CN218740277U - Distillation extracting tank for residual oil treatment - Google Patents
Distillation extracting tank for residual oil treatment Download PDFInfo
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- CN218740277U CN218740277U CN202221767424.7U CN202221767424U CN218740277U CN 218740277 U CN218740277 U CN 218740277U CN 202221767424 U CN202221767424 U CN 202221767424U CN 218740277 U CN218740277 U CN 218740277U
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Abstract
The utility model belongs to the technical field of the residual oil distillation, especially, a residual oil is handled and is drawn jar with distillation, including the preheating tank, preheating tank right side wall upper end intercommunication has mixed liquid supply pipe, and the inside upper end of preheating tank has set firmly the water conservancy diversion piece, and the annular array structure intercommunication is personally submitted to the water conservancy diversion piece bottom has a plurality of nozzles, and the inside crisscross distribution that is of preheating tank has a plurality of heating rods. The utility model discloses carry the mixed liquid of residual oil to the nozzle through mixing the liquid supply pipe and spray, inside the heating rod carries to the retort through the conveyer pipe after preheating and heating, the distributing plate carries out evenly distributed, the hot plate heats the evaporation, steam after the evaporation carries out the condensation through the condensation plate and is the distillate and falls into toper deflector top surface, the distillate of gathering is discharged from the distillate contact tube to outside collection completion distillation operation. Preheating before evaporation is realized, heating efficiency and evaporation effect are improved, evaporation efficiency is improved, condensation effect is improved, gathering and conveying of distillate are facilitated, and using effect is remarkably improved.
Description
Technical Field
The utility model relates to a residual oil distillation technical field especially relates to a residual oil is handled and is drawed jar with distillation.
Background
A byproduct obtained after oil deodorization in the vegetable oil refining process is called vegetable oil deodorization distillate and commonly called DD oil, the distillate is treated as waste in the early stage, sterol, VE and fatty acid methyl ester in the distillate are extracted after technical treatment of raw materials, residual oil is residual waste obtained after the DD oil extracts the phytosterol, the VE and the fatty acid methyl ester, the residual part is treated as the byproduct or the waste after the DD oil extracts required components, and the byproduct or the waste is commonly called residual oil in the industry.
The residual oil is generally sold as combustion oil or treated as waste, but the residual oil contains a large amount of sterol ester, and phytosterol can be extracted after the residual oil is treated by a proper process; the principle is that based on the difference of chemical substances and physical properties of raw materials, the separation of each component is realized by utilizing the changes of saponification, neutralization, enzymolysis, temperature difference, pressure difference and the like; the main methods include solvent crystallization, molecular distillation, saponification complexation and biological enzyme method.
During the existing residual oil treatment, residual sterol ester and phytosterol in residual oil mixed liquor are extracted by distillation, the residual oil mixed liquor is generally boiled to be boiling, water vapor rises synchronously with the sterol ester and the phytosterol, and extraction is carried out after condensation, however, during the residual oil distillation, the residual oil mixed liquor is heated to be boiling for a long time, the distillation efficiency is low, and the residual oil extraction effect is influenced.
SUMMERY OF THE UTILITY MODEL
Based on current residual oil distillation technical problem, the utility model provides a residual oil is handled and is drawed jar with distillation.
The utility model provides a distillation extraction tank for residual oil treatment, including the preheating tank, preheating tank right side wall upper end intercommunication has mixed liquid supply pipe, the inside upper end of preheating tank has set firmly the water conservancy diversion piece, it has a plurality of nozzles to personally submit annular array structure intercommunication at the bottom of the water conservancy diversion piece, inside being the staggered distribution of preheating tank has a plurality of heating rods, preheating tank left side wall lower extreme intercommunication has the conveyer pipe, conveyer pipe left end intercommunication has the distillation retort, the inside lower extreme of distillation retort has set firmly the distributing plate, it has seted up a plurality of through-holes to be annular array structure on the distributing plate, the condensing panel is installed to the distillation retort top surface.
