CN220834159U - Crude fatty acid refining and diverting device - Google Patents
Crude fatty acid refining and diverting device Download PDFInfo
- Publication number
- CN220834159U CN220834159U CN202322492803.0U CN202322492803U CN220834159U CN 220834159 U CN220834159 U CN 220834159U CN 202322492803 U CN202322492803 U CN 202322492803U CN 220834159 U CN220834159 U CN 220834159U
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- Prior art keywords
- fatty acid
- condensing box
- crude fatty
- pipe
- box
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- 235000014113 dietary fatty acids Nutrition 0.000 title claims abstract description 42
- 229930195729 fatty acid Natural products 0.000 title claims abstract description 42
- 239000000194 fatty acid Substances 0.000 title claims abstract description 42
- 150000004665 fatty acids Chemical class 0.000 title claims abstract description 42
- 238000007670 refining Methods 0.000 title claims abstract description 19
- 238000000926 separation method Methods 0.000 claims abstract description 27
- 238000003756 stirring Methods 0.000 claims abstract description 25
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 24
- 238000010438 heat treatment Methods 0.000 claims abstract description 12
- 238000011064 split stream procedure Methods 0.000 claims 5
- 239000000463 material Substances 0.000 claims 3
- 238000009833 condensation Methods 0.000 abstract description 19
- 230000005494 condensation Effects 0.000 abstract description 19
- 230000000694 effects Effects 0.000 abstract description 13
- 239000000203 mixture Substances 0.000 abstract description 4
- 230000009286 beneficial effect Effects 0.000 abstract description 3
- 239000012535 impurity Substances 0.000 abstract description 3
- 239000002245 particle Substances 0.000 abstract description 3
- 239000002699 waste material Substances 0.000 description 5
- 238000000746 purification Methods 0.000 description 4
- 239000007921 spray Substances 0.000 description 4
- 230000006872 improvement Effects 0.000 description 3
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 150000002632 lipids Chemical class 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 238000005452 bending Methods 0.000 description 1
- 239000003054 catalyst Substances 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 229940079593 drug Drugs 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 239000004519 grease Substances 0.000 description 1
- 230000007246 mechanism Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 230000000149 penetrating effect Effects 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 229920003023 plastic Polymers 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 239000005060 rubber Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 230000001502 supplementing effect Effects 0.000 description 1
- 239000004753 textile Substances 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
Classifications
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/74—Recovery of fats, fatty oils, fatty acids or other fatty substances, e.g. lanolin or waxes
Landscapes
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The utility model discloses a crude fatty acid refining and splitting device, which belongs to the technical field of fatty acid refining and comprises separation equipment, a condensing box and a storage box, wherein the condensing box is connected with the separation equipment through a connecting pipe, and the storage box is connected with the condensing box through a conveying pipe; the separation equipment comprises a shell and a screen drum arranged in the shell, wherein stirring blades are arranged in the screen drum and driven by a stirring motor, and the stirring motor is arranged at the top of the separation equipment; the connecting pipe enters the condensing box and then is converted into a plurality of arched branch pipes, and the condensed arched branch pipes are converged into a conveying pipe to be connected with the storage box. The separation effect of the mixture can be greatly improved through the design of the screen drum and the stirring fan blades, wherein larger impurities and particles are heated by the heating rod and are beneficial to purifying and separating crude fatty acid after the stirring fan blades are stirred and broken. The condensation effect can be greatly improved through the mutual matching of the arched branch pipes, the shower heads and the nozzles, and condensed water can be repeatedly utilized through the design of the circulating pump.
Description
Technical Field
The utility model relates to the technical field of refined fatty acid preparation, in particular to a crude fatty acid refining and splitting device.
Background
Fatty acid is an important chemical basic raw material and is widely applied to the industries of rubber, plastics, textiles, washing, papermaking, medicines, foods and the like. Fatty acids are the simplest type of lipid, which is a constituent of many more complex lipids. Under the condition of sufficient oxygen supply, the fatty acid can be oxidatively decomposed into CO2 and H2O to release a large amount of energy, so that the fatty acid is one of main energy sources of organisms, the fatty acid is produced by heating sulfuric acid by grease and matching with a catalyst, crude fatty acid is formed firstly, then the crude fatty acid is heated and dehydrated to form refined fatty acid, and heating is an important condition in the process of dehydrating the crude fatty acid to form the refined fatty acid.
