CN202499710U - Single-pipe reactor for producing diammonium phosphate - Google Patents
Single-pipe reactor for producing diammonium phosphate Download PDFInfo
- Publication number
- CN202499710U CN202499710U CN2012200457193U CN201220045719U CN202499710U CN 202499710 U CN202499710 U CN 202499710U CN 2012200457193 U CN2012200457193 U CN 2012200457193U CN 201220045719 U CN201220045719 U CN 201220045719U CN 202499710 U CN202499710 U CN 202499710U
- Authority
- CN
- China
- Prior art keywords
- nozzle
- diammonium phosphate
- reactor drum
- pipe
- inlet pipe
- 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.)
- Expired - Fee Related
Links
Images
Landscapes
- Manufacture And Refinement Of Metals (AREA)
Abstract
The utility model discloses a single-pipe reactor for producing diammonium phosphate. The single-pipe reactor for producing diammonium phosphate comprises a phosphoric acid inlet pipe (1), a liquid ammonia inlet pipe (2), a reaction pipe (3), a first nozzle (4) and a second nozzle (5). The phosphoric acid inlet pipe (1) and the liquid ammonia inlet pipe (2) are disposed at the end of the reaction pipe (3). The first nozzle (4) and the second nozzle (5) are disposed on the side wall of the reaction pipe (3). The reaction pipe (3), the first nozzle (4) and the second nozzle (5) are all straight pipes. The single-pipe reactor is slantingly disposed above a discharge end of a granulator. By the single-pipe reactor for producing diammonium phosphate, the problem that phosphoric acid with high impurity content is easy to scale and causes severe blockage in reaction is solved, and yield and quality of diammonium phosphate are increased greatly.
Description
Technical field
The utility model relates to a kind of single hose reactor drum, relates in particular to a kind of single hose reactor drum of production diammonium phosphate.
Background technology
China some areas (like Yichang) phosphorus ore grade is low; Foreign matter content is high; After ore dressing; Foreign matter content is still higher when the production diammonium phosphate, how to use the low phosphorus ore of grade such as ore deposit, Yichang to produce the fine diammonium phosphate, and to reach internal class product level be a difficult problem of pendulum in face of ours.
At present can use Yi Changkuang to produce the fine diammonium phosphate, but because of the fluctuation of ore deposit foreign matter content, its quality control is unstable, and is bad during fashion through technological improvement utilization hybrid technique.For stablizing the product appearance quality of diammonium phosphate, existing plan comes the production diammonium phosphate through research and development utilization single hose reactor drum.
Traditional single hose reactor drum is stricter than groove type reactor to the requirement of phosphoric acid quality; And the heat of reaction during the production diammonium phosphate in the tablets press is big; Need remove heat through strengthening air capacity; In addition, also there is effusion ammonia amount big (account for total ammonia amount 15%~20%), problem such as the exhaust scrubber load is big.
Summary of the invention
The purpose of the utility model is to provide a kind of single hose reactor drum that can utilize the phosphorus ore production high-quality diammonium phosphate that grade is low, foreign matter content is high, and solves the above-mentioned problems that exist when traditional single hose reactor drum is produced simultaneously.
The concrete technical scheme of the single hose reactor drum of a kind of production diammonium phosphate of the utility model is:
A kind of single hose reactor drum of production diammonium phosphate; Comprise phosphoric acid inlet pipe, liquefied ammonia inlet pipe, reaction tubes, first nozzle and second nozzle; Phosphoric acid inlet pipe and liquefied ammonia inlet pipe are arranged on the end of reaction tubes; First nozzle and second nozzle are arranged on the sidewall of reaction tubes, and reaction tubes, first nozzle and second nozzle are straight pipe type, and the single hose reactor drum is obliquely installed the top at the tablets press discharge end.
Wherein, single hose reactor drum and tablets press discharge end are 3~10 ° angle of inclination.Be provided with the venturi tube conversion zone in the reaction tubes.
The single hose reactor drum of the production diammonium phosphate of the utility model has solved the problem that traditional single hose reactor drum exists through be installed in tablets press discharge end top by certain angle of inclination (3~10 °); Change single hose reactor drum production diammonium phosphate and only improved output, the problem that does not improve the quality.
