• 专利附录
  • 专利说明
  • 权利要求
  • 类似技术
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    • 专利摘要:
    1490003 Granulating nitrogenous compounds NORSK HYDRO AS 24 July 1975 [26 July 1974] 31060/75 Headings ClA and ClB A method for the pan granulation of nitrogenous compounds, e.g. ammonium nitrate, urea, or NPK fertilizer, comprises charging hot melt and cooled solids to an inclined, rotating pan, the solids being charged to the pan itself so as to slide down and cover the charged material, and the melt being sprayed to the upper portion of the bed where coarser particles appear (location specified) and the temperature of discharged material being maintained at 4-25‹ C. below the melting point of the material.
    公开号:SU873867A3
    申请号:SU752162238
    申请日:1975-07-25
    公开日:1981-10-15
    发明作者:Скаули Эйвинд
    申请人:Норск Гидро А.С. (Фирма)；
    IPC主号:
    专利说明:

    (54)
    METHOD OF GRANULATION OF NITROGEN
    co-operation
    This invention relates to the granulation of nitrogenous products with low water content or substantially anhydrous pure melts or from molten mixtures of compounds selected from the group consisting of urea, ammonium nitrate and ammonium phosphate, with or without the addition of other substances. These products are mainly used as fertilizers, and it is important that they are in the form of hard, retained granules with good flowability.
    When granulating on a rotating plate, the granules are gradually molded by spraying or applying a liquid phase on a rotating layer of material on a round, rotating and inclined plate on which relatively finely divided solid is cooled as a cooler. The grains on the plate are sorted by size. As the particles increase in size, they gradually move upward and outward in the layer towards the edge of the tray in this way, 25
    that when the granules become the right size, they roll over the edge of the plate in the part where the particles are raised by the rotating plate. Smaller particles remain on the tray and grow until they are large enough to roll over. With proper rotation of the plate, particles falling from it are very uniform in size. Particle size is mainly a function of the speed of rotation of the plate as well as the angle of inclination.
    The mass of the material of the rotating layer is unevenly distributed over the surface of the plate.  The greatest amount of material is on the upward moving part, where the particles roll over the edge of the tray.  Here, in the direction opposite to the lifting movement of the plate, there is a continuous rolling action.  The depth of the material decreases in the direction of the diametrically opposite edge.  3 The granulation technique on the plate was originally developed for the conversion of dry ground and finely divided materials with the addition of moisture, usually water, c. larger granules or pellets, and granules are mainly obtained by gluing or agglomerating individual particles.  Granulation by agglomeration is an acceptable process when using free-flowing crushes.  materials, for example, in the production of pellets for metallurgical purposes, in the enrichment of minerals, ores, etc. d. when using water or other low viscosity liquid binders.  Lotkova granulation of essentially anhydrous melts, for example, fertilizers, conducts, with with poor results.  In such processes, it is desirable to obtain rather small particles, and it is important, due to miscibility, separation, flowability, etc. d. so that the particles are strong and approximately the same size.  Using these fertilizer melts, it is impossible to maintain a satisfactory classification simultaneously with a HIGH growth rate and a high density of the particle structure.  The mobility of individual particles decreases if the circulating mass of the solid substance is strongly moistened with warm melt; This worsens the separation and sorting mechanism due to the fact that the free mass creates obstacles and pulsating currents are obtained that lead to uncontrolled growth and the flow of still unfinished particles over the edge of the tray.  At the same time, there is re-agglomeration of very viscous single particles, resulting in the formation of large, warm aggregates that become too hot and disintegrate into a warm, sticky, crystalline mass.  The material accordingly accumulates on the tray, and the process is broken.  In order to avoid such problems and to obtain a satisfactory granulation of such melts, the granulation is carried out at low temperatures and special conditions in order to guarantee a fast and complete solidification of the melt sprayed on the individual particles.  As a result, strong spherical granules consisting of concentric layers of solidified melt are obtained. A method of granulation of essentially anhydrous solutions of urea and ammonium nitrate is known, where the solution has a predetermined water content of 5-8% by weight.  