CN219540283U - Be applied to compound fertilizer's urea sulfate reaction unit - Google Patents
Be applied to compound fertilizer's urea sulfate reaction unit Download PDFInfo
- Publication number
- CN219540283U CN219540283U CN202320116799.5U CN202320116799U CN219540283U CN 219540283 U CN219540283 U CN 219540283U CN 202320116799 U CN202320116799 U CN 202320116799U CN 219540283 U CN219540283 U CN 219540283U
- Authority
- CN
- China
- Prior art keywords
- chamber
- urea sulfate
- stirring
- urea
- reaction
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P60/00—Technologies relating to agriculture, livestock or agroalimentary industries
- Y02P60/20—Reduction of greenhouse gas [GHG] emissions in agriculture, e.g. CO2
- Y02P60/21—Dinitrogen oxide [N2O], e.g. using aquaponics, hydroponics or efficiency measures
Landscapes
- Fertilizers (AREA)
Abstract
The utility model discloses a urea sulfate reaction device applied to compound fertilizers, which is used for reducing the preparation cost of the compound fertilizers. The utility model comprises the following steps: the device comprises a urea valve, a sulfuric acid valve, a flow guiding chamber, a raw material stirring chamber, a urea sulfate reaction chamber, a reaction solution storage chamber and an atomization spraying chamber; the diversion chamber is fixedly connected with the urea valve and the sulfuric acid valve; the diversion chamber is connected with the raw material stirring chamber through a flange plate; a spiral stirring device is arranged in the raw material stirring chamber; a motor is arranged outside the raw material stirring chamber and is coupled with the spiral stirring device; the lower end of the stirring chamber is connected with the urea sulfate reaction chamber through a solid-liquid separation sieve pipeline; the lower end of the urea sulfate reaction chamber is connected with the reaction solution storage chamber; the reaction solution storage chamber is connected with the atomization spraying chamber through a transfusion pipeline; the upper end of the urea sulfate reaction chamber is connected with the spraying chamber through a gas pipeline.
Description
Technical Field
The embodiment of the utility model relates to the field of fertilizers, in particular to a urea sulfate reaction device applied to compound fertilizers.
Background
The current production process of high-concentration compound fertilizer in China mainly comprises the following steps: the method comprises four main production processes of a granulating method, a high-tower granulating and ammonifying granulating method of a melt (comprising a dilute sulfuric acid ammonifying granulating process and a concentrated phosphoric acid ammonifying granulating process), and an ammonifying granulating process of mixed acid full slurry of potassium bisulfate and phosphoric acid. The granulating method is a traditional high-concentration compound fertilizer production process, and various production raw materials are mixed and then are heated by steam in a rotary drum granulator and supplemented with proper water for kneading and granulating. All raw materials in the process of the granule method are solid materials. The high tower granulation process of the melt is to mix nitrogen, phosphorus, potassium and auxiliary materials in three stages, form a co-melt under the condition of heating by an external heat source, spray the co-melt from the top of the granulation tower, form particles by utilizing surface tension and contact with cold air in the falling process to realize the cooling process. All materials in the melt granulation process are solid materials. The ammonification granulation is of various types at present, such as traditional dilute sulfuric acid ammonification granulation, concentrated phosphoric acid ammonification granulation, dilute phosphoric acid ammonification granulation and the like, and is characterized in that acidic liquid and ammonia are subjected to neutralization reaction in a tubular reactor to form high-temperature slurry with certain pressure, and the high-temperature slurry is sprayed on a material bed of a rotary drum granulator through a spray head on the tubular reactor to be mixed with returned materials for hot melt granulation. Although part of raw materials are liquid and gas, a large amount of raw materials are solid materials (phosphorus in the concentrated phosphoric acid ammonification granulation is a full liquid material), more or less secondary processing exists, and the raw material cost and the compound fertilizer production cost are increased. The mixed acid full slurry pelletization is mainly applied to a device for producing sulfur-based compound fertilizer by dechlorination and conversion of potassium chloride, phosphorus and potassium raw materials are mixed liquid and gas ammonia to form high-temperature slurry with certain pressure by neutralization reaction in a tubular reactor, and the high-temperature slurry is sprayed on a material bed of a rotary drum pelletizer through a spray head on the tubular reactor to be mixed with return materials for hot melt pelletization.