Preferably, the water conservancy diversion piece is hollow structure, be about symmetrical structure has set firmly two hot plates on the distributing plate, be the align to grid structure on the hot plate and seted up a plurality of bar holes, the inside heater strip that is equipped with of hot plate inlays.
Through above-mentioned technical scheme, the heating wire heats the hot plate, has improved heating efficiency, has made things convenient for the evaporation to use.
Preferably, the inside upper end of retort has set firmly the toper guide plate, toper guide plate middle part has set firmly circular filter block, the retort upper end is bilateral symmetry structure intercommunication and has two distillate eduction tubes, circular filter block edge top surface and distillate eduction tube bottom surface are located same horizontal plane.
Through above-mentioned technical scheme, the convenient distillate with the gathering of toper guide plate is discharged to the outside from the distillate eduction tube and is collected.
Preferably, a radiator is fixedly arranged on the top surface of the condensation plate, the condensation plate is of a hollow structure, and the condensation plate is communicated with the radiator through a pipeline.
Through above-mentioned technical scheme, the condensing panel has made things convenient for to steam carries out the condensation and is the distillate, has improved the condensation effect.
Preferably, the left end of the rear wall of the condensing plate is communicated with an L-shaped water inlet pipe with a valve, and the rear end of the right wall of the condensing plate is provided with a water pump through a mounting seat.
Through above-mentioned technical scheme, L type inlet tube is convenient annotates coolant liquid or water.
Preferably, the water inlet end of the water pump is communicated with the interior of the condensation plate, and the water outlet end of the water pump is communicated with the metal pipe on the radiator.
Through above-mentioned technical scheme, the water pump exchanges the coolant liquid or the water of cold plate and radiator each other.
The utility model provides a beneficial effect does:
1. residual oil mixed liquid to be evaporated is conveyed to the interior of the flow guide block through the arranged mixed liquid supply pipe and is sprayed to the interior of the preheating tank from a nozzle, preheating and heating are carried out through the heating rod, the residual oil mixed liquid is conveyed to the interior of the distillation tank through the conveying pipe after being heated, after uniform distribution is carried out through the distribution plate, the heating plate is heated through the heating wire, the preheated mixed liquid is heated and evaporated when passing through the strip-shaped hole, steam after evaporation passes through the circular filter block and is condensed through the condensing plate to form distillate which falls into the top surface of the conical flow guide plate, and the collected distillate is discharged from the distillate discharge pipe to the outside to be collected and distilled. Preheating before evaporation is realized, heating efficiency and evaporation effect are improved, evaporation efficiency is improved, condensation effect is improved, gathering and conveying of distillate are facilitated, and using effect is remarkably improved.
2. Through L type inlet tube add notes coolant liquid or water to the condensing plate, carry the inside coolant liquid of condensing plate or water to the metal pipe on the radiator through the water pump intraduct, get into the inside used repeatedly of condensing plate again after the radiator cooling, for the inside coolant liquid of condensing plate or water effectively cool down, provide the advantage for the use of condensing plate, simple structure simple operation.
Drawings
FIG. 1 is a schematic diagram of the overall structure of a distillation extraction tank for residual oil treatment according to the present invention;
FIG. 2 is a sectional view showing the structure of a preheating tank of a distillation and extraction tank for residual oil treatment according to the present invention;
FIG. 3 is a sectional view of the flow guide block of the distillation extraction tank for residual oil treatment according to the present invention;
FIG. 4 is a sectional view of the distillation tank structure of a distillation extraction tank for residual oil treatment according to the present invention;
FIG. 5 is a sectional view showing the structure of a heating plate of a distillation and extraction tank for residual oil treatment according to the present invention;
fig. 6 is a top view of the heat sink structure of the distillation extraction tank for residual oil treatment according to the present invention.
In the figure: 1. a preheating tank; 2. a mixed liquid supply pipe; 3. a flow guide block; 4. a nozzle; 5. a heating rod; 6. a delivery pipe; 7. a distillation tank; 8. a distribution plate; 9. a through hole; 10. a condensing plate; 11. heating plates; 12. a strip-shaped hole; 13. heating wires; 14. a conical deflector; 15. a circular filter block; 16. a distillate delivery pipe; 17. a heat sink; 18. an L-shaped water inlet pipe; 19. and (4) a water pump.
