CN1884078A - Method for producing ammonium nitrate - Google Patents
Method for producing ammonium nitrate Download PDFInfo
- Publication number
- CN1884078A CN1884078A CN 200610012913 CN200610012913A CN1884078A CN 1884078 A CN1884078 A CN 1884078A CN 200610012913 CN200610012913 CN 200610012913 CN 200610012913 A CN200610012913 A CN 200610012913A CN 1884078 A CN1884078 A CN 1884078A
- Authority
- CN
- China
- Prior art keywords
- pipe
- control valve
- steam
- tubular reactor
- measuring device
- 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.)
- Granted
Links
Landscapes
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
The invention discloses a manufacturing method of ammonium nitrate through neutralizing reaction of nitrate and ammonia gas in the pipe-typed reactor, setting temperature testing device on the pipe-typed reactor; connecting steam pipe on the feeder pipe of nitrate and ammonia gas; assembling steam control valve; interlocking temperature testing device, material controlling valve and steam controlling valve; closing material controlling valve once the reacting temperature reaches the preset control temperature; opening steam controlling valve to guide low-pressure steam to pipe typed reactor; brushing reacting material; avoiding accident to realize safe manufacturing.
Description
Technical Field
The invention relates to a method for producing ammonium nitrate by neutralizing nitric acid with ammonia, in particular to a method for producing ammonium nitrate by neutralizing nitric acid and gaseous ammonia in a tubular reactor.
Background
Nitric acid reacts with ammonia very vigorously to produce ammonium nitrate, and the reaction equation is as follows:
as can be seen from the equation, a large amount of heat is evolved during the reaction, and if the amount of heat evolved by the reaction is not effectively controlled or removed in time, the temperature of the reaction system rapidly increases. Ammonium nitrate can generate violent decomposition reaction at a certain high temperature, a large amount of gas is released, the volume is expanded sharply, and the danger of explosion is generated.
In addition, the amount of heat released by the reaction of nitric acid and ammonia is closely related to the concentration of nitric acid, and the higher the concentration of nitric acid involved in the reaction, the more vigorous the reaction, the more heat released.
The reaction for preparing ammonium nitrate solution is a normal pressure kettle type reaction, i.e. under normal pressure, the neutralization reaction of nitric acid and ammonia is carried out in a reaction kettle. The concentration of the nitric acid participating in the reaction is generally low (45-55%) because the heat generated in the reaction process cannot be removed in time, and if the nitric acid with higher concentration is used, the danger of explosion is generated. Meanwhile, the temperature of the neutralization steam generated in the reaction process of the normal pressure kettle type reaction is low, and the value of recycling is not available, so that the energy loss is caused.
However, in actual production, the concentration of the nitric acid participating in the reaction is always desired to be higher, so that energy can be saved and the production cost can be reduced. For this purpose, research institutes at home and abroad havedeveloped a tubular reactor for reacting ammonia and nitric acid in recent years, that is, nitric acid (higher concentration nitric acid can be used) and gaseous ammonia are introduced into a pipeline with a relatively small diameter in a certain proportion under a pressurized state to react to generate ammonium nitrate, and the ammonium nitrate is sent out from the other end of the tubular reactor. The tubular reactor is used for neutralization reaction of ammonia and nitric acid, and has the advantages of few materials participating in the reaction instantly, short retention time of the materials in a reaction area, avoidance of explosion danger, and capability of recycling heat energy of the neutralization steam generated by the reaction.
However, even if the method is adopted, because the nitric acid with higher concentration (56% -62%) is used for the neutralization reaction, although the reaction materials are few, the heat release is still very violent, and in addition, the reaction is continuously fed, the reaction is controlled improperly, the neutralization reaction is still easy to exceed the critical temperature, and explosion accidents occur.
Disclosure of Invention
The invention aims to provide a method for producing ammonium nitrate, which improves the explosion danger existing in the prior pressurized tubular reaction of nitric acid and gaseous ammonia, prevents the explosion to the maximum extent and realizes the safe production of ammonium nitrate.
The original ammonium nitrate production method is that nitric acid and gas ammonia are led into a tubular reactor through respective feeding pipes to carry out neutralization reaction, reaction products are discharged into a container from the other end of the tubular reactor, and ammonium nitrate solution is obtained after steam is flashed off.