With the continuous advancement of technology, few enterprises have begun to use urea sulfate ammoniation slurry spraying. The urea sulfate ammoniation slurry spraying method is an advanced granulation method which integrates the advantages of the various granulation methods, and is suitable for the compound fertilizer which can be produced by the granulation method, the compound fertilizer which can not be or is difficult to produce by the granulation method, and elemental fertilizers such as ammonium sulfate granulation, potassium fertilizer granulation, potassium sulfate granule and the like. However, in practical production, the urea sulfate reaction device used by the traditional urea sulfate process equipment has the advantages of complex structure, troublesome operation and short service period. When participating in granulation, the urea sulfate reaction device is usually required to be placed in a granulator, urea sulfate is sprayed to a material bed of the granulator, and a subsequent granulation link is performed. However, the whole process not only needs to discharge the granulated tail gas, but also needs to discharge the tail gas produced by urea sulfate, and the purification treatment is carried out, so that the production cost of the compound fertilizer is increased.
Disclosure of Invention
The utility model discloses a urea sulfate reaction device applied to compound fertilizers, which is used for reducing the preparation cost of the compound fertilizers.
The utility model provides a urea sulfate reaction device applied to compound fertilizers, which comprises:
the device comprises a urea valve, a sulfuric acid valve, a flow guiding chamber, a raw material stirring chamber, a urea sulfate reaction chamber, a reaction solution storage chamber and an atomization spraying chamber;
the diversion chamber is fixedly connected with the urea valve and the sulfuric acid valve;
the diversion chamber is connected with the raw material stirring chamber through a flange plate;
a spiral stirring device is arranged in the raw material stirring chamber;
a motor is arranged outside the raw material stirring chamber and is coupled with the spiral stirring device;
the lower end of the stirring chamber is connected with the urea sulfate reaction chamber through a solid-liquid separation sieve pipeline;
the lower end of the urea sulfate reaction chamber is connected with the reaction solution storage chamber;
the reaction solution storage chamber is connected with the atomization spraying chamber through a transfusion pipeline;
the upper end of the urea sulfate reaction chamber is connected with the spraying chamber through a gas pipeline.
Optionally, a stirrer is arranged in the urea sulfate reaction chamber;
the stirrer comprises a stirring rod and a stirring head;
the first end of the stirring rod is positioned on the upper side of the urea sulfate reaction chamber;
the second end of the stirring rod is connected with the stirring head.
Optionally, at least two auxiliary stirrers are placed in the urea sulfate reaction chamber;
the auxiliary stirring material is tetrachloroethylene balls with holes;
at least two through holes are formed in the tetrachloroethylene ball with the holes, and the through holes penetrate through the tetrachloroethylene ball with the holes.
Optionally, the stirring head comprises stirring blades and a solid-liquid screening protective sleeve;
the solid-liquid screening protective sleeve wraps the stirring fan blade;
the solid-liquid screening protective sleeve is provided with a liquid circulation hole, and the size of the liquid circulation hole is smaller than that of the tetrachloroethylene ball with the hole.
Optionally, the urea sulfate reaction chamber comprises a reaction tank and a filter chamber;
the filter chamber is positioned at the lower part of the reaction tank;
the filter chamber is funnel-shaped;
the lower side of the filtering chamber is connected with the upper side of the reaction solution storage chamber;
the upper part of the filtering chamber is provided with a normally closed filtering hole;
the diameter of the normally closed filtering holes is smaller than that of the tetrachloroethylene balls with holes.
Optionally, a flow guide partition plate is arranged in the flow guide chamber;
the flow guide partition plate divides the flow guide chamber into an upper flow guide chamber and a lower flow guide chamber;
the urea valve is connected with the upper diversion chamber so that urea solution enters the upper diversion chamber from top to bottom;
the sulfuric acid method door is connected with the lower diversion chamber so that sulfuric acid solution enters the lower diversion chamber from bottom to top.
Optionally, at least two auxiliary stirrers are placed in the raw material stirring chamber;
the auxiliary stirring material is tetrachloroethylene balls with holes;
at least two through holes are formed in the tetrachloroethylene ball with the holes, and the through holes penetrate through the tetrachloroethylene ball with the holes.
Optionally, an air valve is arranged on the air transmission pipeline;
the air valve is used for introducing high-pressure reaction tail gas into the atomizing spray chamber from top to bottom.