Detailed Description
The technical solutions in the embodiments of the present invention will be described clearly and completely with reference to the 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.
Example one
Referring to fig. 1-5, a distillation extraction tank for residual oil treatment comprises a preheating tank 1, wherein the upper end of the right wall of the preheating tank 1 is communicated with a mixed liquid supply pipe 2, the upper end inside the preheating tank 1 is fixedly provided with a flow guide block 3, the bottom surface of the flow guide block 3 is communicated with a plurality of nozzles 4 in an annular array structure, a plurality of heating rods 5 are distributed inside the preheating tank 1 in a staggered manner, the lower end of the left wall of the preheating tank 1 is communicated with a conveying pipe 6, the left end of the conveying pipe 6 is communicated with a distillation tank 7, the lower end inside the distillation tank 7 is fixedly provided with a distribution plate 8, the distribution plate 8 is provided with a plurality of through holes 9 in an annular array structure, and a condensation plate 10 is mounted on the top surface of the distillation tank 7.
The water conservancy diversion piece 3 is hollow structure, is upper and lower symmetrical structure on the distributing plate 8 and has set firmly two hot plates 11, is align to grid structure on the hot plate 11 and has seted up a plurality of bar holes 12, and 11 inside heater strips 13 that are equipped with of hot plate are inlayed. The heating wire 13 heats the heating plate 11, so that the heating efficiency is improved, and the evaporation and the use are facilitated.
The upper end of the inner part of the distillation retort 7 is fixedly provided with a conical guide plate 14, the middle part of the conical guide plate 14 is fixedly provided with a circular filter block 15, the upper end of the distillation retort 7 is in a bilateral symmetry structure and is communicated with two distillate delivery pipes 16, and the top surface of the edge of the circular filter block 15 and the bottom surface of the distillate delivery pipe 16 are positioned on the same horizontal plane. The conical baffle 14 facilitates the discharge of the collected distillate from the distillate lead-out pipe 16 to the outside for collection.
The utility model discloses a theory of operation: when using the utility model discloses the time, at first mixed liquid of residual oil that will evaporate is carried to inside water conservancy diversion piece 3 through mixing liquid supply pipe 2, and spray to preheating tank 1 inside from nozzle 4, preheat the heating through heating rod 5, carry to 7 insides of retort through conveyer pipe 6 after the heating, carry out evenly distributed back through distributing plate 8, heat heating plate 11 through heater strip 13, make the mixed liquid after preheating heat evaporation when passing bar hole 12, steam after the evaporation carries out the condensation through condensing plate 10 after passing circular filter block 15 and is the distillate and falls into 14 top surfaces of toper guide plate, the distillate of gathering is discharged from distillate contact tube 16 to outside and is collected the completion distillation operation.
Example two
Referring to fig. 6, on the basis of the first embodiment, a radiator 17 is fixedly disposed on the top surface of the condensation plate 10, the condensation plate 10 is in a hollow structure, and the condensation plate 10 is communicated with the radiator 17 through a pipeline. The condensing plate 10 facilitates condensing the steam into distillate, and improves the condensing effect.
The left end of the rear wall of the condensation plate 10 is communicated with an L-shaped water inlet pipe 18 with a valve, and the rear end of the right wall of the condensation plate 10 is provided with a water pump 19 through a mounting seat. The L-shaped water inlet pipe 18 facilitates the filling of cooling liquid or water.
The water inlet end of the water pump 19 is communicated with the interior of the condensation plate 10, and the water outlet end of the water pump 19 is communicated with the metal pipe on the radiator 17. The water pump 19 exchanges the cooling liquid or water of the cold plate 10 and the radiator 17 with each other.
