CN219121116U - Phosphorus pentasulfide flaking heat sink - Google Patents

Phosphorus pentasulfide flaking heat sink Download PDF

Info

Publication number
CN219121116U
CN219121116U CN202222911208.1U CN202222911208U CN219121116U CN 219121116 U CN219121116 U CN 219121116U CN 202222911208 U CN202222911208 U CN 202222911208U CN 219121116 U CN219121116 U CN 219121116U
Authority
CN
China
Prior art keywords
oil
roller
phosphorus pentasulfide
storage tank
pelleter
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
Application number
CN202222911208.1U
Other languages
Chinese (zh)
Inventor
郑雄飞
郑传泽
李植刚
邓绍裕
路明彪
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Hubei Xingfa Chemicals Group Co Ltd
Original Assignee
Hubei Xingfa Chemicals Group Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Hubei Xingfa Chemicals Group Co Ltd filed Critical Hubei Xingfa Chemicals Group Co Ltd
Priority to CN202222911208.1U priority Critical patent/CN219121116U/en
Application granted granted Critical
Publication of CN219121116U publication Critical patent/CN219121116U/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Classifications

    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/10Process efficiency

Abstract

The utility model discloses a phosphorus pentasulfide flaking cooling device, which comprises a phosphorus pentasulfide storage tank and a roller flaking machine, wherein a submerged pump is connected between the phosphorus pentasulfide storage tank and the roller flaking machine, the phosphorus pentasulfide flaking machine further comprises an oil cooling system communicated with a jacket of the roller flaking machine, the oil cooling system comprises a heat conducting oil circulating pump connected to an oil inlet pipe communicated with the jacket of the roller flaking machine, and a heat conducting oil condenser connected to the jacket of the roller flaking machine, an oil outlet of the heat conducting oil condenser is connected with an oil storage tank, an inlet of the heat conducting oil circulating pump is communicated with the oil storage tank, and a heat conducting oil heating device is arranged in the oil storage tank. According to the utility model, the phosphorus pentasulfide roller pelleter is cooled by adopting the heat conduction oil system, and then the heat conduction oil is subjected to heat exchange and cooling by adopting the water cooling mode, so that cooling water is prevented from entering the phosphorus pentasulfide roller pelleter, and the risk of serious production accidents after production equipment fails can be avoided.

