. It can be obtained by evaporation of urea solutions or by melting urea crystals. If a melt that was obtained by melting carbamide crystals is sprayed, it should be preferred to melt in the presence of spray devices, for example, located in the upper part of the tower to obtain granules so as to prevent 7 1 formation of biuret as reliably as possible. The crystals are preferably supplied pneumatically to the upper part of the granule tower, separated from the carrier gas by means of a cyclone and then melted. The operating conditions of the cyclone should be chosen so that the carrier gas contains particles of 2-10 microns in size. After exiting the cyclone, the carrier gas, in which the fine particles of urea are scattered, can be fully or partially added to the cooling gas fed to the cooling zone, as a result of which the amount of seed crystals creating the material, which is obtained by grinding, can be reduced. the solidification of the sprayed droplets when turning them into granules produces larger and / or smaller crystals depending on the method and rate of cooling. The impact strength of granules consisting of small crystals with an arbitrary orientation is significantly higher than the impact strength of granules consisting of large crystals that have essentially the same orientation. The formation of small crystals in the granule increases when the droplet comes into contact with a large number of fine particles of material that gives seed crystals, while (THIS fine particles act as crystallization centers. The relationship between the number of crystallization centers and the impact strength is determined experimentally for granules with an average diameter of about 2 mm (i.e. 50% of the granules have a diameter equal to or greater than 2 mm) with a maximum diameter deviation of plus or minus 40% (see Fig. 3). Inat lay the values of impact strength, and on the abscissa axis the number of crystallization centers per single granule (impact strength is determined using the method written off above. The graph (Fig. 3) shows that at least 10 centers of crystallization per granule are required to achieve an impact strength of 70%, having a diameter of 2 mm. To achieve a toughness of 80%, at least 20 crystallization centers are required per granule with a diameter of 2 mm. In practice, this means that to obtain granules with a good impact strength of 1000 kg of molten carbamide and about 0.125-0.375 kg of carbamide pypi with a particle size of 2-10 microns is required. It has been found that with an increase in the relative humidity of the cooling gas, a greater amount of material that creates seed crystals is required in order to achieve an appropriate impact strength. Any gas that is inert with respect to urea, such as air, nitrogen, and carbon dioxide can be used as a cooling gas (air is used in practice as a rule) The indicated amounts of material that creates seed crystals are sufficient to produce pellets at the highest relative humidity . The material that creates the seed crystals is fed into the cooling zone in one place or in several places and is distributed as evenly as possible in this zone. When air enters the solidification column, its temperature increases due to heat exchange with falling drops and solid particles. The exact temperature of the removal stream can be determined at each point of the solidification column. According to the result of experiments, as well as literary data, you can build a graph. The difference in the pressure of water vapor between the particles of urea and air is the higher, the higher the temperature. A good seed is possible only when the pressure of water vapor of urea particles at the point of entry of ravio or higher pressure of water vapor of air, so that water is not captured at all by the particles. At the highest possible temperature, napr (303 K), the air vapor pressure is 0.042 bar, which corresponds to a urea particle temperature of 310 K (). As the particles with a size of 2-10 microns reach room temperature, good seed is obtained when the particles are introduced into the well column at a level where the temperature is at least. In order to maintain the distribution of fine urea particles in the cooling zone, the water vapor pressure of the cooling air should be at any local state of the atmosphere less than or equal to the water vapor pressure of the carbamide particles at the temperature of the cooling air. If the water vapor pressure of the cooling air is higher, the carbamide particles may even dissolve, so that the effect of the formation of crystallization centers will be completely lost. Consequently, the place of supply of the material that creates the seed crystals is chosen so that the cooling air at this Place is heated to such an extent that the water vapor pressure is less than or equal to the water vapor pressure of the material that creates the seed crystals. The air flow supplying the material that creates the seed crystals into the cooling zone should have a low water vapor pressure. For this purpose, the air can be dried or heated, for example, up to 50 ° C. In addition to the fine fractions of urea, other substances, such as chalk, gypsum, potassium chloride, can be used as the material created by the seed crystals. However, when using these substances, the urea granules are contaminated with them and become less suitable for further use. Example. In a tower for the preparation of granules having a height of 52 meters, 40,000 kg / h is sprayed. 