Optionally, an exhaust hole and an air pressure switch are arranged on the air valve;
the air pressure switch is used for detecting the pressure of the air transmission pipeline;
the air pressure switch is also used for opening the air exhaust hole.
Optionally, a liquid valve is arranged on the infusion pipeline;
the liquid valve is used for controlling urea sulfate in the reaction solution storage chamber to be input into the atomization spraying chamber.
From the above technical solutions, the embodiment of the present utility model has the following advantages:
in the utility model, the urea sulfate reaction device comprises a urea valve, a sulfuric acid valve, a flow guide chamber, a raw material stirring chamber, a urea sulfate reaction chamber, a reaction solution storage chamber and an atomization spraying chamber. The diversion chamber is fixedly connected with the urea valve and the sulfuric acid valve. The diversion chamber is connected with the raw material stirring chamber through a flange plate. A spiral stirring device is arranged in the raw material stirring chamber. The outside of the raw material stirring chamber is provided with a motor, and the motor is coupled with the spiral stirring device. The lower end of the stirring chamber is connected with the urea sulfate reaction chamber through a solid-liquid separation sieve pipeline. The lower end of the urea sulfate reaction chamber is connected with the reaction solution storage chamber. The reaction solution storage chamber is connected with the atomization spraying chamber through an infusion pipeline. The upper end of the urea sulfate reaction chamber is connected with the spraying chamber through a gas pipeline. In the diversion chamber, concentrated sulfuric acid and urea enter the proportion, then the concentrated sulfuric acid and the urea enter a raw material stirring chamber for stirring, the concentrated sulfuric acid and the urea are introduced into a urea sulfate reaction chamber for full reaction after being uniformly stirred, then urea sulfate solution after full reaction is introduced into a reaction solution storage chamber, the urea sulfate solution is introduced into an atomization spraying chamber through a pipeline, and then high-pressure tail gas generated during the reaction of phosphoric acid and urea is collected through a gas transmission pipeline and is introduced into the atomization spraying chamber for pressurized spraying. The tail gas is utilized to the link of pressurized spraying, so that pressurized treatment is not required to be carried out by installing pressurizing equipment, and the preparation cost of the compound fertilizer is reduced.
Drawings
In order to more clearly illustrate the technical solutions of the embodiments of the present utility model, the drawings that are needed in the embodiments or the description of the prior art will be briefly described below, it being obvious that the drawings in the following description are only some embodiments of the present utility model, and that other drawings may be obtained according to these drawings without inventive effort for a person skilled in the art.
FIG. 1 is a schematic view showing an example of a urea sulfate reaction apparatus applied to a compound fertilizer according to the present utility model.
Detailed Description
In the following description, for purposes of explanation and not limitation, specific details are set forth such as the particular system architecture, techniques, etc., in order to provide a thorough understanding of the embodiments of the present utility model. It will be apparent, however, to one skilled in the art that the present utility model may be practiced in other embodiments that depart from these specific details. In other instances, detailed descriptions of well-known systems, devices, circuits, and methods are omitted so as not to obscure the description of the present utility model with unnecessary detail.
It should be understood that the terms "comprises" and/or "comprising," when used in this specification and the appended claims, specify the presence of stated features, integers, steps, operations, elements, and/or components, but do not preclude the presence or addition of one or more other features, integers, steps, operations, elements, components, and/or groups thereof.
It should also be understood that the term "and/or" as used in the present specification and the appended claims refers to any and all possible combinations of one or more of the associated listed items, and includes such combinations.
As used in the present description and the appended claims, the term "if" may be interpreted as "when..once" or "in response to a determination" or "in response to detection" depending on the context. Similarly, the phrase "if a determination" or "if a [ described condition or event ] is detected" may be interpreted in the context of meaning "upon determination" or "in response to determination" or "upon detection of a [ described condition or event ]" or "in response to detection of a [ described condition or event ]".
Furthermore, the terms "first," "second," "third," and the like in the description of the present specification and in the appended claims, are used for distinguishing between descriptions and not necessarily for indicating or implying a relative importance.