The improvement measure of the invention is that a temperature measuring device is arranged on the tubular reactor to carry out real-time monitoring on the temperature in the tubular reactor; the nitric acid and ammonia feeding pipes are respectively connected with a steam pipe and are provided with a steam control valve; the temperature measuring device is interlocked with the material control valve on the nitric acid and ammonia feeding pipe and the steam control valve on each steam pipe. When the reaction temperature in the tubular reactor is lower than the set control temperature, the material control valves on the nitric acid and ammonia gas feeding pipes are allowed to be opened, the steam control valves on the steam pipes are closed, and the reaction in the tubular reactor is normally carried out. Once the reaction temperature in the tubular reactor reaches the set control temperature, the material control valves on the nitric acid and gas ammonia feeding pipes are immediately closed in an interlocking manner, the reaction materials are cut off, meanwhile, the steam control valve on the steam pipe connected with the nitric acid and gas ammonia feeding pipes is rapidly opened, low-pressure steam is introduced into the tubular reactor, the residual reaction materials in the tubular reactor are washed out, and the occurrence of explosion accidents in the tubular reactor is avoided.
The device is characterized in that a flash evaporation tank is connected behind the tubular reactor, the main function of the flash evaporation tank is two points, one is that the ammonium nitrate solution generated by the reaction is discharged into the flash evaporation tank from the other end of the tubular reactor, and after steam is flashed out, concentrated ammonium nitrate solution is obtained; and secondly, the reacted materials enter a relatively enlarged space, and even if a small amount of materials explode, the energy can be released in a larger space without danger.
However, because a certain amount of concentrated ammonium nitrate solution is accumulated at the bottom of the flash tank, the solution temperature is out of control and exceeds the critical temperature, and the explosion accident is hidden. Therefore, the invention also has further safety protection measures for the flash tank, and particularly, the temperature measuring device is arranged at the lower part of the flash tank and used for monitoring the temperature of the ammonium nitrate solution at the bottom of the flash tank in real time, and meanwhile, a steam condensate pipe is introduced into the flash tank and is interlocked with a control valve on the steam condensate pipe. Once the liquid phase temperature in the flash tank reaches the set control temperature, a control valve on a steam condensate pipe is opened immediately, condensate with lower temperature enters the flash tank, the temperature of the liquid phase in the flash tank is rapidly reduced, and ammonium nitrate solution is diluted to avoid explosion accidents.
The device for realizing the ammonium nitrate production method comprises the following steps:
a tubular reactor;
the front end of the tubular reactor is connected with a nitric acid feeding pipe and a gas ammonia feeding pipe, and material control valves are arranged on the nitric acid feeding pipe and the gas ammonia feeding pipe;
the vapor control valves are respectively connected with the vapor pipe on the nitric acid feeding pipe and the ammonia feeding pipe and are arranged on the vapor pipe;
a temperature measuring device mounted on the tubular reactor;
and a flash tank connected to the rear end of the tubular reactor;
the temperature measuring device is interlocked with the material control valve and the steam control valve.
The device for realizing the ammonium nitrate production method of the invention also comprises:
a temperature measuring device is arranged on the flash tank;
a steam condensate pipe led into the flash tank and a control valve arranged on the steam condensate pipe;
the temperature measuring device is interlocked with the control valve.
The invention adopts multiple safety protection measures for the tubular reactor and the flash evaporation tank in the method for producing the ammonium nitrate by the pressurized tubular reaction of the nitric acid and the gas ammonia, greatly reduces the possibility of explosion and realizes the safe production of the pressurized tubular reaction of the ammonium nitrate.
Drawings
Figure 1 is a schematic diagram of an ammonium nitrate production plant of the present invention.
Detailed Description
One end of the tubular reactor 1 was equipped with a nitric acid feed pipe 3 and a gaseous ammonia feed pipe 4, and material control valves FC1 and FC2 were provided on the feed pipes. Vapor pipes 5 and 6 are respectively connected with the back of the material control valves of the nitric acid feeding pipe 3 and the ammonia gas feeding pipe 4, and vapor control valves HV1 and HV2 are arranged. The tubular reactor 1 is equipped with a temperature measuring device T1, FC1, FC2, HV1, HV2 and T1 interlock. The rear end of the tubular reactor 1 is connected with a flash tank 2, the bottom of the flash tank is connected with an ammonium nitrate conveying pipe8, and a neutralization steam output pipe 9 is arranged above the flash tank. The temperature measuring device T2 is installed at the lower part of the flash tank 2, a steam condensate pipe 7 is led into the flash tank 2, and the T2 is interlocked with a control valve FC3 on the steam condensate pipe 7.
During normal production, the material control valves FC1 and FC2 are opened, the vapor control valves HV1 and HV2 are closed, and nitric acid and ammonia gas enter the tubular reactor 1 through the feeding pipes 3 and 4 to carry out neutralization reaction; the generated ammonium nitrate is discharged into the flash tank 2 from the other end of the tubular reactor; the steam flashed off is discharged from a neutralizing steam output pipe 9 and can be used for other heating devices to recover the heat energy of the steam; the concentrated ammonium nitrate solution is stored at the bottom of the flash tank and is sent out by an ammonium nitrate conveying pipe 8, and the concentration of the ammonium nitrate solution is 76-82%.