Application number: CN202121271815.5; the utility model discloses a crude fatty acid purifying device, which comprises a fractionating tower and a controller, wherein a heat conduction oil furnace is connected and arranged on the fractionating tower, a condenser is connected and arranged on the top of the fractionating tower, a reboiler is connected and arranged at the bottom of the fractionating tower, and a temperature adjusting mechanism is communicated and arranged on the reboiler; the condenser is characterized in that a plurality of layers of independent condensing pipes are arranged in parallel inside the condenser, the two ends of the condenser are respectively connected with a water inlet pipe and a water outlet pipe, a water pipe split head is arranged on the water inlet pipe and is respectively communicated with the water inlet end of each independent condensing pipe, the water outlet end of each independent condensing pipe is communicated with the water outlet pipe, and each independent condensing pipe is arranged in an S-shaped bending mode in the same plane. The utility model has better condensation effect, can separate fatty acid from waste liquid to the greatest extent, and improves the yield.
The above crude fatty acid splitting device of the reference has poor separation effect, general purification effect on fatty acid in waste, and general condensation effect of the condensation device, resulting in incomplete condensation, so a crude fatty acid refining splitting device is designed here in order to solve the above problems.
Disclosure of utility model
The utility model aims at: in order to solve the problems that the traditional crude fatty acid splitting device has poor separation effect, has a general purification effect on fatty acid in waste, and the condensation effect of the condensation device is general and the condensation is not thorough, the crude fatty acid refining splitting device is provided.
In order to achieve the above purpose, the technical scheme of the utility model is as follows: the crude fatty acid refining and splitting device comprises separation equipment, a condensing box and a storage box, wherein the condensing box is connected with the separation equipment through a connecting pipe, and the storage box is connected with the condensing box through a conveying pipe; the separation equipment comprises a shell and a screen drum arranged in the shell, wherein stirring blades are arranged in the screen drum and driven by a stirring motor, and the stirring motor is arranged at the top of the separation equipment; the connecting pipe enters the condensing box and then is converted into a plurality of arched branch pipes, and the condensed arched branch pipes are converged into the conveying pipe to be connected with the storage box.
As still further aspects of the utility model: the inner wall of the shell is provided with a plurality of uniformly distributed heating rods, the bottom of the screen cylinder is provided with a discharge pipe, the discharge pipe penetrates through the bottom of the shell, and the discharge pipe is further provided with a valve.
As still further aspects of the utility model: the top of the screen cylinder is provided with a feeding port, and the feeding port penetrates through the side wall of the shell.
As still further aspects of the utility model: the top of the condensing box is provided with a spiral coil pipe, and a plurality of shower heads are uniformly distributed on the spiral coil pipe; the side of the condensing box is provided with a plurality of nozzles, the bottom of the condensing box is provided with a circulating pump, and the circulating pump is communicated with the spiral coil and the nozzles through a circulating pipe.
As still further aspects of the utility model: the sieve barrels are uniformly provided with sieve holes, and the arched branch pipes are uniformly distributed in the vertical direction.
As still further aspects of the utility model: the bottom of the condensing box is provided with a water outlet, and the top of the condensing box is provided with a water adding tank.
The utility model provides a crude fatty acid refining and splitting device through improvement, which has the following improvement and advantages compared with the prior art:
the method comprises the following steps: the utility model can greatly improve the separation effect of the mixture through the design of the screen drum and the stirring fan blade, wherein larger impurities and particles are heated by the heating rod and are beneficial to the purification and separation of the crude fatty acid after the stirring fan blade is stirred and broken.
And two,: the utility model can greatly improve the condensation effect through the mutual matching of the arched branch pipes, the shower heads and the nozzles, wherein the arched branch pipes can effectively split the connecting pipes, and the shower heads and the nozzles can repeatedly spray and cool the arched branch pipes. In addition, the condensed water can be recycled through the design of the circulating pump, so that the water saving capability of the crude fatty acid refining and splitting device is greatly improved.
Drawings
The utility model is further explained below with reference to the drawings and examples:
FIG. 1 is a cross-sectional view of the structure of the present utility model;
FIG. 2 is an exploded bottom view of the present utility model;
FIG. 3 is an enlarged view of the structure of FIG. 2A in accordance with the present utility model;
fig. 4 is a side view of a condensing tank in the construction of the present utility model.
Reference numerals illustrate:
1. A separation device; 101. a housing; 102. a screen drum; 103. a discharge pipe; 104. a valve; 105. stirring fan blades; 106. a stirring motor; 107. a connecting pipe; 108. a feeding port; 109. a heating rod; 2. a condensing box; 201. an arcuate branch pipe; 202. a delivery tube; 203. a spiral coil; 204. shower head; 205. a nozzle; 206. a circulation pump; 207. a circulation pipe; 3. a storage box.