The granulation is carried out under conditions that lead to evaporation of water as the solution is sprayed onto the moving particles of the layer, which is maintained at a sufficiently low temperature to ensure immediate solidification of the added layer.  The upper limit of the solution concentration is 95 wt. % Of water content less than 5 wt. The% results in such a decrease in heat sink such that the rotating particles of the layer turn into a sticky mass that cannot be controlled.  A known method of granulating melts of urea and ammonium nitrate involves loading a hot melt of nitrogenous compounds and cooled solid material into an inclined rotating plate and forming, when rotating the plate, a layer of semicircular shape having a depth gradually increasing towards the edge of the plate.  The particles move along with the plate as it rotates, while the cooled solids are poured onto the uppermost part of the plate and mixed with warmer small particles just before the hot melt is sprayed onto the plate, here the rapid cooling and solidification of the melt takes place, by means of which eliminates uncontrolled agglomeration.  The resulting dense grail has an onion structure and consists of several concentric layers of solidified t2l melt.  Although the problems arising from plate granulation of essentially anhydrous nitrogenous products have already been solved, these known methods using a layer-by-layer method for producing granules consisting of a layer-hardened melt do not provide industrial advantages compared to pelletizing using a rotating drum and cooled in the tower.  This is mainly due to an excessively low yield with such low-temperature methods, where the melt solidification in the layers exceeds the particle growth and where the plate capacity of 500,800 kg / m is considered very high. The capacity of the tray when granulating urea, ammonium nitrate and mixtures of ammonium nitrate with calcium carbonate are 15.6 and 8 tons / m per day, respectively, which is considered the natural upper limit of productivity for one unit.  The aim of the invention is to create a new and.  an improved method of splicing plate granulation of substantially anhydrous nitrogenous products intended for fertilizers, with a significantly higher specific yield and productivity than in the known methods.  In this method, I use especially high temperatures in the particle layer and at the same time regulate and control the growth and size of particles.  This goal is achieved by implementing a granulation method to obtain shallow or substantially anhydrous nitrogen compounds, including loading hot melt nitrogen and cooled solids onto a plate, whereby a substantially sickle-shaped layer of rotating particles is formed during rotation of the plate, the thickness or depth of which is gradually increases towards the periphery of the tray and its overflowing part, t. e.  from a position approximately corresponding to 2 hours at a position corresponding to 6 hours, if the tray surface is considered the clock face, and the tray rotates counter clockwise.  The solid material is loaded onto the bottom of the tray in such a way that the particles sliding backward will load up the cooler material.  The temperature of the material discharged from the tray is maintained in the range from 4 to below the melting point of the material.  The main part of the melt is sprayed on the noBepxHOCiM layer in the zone within a square of 12 to 3 hours, where coarser particles are observed, with the highest temperature occurring in the rotating material layer concentrated in this zone.  FIG.  I is a diagram of an installation for carrying out the proposed method; FIG.  2 is a top view of a plate schematically showing the paths of movement of the particles; FIG. 3 is a vertical section A-A in FIG.  2, which shows the location and classification of particles on the plate; in fig.  A is a cross-sectional view of a urea particle; in fig.  5 is a partial view of the fracture surface of the ammonium nitrate particle t in FIG.  6 is a cross-sectional view of a urea particle.  The possibility of implementing the method of controlled agglomeration has been determined under the condition that the temperature in the layer measured in the loaded material flow is in the range from 4 to below the melting point of the material.  In multicomponent systems with an indefinite melting point, the temperatures indicated are those at which substantial portions of the material are in the molten phase.  After the start of the process, the temperature in the bed is the most important parameter of the process and must be maintained within narrow limits.  A sufficiently high strength of the particles is achieved at temperatures that are close to the melting temperature of the material, and the particles do not crack and do not lose their mobility.  