The temperature measuring device T1 arranged on the tubular reactor 1 monitors the temperature in the tubular reactor in real time, and once the set control temperature is reached, the material control valves FC1 and FC2 are immediately closed in an interlocking manner, reaction materials are cut off, the steam control valves HV1 and HV2 are rapidly opened, low-pressure steam is introduced, residual reaction materials in the tubular reactor are flushed out, and explosion in the tubular reactor is avoided.
The temperature measuring device T2 arranged at the lower part of the flash tank 2 monitors the temperature of the ammonium nitrate solution at the bottom of the flash tank in real time, once the liquid phase temperature reaches the set control temperature, the control valve FC3 on the steam condensate pipe 7 is opened immediately, the low-temperature condensate is added into the flash tank, the temperature of the ammonium nitrate solution is reduced rapidly, and the ammonium nitrate solution is diluted to avoid explosion.
Claims (4)
1. A method for producing ammonium nitrate, introduce nitric acid and gas ammonia into a tubular reactor to carry on the neutralization reaction through the respective inlet pipe, the reaction product is discharged to a flash tank from another end of the tubular reactor, after the vapor flash distillation, get the ammonium nitrate solution, its characteristic is to mount the temperature measuring device on the tubular reactor, connect the vapor pipe on the inlet pipe of nitric acid and gas ammonia respectively, and mount the steam control valve; the temperature measuring device is interlocked with a material control valve on the feeding pipe and a steam control valve on the steam pipe; when the reaction temperature is lower than the set control temperature, the material control valve is opened, the steam control valve is closed, when the reaction temperature reaches the set control temperature, the material control valve is closed, and the steam control valve is opened.
2. The method for producing ammonium nitrate as claimed in claim 1, wherein a temperature measuring device is installed at a lower portion of the flash drum, and the flash drum is connected to a steam condensate pipe, and the temperature measuring device is interlocked with a control valve on the steam condensate pipe.
3. The utility model provides a device for producing ammonium nitrate, includes a tubular reactor, the nitric acid inlet pipe and the gaseous ammonia inlet pipe that tubular reactor front end is connected, installs the material control valve on nitric acid inlet pipe and gaseous ammonia inletpipe to and a flash tank of connection in the tubular reactor rear end, characterized by still includes:
a temperature measuring device mounted on the tubular reactor;
the vapor control valves are respectively connected with the vapor pipe on the nitric acid feeding pipe and the ammonia feeding pipe and are arranged on the vapor pipe;
the temperature measuring device is interlocked with the material control valve and the steam control valve.
4. The apparatus of claim 3, further comprising:
a temperature measuring device mounted on the flash tank;
a steam condensate pipe led into the flash tank and a control valve arranged on the steam condensate pipe;
the temperature measuring device is interlocked with the control valve.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2006100129130A CN100360407C (en) | 2006-07-03 | 2006-07-03 | Method for producing ammonium nitrate |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2006100129130A CN100360407C (en) | 2006-07-03 | 2006-07-03 | Method for producing ammonium nitrate |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1884078A true CN1884078A (en) | 2006-12-27 |
| CN100360407C CN100360407C (en) | 2008-01-09 |
Family
ID=37582402
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNB2006100129130A Active CN100360407C (en) | 2006-07-03 | 2006-07-03 | Method for producing ammonium nitrate |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN100360407C (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102583441A (en) * | 2012-01-16 | 2012-07-18 | 河北克尔化工有限公司 | Method for producing ammonium nitrate solid |
| CN102603387A (en) * | 2012-03-19 | 2012-07-25 | 深圳市芭田生态工程股份有限公司 | Method for producing compound fertilizer by high tower tubular reactor |
| CN103402919A (en) * | 2011-05-16 | 2013-11-20 | 悉尼大学 | Integrated process for producing ammonium nitrate |
| CN106145072A (en) * | 2015-04-09 | 2016-11-23 | 辽宁庆阳特种化工有限公司 | A kind of to the processing method and processing device containing organic impurities dust technology |
| CN106348315A (en) * | 2016-08-18 | 2017-01-25 | 赛鼎工程有限公司 | Ammonium nitrate preparation technology by flash evaporation |
| CN106365177A (en) * | 2016-08-18 | 2017-02-01 | 赛鼎工程有限公司 | Method for preparing concentrated ammonium nitrate solution through flash evaporation |