Reference in the specification to "one embodiment" or "some embodiments" or the like means that a particular feature, structure, or characteristic described in connection with the embodiment is included in one or more embodiments of the utility model. Thus, appearances of the phrases "in one embodiment," "in some embodiments," "in other embodiments," and the like in the specification are not necessarily all referring to the same embodiment, but mean "one or more but not all embodiments" unless expressly specified otherwise. The terms "comprising," "including," "having," and variations thereof mean "including but not limited to," unless expressly specified otherwise.
In the prior art, the current production process of the high-concentration compound fertilizer in China mainly comprises the following steps: the method comprises four main production processes of a granulating method, a high-tower granulating and ammonifying granulating method of a melt (comprising a dilute sulfuric acid ammonifying granulating process and a concentrated phosphoric acid ammonifying granulating process), and an ammonifying granulating process of mixed acid full slurry of potassium bisulfate and phosphoric acid. The granulating method is a traditional high-concentration compound fertilizer production process, and various production raw materials are mixed and then are heated by steam in a rotary drum granulator and supplemented with proper water for kneading and granulating.
With the continuous advancement of technology, few enterprises have begun to use urea sulfate ammoniation slurry spraying. The urea sulfate ammoniation slurry spraying method is an advanced granulation method which integrates the advantages of the various granulation methods, and is suitable for the compound fertilizer which can be produced by the granulation method, the compound fertilizer which can not be or is difficult to produce by the granulation method, and elemental fertilizers such as ammonium sulfate granulation, potassium fertilizer granulation, potassium sulfate granule and the like. However, in practical production, the urea sulfate reaction device used by the traditional urea sulfate process equipment has the advantages of complex structure, troublesome operation and short service period. When participating in granulation, the urea sulfate reaction device is usually required to be placed in a granulator, urea sulfate is sprayed to a material bed of the granulator, and a subsequent granulation link is performed. However, the whole process not only needs to discharge the granulated tail gas, but also needs to discharge the tail gas produced by urea sulfate, and the purification treatment is carried out, so that the production cost of the compound fertilizer is increased.
Based on the above, the utility model discloses a urea sulfate reaction device applied to compound fertilizers, which is used for reducing the preparation cost of the compound fertilizers.
The following description of the embodiments of the present utility model will be made clearly and fully with reference to the accompanying drawings, in which it is evident that the embodiments described are only some, but not all embodiments of the utility model. All other embodiments, which can be made by those skilled in the art based on the embodiments of the utility model without making any inventive effort, are intended to be within the scope of the utility model.
Referring to fig. 1, the present utility model provides an embodiment of a urea sulfate reaction apparatus for compound fertilizer, comprising:
the urea valve 1, the sulfuric acid valve 2, the diversion chamber 3, the raw material stirring chamber 4, the urea sulfate reaction chamber 5, the reaction solution storage chamber 6 and the atomization spraying chamber 7;
the diversion chamber 3 is fixedly connected with the urea valve 1 and the sulfuric acid valve 2;
the diversion chamber 3 is connected with the raw material stirring chamber 4 through a flange 8;
a spiral stirring device 9 is arranged in the raw material stirring chamber 4;
a motor 10 is arranged outside the raw material stirring chamber 4, and the motor 10 is coupled with the spiral stirring device 9;
the lower end of the stirring chamber is connected with the urea sulfate reaction chamber 5 through a solid-liquid separation sieve pipeline 11;
the lower end of the urea sulfate reaction chamber 5 is connected with the reaction solution storage chamber 6;
the reaction solution storage chamber 6 is connected with the atomizing spray chamber 7 through a transfusion pipeline 12;
the upper end of the urea sulfate reaction chamber 5 is connected with the spraying chamber through a gas pipeline 17.