The growth rate increases under these conditions and the resulting product has a homogeneous and mechanically strong structure.  Tarel 1. equipped with a rim 2 (FIG. 1) whose height can be changed.  Angle dt.  the tilt of the plate to the horizontal plane and the speed of rotation can also be varied.  The rotational speed varies from 50 to 80% of the critical rotational speed.  The solids from the conveyor 3 flow with the help of the pipeline 4 close to the bottom surface of the plate and preferably fall on the plate.  The melt stream from line 5 is fed through a flexible reinforced hose 6 to the nozzle 7, which provides more or less fine dispersion of the melt onto solids.  The installation makes it possible to use one or several nozzles at the desired positions and angles relative to the plane of the plate because the method is supposed to concentrate the main part of the hot melt so that the heat zone is formed on the surface of the layer in that part of the plate where. the rougher parts are moving.  On section 8 (FIG.  2 and 3) unload the main part of the melt.  Zone 9 shows such an area, kotorz) called the collection area of the most saturated melt, where the largest part of the melt supplied from the nozzle 7 falls on the tray. , FIG. 2 shows the paths of movement of the particles that pass over the surface.  The heat zone, where the particles quickly stick together and round, has a limited extension (Fig. H).  Good particle movement is obtained within this warm zone, if only a small number of small particles are contained within it.  If the cross section (fig. 3) is taken, for example, along the 2-8 h line or along the 39 h line instead of the 4-10 h line, the picture in fig.  3 should remain basically the same, because the main agglomeration area on the chute is usually 1 and 5 oz.  The particle stream shows an accurate classification, so that the growing particles of the product at temperatures below the melting point of the material are reached farther and farther to the right.  Finally, the particles go beyond the growth zone and fall over the edge of the tray after they make several turns around the center of rotation of the paths 10.  The temperature is measured by a sensor in zone B (FIG. 2) in the area where the finished particles flow over the edge of the tray, and this sensor is placed directly under the surface and in the direction of movement of the particles.  The limited extent of the warm zone in the plane (FIG.  3, the shaded area) perpendicular to the tray. Some granulation of the granules, the smallest grains occur in the transition zones surrounding the warm zone.  However, the majority of the solid fine particles are slightly heated and therefore their free flowing ability is maintained.  This is necessary in order to obtain a classification that transfers the growing particles to the warmer zone at the top (FIG.  3, shaded) and sorts them by surface.  A stable operating temperature is established relatively quickly.  Conditions will soon be established under which the pre-heating, agglomeration, leveling, sorting and unloading of particles will come to equilibrium.  If the temperature is kept too high, then slip 7. 8 and good classification is violated.  The wire process at low temperatures will produce less dense and less smooth particles.  Work at high temperatures, which are 4–25 ° C below the melting point of the material, gives particles that, when rolled over the edge of the plate, show signs of a wet volume and not yet solidified melt.  Surface cooling, however, gives them. sufficient strength to flow in the intact state along the chute 11 into the cooler 12 of the resulting product, which may be a cooler of the known drum, boiling or mine type, from which the granules and the heated air are removed.  From the heated air leaving the product cooler 12, the filter is removed by means of the filter 13.  The product is sieved with a sieve 14 and the dust and sifted fine solids are recirculated to the plate via lines 15 and 16, and also partially through a crusher 17.  The heat balance of the tray can in some cases be obtained by adding another material that returns from the air filter 13 and the screen 14, for example, by adding solid cooling agent through the pipe 18.  Typically, the thermal regulation of the process is carried out by returning the cooled product by means of a tube 19.  Such recycling was previously considered a disadvantage because it limited the resultant tray capacity, but according to the invention, this is almost irrelevant due to the very high yields of the tray per unit area.  In the production of nitrogen-phosphorus-potassium fertilizers, for example, the addition of potassium salt provides a significant portion of the desired solid cooler.  The use of a portion of the melt compound in the form of a solid cooler has also been tested with success.  