Family Cites Families (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE1288081B (en) * | 1965-05-07 | 1969-01-30 | Kaltenbach, Roger, Paris | Process and saturator for the production of ammonium nitrate |
| CN1008888B (en) * | 1987-10-24 | 1990-07-25 | 国家机械委沈阳铸造研究所 | High-strength insulation rising head class material and manufacturing process |
| UA33681C2 (en) * | 1999-03-23 | 2002-11-15 | Горлівське Відкрите Акціонерне Товариство "Концерн Стирол" | Method for production of ammonium nitrate and tubular reactor for exothermic reactions |
| UA76139C2 (en) * | 2003-09-24 | 2006-07-17 | Open Joint Stock Company Conce | A device for producing ammonium nitrate solution and a process for producing ammonium nitrate solution |
-
2006
- 2006-07-03 CN CNB2006100129130A patent/CN100360407C/en active Active
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103402919A (en) * | 2011-05-16 | 2013-11-20 | 悉尼大学 | Integrated process for producing ammonium nitrate |
| CN103402919B (en) * | 2011-05-16 | 2016-05-11 | 悉尼大学 | Manufacture the integration method of ammonium nitrate |
| CN102583441A (en) * | 2012-01-16 | 2012-07-18 | 河北克尔化工有限公司 | Method for producing ammonium nitrate solid |
| CN102603387A (en) * | 2012-03-19 | 2012-07-25 | 深圳市芭田生态工程股份有限公司 | Method for producing compound fertilizer by high tower tubular reactor |
| CN102603387B (en) * | 2012-03-19 | 2013-11-27 | 深圳市芭田生态工程股份有限公司 | Method for producing compound fertilizer by high tower tubular reactor |
| CN106145072A (en) * | 2015-04-09 | 2016-11-23 | 辽宁庆阳特种化工有限公司 | A kind of to the processing method and processing device containing organic impurities dust technology |
| CN106348315A (en) * | 2016-08-18 | 2017-01-25 | 赛鼎工程有限公司 | Ammonium nitrate preparation technology by flash evaporation |
| CN106365177A (en) * | 2016-08-18 | 2017-02-01 | 赛鼎工程有限公司 | Method for preparing concentrated ammonium nitrate solution through flash evaporation |
Also Published As
| Publication number | Publication date |
|---|---|
| CN100360407C (en) | 2008-01-09 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN1884078A (en) | Method for producing ammonium nitrate | |
| CN220835498U (en) | Device for continuously synthesizing 2-methyl-alpha-hydroxy iminobenzyl cyanide sodium salt | |
| CN101891762A (en) | Preparation method and application of diethyl phosphinates | |
| CN101638224B (en) | Method for purifying phosphine by-product and application method of phosphine by-product | |
| CN103539704A (en) | Method for preparing diuron | |
| CN103159271A (en) | Industrial sewage treating agent and preparation method thereof | |
| CN1724546A (en) | Production method of triethyl phosphite | |
| CN106278922B (en) | A kind of preparation method of fatty acid amide propyl tertiary amine | |
| CN106348315B (en) | The technique of full flashing ammonium nitrate | |
| US9115215B2 (en) | Method for completely dissolving and rapidly hydrolyzing cellulose, and uses of said method | |
| CN1300119C (en) | Process for preparing cyanuric acid | |
| CN104781425B (en) | Instantaneous cooling for biomass material hydrolysis to be quenched | |
| CN101828486A (en) | Flower forcing method for inducing pineapple to bloom | |
| CN101560225B (en) | Preparation method of tetrakis hydroxymetyl phosphonium sulfuric-urea polymer | |
| CN1142542A (en) | Process and apparatus for preparing chlorinated rare-earth from fine rare-earth minerals by alkali water heating process | |
| CN106365177B (en) | A kind of method that flash distillation prepares ammonium nitrate concentrated solution | |
| CN101875628A (en) | Preparation method of paraquat chloride | |
| CN201603559U (en) | Tower-type continuous rearrangement reactor | |
| US20130125877A1 (en) | Method and apparatus of hydrolytic saccharification of cellulosic biomass | |
| CN104292257A (en) | Preparation method of dialkyl hypophosphorous acid | |
| CN101148424A (en) | Continuous and clean producing method for iminodiacetonitrile by using combined reactor | |
| CN102908970A (en) | Dual-circulation injection reactor | |
| CN104058375B (en) | A kind of Safe production technology of extensive manufacture high purity phosphine | |
| CN218510692U (en) | Ammonia discharge device of ammonia synthesis cold exchanger | |
| CN102492756A (en) | Method and device for converting straws into fermentable saccharides |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C41 | Transfer of patent application or patent right or utility model | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20090206 Address after: No. 461, South Central Street, hi tech Development Zone, Shanxi, Taiyuan Patentee after: Sedin Engineering Co., Ltd. Address before: No. 18 Kangle street, Xinjian South Road, Shanxi, Taiyuan Patentee before: Second Design Institute of chemical Industry |
|
| ASS | Succession or assignment of patent right |
Owner name: SAIDING ENGINEERING CO., LTD. Free format text: FORMER OWNER: SECOND DESIGN INSTITUTE OF CHEMICAL INDUSTRY Effective date: 20090206 |