In this embodiment, the urea sulfate reaction device comprises a urea valve 1, a sulfuric acid valve 2, a diversion chamber 3, a raw material stirring chamber 4, a urea sulfate reaction chamber 5, a reaction solution storage chamber 6 and an atomization spraying chamber 7. The diversion chamber 3 is fixedly connected with the urea valve 1 and the sulfuric acid valve 2. The diversion chamber 3 is connected with the raw material stirring chamber 4 through a flange plate 8. A spiral stirring device 9 is arranged in the raw material stirring chamber 4. The motor 10 is arranged outside the raw material stirring chamber 4, and the motor 10 is coupled with the spiral stirring device 9. The lower end of the stirring chamber is connected with the urea sulfate reaction chamber 5 through a solid-liquid separation sieve pipeline 11. The lower end of the urea sulfate reaction chamber 5 is connected with the reaction solution storage chamber 6. The reaction solution storage chamber 6 is connected with the atomizing spray chamber 7 through a transfusion pipeline 12. The upper end of the urea sulfate reaction chamber 5 is connected with the spraying chamber through a gas pipeline 17. In the diversion chamber 3, concentrated sulfuric acid and urea enter the proportion, then the concentrated sulfuric acid and the urea enter the raw material stirring chamber 4 for stirring, the urea sulfate reaction chamber 5 is filled for full reaction after uniform stirring, then the urea sulfate solution after full reaction is input into the reaction solution storage chamber 6, the urea sulfate solution is input into the atomization spraying chamber 7 through a pipeline, and then the high-pressure tail gas generated during the reaction of phosphoric acid and urea is collected through the gas transmission pipeline 17 and is input into the atomization spraying chamber 7 for pressurized spraying. The tail gas is utilized to the link of pressurized spraying, so that pressurized treatment is not required to be carried out by installing pressurizing equipment, and the preparation cost of the compound fertilizer is reduced.
Optionally, a stirrer 13 is arranged in the urea sulfate reaction chamber 5;
the stirrer 13 comprises a stirring rod and a stirring head;
the first end of the stirring rod is positioned on the upper side of the urea sulfate reaction chamber 5;
the second end of the stirring rod is connected with the stirring head.
In this embodiment, when the mixed solution in the raw material stirring chamber 4 is unevenly mixed, the mixed solution can be mixed by pushing the mixed solution forward and mixing the mixed solution on the surface of the spiral stirring device 9 in addition to the stirring function of the spiral stirring device 9 in the raw material stirring chamber 4 by the stirrer 13 in the urea sulfate reaction chamber 5.
The stirrer 13 comprises a stirring rod and a stirring head, a first end of the stirring rod is positioned on the upper side of the urea sulfate reaction chamber 5, and a second end of the stirring rod is connected with the stirring head. The stirrer 13 in the urea sulfate reaction chamber 5 is more suitable for stirring the mixed liquid more uniformly than the spiral stirring device 9 in the raw material stirring chamber 4 to promote the reaction, and the whole urea sulfate reaction chamber 5 is easier to clean in the cleaning process of subsequent equipment.
Optionally, at least two auxiliary stirrers 14 are placed in the urea sulfate reaction chamber 5;
the auxiliary stirring objects 14 are tetrachloroethylene balls with holes;
at least two through holes are formed in the tetrachloroethylene ball with the holes, and the through holes penetrate through the tetrachloroethylene ball with the holes.
In the urea sulfate reaction chamber 5, a plurality of auxiliary stirring objects 14 can be placed in the urea sulfate reaction chamber to enable the reaction process to be smoother, in this embodiment, the auxiliary stirring objects 14 are tetrachloroethylene, specifically, tetrachloroethylene balls with holes, wherein the holes are through holes, that is, the whole tetrachloroethylene balls are penetrated, so that the mixed liquid can flow more irregularly in the stirring process of the tetrachloroethylene balls with holes, and further, the liquid is uniformly mixed. At least two through holes are formed in the tetrachloroethylene ball with holes, so that the mixed liquid is more easily influenced by the tetrachloroethylene ball with holes.
Optionally, the stirring head comprises stirring blades and a solid-liquid screening protective sleeve;
the solid-liquid screening protective sleeve wraps the stirring fan blade;
the solid-liquid screening protective sleeve is provided with a liquid circulation hole, and the size of the liquid circulation hole is smaller than that of the tetrachloroethylene ball with the hole.
The stirring head comprises stirring blades and a solid-liquid screening protective sleeve, and aims to protect the blades, and the stirring blades need to avoid cutting the auxiliary stirring objects 14 because at least two auxiliary stirring objects 14 are added in the urea sulfate reaction chamber 5. The solid-liquid screening protective sleeve is provided with the liquid flowing hole, so that liquid can be influenced by the rotating fan blade, the size of the liquid flowing hole is smaller than that of the tetrachloroethylene ball with the hole, the tetrachloroethylene ball with the hole is prevented from entering the solid-liquid screening protective sleeve to be cut by the stirring fan blade, and the stirring head is blocked.