In addition,, solved the more phosphoric acid of foreign matter content and when reaction, be prone to fouling and serious blocking problem, improved the output and the quality of diammonium phosphate greatly through reform and innovation to the single hose reactor drum.Particularly present dilution day by day along with domestic phosphate rock resource; It uses the large-scale diammonium phosphate device product quality of hybrid technique that decline is in various degree all arranged; The single hose reactor drum of the utility model is strong to the flexibility of phosphorus ore quality, has obvious competitive advantages.
Description of drawings
Fig. 1 is the forward sectional view of diammonium phosphate tablets press that the single hose reactor drum of the utility model is installed;
Fig. 2 is the side sectional view of diammonium phosphate tablets press that the single hose reactor drum of the utility model is installed.
Embodiment
In order better to understand purpose, structure and the function of the utility model,, the single hose reactor drum of a kind of production diammonium phosphate of the utility model is done further detailed description below in conjunction with accompanying drawing.
As shown in Figure 1, the single hose reactor drum of the production diammonium phosphate of the utility model comprises phosphoric acid inlet pipe 1, liquefied ammonia inlet pipe 2, reaction tubes 3, first nozzle 4 and second nozzle 5.Wherein, Phosphoric acid import 1 pipe and liquefied ammonia inlet pipe 2 are arranged on the end of reaction tubes 3; Phosphoric acid inlet pipe 1 links to each other with phosphoric acid storage tank (not shown); Be used for that phosphoric acid is input into reaction tubes 3 and carry out neutralization reaction, liquefied ammonia inlet pipe 2 links to each other with the liquid ammonia storage tank (not shown), is used for liquefied ammonia is input into reaction tubes 3 and phosphatase reaction.
The sidewall of reaction tubes 3 is provided with first nozzle 4 and second nozzle 5; The phosphor ammonium slurry that phosphoric acid in the reaction tubes 3 and liquefied ammonia carry out generating after the neutralization reaction can be ejected in the tablets press through first nozzle 4 and second nozzle 5, to carry out the subsequent production process in the tablets press.First nozzle 4 in the utility model and the big I of second nozzle 5 are specifically set according to slip viscosity, atomizing effect and pressure etc.
In addition; The reaction tubes 3 in the single hose reactor drum of the production diammonium phosphate of the utility model and first nozzle 4 thereof and second nozzle 5 all are straight pipe type; And the single hose reactor drum of the utility model is installed in the top of tablets press discharge end with 3~10 ° angle of inclination; Thereby the heat of reaction that has solved traditional single hose reactor drum existence is big, effusion ammonia amount is many, the exhaust scrubber load heavily waits defective; Change traditional single hose reactor drum production diammonium phosphate and only improved output, the problem that does not improve the quality.
Fig. 1 and Fig. 2 are installed to the structural representation in the tablets press for the single hose reactor drum of the utility model; Wherein, The tablets press 6 preferred rotary drum granulators that adopt; And also can be provided with ammonia sparger 7 at first nozzle 4 of single hose reactor drum and the opening part of second nozzle 5, make that the phosphor ammonium slurry of ejection can carry out the secondary neutralization reaction with ammonia fully in tablets press from first nozzle 4 and second nozzle 5.Ammonia sparger 7 can adopt the structure formation of ammonia sparger commonly used in this area.
The production process of the diammonium phosphate of the single hose reactor drum of employing the utility model is:
SPA, is specially from phosphoric acid inlet pipe 1 entering reaction tubes 3 to tubular reactor through pump delivery after the tail system of washing absorbs ammonia, and liquefied ammonia then is transported in the reaction tubes 3 through liquefied ammonia inlet pipe 2 by liquid ammonia storage tank.Liquefied ammonia and phosphoric acid carry out neutralization reaction in reaction tubes 3, produce phosphor ammonium slurry.
Further, phosphor ammonium slurry sprays in the tablets press 6 through first nozzle 4 and second nozzle 5.The liquefied ammonia of phosphor ammonium slurry ejection in tablets press 6 and in the ammonia sparger 7 carries out the secondary neutralization reaction again, and carries out granulation.
Product after the granulation sieves and fragmentation after getting into the drying machine drying, and the qualified particle entering parcel tube after the screening wraps up, and the finished product behind the parcel is sent into and packed after cool off in the storehouse of loosing.
More than by specific embodiment the utility model is further described; But it should be understood that; Here concrete description; Should not be construed as the qualification to the essence and the scope of the utility model, the various modifications that the one of ordinary skilled in the art makes the foregoing description after reading this specification sheets all belong to the scope that the utility model is protected.