As shown in the examples, the use of high-performance sifting gives more advantages njo compared with the forced return of a part of the granulated product to the type of refrigerant.  A satisfactory heat balance can be obtained by freely choosing the number of compounds that need to be loaded as a melt and solid material.  The sifted product can be unloaded from the device via line 20 without returning any part of it again to the granulation process.  Particles of urea and ammonium nitrate (FIG.  4 and 5) have a dense and homogeneous internal structure, surrounded by a very homogeneous and smooth outer shell.  The particle is completely impregnated with the molten phase and subjected to such high temperatures that the boundary between the stuck particles is erased and there are no hardened layers or plates in the internal structure.  In contrast, a urea particle (FIG.  6), stained to enhance photographic contrast, has a structure consisting of concentric layers formed upon re-cooling and solidification of the melt.  Example 1  Ammonium nitrate with a granule size of 1.5-4.5 mm.   The preparation was carried out on a plate having 3.5 m, a rim height of 0.7 m.  The MNDMO melt evaporated to a moisture content of 0.5%, is discharged onto a plate through a conical nozzle at 178 in an amount of 10,300 kg / h.  Melt crystallization temperature The nozzle operates at a low static feed pressure (I kg / cm).  The largest axis in the approximately elliptical spray area for the melt is 1.3 m, with the majority of the melt falling on the surface of solids within 12 to 3 hours. . The rotation speed is 11.6 rpm, the angle of inclination is 57.5.  As a solid, 2,700 kg / h of finely divided material are used. The total amount is 13,000 kg / h, and this is obviously a small load for the tray, with 30-40% of the tray area not being used.  Solids GpOday to the bottom of the tray at 78 o'clock.  The temperature of the product stream is 140 ° C.  The process is stable, 77% of the product has a grain size of 1.5 to A, 5 mm.  The sifted material is added and dissolved in unpairing from the production stage.  The net yield of this method is loaded plate, thus 1030 kg / h.  Such a low loading of the plate was caused not by the design of the plate, but by the limited performance of other parts of the production chain.  Example 2  Ammonium nitrate 4ill mm.  Melt NHjj. NOj is the same as in example 1, in the amount of 13,500 kg / h served on the plate through a flat jet nozzle at low feed pressure.  Spray full area squared 12-3 hours.  The height of the edge is 0.8 m.  The solid is used in crushed form with, and all particles have a size less than I mm.  The loading is carried out at a rate of 4400 kg / h, the process is stable, the product temperature is 147s.  Particle growth is very fast at this temperature.  The angle of inclination is 52.5 °, and even so, part of the bottom surface is not covered in the upper left corner, which indicates that the exit can be even greater.  The rotation speed is about 8 revolutions per minute.  96% of the product has the desired size of 4-11 mm, while the specific productivity. Th 1780 kg / h m.  The coarser product is also tested by using a wider spray nozzle.  Temperatures up to 152 ° C are used. Under these conditions, it is important to position the spray zone so that the heat zone does not get too widespread.  If this happens, the slip angle becomes too large, the hot material is recycled and mixed with the finer material, the classification and flow is disturbed and the process is broken.  Example 3  Urea 1-4.5 mm.  Two streams are fed to the plate with a diameter of 0.9 m and with a rim with a height of 0.26 m.  Urea melt with in the amount of 1650 kg / h.  The pressure in the nozzle is 4.6 atm.  Use one conical nozzle.  Urea solid at 28 ° C is in the amount of 1310 kg / h.  The solid consists exclusively of the milled product stream, 4-8% of the grains of which have a size less than 1.5 mm.  Solid substances are served deep on the plate.  Temperature of the material of the unloaded product I28 С.  The paths of movement of the permanent classifications across the plate are good.  Accordingly, there is no indication that this is the maximum output.  The product has narrow size limits: 88.7% within the desired range from 1.5 to 4.5 mm, and 73% within 2-4 mm.  The weight of a packaged liter is 1.5–4 mm of a fraction of 748 grams per liter, and the mechanical strength of the particles is high.  The specific productivity in this case is 2480 kg / h. Stable operation is provided at a temperature of 129-130 C.
    Periodically, solids are fed to it, 50% of which are below 1.5 m. This gives stable operation at 127128С, but the position of the nozzle is britical. Fine material can easily become too warm and sticky, which leads to a breakdown.