Optionally, the urea sulfate reaction chamber 5 includes a reaction tank 51 and a filter chamber 52;
the filtering chamber 52 is positioned at the lower part of the reaction tank 51;
the filter chamber 52 is funnel-shaped;
the lower side of the filtering chamber 52 is connected with the upper side of the reaction solution storage chamber 6;
a normally closed filter hole 521 is arranged at the upper part of the filter chamber 52;
the normally closed filter holes 521 have a smaller diameter than the perforated tetrachloroethylene balls.
Since the urea sulfate reaction chamber 5 is added with the auxiliary stirring material 14, the auxiliary stirring material 14 needs to be filtered out, and the reaction-completed solution is fed into the reaction solution storage chamber 6. In this embodiment, the urea sulfate reaction chamber 5 is divided into a reaction tank 51 and a filtration chamber 52, the filtration chamber 52 is located at the lower part of the reaction tank 51, and the reaction can be completed to filter downwards. The filter chamber 52 is funnel-shaped and serves as a collection. The lower side of the filtering chamber 52 is connected to the upper side of the reaction solution storage chamber 6, so that the reaction solution storage chamber 6 receives the reaction-completed solution after the completion of the filtering.
The filtering chamber 52 is provided with a normally closed filtering hole 521 at the upper part, the normally closed filtering hole 521 receives the switch control, when the reaction is not completed, the reaction is in a closed state, and when the reaction is completed, the reaction can be started, the diameter of the normally closed filtering hole 521 is smaller than that of the tetrachloroethylene ball with holes, and the tetrachloroethylene ball with holes is placed to fall. And even if the tetrachloroethylene ball with holes blocks the normally closed filter holes 521, the reaction solution can enter the filter chamber 52 through the through holes due to the presence of at least two through holes.
Optionally, a baffle 31 is disposed in the diversion chamber 3;
the flow guide partition plate 31 divides the flow guide chamber 3 into an upper flow guide chamber 3 and a lower flow guide chamber 3;
the urea valve 1 is connected with the upper diversion chamber 3 so that urea solution enters the upper diversion chamber 3 from top to bottom;
the sulfuric acid method door is connected with the lower diversion chamber 3 so that sulfuric acid solution enters the lower diversion chamber 3 from bottom to top.
The flow guiding chamber 3 is internally provided with a flow guiding baffle plate 31, and the flow guiding baffle plate has the function of firstly proportioning and guiding two liquids, the flow guiding baffle plate 31 divides the flow guiding chamber 3 into an upper flow guiding chamber 3 and a lower flow guiding chamber 3, and the urea valve 1 is connected with the upper flow guiding chamber 3 so that urea solution enters the upper flow guiding chamber 3 from top to bottom. The sulfuric acid method gate is connected with the lower diversion chamber 3, so that sulfuric acid solution enters the lower diversion chamber 3 from bottom to top, and the sulfuric acid is safer to input from bottom to top.
Optionally, at least two auxiliary stirrers 14 are placed inside the raw material stirring chamber 4;
the auxiliary stirring objects 14 are tetrachloroethylene balls with holes;
at least two through holes are formed in the tetrachloroethylene ball with the holes, and the through holes penetrate through the tetrachloroethylene ball with the holes.
At least two auxiliary agitators 14 are placed inside the raw material stirring chamber 4, the function of which has been described in the above paragraphs of the urea sulfate reaction chamber 5 and will not be described here.
Optionally, the gas pipeline 17 is provided with a gas valve 15;
the air valve 15 is used for introducing high-pressure reaction tail gas into the atomizing spray chamber 7 from top to bottom.
The air valve 15 is arranged on the air transmission pipeline 17, so that the output of the high-pressure tail gas of the urea sulfate reaction chamber 5 can be freely controlled, and the atomization spraying chamber 7 can be better controlled to finish the spraying operation.
Optionally, an exhaust hole and an air pressure switch are arranged on the air valve 15;
the air pressure switch is used for detecting the pressure of the air conveying pipeline 17;
the air pressure switch is also used for opening the air exhaust hole.
The air valve 15 is provided with an air vent and an air pressure switch, so that when the high-pressure tail gas of the urea sulfate reaction chamber 5 is excessive, the pressure is caused to the air conveying pipeline 17, and when the pressure reaches a certain value, the air pressure switch is required to open the air vent to release pressure, so that the air conveying pipeline 17 is prevented from being burst
Optionally, the infusion tube 12 is provided with a liquid valve 16;
the liquid valve 16 is used for controlling the urea sulfate in the reaction solution storage chamber 6 to be fed into the atomizing spray chamber 7.