Description

Phosphorus pentasulfide flaking heat sink
Technical Field
The utility model relates to the technical field of phosphorus pentasulfide production, in particular to a phosphorus pentasulfide tablet cooling device.
Background
During the conventional production process of phosphorus pentasulfide, a tablet production device adopts a stainless steel double-roller tablet machine, tablet condensate adopts circulating water, and the high-temperature liquid phosphorus pentasulfide at 300-350 ℃ on the surface of a roller is cooled into a low-temperature solid at 50-60 ℃ by introducing the circulating water in the roller in the production process.
Because the high-temperature phosphorus pentasulfide and water can be in contact with each other to perform rapid reaction and release a large amount of heat, and meanwhile, highly toxic gas hydrogen sulfide is generated to cause combustion and explosion, once the roller leaks in the production process, the water and materials can be in contact with each other to generate combustion and explosion, so that a large safety risk exists.
Disclosure of Invention
The utility model aims to provide a phosphorus pentasulfide flaking cooling device, which adopts an oil cooling system as a cooling system of phosphorus pentasulfide flaking equipment and adopts a water cooling mode to cool heat conduction oil, thereby avoiding the possibility of contact between phosphorus pentasulfide and water and reducing the production accident risk of phosphorus pentasulfide flaking process links.
In order to achieve the above purpose, the present utility model provides the following technical solutions: the utility model provides a phosphorus pentasulfide film-making heat sink, includes phosphorus pentasulfide storage tank and roller pelleter, is connected the submerged pump between phosphorus pentasulfide storage tank and the roller pelleter, still includes the oil cooling system that presss from both sides the cover intercommunication with the roller pelleter, the oil cooling system including connect with the roller pelleter presss from both sides the conduction oil circulating pump on the oil feed pipe of cover intercommunication, and connect with the roller pelleter presss from both sides the conduction oil condenser that the cover communicates, the oil-out and the oil storage tank of conduction oil condenser are connected, the import of conduction oil circulating pump with the oil storage tank intercommunication, set up conduction oil heating device in the oil storage tank.
Preferably, the oil storage tank contains heat conduction oil at 35-45 ℃.
Preferably, a pressure transmitter is connected to a pipeline between the conduction oil circulating pump and the roller pelleter.
Preferably, the roller pelleter is made of stainless steel material.
Preferably, a thermometer is arranged on the oil storage tank.
Preferably, an automatic feeding control valve is connected to a pipeline between the phosphorus pentasulfide storage tank and the roller pelleter, and an overflow pipe is further connected between the roller pelleter and the phosphorus pentasulfide storage tank.
Preferably, a flow regulating valve is connected to a cooling water inlet pipe of the heat conducting oil condenser.
Compared with the prior art, the utility model has the following beneficial effects:
1. according to the utility model, the phosphorus pentasulfide roller pelleter is cooled by adopting the heat conduction oil system, and then the heat conduction oil is subjected to heat exchange and cooling by adopting the water cooling mode, so that cooling water is prevented from entering the phosphorus pentasulfide roller pelleter, and the risk of serious production accidents after production equipment fails can be avoided.
2. In the oil cooling system, the pressure transmitter, the thermometer and the cooling water flow regulating valve are arranged on the pipeline, so that smooth circulation of the heat conduction oil is ensured, and the temperature of the heat conduction oil can be accurately controlled by arranging the regulating valve on the heat conduction oil condenser, and the heat exchange efficiency of the oil cooling system is ensured.
Drawings
Fig. 1 is a schematic structural view of the present utility model.
In the figure: 1. a phosphorus pentasulfide storage tank; 2. roller pelleter; 3. a submerged pump; 4. an oil cooling system; 5. an oil inlet pipe; 6. a heat transfer oil circulation pump; 7. a heat transfer oil condenser; 8. an oil storage tank; 9. a conduction oil heating device; 10. a pressure transmitter; 11. a thermometer; 12. an automatic feed control valve; 13. an overflow pipe; 14. a flow regulating valve.
Detailed Description
The following description of the embodiments of the present utility model will be made clearly and completely with reference to the accompanying drawings, in which it is apparent that the embodiments described are only some embodiments of the present utility model, but not all embodiments. 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.
As a preferred embodiment of the present utility model, referring to fig. 1, the arrow in the figure represents the flow direction of the medium, the present embodiment provides a phosphorus pentasulfide flaking cooling device, which comprises a phosphorus pentasulfide storage tank 1 and a roller flaking machine 2, a submerged pump 3 is connected on a pipeline between the phosphorus pentasulfide storage tank 1 and the roller flaking machine 2, and further comprises an oil cooling system 4 communicated with a jacket of the roller flaking machine 2, the oil cooling system 4 comprises a heat-conducting oil circulating pump 6 connected on an oil inlet pipe 5 communicated with the jacket of the roller flaking machine 2, and a heat-conducting oil condenser 7 connected with the jacket of the roller flaking machine 2, an oil outlet of the heat-conducting oil condenser 7 is connected with an oil storage tank 8, heat-conducting oil at 35-45 ℃ is contained in the oil storage tank 8, an inlet of the heat-conducting oil circulating pump 6 is communicated with the oil storage tank 8, and a heat-conducting oil heating device 9 is arranged in the oil storage tank 8.
In the above embodiment, the heat conducting oil heating device 9 adopts the electric heater, and when the above embodiment is implemented, the heat conducting oil is heated by the heat conducting oil heating device, then is pumped into the jacket of the roller pelleter 2 by the heat conducting oil circulating pump 6, flows into the heat conducting oil heat exchanger 7 for water cooling after heat exchange between the heat conducting oil and the high-temperature phosphorus pentasulfide is completed, and then circulates again, thereby thoroughly replacing the production mode of directly adopting the water cooling system to cool the roller pelleter 2 and preventing major safety accidents after leakage occurs in the roller pelleter 2.
In some preferred embodiments, in order to monitor the pressure of the conduction oil in the oil cooling system 4 in real time and ensure smooth operation of the oil cooling system, the present embodiment connects a pressure transmitter 10 on a pipeline between the conduction oil circulation pump 6 and the roller pelleter 2.
In some preferred embodiments, the roll pelleter 2 is made of stainless steel material in this embodiment in order to extend the useful life of the roll pelleter 2.
In other preferred embodiments, in order to monitor the heat exchange temperature of the heat conducting oil and ensure that the oil cooling system 4 exchanges heat effectively to the roller pelleter 2, the embodiment is provided with a thermometer 11 on the oil storage tank 8, and when the temperature of the heat conducting oil exceeds or is lower than the expected temperature, the temperature of the heat conducting oil is adjusted by using the outer oil inlet pipe 9 and the heat conducting oil heating device.
In other preferred embodiments, in order to precisely control the feeding amount, the embodiment connects an automatic feeding control valve 12 on a pipeline between the phosphorus pentasulfide storage tank 1 and the roller pelleter 2, and an overflow pipe 13 is also connected between the roller pelleter 2 and the phosphorus pentasulfide storage tank 1, and when the feeding amount exceeds the feeding amount expected by the reaction, the feeding amount overflows into the phosphorus pentasulfide storage tank 1 through the overflow pipe to prevent the leakage of raw materials.
In other preferred embodiments, in order to control the temperature of the heat transfer oil in the oil cooling system 4 in multiple ways, the present embodiment connects the flow control valve 14 to the cooling water inlet pipe of the heat transfer oil condenser 7, and when the temperature of the heat transfer oil after passing through the heat transfer oil cooler exceeds the expected temperature, the temperature of the heat transfer oil is reduced by increasing the flow of the cooling water.
Finally, it is noted that the above embodiments are only for illustrating the technical solution of the present utility model and not for limiting the same, and although the present utility model has been described in detail with reference to the preferred embodiments, it should be understood by those skilled in the art that modifications and equivalents may be made thereto without departing from the spirit and scope of the technical solution of the present utility model, which is intended to be covered by the scope of the claims of the present utility model.