    When using even smaller particles, the temperature must be reduced to G25C, and the product is less dense and homogeneous.,
    Example 4. Production of nitrogen phosphate potassium fertilizer using KCC as a potassium compound.
    On a tray with a diameter of 0.75 m with a rim of 0.255 m, 840 kg per hour of nitrogen-phosphorus-potassium fertilizers are obtained. 90% of this material is within 35 mm. About 320 kg per hour of a substantially anhydrous ammonium ammonium nitrate ammonium nitrate melt, having an N / P ratio of about 4 and a temperature, is fed to the tray through a 15 cm wide spray nozzle, across the direction of movement of the gliding coarse particles on the side of the tray, moving up.
    The flow of solids, which is directed to the bottom of the plate, contains the following compounds, kg: KC6 242 and kieserite at 70 ° C 54, ground recycled fertilizer material at 76 and nitrogen-fsformal compound in the unmelted state at 148, all in one hour and when the water content is below 0.5%. In a nitrogen-phosphorus-potassium product having this composition, small amounts of the molten phase can occur approximately from 124c, while substantial amounts of the molten phase are initially present, starting from.
    Acceptable upper granulation temperatures used in this method are 1 15-1 25 ° C. The obtained granules are equal and uniform in size.
    Constraints in the feed part do not allow experiments with a higher capacity than 1720 kg / hr. A high sifting yield indicates that the capacity is still greater.
    Example 5. Production of nitrogen-phosphorus-potassium fertilizer having K 50 as a compound
    Kali.
    Upon receipt of the nitrogen-phosphorus-potassium fertilizer method, according to. for example 4, KCE is replaced by K 250. In the resulting nitrogen-phosphorus-potassium product having this composition, small amounts of the molten phase occur, starting at about 140 ° C, while significant amounts of the molten phase first appear at about
    145 ° C. Acceptable granulation temperatures in this case are within 130137 ° C.
    In none of the experiments in examples 1-5, the performance limits were not reached, even when using a plate with a Q of 0.9 m and with a material transmission rate of up to 4.65 t / h-mH High yields that can be obtained from a plate operating According to the proposed method, they are very important in creating simple granulating aggregates that have large productive capacities.
    Accordingly, a productivity of 25-30 tons per hour is quite achievable if using plates with a diameter of 4 m.
    权利要求:
    Claims (2)
    [1]
    1. Method of granulating nitrogenous compounds, including loading
    5 hot melt of nitrogenous compounds and cooled solid material in an inclined rotating plate and the formation during rotation of the plate of a layer of material of a semicircular shape, having a Q depth gradually increasing to the edge of the plate, characterized in that in order to increase productivity, the solid material is loaded into the bottom a portion of the plate melted onto the surface of the layer in the zone lying between 12 and 3 hours while rotating the plate counterclockwise or between 9 and 12 hours while turning clockwise, the temperature unloaded from the plates 4-25S material is maintained below the melting point of the material, according to claim 2.Sposob. 1, characterized schiys in that in the granulation of ammonium nitrate temperature of the discharged material is maintained at a UO-ISO C level 0 at 11-23 below the melting temperature of the ammonium nitrate. 3. The method according to claim 1, which differs from the fact that during the granulation of urea, the temperature of the discharged material is maintained at 124-129 0, below the melting point of urea. 4. The method according to claim 1, characterized by the fact that when granulating nitrogen-phosphorus-potassium fertilizers containing potassium chloride as potassium compound, the temperature of the discharged material is maintained at 115-125 0 below the melting point of the fertilizers. 5. The method of claim 1, wherein granulating nitrogen-phosphorus-potassium fertilizers containing potassium sulfate potassium as the potassium compound, the temperature of the discharged granules is maintained at 130-137 ° C, below the fertilizer melting point. Sources of information taken into account in the examination, US Patent No. 3117020, cl. 117-100, published. 07.01.64.