99.8% carbamide melt (temperature of melting); using a rotating sprayer of pellets having an orifice diameter of about 1.3 mm. At four locations around the periphery of the tower, to obtain granules, a mixture of air and carbamide particles, with an average size of 4 microns with a size range of 2-10 microns, is blown into the tower through pipes using an ejector and distributed uniformly. Particles are obtained by grinding granules of carbamide, to which calcium stearate is added in an amount of 3 wt.%. The preparation of the seed material is carried out by grinding the crystalline urea in an aerodynamic mill. The pressure of an aerodynamic mill is adjustable at a certain level. As a result, more than 80% of the obtained ground urea has a particle size of 2-10 microns, less than 10% less than 2, and less than 10% more than 10 microns. It is not necessary to separate the 2-10 micron fraction. The particles, having the dimensions of the lower and upper limits, together with the majority of the 2-10 µm fraction, are carried away from the head of the solidified molten column by spraying together with the air stream. The particle is removed from the air stream, for example, by filtration and / or gas purification, and the urea is returned to the process, for example, at the stage of concentration and penetration. The speed of movement in the pipes is 35 M / cJ and the relative humidity of the transport air is 30%. The openings for feeding the material that creates the seed crystals in the tower for the production of granules are located 20 m below the atomizer of the granules. Cooling air, which moves in the opposite direction with respect to the direction of movement of the urea melt, is supplied to the bottom of the tower in an amount of 600,000 m / h with an inlet temperature. The average temperature of the granules at the outlet of the granulation tower and ranges from 50 to 74 ° C, depending on the ambient temperature. The average air temperature at the outlet of the granulation tower varies from 48 to. The average diameter of the obtained granules 2, OtO, 1 mm. The amount of material that creates the seed crystals varies during the experiments, which are carried out at different relative humidity of the cooling air. The test results are presented in Table. 2
    P
    As can be seen from the table. 2, to achieve the same toughness, a larger amount of material, 95 la, creates seed crystals at high relative humidity than at low relative humidity.
    12
    11A5924 T-a blitz 2
    The impact strength of the granules obtained by the proposed method is higher than the impact strength of the granules obtained in a known manner, i.e. without the use of material that creates seed crystals.
    权利要求:
    Claims (3)
    [1]
    1. METHOD FOR PRODUCING CARBAMIDE GRANULES, including passing falling drops of urea melt towards the flow of cooling air through the cooling zone and supplying urea seed particles to this zone, characterized in that, in order to increase the impact strength of the granules, the content of urea particles with sizes is maintained in the cooling zone 2-10 microns in an amount of 8 - 25 mg per 1 m 3 of air.
    FIG. 1
    [2]
    2. The method according to π. 1, characterized in that the urea particles are obtained at least partially by grinding crystalline urea.
    [3]
    3. The method according to p. 1, with the exception that the particles are supplied with carbides to the cooling zone in such a place that, under all local atmospheric conditions, the vapor pressure of the cooling air is less than or equal to the vapor pressure of water particles at a temperature of cooling air.
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    引用文献:
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    GB1168444A|1965-12-08|1969-10-22|Fisons Ltd|Improved Granular Materials|
    NL135916C|1966-11-26|
    US3450804A|1967-01-05|1969-06-17|Chemical Construction Corp|Method of prilling urea|
    US3836611A|1971-01-08|1974-09-17|I Mavrovic|Process for prilling urea|
    US3795504A|1972-09-07|1974-03-05|Uhde Gmbh Friedrich|Process for prilling fertilizer melts|
    GB1503504A|1974-04-29|1978-03-15|Fisons Ltd|Prilling process|
    GB1493612A|1974-07-06|1977-11-30|Fisons Ltd|Prilling|
    US4076773A|1974-11-25|1978-02-28|W. R. Grace & Co.|Process for prilling ammonium nitrate|JPH0134485Y2|1984-12-24|1989-10-20|
    US4885021A|1988-02-22|1989-12-05|Tennessee Valley Authority|Particulate urea with clay incorporated for hardness and/or gelling|
    US5514307A|1992-10-13|1996-05-07|Laroche Industries, Inc.|Process for the reducing emissions during prilling of material such as ammonium nitrate|
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    US7862642B2|2006-12-14|2011-01-04|Georgia-Pacific Chemicals Llc|Extended-release urea-based granular fertilizer|
    法律状态:
    优先权:
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    NL8001876A|NL8001876A|1980-03-29|1980-03-29|METHOD FOR MAKING UREU PRILLS AND UREU PRILLS OBTAINED BY THIS METHOD|LV930296A| LV5212A3|1980-03-29|1993-05-06|Karmabida pellet retrieval tolerance|
    LTRP724A| LT2205B|1980-03-29|1993-06-30|THE BENEFIT OF CARBAMIDE GRANULES|
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