Claims (7)

1. The utility model provides a phosphorus pentasulfide pelleter heat sink, includes phosphorus pentasulfide storage tank and roller pelleter, is connected submerged pump, its characterized in that between phosphorus pentasulfide storage tank and the roller pelleter: the oil cooling system is connected to the oil inlet pipe communicated with the jacket of the roller pelleter, the oil cooling system comprises a heat-conducting oil circulating pump connected to the oil inlet pipe communicated with the jacket of the roller pelleter, and a heat-conducting oil condenser connected to the jacket of the roller pelleter, an oil outlet of the heat-conducting oil condenser is connected with an oil storage tank, an inlet of the heat-conducting oil circulating pump is communicated with the oil storage tank, and a heat-conducting oil heating device is arranged in the oil storage tank.
2. The phosphorus pentasulfide tablet cooling device according to claim 1, wherein: the oil storage tank contains heat conduction oil at 35-45 ℃.
3. The phosphorus pentasulfide tablet cooling device according to claim 1, wherein: and a pressure transmitter is connected to a pipeline between the conduction oil circulating pump and the roller pelleter.
4. The phosphorus pentasulfide tablet cooling device according to claim 1, wherein: the roller pelleter is made of stainless steel materials.
5. The phosphorus pentasulfide tablet cooling device according to claim 1, wherein: and a thermometer is arranged on the oil storage tank.
6. The phosphorus pentasulfide tablet cooling device according to claim 1, wherein: an automatic feeding control valve is connected to a pipeline between the phosphorus pentasulfide storage tank and the roller pelleter, and an overflow pipe is further connected between the roller pelleter and the phosphorus pentasulfide storage tank.
7. The phosphorus pentasulfide tablet cooling device according to claim 1, wherein: and a cooling water inlet pipe of the heat conducting oil condenser is connected with a flow regulating valve.
CN202222911208.1U 2022-11-02 2022-11-02 Phosphorus pentasulfide flaking heat sink Active CN219121116U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202222911208.1U CN219121116U (en) 2022-11-02 2022-11-02 Phosphorus pentasulfide flaking heat sink

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202222911208.1U CN219121116U (en) 2022-11-02 2022-11-02 Phosphorus pentasulfide flaking heat sink

Publications (1)

Publication Number Publication Date
CN219121116U true CN219121116U (en) 2023-06-02

Family

ID=86527463

Family Applications (1)

Application Number Title Priority Date Filing Date
CN202222911208.1U Active CN219121116U (en) 2022-11-02 2022-11-02 Phosphorus pentasulfide flaking heat sink

Country Status (1)

Country Link
CN (1) CN219121116U (en)

Similar Documents

Publication Publication Date Title
CN101078532B (en) Device for heating using residual heat of sulfuric acid production
CN219121116U (en) Phosphorus pentasulfide flaking heat sink
CN101517795A (en) Method and device for operating fuel cell used together with condenser
CN103111248B (en) The device and method that conduction oil reactor heating chilling temperature controls
CN211529021U (en) TCU temperature control system
CN212179661U (en) External circulation steam drum heat taking system
CN108726520B (en) Waste heat recovery system of reducing furnace
CN214916008U (en) Device for controlling reaction temperature in reaction kettle
CN212215471U (en) Temperature adjusting system of reaction kettle
CN211204605U (en) Heat exchange device of adsorption system
CN113097540A (en) Fuel cell with side radiator thermal management system and cold start
CN206420346U (en) A kind of heat-exchange device for sludge carbonization technique
CN215560129U (en) Semi-continuous hot water heating and low-temperature hot water cooling device replaced by oil-oil heat exchange
CN206420345U (en) A kind of heat-exchange device for sludge carbonization technique
CN212658114U (en) High-temperature machine type cooling control system
CN217560106U (en) Heat-conducting oil furnace circulating heat exchanger
CN210916287U (en) Self-heat-exchange type copper dissolving and liquid making device
TWM488496U (en) Recycling processing device of sulfuric acid-hydrogen peroxide solution
CN214406691U (en) Ultra-temperature heat conduction oil cooling device
CN220793318U (en) Cooling water waste heat recycling device
CN215550245U (en) Heating mechanism of film press
CN219511337U (en) Multistage heat exchanger with temperature monitoring function
CN219596599U (en) Constant-pressure reaction kettle system
CN219502003U (en) Device for chlorination condensation process
CN215724362U (en) Device for reducing temperature of industrial cooling water

Legal Events

Date Code Title Description
GR01 Patent grant
GR01 Patent grant