    [2]
    2. US Patent No. 3408169, cl. 23-313, published, 10/29/68 (prototype). Phage. five
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    同族专利:
    公开号 | 公开日
    NL184097C|1989-04-17|
    DK137068C|1978-07-31|
    DE2533328A1|1976-02-12|
    NO133872B|1976-04-05|
    FI752127A|1976-01-27|
    TR18469A|1977-02-24|
    YU188775A|1982-02-28|
    NL7508914A|1976-01-28|
    IT1040154B|1979-12-20|
    IE41302B1|1979-12-05|
    AU8335975A|1977-01-27|
    IL47754A|1978-08-31|
    YU40444B|1986-02-28|
    IN142375B|1977-07-02|
    HU173369B|1979-04-28|
    BE831779A|1975-11-17|
    FR2279457B1|1979-05-11|
    CA1063778A|1979-10-09|
    JPS5648202B2|1981-11-14|
    DK338275A|1976-01-27|
    NO742729L|1976-01-27|
    BG39806A3|1986-08-15|
    SE7508183L|1976-01-28|
    ES439715A1|1977-03-01|
    SE395617B|1977-08-22|
    FR2279457A1|1976-02-20|
    BR7504741A|1976-07-06|
    DK137068B|1978-01-16|
    NO133872C|1976-07-14|
    FI62628C|1983-02-10|
    KE2852A|1978-08-04|
    DD118995A5|1976-04-05|
    US4008064A|1977-02-15|
    RO71993A|1981-06-30|
    IE41302L|1976-01-26|
    GB1490003A|1977-10-26|
    DE2533328C2|1981-11-19|
    FI62628B|1982-10-29|
    JPS5137098A|1976-03-29|
    OA05060A|1980-12-31|
    IL47754D0|1975-10-15|
    EG11720A|1978-03-29|
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    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    US2436766A|1943-07-19|1948-02-24|Monsanto Chemicals|Method of making pellets|
    US2860598A|1956-07-27|1958-11-18|Loesche Ernst Gunter|Production of granulated materials consisting of a core and one or more shells|
    US3117020A|1957-11-29|1964-01-07|Montedison Spa|Process for the spherical granulation of water-soluble nitrogenous material|
    US3408169A|1967-05-31|1968-10-29|Cominco Ltd|Pan granulation|DE2714601C2|1977-04-01|1984-12-06|Skw Trostberg Ag, 8223 Trostberg|Process for the preparation of a urea dicyandiamide fertilizer|
    JPS54153459U|1978-04-19|1979-10-25|
    NL184769C|1981-07-03|1989-11-01|Azote Sa Cie Neerlandaise|METHOD FOR MANUFACTURING UREUM granules|
    JPS6338059B2|1982-09-29|1988-07-28|Sekisui Kaseihin Kogyo Kk|
    DE3519920A1|1985-06-04|1986-12-04|Uhde Gmbh, 4600 Dortmund|METHOD FOR PRODUCING GRANULATED AMMONNITRATE|
    US5019302A|1986-03-12|1991-05-28|Washington University Technology Associates, Inc.|Method for granulation|
    JPH0764666B2|1988-11-25|1995-07-12|宇部興産株式会社|Slow-release fertilizer and method for producing the same|
    US5091132A|1989-08-07|1992-02-25|J. M. Huber Corporation|Method and apparatus for production of rubber dispersible pellets|
    US5178948A|1989-08-07|1993-01-12|J. M. Huber Corporation|Method and apparatus for production of rubber dispersible pellets|
    FI981490A|1998-06-29|1999-12-30|Kemira Agro Oy|Process for making manure mixtures|
    FI108028B|1999-09-21|2001-11-15|Kemira Agro Oy|Improved process for the preparation of urea-based fertilizer mixture|
    US7862642B2|2006-12-14|2011-01-04|Georgia-Pacific Chemicals Llc|Extended-release urea-based granular fertilizer|
    EP3656463A1|2018-11-22|2020-05-27|Yara International ASA|Method for granulating a melt of a nitrate mineral salt-based composition, system and use thereof|
    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    NO742729A|NO133872C|1974-07-26|1974-07-26|
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