CN217041338U - Octyl stearate production system - Google Patents
Octyl stearate production system Download PDFInfo
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- CN217041338U CN217041338U CN202123292596.1U CN202123292596U CN217041338U CN 217041338 U CN217041338 U CN 217041338U CN 202123292596 U CN202123292596 U CN 202123292596U CN 217041338 U CN217041338 U CN 217041338U
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Abstract
The utility model discloses an octyl stearate production system, which comprises a reaction kettle, a distillation kettle, a finished product tank, a temperature control system and a vacuum system, and further comprises a dissolving pot, wherein the dissolving pot is connected with a feed inlet of the reaction kettle and comprises a first condenser, a first oil-water separator, a first water tank, a second condenser, a second oil-water separator and a second water tank, the first condenser is respectively connected with the reaction kettle and an inlet of the first oil-water separator, the first oil-water separator comprises a first oil outlet, a first water outlet and a first vacuum port, the first water outlet is connected with the first water tank, the first oil outlet is connected with the feed inlet of the reaction kettle, the second condenser is respectively connected with a steam outlet of the distillation kettle and an inlet of the second oil-water separator, the second oil-water separator comprises a second oil outlet, a second water outlet and a second vacuum port, the second oil outlet is connected with the finished product tank, the second water outlet is connected with a second water tank; avoiding waste, damage and pollution to the vacuum system.
Description
Technical Field
The utility model relates to a chemical production equipment field especially relates to an octyl stearate production system.
Background
The prior octyl stearate is a finished product obtained by carrying out reactive distillation on a reaction kettle and a distillation kettle at a certain temperature under a vacuum environment. However, the existing vacuum system is directly connected to the reaction vessel and the distillation vessel and performs the vacuum environment, and the gas in the distillation vessel of the reaction vessel contains raw material or product, and the raw material or product is partially corrosive or other dangerous substances, and the gas directly entering the vacuum system may damage the equipment of the vacuum system, and the gas discharged during the operation of the vacuum system may also affect the environment due to the various raw materials or products contained therein.
SUMMERY OF THE UTILITY MODEL
In view of the vacuum system that present octyl stearate production exists directly links and easily causes vacuum system to damage and environmental pollution problem, the utility model provides an octyl stearate production system makes reation kettle, stills are respectively through the condenser, just be connected with vacuum system behind the oil water separator, the raw materials of the condenser oil water separator separation that reation kettle connects continue to input reation kettle, avoid the raw materials extravagant, just input vacuum system after condensation and oil water separation get rid of impurity is got rid of to the gas in reation kettle and the stills, avoid causing destruction to vacuum system, and avoided discharging and caused pollution etc..
In order to achieve the above object, the embodiments of the present invention adopt the following technical solutions:
a production system of octyl stearate comprises a reaction kettle, a distillation kettle, a finished product tank, a temperature control system and a vacuum system, wherein the temperature control system and the vacuum system are respectively connected with the reaction kettle, the distillation kettle and the finished product tank, the production system further comprises a dissolving pot, the dissolving pot is connected with a feed inlet of the reaction kettle, the production system further comprises a first condenser, a first oil-water separator, a first water tank, a second condenser, a second oil-water separator and a second water tank, the first condenser is respectively connected with the reaction kettle and an inlet of the first oil-water separator, the first oil-water separator comprises a first oil outlet, a first water outlet and a first vacuum port, the first water outlet is connected with the first water tank, the first oil outlet is connected with the feed inlet of the reaction kettle, the second condenser is respectively connected with a steam outlet of the distillation kettle and an inlet of the second oil-water separator, the second oil-water separator comprises a second oil outlet, a second water outlet and a second vacuum port, the second oil outlet is connected with the finished product tank, the second water outlet is connected with the second water tank, and the vacuum system is respectively connected with the first vacuum port and the second vacuum port.
According to an aspect of the present invention, the dissolving pot is connected with a temperature control system.
According to an aspect of the present invention, the dissolving pot includes a stirring motor and a temperature measuring device disposed in the dissolving pot.
According to one aspect of the present invention, the first water tank and the second water tank are respectively provided with a liquid level indicator.
According to one aspect of the utility model, be equipped with temperature measuring device in reation kettle and the stills respectively.
According to an aspect of the invention, the product tank is connected with a vacuum system.
According to an aspect of the present invention, the distillation still is provided with a stirring motor.
According to an aspect of the utility model, reation kettle is equipped with agitator motor.
According to the utility model discloses an aspect, temperature control system includes steam system and cooling water system, steam system is connected with dissolving pot, reation kettle, stills and finished product jar respectively to provide the temperature of demand separately for dissolving pot, reation kettle, stills and finished product jar respectively, cooling water system is connected with dissolving pot, reation kettle, stills and finished product jar respectively and carries out temperature control to dissolving pot, reation kettle, stills and finished product jar respectively.
According to the utility model discloses an aspect, be equipped with the pressure indicator respectively on the pipeline that steam system and dissolving pot, reation kettle, stills and finished product jar are connected.
The utility model discloses the advantage of implementing: make reation kettle, stills pass through condenser, oil water separator respectively just after being connected with vacuum system, gaseous just input vacuum system after getting rid of impurity through condensation and oil water separation in reation kettle and the stills, avoid causing destruction to vacuum system, and avoided discharging and caused pollution etc..
The raw materials separated by the oil-water separator of the condenser connected with the reaction kettle are continuously input into the reaction kettle, so that the waste caused by the discharge of the raw materials through a vacuum system is avoided, and the yield and the benefit are improved.
Drawings
In order to more clearly illustrate the technical solutions of the embodiments of the present invention, the drawings required to be used in the embodiments will be briefly described below, it is obvious that the drawings in the following description are only some embodiments of the present invention, and it is obvious for those skilled in the art that other drawings can be obtained according to the drawings without creative efforts.
Fig. 1 is a schematic diagram of the production system of octyl stearate of the present invention.
Detailed Description
The technical solutions in the embodiments of the present invention will be described clearly and completely with reference to the accompanying drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only some embodiments of the present invention, not all embodiments. Based on the embodiments in the present invention, all other embodiments obtained by a person skilled in the art without creative efforts all belong to the protection scope of the present invention.
As shown in fig. 1, the octyl stearate production system comprises a reaction kettle 1, a distillation kettle 2, a finished product tank 3, a temperature control system 4 and a vacuum system 5, the production system further comprises a dissolving pot 6, the dissolving pot 6 is connected with a feed inlet 11 of the reaction kettle 1, the production system further comprises a first condenser 12, a first oil-water separator 13, a first water tank 14, a second condenser 21, a second oil-water separator 22 and a second water tank 23, the first condenser 12 is respectively connected with inlets of the reaction kettle 1 and the first oil-water separator 13, the first oil-water separator 13 comprises a first oil outlet 131, a first water outlet 132 and a first vacuum port 133, the first water outlet is connected with the first water tank, the first oil outlet is connected with a feed inlet of the reaction kettle, the second condenser 21 is respectively connected with a steam outlet of the distillation kettle and an inlet of the second oil-water separator 22, the second oil-water separator 22 includes a second oil outlet 221, a second water outlet 222, and a second vacuum port 223, the second oil outlet 221 is connected to the finished product tank 3, the second water outlet is connected to the second water tank, and the vacuum system is connected to the first vacuum port and the second vacuum port, respectively. Temperature control system 4 includes steam system 41 and cooling water system 42, steam system is connected with dissolving pot, reation kettle, stills and finished product jar respectively to for dissolving pot, reation kettle, stills and finished product jar provide the temperature of demand separately respectively, cooling water system is connected and carries out temperature control to dissolving pot, reation kettle, stills and finished product jar respectively with dissolving pot, reation kettle, stills and finished product jar respectively.
In this embodiment, the dissolving pot includes agitator motor and the temperature measuring device of setting in the dissolving pot, and agitator motor stirs the raw materials in order to promote dissolving speed and efficiency. The temperature measuring device measures the temperature in real time and provides the temperature for the temperature control system to control the temperature so as to avoid insufficient dissolution.
In this embodiment, reation kettle is equipped with agitator motor and temperature measuring device, stirs in order to promote reaction rate and efficiency to the raw materials through agitator motor, and temperature measuring device real-time measurement temperature provides temperature control system and carries out temperature control to avoid the high temperature or lead to the reaction incompletely excessively low.
In this embodiment, reation kettle is equipped with agitator motor and temperature measuring device, stirs the raw materials through agitator motor in order to promote reaction rate and efficiency, and temperature measuring device real-time measurement temperature provides temperature control system for and carries out temperature control to avoid the high temperature or lead to the reaction incomplete excessively.
In this embodiment, be equipped with agitator motor and temperature measurement device in the stills, generate and carry the product of coming to stir in order to promote evaporation rate and efficiency to reation kettle through agitator motor, temperature measurement device real-time measurement temperature provides temperature control system for carrying out temperature control to avoid the temperature to hang down excessively to lead to evaporation rate to hang down, piled up by the product.
In practical application, the first water tank and the second water tank are respectively provided with a liquid level indicator, and when the liquid levels in the first water tank and the second water tank reach a certain degree, water is drained or the water tanks are replaced in time.
In this embodiment, the finished product jar is connected with vacuum system, and under certain vacuum condition, the product is purer.
In practical application, pressure indicators are respectively arranged on pipelines of the steam system, which are connected with the dissolving pot, the reaction kettle, the distillation kettle and the finished product tank, so that the steam pressure is controlled in time, and the bursting condition is avoided.
The above description is only for the specific embodiments of the present invention, but the protection scope of the present invention is not limited thereto, and any changes or substitutions that can be easily conceived by those skilled in the art within the technical scope of the present invention should be covered within the protection scope of the present invention. Therefore, the protection scope of the present invention shall be subject to the protection scope of the claims.
Claims (10)
1. A production system of octyl stearate comprises a reaction kettle, a distillation kettle, a finished product tank, a temperature control system and a vacuum system, wherein the temperature control system and the vacuum system are respectively connected with the reaction kettle, the distillation kettle and the finished product tank, and is characterized in that the production system further comprises a dissolving pot, the dissolving pot is connected with a feed inlet of the reaction kettle, the production system further comprises a first condenser, a first oil-water separator, a first water tank, a second condenser, a second oil-water separator and a second water tank, the first condenser is respectively connected with the reaction kettle and an inlet of the first oil-water separator, the first oil-water separator comprises a first oil outlet, a first water outlet and a first vacuum port, the first water outlet is connected with the first water tank, the first oil outlet is connected with the feed inlet of the reaction kettle, the second condenser is respectively connected with a steam outlet of the distillation kettle and an inlet of the second oil-water separator, the second oil-water separator comprises a second oil outlet, a second water outlet and a second vacuum port, the second oil outlet is connected with the finished product tank, the second water outlet is connected with the second water tank, and the vacuum system is respectively connected with the first vacuum port and the second vacuum port.
2. The octyl stearate production system of claim 1, wherein the dissolution kettle is coupled to a temperature control system.
3. The octyl stearate production system according to claim 1, wherein the dissolving tank comprises a stirring motor and a temperature measuring device disposed within the dissolving tank.
4. The octyl stearate production system of claim 1, wherein level indicators are provided on each of the first and second water tanks.
5. The octyl stearate production system according to claim 1, wherein temperature measuring devices are provided in the reaction still and the distillation still, respectively.
6. The octyl stearate production system according to claim 1, wherein the finishing tank is connected to a vacuum system.
7. The octyl stearate production system of claim 1, wherein the still pot is provided with a stirring motor.
8. The octyl stearate production system according to claim 1, wherein the reaction kettle is provided with a stirring motor.
9. The octyl stearate production system according to any one of claims 1 to 8, wherein the temperature control system comprises a steam system and a cooling water system, the steam system is respectively connected with the dissolution kettle, the reaction kettle, the distillation kettle and the finished product tank and respectively provides the dissolution kettle, the reaction kettle, the distillation kettle and the finished product tank with the required temperatures, and the cooling water system is respectively connected with the dissolution kettle, the reaction kettle, the distillation kettle and the finished product tank and respectively controls the temperatures of the dissolution kettle, the reaction kettle, the distillation kettle and the finished product tank.
10. The octyl stearate production system according to claim 9, wherein pressure indicators are provided on the pipes connecting the steam system to the dissolution kettle, the reaction kettle, the distillation kettle and the finished product tank, respectively.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202123292596.1U CN217041338U (en) | 2021-12-25 | 2021-12-25 | Octyl stearate production system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202123292596.1U CN217041338U (en) | 2021-12-25 | 2021-12-25 | Octyl stearate production system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN217041338U true CN217041338U (en) | 2022-07-26 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202123292596.1U Active CN217041338U (en) | 2021-12-25 | 2021-12-25 | Octyl stearate production system |
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| Country | Link |
|---|---|
| CN (1) | CN217041338U (en) |
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2021
- 2021-12-25 CN CN202123292596.1U patent/CN217041338U/en active Active
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| EE01 | Entry into force of recordation of patent licensing contract |
Assignee: Shanghai Quanshuo Technology Co.,Ltd. Assignor: Shanghai Shengliang Technology Co.,Ltd. Contract record no.: X2023980036083 Denomination of utility model: A Production System for Octyl Stearate Granted publication date: 20220726 License type: Common License Record date: 20230530 |