Detailed Description
The following detailed description of the present utility model will provide clear and complete description of the technical solutions of the embodiments of the present utility model, with reference to fig. 1 to 4, and it is obvious that the described embodiments 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.
The utility model provides a crude fatty acid refining and splitting device by improvement, as shown in fig. 1-4, which comprises a separation device 1, a condensing box 2 and a storage box 3, wherein the condensing box 2 is connected with the separation device 1 through a connecting pipe 107, and the storage box 3 is connected with the condensing box 2 through a conveying pipe 202; the separation device 1 comprises a shell 101 and a screen drum 102 arranged in the shell 101, wherein stirring blades 105 are arranged in the screen drum 102, the stirring blades 105 are driven by a stirring motor 106, and the stirring motor 106 is arranged at the top of the separation device 1; the connecting pipe 107 enters the condensing box 2 and is converted into a plurality of arched branch pipes 201, and the condensed arched branch pipes 201 are converged into a conveying pipe 202 to be connected with the storage box 3.
In this embodiment: the utility model is mainly divided into three parts: a separation device 1, a condensation tank 2 and a storage tank 3. When the present utility model is in operation, raw materials are first fed into the interior of the screen drum 102 through the feed port 108, and then the agitator motor 106 is turned on. The crude fatty acid is gasified and accumulated on the top of the separation apparatus 1 by the stirring operation of the stirring blade 105 and the heating rod 109. The separated waste is discharged through the discharge pipe 103 and the gas is introduced into the condensation tank 2 through the connection pipe 107. The connection pipe 107 is divided into a plurality of arcuate branch pipes 201 in the condensation tank 2, and the gas inside the arcuate branch pipes 201 is converted into liquid under repeated shower condensation of the shower head 204 and the nozzles 205. The condensed crude fatty acids follow the arcuate branch 201 and are collected into a transfer pipe 202 to be stored in the storage tank 3. The condensed water at the bottom of the condensing tank 2 is circulated and condensed again through the shower head 204 and the nozzle 205 by the circulation pump 206 and the circulation pipe 207. When the condensed water needs to be replaced, a water outlet arranged at the bottom of the condensing box 2 is opened, and when the condensed water needs to be supplemented, a water adding tank arranged at the top of the condensing box 2 is opened.
The utility model can greatly improve the separation effect of the mixture through the design of the screen drum 102 and the stirring fan blades 105, wherein larger impurities and particles are beneficial to the purification and separation of the crude fatty acid after the heating rod 109 heats and the stirring fan blades 105 stir and break, and the design can reduce the labor cost and the time cost of the crude fatty acid refining and splitting device. The utility model can greatly improve the condensation effect through the mutual matching of the arched branch pipe 201, the shower head 204 and the nozzle 205, wherein the arched branch pipe 201 can effectively split the connecting pipe 107, and the shower head 204 and the nozzle 205 can repeatedly spray and cool the arched branch pipe 201. In addition, condensed water can be recycled through the design of the circulating pump 206, so that the water saving capacity of the crude fatty acid refining and splitting device is greatly improved.
Referring to fig. 1-2, a plurality of uniformly distributed heating rods 109 are arranged on the inner wall of the housing 101, a discharge pipe 103 is arranged at the bottom of the screen drum 102, the discharge pipe 103 penetrates through the bottom of the housing 101, and a valve 104 is further arranged on the discharge pipe 103.
In this embodiment: for the purpose of heating and separating the mixture, a plurality of uniformly distributed heating rods 109 are provided on the inner wall of the housing 101. In order to facilitate the discharge of the waste material, a discharge pipe 103 is provided at the bottom of the screen cylinder 102, and a valve 104 is further provided on the discharge pipe 103.
Referring to fig. 1-2, the top of the screen cylinder 102 is provided with a feed port 108, the feed port 108 extending through the side wall of the housing 101.
In this embodiment: for convenience of feeding, a feed port 108 penetrating the side wall of the casing 101 is provided at the top of the screen cylinder 102.
Referring to fig. 2-4, a spiral coil 203 is arranged at the top of the condensing box 2, and a plurality of shower heads 204 are uniformly distributed on the spiral coil 203; the side of the condensing tank 2 is provided with a plurality of nozzles 205, the bottom of the condensing tank 2 is provided with a circulation pump 206, and the circulation pump 206 communicates with the spiral coil 203 and the nozzles 205 through a circulation pipe 207.