Claims (3)
1. single hose reactor drum of producing diammonium phosphate; It is characterized in that; Comprise phosphoric acid inlet pipe (1), liquefied ammonia inlet pipe (2), reaction tubes (3), first nozzle (4) and second nozzle (5), phosphoric acid inlet pipe (1) and liquefied ammonia inlet pipe (2) are arranged on the end of reaction tubes (3), and first nozzle (4) and second nozzle (5) are arranged on the sidewall of reaction tubes (3); Reaction tubes (3), first nozzle (4) and second nozzle (5) are straight pipe type, and the single hose reactor drum is obliquely installed the top at the tablets press discharge end.
2. the single hose reactor drum of production diammonium phosphate according to claim 1 is characterized in that, single hose reactor drum and tablets press discharge end are 3~10 ° angle of inclination.
3. the single hose reactor drum of production diammonium phosphate according to claim 1 is characterized in that, reaction tubes is provided with the venturi tube conversion zone in (3).
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN2012200457193U CN202499710U (en) | 2012-02-06 | 2012-02-06 | Single-pipe reactor for producing diammonium phosphate |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN2012200457193U CN202499710U (en) | 2012-02-06 | 2012-02-06 | Single-pipe reactor for producing diammonium phosphate |
Publications (1)
Publication Number | Publication Date |
---|---|
CN202499710U true CN202499710U (en) | 2012-10-24 |
Family
ID=47036330
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN2012200457193U Expired - Fee Related CN202499710U (en) | 2012-02-06 | 2012-02-06 | Single-pipe reactor for producing diammonium phosphate |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN202499710U (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103664239A (en) * | 2013-11-29 | 2014-03-26 | 安徽六国化工股份有限公司 | Gunite pelleting machine for producing diammonium phosphate |
-
2012
- 2012-02-06 CN CN2012200457193U patent/CN202499710U/en not_active Expired - Fee Related
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103664239A (en) * | 2013-11-29 | 2014-03-26 | 安徽六国化工股份有限公司 | Gunite pelleting machine for producing diammonium phosphate |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN103848670B (en) | A kind of with the technique of phosphorus ammonium thickened pulp One-step production high-concentration compound fertilizer | |
CN101850989A (en) | Preparation method of large-particle ammonium sulfate | |
CN100371238C (en) | Method for producing diammonium phosphate by concentrating acid slime, and secondary ammoniation reactor | |
CN202499710U (en) | Single-pipe reactor for producing diammonium phosphate | |
CN102674904B (en) | Diammonium phosphate system and production technique for producing diammonium phosphate with single-tube reactor | |
CN102731191B (en) | Neutralization process for ammonia in a mother liquor used for producing nitric acid phosphate fertilizer | |
CN205815385U (en) | A kind of phosphoric acid tail gas processing system | |
CN202671209U (en) | Mother liquor ammonia neutralization device for nitric phosphate production | |
CN101734813A (en) | Technology for recovering ammonium sulfate by waste acid pickle generated in process of producing cyanuric acid and equipment therefor | |
CN206108901U (en) | A highly efficient reaction cauldron for diammonium phosphate production | |
CN102924128B (en) | Neutralization apparatus for nitric phosphate fertilizer production mother liquid ammonia neutralization process | |
CN201721895U (en) | Energy-saving and noise-reduction sandstone aggregate conveying shuttle groove | |
CN205635411U (en) | Improve energy utilization's compound fertilizer production equipment | |
CN202063847U (en) | Ammonization-granulating barrel with ammonia distributor | |
CN204058292U (en) | A kind of phosphorus ammonium sludge produces nitro-compound fertilizer device | |
CN102249776B (en) | Ammonification granulation cylinder with ammonia distributor | |
CN205833396U (en) | A kind of sour method composite heat transfer dilute sulfuric acid spray appliance | |
CN205313426U (en) | System for improve three acetylene hydrogenation selectivity in ethylene plant carbon | |
CN202072637U (en) | Ammonification pelleting cylinder | |
CN202729807U (en) | Circular-flowing type energy-saving neutral reactor in ammonium phosphate systematic production | |
CN203373155U (en) | Improved ammonium phosphate flashing chamber structure | |
CN203346082U (en) | Rapid online cleaning device for tubular reactors of ammonium phosphate device | |
CN210187175U (en) | Energy-saving ammonia acid granulation device | |
CN203244939U (en) | Emulsion powder production system | |
CN102249822B (en) | Ammonization granulation cylinder |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20121024 Termination date: 20180206 |
|
CF01 | Termination of patent right due to non-payment of annual fee |