In the present utility model, the terms "upper", "lower", "left", "right", "front", "rear", "top", "bottom", "inner", "outer", "middle", "vertical", "horizontal", "lateral", "longitudinal", and the like indicate orientations or positional relationships based on the orientations or positional relationships shown in the drawings, and are merely used to illustrate the relative positional relationships between the components or portions, and do not particularly limit the specific mounting orientations of the components or portions.
Also, some of the terms described above may be used to indicate other meanings in addition to orientation or positional relationships, for example, the term "upper" may also be used to indicate some sort of attachment or connection in some cases. The specific meaning of these terms in the present utility model will be understood by those of ordinary skill in the art according to the specific circumstances.
Furthermore, the terms "mounted," "configured," "provided," "connected," and "connected" are to be construed broadly. For example, it may be a fixed connection, a removable connection, or a unitary construction; may be a mechanical connection, or an electrical connection; may be directly connected, or indirectly connected through intervening media, or may be in internal communication between two devices, elements, or components. The specific meaning of the above terms in the present utility model can be understood by those of ordinary skill in the art according to the specific circumstances.
In addition, the structures, proportions, sizes, etc. shown in the drawings are shown only in connection with the present disclosure for the purpose of understanding and reading by those skilled in the art, and are not intended to limit the scope of the utility model, which is defined by the appended claims, so that any structural modifications, proportional changes, or dimensional adjustments should not be made in the essential significance of the present disclosure without affecting the efficacy or achievement of the present utility model.
Claims (10)
1. A urea sulfate reaction device for a compound fertilizer, comprising:
the device comprises a urea valve, a sulfuric acid valve, a flow guiding chamber, a raw material stirring chamber, a urea sulfate reaction chamber, a reaction solution storage chamber and an atomization spraying chamber;
the diversion chamber is fixedly connected with the urea valve and the sulfuric acid valve;
the diversion chamber is connected with the raw material stirring chamber through a flange plate;
a spiral stirring device is arranged in the raw material stirring chamber;
a motor is arranged outside the raw material stirring chamber and is coupled with the spiral stirring device;
the lower end of the stirring chamber is connected with the urea sulfate reaction chamber through a solid-liquid separation sieve pipeline;
the lower end of the urea sulfate reaction chamber is connected with the reaction solution storage chamber;
the reaction solution storage chamber is connected with the atomization spraying chamber through a transfusion pipeline;
the upper end of the urea sulfate reaction chamber is connected with the spraying chamber through a gas pipeline.
2. The urea sulfate reaction device according to claim 1, wherein a stirrer is provided in the urea sulfate reaction chamber;
the stirrer comprises a stirring rod and a stirring head;
the first end of the stirring rod is positioned on the upper side of the urea sulfate reaction chamber;
the second end of the stirring rod is connected with the stirring head.
3. The urea sulfate reaction device of claim 2, wherein at least two auxiliary agitators are placed in the urea sulfate reaction chamber;
the auxiliary stirring material is tetrachloroethylene balls with holes;
at least two through holes are formed in the tetrachloroethylene ball with the holes, and the through holes penetrate through the tetrachloroethylene ball with the holes.
4. A urea sulfate reaction device according to claim 3, wherein the stirring head comprises stirring blades and a solid-liquid screening protective sleeve;
the solid-liquid screening protective sleeve wraps the stirring fan blade;
the solid-liquid screening protective sleeve is provided with a liquid circulation hole, and the size of the liquid circulation hole is smaller than that of the tetrachloroethylene ball with the hole.
5. A urea sulfate reaction device according to claim 3, characterized in that the urea sulfate reaction chamber comprises a reaction tank and a filter chamber;
the filter chamber is positioned at the lower part of the reaction tank;
the filter chamber is funnel-shaped;
the lower side of the filtering chamber is connected with the upper side of the reaction solution storage chamber;
the upper part of the filtering chamber is provided with a normally closed filtering hole;
the diameter of the normally closed filtering holes is smaller than that of the tetrachloroethylene balls with holes.