During the use, annotate coolant liquid or water through L type inlet tube 18 to condensing plate 10, carry the inside coolant liquid or the water of condensing plate 10 to the metal pipe on the radiator 17 through water pump 19 inside, get into the inside used repeatedly of condensing plate 10 again after the radiator 17 cools off, for the inside coolant liquid or the water of condensing plate 10 effectively cool down, provide the advantage for the use of condensing plate 10.
The above, only be the embodiment of the preferred of the present invention, but the protection scope of the present invention is not limited thereto, and any person skilled in the art is in the technical scope of the present invention, according to the technical solution of the present invention and the utility model, which are designed to be replaced or changed equally, all should be covered within the protection scope of the present invention.
Claims (6)
1. A distillation extraction tank for residual oil treatment comprises a preheating tank (1), and is characterized in that: the utility model discloses a preheating tank, including preheating tank (1), guide block (3), retort (1), retort (7), distributing plate (8), it has a plurality of through-holes (9) to be annular array structure on distributing plate (8), preheating tank (7) top surface installation condensing plate (10), preheating tank (1) inside upper end has set firmly guide block (3), guide block (3) bottom surface is annular array structure intercommunication has a plurality of nozzles (4), preheating tank (1) inside is staggered distribution and has a plurality of heating rods (5), preheating tank (1) left side wall lower extreme intercommunication has conveyer pipe (6), conveyer pipe (6) left end intercommunication has retort (7), retort (7) inside lower extreme has set firmly distributing plate (8), it has seted up a plurality of through-holes (9) to be annular array structure on distributing plate (8).
2. A distillation extraction tank for residue treatment according to claim 1, characterized in that: flow guide block (3) are hollow structure, be upper and lower symmetrical structure on distributing plate (8) and set firmly two hot plates (11), be align to grid on hot plate (11) and seted up a plurality of bar holes (12), hot plate (11) inside inlays and is equipped with heater strip (13).
3. The distillation extraction tank for residue treatment according to claim 1, characterized in that: the distillation retort (7) inside upper end has set firmly toper guide plate (14), toper guide plate (14) middle part has set firmly circular filter block (15), distillation retort (7) upper end is bilateral symmetry structure intercommunication and has two distillate eduction tubes (16), circular filter block (15) edge top surface and distillate eduction tube (16) bottom surface are located same horizontal plane.
4. A distillation extraction tank for residue treatment according to claim 1, characterized in that: the top surface of the condensation plate (10) is fixedly provided with a radiator (17), the condensation plate (10) is of a hollow structure, and the condensation plate (10) is communicated with the radiator (17) through a pipeline.
5. The distillation extraction tank for residue treatment according to claim 4, characterized in that: the left end of the rear wall of the condensing plate (10) is communicated with an L-shaped water inlet pipe (18) with a valve, and the rear end of the right wall of the condensing plate (10) is provided with a water pump (19) through a mounting seat.
6. The distillation extraction tank for residue treatment according to claim 5, characterized in that: the water inlet end of the water pump (19) is communicated with the interior of the condensation plate (10), and the water outlet end of the water pump (19) is communicated with the metal pipe on the radiator (17).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202221767424.7U CN218740277U (en) | 2022-07-01 | 2022-07-01 | Distillation extracting tank for residual oil treatment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202221767424.7U CN218740277U (en) | 2022-07-01 | 2022-07-01 | Distillation extracting tank for residual oil treatment |
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| Publication Number | Publication Date |
|---|---|
| CN218740277U true CN218740277U (en) | 2023-03-28 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN202221767424.7U Active CN218740277U (en) | 2022-07-01 | 2022-07-01 | Distillation extracting tank for residual oil treatment |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN118325666A (en) * | 2024-03-30 | 2024-07-12 | 广东善百年特医食品有限公司 | Process and equipment for reducing 3-chloropropanol ester and glycidyl ester content in diglyceride oil |
-
2022
- 2022-07-01 CN CN202221767424.7U patent/CN218740277U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN118325666A (en) * | 2024-03-30 | 2024-07-12 | 广东善百年特医食品有限公司 | Process and equipment for reducing 3-chloropropanol ester and glycidyl ester content in diglyceride oil |
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