In this embodiment: in order to perform omnibearing and multi-angle spray condensation on the arched branch pipe 201, a spiral coil 203 is arranged at the top of the condensing box 2, a plurality of shower heads 204 are uniformly distributed on the spiral coil 203, and a plurality of nozzles 205 are arranged on the circumferential side surface of the condensing box 2. In order to recycle the condensed water, a circulation pump 206 is provided at the bottom of the condensation tank 2, and the circulation pump 206 communicates with the spiral coil 203 and the nozzle 205 through a circulation pipe 207. This ensures that the sprayed condensate is concentrated at the bottom of the condensation tank 2 and then circulated through the shower head 204 and the nozzle 205.
Referring to fig. 2-3, the screen holes are uniformly distributed on the screen cylinder 102, and the arcuate branch pipes 201 are uniformly distributed in the vertical direction.
In this embodiment: for the separation treatment of the crude fatty acid, the sieve holes are uniformly distributed in the sieve cylinder 102. In order to uniformly spray and condense the arched branch pipes 201, the arched branch pipes 201 are uniformly distributed in the vertical direction.
Referring to fig. 2-4, a drain outlet is arranged at the bottom of the condensing box 2, and a water adding tank is arranged at the top of the condensing box 2.
In this embodiment: for the purpose of supplementing and replacing the condensed water, a drain port is provided at the bottom of the condensation tank 2, and a water-adding tank is provided at the top of the condensation tank 2.
The previous description of the disclosed embodiments is provided to enable any person skilled in the art to make or use the present utility model. Various modifications to these embodiments will be readily apparent to those skilled in the art, and the generic principles defined herein may be applied to other embodiments without departing from the spirit or scope of the utility model. Thus, the present utility model is not intended to be limited to the embodiments shown herein but is to be accorded the widest scope consistent with the principles and novel features disclosed herein.
Claims (6)
1. A crude fatty acid refining and splitting device, which is characterized in that: the device comprises separation equipment (1), a condensing box (2) and a storage box (3), wherein the condensing box (2) is connected with the separation equipment (1) through a connecting pipe (107), and the storage box (3) is connected with the condensing box (2) through a conveying pipe (202); the separation equipment (1) comprises a shell (101) and a screen drum (102) arranged in the shell (101), wherein stirring blades (105) are arranged in the screen drum (102), the stirring blades (105) are driven by a stirring motor (106), and the stirring motor (106) is arranged at the top of the separation equipment (1); the connecting pipe (107) enters the condensing box (2) and then is converted into a plurality of arched branch pipes (201), and the condensed arched branch pipes (201) are converged into a conveying pipe (202) to be connected with the storage box (3).
2. The crude fatty acid refining split stream device according to claim 1, characterized in that: be provided with many evenly distributed's heating rod (109) on the inner wall of shell (101), the bottom of screen cylinder (102) is provided with row material pipe (103), row material pipe (103) run through the bottom of shell (101), it still is provided with valve (104) on material pipe (103).
3. A crude fatty acid refining split stream device according to any one of claims 1-2, characterized in that: the top of the screen cylinder (102) is provided with a feeding port (108), and the feeding port (108) penetrates through the side wall of the shell (101).
4. A crude fatty acid refining split stream device according to any one of claims 1-2, characterized in that: a spiral coil (203) is arranged at the top of the condensing box (2), and a plurality of shower heads (204) are uniformly distributed on the spiral coil (203); the side of the condensing box (2) is provided with a plurality of nozzles (205), the bottom of the condensing box (2) is provided with a circulating pump (206), and the circulating pump (206) is communicated with the spiral coil (203) and the nozzles (205) through a circulating pipe (207).
5. A crude fatty acid refining split stream device according to any one of claims 1-2, characterized in that: the sieve barrels (102) are uniformly provided with sieve holes, and the arched branch pipes (201) are uniformly distributed in the vertical direction.
6. A crude fatty acid refining split stream device according to any one of claims 1-2, characterized in that: the bottom of the condensing box (2) is provided with a water outlet, and the top of the condensing box (2) is provided with a water adding tank.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202322492803.0U CN220834159U (en) | 2023-09-14 | 2023-09-14 | Crude fatty acid refining and diverting device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202322492803.0U CN220834159U (en) | 2023-09-14 | 2023-09-14 | Crude fatty acid refining and diverting device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN220834159U true CN220834159U (en) | 2024-04-26 |
Family
ID=90742383
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202322492803.0U Active CN220834159U (en) | 2023-09-14 | 2023-09-14 | Crude fatty acid refining and diverting device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN220834159U (en) |
-
2023
- 2023-09-14 CN CN202322492803.0U patent/CN220834159U/en active Active
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| Date | Code | Title | Description |
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| GR01 | Patent grant | ||
| GR01 | Patent grant |