CN210252289U - Reaction device for producing phosphorus pentasulfide - Google Patents
Reaction device for producing phosphorus pentasulfide Download PDFInfo
- Publication number
- CN210252289U CN210252289U CN201921126662.8U CN201921126662U CN210252289U CN 210252289 U CN210252289 U CN 210252289U CN 201921126662 U CN201921126662 U CN 201921126662U CN 210252289 U CN210252289 U CN 210252289U
- Authority
- CN
- China
- Prior art keywords
- kettle
- phosphorus
- tail gas
- cooling
- liquid metering
- 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
Images
Landscapes
- Physical Or Chemical Processes And Apparatus (AREA)
Abstract
The utility model relates to a reaction unit for producing phosphorus pentasulfide, which comprises a sulfur liquid metering kettle, a phosphorus liquid metering kettle, a reaction kettle and a cooling kettle, wherein a stirring motor and a tail gas pipe are arranged at the top of the reaction kettle, a discharging pipe is arranged at the bottom of the reaction kettle and is connected with a feeding port of the cooling kettle, the outer end of the tail gas pipe is connected with a tail gas treatment device, the top of the cooling kettle is provided with a stirring motor, the discharging ports of the sulfur liquid metering kettle and the phosphorus liquid metering kettle are respectively provided with a feeding pipe connected with the reaction kettle, and two feeding pipes are respectively provided with a control valve; the utility model discloses the reactant proportion is accurate, and production efficiency is high.
Description
Technical Field
The utility model relates to a phosphorus pentasulfide production technical field specifically is a reaction unit of phosphorus pentasulfide of production.
Background
The production of phosphorus pentasulfide requires that sulfur and yellow phosphorus are firstly melted into liquid, then the liquid is mixed in a reaction kettle to generate chemical reaction to generate phosphorus pentasulfide, the reaction requires that sulfur and phosphorus are added according to a certain proportion, a high-temperature and high-pressure environment is required in the reaction process, the phosphorus pentasulfide generated after the reaction is in the molten liquid state and needs to be cooled and solidified into a solid state, a factory for producing the product at present does not have a systematic reaction device, the adding proportion is inaccurate, and the cooling mode after the reaction is unreasonable.
Disclosure of Invention
The utility model aims at providing a producer who produces this product does not have systematic reaction unit at present, and reinforced proportion is inaccurate, and the unreasonable problem of cooling method provides a reaction unit of production phosphorus pentasulfide.
The utility model has the following concrete scheme: the utility model provides a reaction unit of production phosphorus pentasulfide, includes sulphur liquid measurement cauldron, phosphorus liquid measurement cauldron, reation kettle, cooling kettle, and agitator motor and tail gas pipe are equipped with to the reation kettle top, and the blowing pipe is equipped with to the reation kettle bottom, the blowing pipe is connected with cooling kettle's feed inlet, tail gas pipe outer end is connected with tail gas processing apparatus, agitator motor is equipped with to the cooling kettle top, sulphur liquid measurement cauldron and phosphorus liquid measurement cauldron's discharge gate respectively are provided with a conveying pipe of being connected with reation kettle, all is equipped with the control valve on two conveying pipes.
The volume ratio of the sulfur liquid metering kettle to the phosphorus liquid metering kettle is 2.3-2.7.
The control valve is a pneumatic membrane regulating valve.
The outside of the sulfur liquid metering kettle, the phosphorus liquid metering kettle and the two feeding pipes are all provided with a heat preservation layer.
The utility model discloses the theory of operation as follows: sulphur liquid and phosphorus liquid are carried in sulphur liquid measurement cauldron and the phosphorus liquid measurement cauldron respectively, carry out chemical reaction through the pneumatic film governing valve of conveying pipe separately and generate phosphorus pentasulfide in carrying the reation kettle in proportion, liquid phosphorus pentasulfide flows into the cooling kettle from reation kettle's discharge gate, make it cool down to closing on the melting point by a wide margin through stirring and cooling, then in the discharge gate outflow of cooling kettle sent into the film-making device, the poisonous tail gas that produces in the reation kettle flows into in the tail gas processing apparatus through the tail gas duct.
Compared with the prior art, the utility model has the following advantages: the sulfur and the phosphorus are conveyed to the reaction kettle in proportion through the two metering kettles and the pneumatic film regulating valve, so that the proportion is more accurate; after the reaction, the liquid phosphorus pentasulfide is stirred and cooled by a cooling kettle to be greatly cooled, the cooling speed is high, and the production efficiency is improved.
Drawings
Fig. 1 is a perspective view of the present invention;
FIG. 2 is a front view of FIG. 1;
in the figure: 1-sulfur liquid metering kettle, 2-phosphorus liquid metering kettle, 3-feeding pipe, 4-reaction kettle, 5-stirring motor, 6-discharging pipe, 7-cooling kettle, 8-tail gas pipe and 9-tail gas treatment device.