6. The urea sulfate reaction device according to any one of claims 1 to 5, wherein a baffle plate is provided in the baffle chamber;
the flow guide partition plate divides the flow guide chamber into an upper flow guide chamber and a lower flow guide chamber;
the urea valve is connected with the upper diversion chamber so that urea solution enters the upper diversion chamber from top to bottom;
the sulfuric acid method door is connected with the lower diversion chamber so that sulfuric acid solution enters the lower diversion chamber from bottom to top.
7. The urea sulfate reaction device according to any one of claims 1 to 5, wherein at least two auxiliary agitators are placed inside the raw material agitating chamber;
the auxiliary stirring material is tetrachloroethylene balls with holes;
at least two through holes are formed in the tetrachloroethylene ball with the holes, and the through holes penetrate through the tetrachloroethylene ball with the holes.
8. The urea sulfate reaction device according to any one of claims 1 to 5, wherein a gas valve is provided on the gas line;
the air valve is used for introducing high-pressure reaction tail gas into the atomizing spray chamber from top to bottom.
9. The urea sulfate reaction device according to claim 8, wherein the air valve is provided with an air vent and an air pressure switch;
the air pressure switch is used for detecting the pressure of the air transmission pipeline;
the air pressure switch is also used for opening the air exhaust hole.
10. The urea sulfate reaction device according to any one of claims 1 to 5, wherein a liquid valve is provided on the liquid transfer line;
the liquid valve is used for controlling urea sulfate in the reaction solution storage chamber to be input into the atomization spraying chamber.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202320116799.5U CN219540283U (en) | 2023-02-03 | 2023-02-03 | Be applied to compound fertilizer's urea sulfate reaction unit |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202320116799.5U CN219540283U (en) | 2023-02-03 | 2023-02-03 | Be applied to compound fertilizer's urea sulfate reaction unit |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN219540283U true CN219540283U (en) | 2023-08-18 |
Family
ID=87708064
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202320116799.5U Active CN219540283U (en) | 2023-02-03 | 2023-02-03 | Be applied to compound fertilizer's urea sulfate reaction unit |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN219540283U (en) |
-
2023
- 2023-02-03 CN CN202320116799.5U patent/CN219540283U/en active Active
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN103657498B (en) | The device of the production urea for vehicle aqueous solution and its using method | |
| CN102942185B (en) | Method for preparing nano-scale white carbon black product | |
| AU2021411535A1 (en) | Method for preparing high-solubility nitrogen-phosphorus water-soluble fertilizer | |
| CN208987789U (en) | A kind of cooling equipment of granulation feed | |
| CN219540283U (en) | Be applied to compound fertilizer's urea sulfate reaction unit | |
| CN102583484B (en) | Carbonization kettle and method for preparing nanometer calcium carbonate by using same | |
| CN204151247U (en) | A kind of for the prilling granulator after nitrophosphate fertilizer evaporation technology | |
| CN105233756B (en) | A kind of granulating system and its method | |
| CN108947099A (en) | A kind of advanced oxidation processes treatment process device and method of the waste water containing sodium phenolate | |
| US4604126A (en) | NP/NPK fertilizer granules comprised of ammonium phosphate | |
| CN210367481U (en) | Compound fertilizer production prilling granulator | |
| CN103274797B (en) | Preparation method and activating reactor for granular potassium-containing humic acid urea | |
| CN203220899U (en) | Multi-tandem-chamber liquid-solid mixing and reaction continuation device | |
| CN108314632A (en) | A method of recycling biruea prepares azodicarbonamide | |
| CN209872817U (en) | Continuous production device for acid fertilizer | |
| CN105316480A (en) | Adding method and device of inhibitor used for reducing generation of dioxin in sintering process | |
| CN2936413Y (en) | High efficiency stirrer of high tower prilling smelting slurry mixing bath | |
| CN210711334U (en) | Organic-inorganic compound fertilizer production line | |
| CN211612676U (en) | Reation kettle that production liquid is fertile | |
| CN211612118U (en) | Urea prilling tower top of tower dust recovery device | |
| CN209481451U (en) | A kind of sludge drying prilling granulator | |
| CN207872101U (en) | A kind of novel comminutor | |
| CN212147089U (en) | Nylon 6 semi-dull slice feeding system | |
| CN205127885U (en) | Pelleting system | |
| CN213493590U (en) | Reaction unit for chemical industry experiments |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant |