CN219783837U - Methyl thio propanol rectifying device - Google Patents
Methyl thio propanol rectifying device Download PDFInfo
- Publication number
- CN219783837U CN219783837U CN202320728868.8U CN202320728868U CN219783837U CN 219783837 U CN219783837 U CN 219783837U CN 202320728868 U CN202320728868 U CN 202320728868U CN 219783837 U CN219783837 U CN 219783837U
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- Prior art keywords
- pipe
- cooling device
- water
- distillation plant
- condensation
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- WSHATRMQLGGTRX-UHFFFAOYSA-N 1-methylsulfanylpropan-1-ol Chemical compound CCC(O)SC WSHATRMQLGGTRX-UHFFFAOYSA-N 0.000 title claims abstract description 17
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 55
- 238000001816 cooling Methods 0.000 claims abstract description 25
- 238000004821 distillation Methods 0.000 claims description 21
- 238000009833 condensation Methods 0.000 claims description 15
- 230000005494 condensation Effects 0.000 claims description 15
- 238000007599 discharging Methods 0.000 abstract description 3
- 239000000463 material Substances 0.000 abstract description 3
- 238000010586 diagram Methods 0.000 description 2
- 239000007791 liquid phase Substances 0.000 description 2
- 239000012071 phase Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
Landscapes
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The utility model discloses a methylthio propanol rectifying device which comprises a distilling device, a feeding hole, a water pump, a connecting pipe, a discharging hole, a steam pipeline, a cooling device, a cold water pipe, a hot water pipe, a main pipeline and a condensed water outlet. The utility model has reasonable design and simple and convenient use, and can precisely control the temperature of the materials to be 76-98 ℃ by multistage rectification to obtain the methylthiopropanol finished product meeting the requirements.
Description
Technical Field
The utility model relates to a methylthiopropanol rectifying device.
Background
The rectifying device is a tower type gas-liquid contacting device for rectifying. By utilizing the characteristic that each component in the mixture has different volatility, namely, the vapor pressures of the components are different at the same temperature, the light component (low-boiling-point substance) in the liquid phase is transferred to the gas phase, and the heavy component (high-boiling-point substance) in the gas phase is transferred to the liquid phase, so that the purpose of separation is realized.
Disclosure of Invention
The utility model aims to provide a methylthiopropanol rectifying device, which solves the problems in the background art.
In order to achieve the above purpose, the present utility model provides the following technical solutions:
the utility model provides a methylthio propanol rectifying device, includes distillation plant, feed inlet, water pump, connecting pipe, discharge gate, steam conduit, cooling device, cold water pipe, hot-water line, trunk line, comdenstion water export, the feed inlet is installed to the distillation plant top, the water pump is installed to the distillation plant bottom, install the connecting pipe on the water pump, the connecting pipe top is connected with adjacent distillation plant top, the distillation plant is tertiary in proper order connected, the discharge gate is installed to distillation plant end below, distillation plant top rear end is all connected with cooling device through steam conduit, the cold water pipe is all installed at the cooling device top, and the hot-water line is all installed to the cooling device bottom, cold water pipe and hot-water line are connected through the trunk line respectively, the comdenstion water export has all been seted up to cooling device rear end below.
Preferably: the methylthio propanol rectifying device further comprises a condensing pipe, the condensing pipe is arranged in the cooling device, the top of the condensing pipe is connected with the cold water pipe, the bottom of the condensing pipe is connected with the hot water pipe, and water vapor outside the condensing pipe is liquefied through the condensing pipe and is discharged through a condensation water outlet at the bottom of the cooling device.
Preferably: the distillation device is arranged in three stages, and the temperature is sequentially increased between 76 ℃ and 98 ℃.
The beneficial effects of the utility model are as follows: the utility model has reasonable design and simple and convenient use, and can precisely control the temperature of the materials to be 76-98 ℃ by multistage rectification to obtain the methylthiopropanol finished product meeting the requirements.
Drawings
FIG. 1 is a schematic structural diagram of a rectification apparatus for methylthiopropanol according to the present utility model;
fig. 2 is a schematic structural diagram of the rectification apparatus of methylthiopropanol according to the present utility model.
In the figure: 1. distillation plant 2, feed inlet, 3, water pump, 4, connecting pipe, 5, discharge gate, 6, steam pipe, 7, cooling device, 8, cold water pipe, 9, hot water pipe, 10, trunk line, 11, comdenstion water export, 12, condenser pipe.
Description of the embodiments
The utility model is further illustrated by the following description in conjunction with the accompanying drawings and specific embodiments:
as shown in fig. 1-2, a methylthiopropanol rectifying device comprises a distilling device 1, a feeding hole 2, a water pump 3, a connecting pipe 4, a discharging hole 5, a steam pipeline 6, a cooling device 7, a cold water pipe 8, a hot water pipe 9, a main pipeline 10 and a condensed water outlet 11, wherein the feeding hole 2 is arranged above the distilling device 1, the water pump 3 is arranged at the bottom of the distilling device 1, the connecting pipe 4 is arranged on the water pump 3, the top of the connecting pipe 4 is connected with the upper part of the adjacent distilling device 1, the distilling device 1 is sequentially connected in three stages, the discharging hole 5 is arranged below the tail end of the distilling device 1, the rear end of the upper part of the distilling device 1 is connected with the cooling device 7 through the steam pipeline 6, the cold water pipe 8 is arranged at the top of the cooling device 7, the hot water pipe 8 is arranged at the bottom of the cooling device 7, the cold water pipe 8 and the hot water pipe 9 are respectively connected through the main pipeline 10, and the condensed water outlet 11 is arranged below the rear end of the cooling device 7. The methylthio propanol rectifying device further comprises a condensation pipe 12, the condensation pipe 12 is arranged in the cooling device 7, the top of the condensation pipe 12 is connected with the cold water pipe 8, the bottom of the condensation pipe 12 is connected with the hot water pipe 9, water vapor outside the condensation pipe 12 is liquefied through the condensation pipe, and is discharged through a condensation water outlet 11 at the bottom of the cooling device 7. The distillation device 1 is arranged in three stages, and the temperature is sequentially increased between 76 ℃ and 98 ℃.
The application method of the utility model comprises the following steps: coarse materials are added through the feed inlet 2, distilled by the distillation device 1 and then enter the distillation device 1 of the next stage of the connecting pipe 4 through the water pump 3, water vapor enters the cooling area of the cooling device 7 through the steam pipeline 6, and finished products are discharged through the discharge outlet 5 on the distillation device 1 of the last stage.
It will be evident to those skilled in the art that the utility model is not limited to the details of the foregoing illustrative embodiments, and that the present utility model may be embodied in other specific forms without departing from the spirit or essential characteristics thereof. Accordingly, the embodiments are to be considered in all respects as illustrative and all equivalent variations within the scope of the utility model are intended to be embraced thereby.
Claims (3)
1. The utility model provides a methylthio propanol rectifying device, includes distillation plant (1), feed inlet (2), water pump (3), connecting pipe (4), discharge gate (5), steam conduit (6), cooling device (7), cold water pipe (8), hot-water line (9), trunk line (10), comdenstion water export (11), its characterized in that: feed inlet (2) are installed to distillation plant (1) top, water pump (3) are installed to distillation plant (1) bottom, install connecting pipe (4) on water pump (3), connecting pipe (4) top is connected with adjacent distillation plant (1) top, distillation plant (1) tertiary in proper order is connected, discharge gate (5) are installed to distillation plant (1) end below, distillation plant (1) top rear end all is connected with cooling device (7) through steam conduit (6), cold water pipe (8) are all installed at cooling device (7) top, and hot water pipe (9) are all installed to cooling device (7) bottom, cold water pipe (8) and hot water pipe (9) are connected through trunk line (10) respectively, condensate water export (11) have all been seted up to cooling device (7) rear end below.
2. The methylthiopropanol rectification apparatus according to claim 1, wherein: the methylthio propanol rectifying device further comprises a condensation pipe (12), the condensation pipe (12) is arranged in the cooling device (7), the top of the condensation pipe (12) is connected with the cold water pipe (8), the bottom of the condensation pipe (12) is connected with the hot water pipe (9), and water vapor outside the condensation pipe (12) is liquefied through the condensation pipe and is discharged through a condensation water outlet (11) at the bottom of the cooling device (7).
3. The methylthiopropanol rectification apparatus according to claim 1, wherein: the distillation device (1) is arranged in three stages, and the temperature is sequentially increased between 76 ℃ and 98 ℃.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202320728868.8U CN219783837U (en) | 2023-04-06 | 2023-04-06 | Methyl thio propanol rectifying device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202320728868.8U CN219783837U (en) | 2023-04-06 | 2023-04-06 | Methyl thio propanol rectifying device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN219783837U true CN219783837U (en) | 2023-10-03 |
Family
ID=88157841
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202320728868.8U Active CN219783837U (en) | 2023-04-06 | 2023-04-06 | Methyl thio propanol rectifying device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN219783837U (en) |
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2023
- 2023-04-06 CN CN202320728868.8U patent/CN219783837U/en active Active
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