Detailed Description
Referring to fig. 1-2, this embodiment includes a sulfur liquid metering kettle 1, a phosphorus liquid metering kettle 2, a reaction kettle 4, and a cooling kettle 7, where a stirring motor 5 and a tail gas pipe 8 are installed at the top of the reaction kettle 4, a discharging pipe 6 is installed at the bottom of the reaction kettle 4, the discharging pipe 6 is connected to a feeding port of the cooling kettle 7, the outer end of the tail gas pipe 8 is connected to a tail gas processing apparatus 9, the stirring motor 5 is installed at the top of the cooling kettle 7, the discharging ports of the sulfur liquid metering kettle 1 and the phosphorus liquid metering kettle 2 are respectively provided with a feeding pipe 3 connected to the reaction kettle 4, and two feeding pipes 3 are respectively provided with a control valve.
In this example, the volume ratio of the sulfur liquid measuring kettle 1 to the phosphorus liquid measuring kettle 2 is 2.5.
The control valve described in this embodiment is a pneumatic diaphragm regulating valve.
In this embodiment, the sulfur liquid metering kettle 1, the phosphorus liquid metering kettle 2 and the two feeding pipes 3 are all provided with heat insulating layers outside.
Claims (4)
1. The utility model provides a reaction unit of production phosphorus pentasulfide, includes sulphur liquid measurement cauldron, phosphorus liquid measurement cauldron, reation kettle, cooling kettle, characterized by: stirring motor and tail gas pipe are equipped with to the reation kettle top, and the blowing pipe is equipped with to the reation kettle bottom, the blowing pipe is connected with cooling kettle's feed inlet, tail gas outside of tubes end is connected with tail gas processing apparatus, stirring motor is equipped with to the cooling kettle top, sulphur liquid measurement cauldron and phosphorus liquid measurement cauldron's discharge gate respectively are provided with a conveying pipe of being connected with reation kettle, all is equipped with the control valve on two conveying pipes.
2. The reactor apparatus for producing phosphorus pentasulfide as claimed in claim 1, wherein: the volume ratio of the sulfur liquid metering kettle to the phosphorus liquid metering kettle is 2.3-2.7.
3. The reactor apparatus for producing phosphorus pentasulfide as claimed in claim 1, wherein: the control valve is a pneumatic diaphragm regulating valve.
4. The reactor apparatus for producing phosphorus pentasulfide as claimed in claim 1, wherein: and heat insulation layers are arranged outside the sulfur liquid metering kettle, the phosphorus liquid metering kettle and the two feeding pipes.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201921126662.8U CN210252289U (en) | 2019-07-18 | 2019-07-18 | Reaction device for producing phosphorus pentasulfide |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201921126662.8U CN210252289U (en) | 2019-07-18 | 2019-07-18 | Reaction device for producing phosphorus pentasulfide |
Publications (1)
Publication Number | Publication Date |
---|---|
CN210252289U true CN210252289U (en) | 2020-04-07 |
Family
ID=70012985
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201921126662.8U Active CN210252289U (en) | 2019-07-18 | 2019-07-18 | Reaction device for producing phosphorus pentasulfide |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN210252289U (en) |
-
2019
- 2019-07-18 CN CN201921126662.8U patent/CN210252289U/en active Active
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN102924285B (en) | Preparation method of dimethyldiallylammonium chloride | |
CN104555975B (en) | Continuous lithium iron phosphate preparation device and continuous lithium iron phosphate preparation method | |
CN102230166A (en) | Double-layer gas inlet shower nozzle device of MOCVD (Metal Organic Chemical Vapor Deposition) equipment | |
CN104446098A (en) | Automatic production technology equipment for polycarboxylic acid water-reducing agent | |
CN210252289U (en) | Reaction device for producing phosphorus pentasulfide | |
CN104496624B (en) | A kind of method and device for producing high tower nitro-compound fertilizer | |
CN211435164U (en) | Continuous crystallization process unit of sodium bisulfite menadione | |
CN203741454U (en) | Secondary feeding device in polycrystalline silicon ingot casting process | |
CN205392446U (en) | Nitromethane continuous reactor | |
CN106732290A (en) | A kind of reactor of continuous production nitromethane | |
CN205392441U (en) | Reaction kettle capable of uniformly mixing | |
CN211070082U (en) | Polycarboxylate water reducing agent mother liquor synthesizer | |
CN205760997U (en) | A kind of industrialization automatic batching system | |
CN209237897U (en) | A kind of sour solvent flows feeder apparatus online | |
CN203007178U (en) | Continuous production system for lithium alkylide | |
CN205575629U (en) | High -efficient apparatus for producing of dry hydrogen chloride preparation hydrochloric acid of water uptake | |
CN206381978U (en) | A kind of sulfonating reaction workshop film sulfonation reactor | |
CN108054427B (en) | Production method and production equipment for organic electrolyte of lithium ion battery | |
CN104984704A (en) | Power transformation equipment double-component casting material synchronization preparation system and power transformation equipment double-component casting material synchronization preparation method | |
CN112044362A (en) | Continuous synthesis device for magnesium chloride | |
CN207793089U (en) | A kind of naphthalene water reducer synthesizer | |
CN206911305U (en) | A kind of chemical industry feeding device | |
CN204746256U (en) | Surface coating agent mixes quantitative feeding device | |
CN204911377U (en) | Heat transfer oil processingequipment | |
CN104474986B (en) | The continuous sulfonation production device of gaseous sulfur trioxide |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
GR01 | Patent grant | ||
GR01 | Patent grant |