CN217324003U - Illegal cooking oil-catalyst mixing and dispersing device - Google Patents
Illegal cooking oil-catalyst mixing and dispersing device Download PDFInfo
- Publication number
- CN217324003U CN217324003U CN202220092312.XU CN202220092312U CN217324003U CN 217324003 U CN217324003 U CN 217324003U CN 202220092312 U CN202220092312 U CN 202220092312U CN 217324003 U CN217324003 U CN 217324003U
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- China
- Prior art keywords
- catalyst
- cooking oil
- illegal cooking
- oil
- mixing
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- 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.)
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- 239000003054 catalyst Substances 0.000 title claims abstract description 109
- 238000010411 cooking Methods 0.000 title claims abstract description 16
- 239000008162 cooking oil Substances 0.000 claims abstract description 76
- 239000003921 oil Substances 0.000 claims abstract description 52
- 238000004090 dissolution Methods 0.000 claims abstract description 14
- 238000006243 chemical reaction Methods 0.000 claims description 22
- 238000003756 stirring Methods 0.000 claims description 22
- 239000007788 liquid Substances 0.000 claims description 17
- 230000005540 biological transmission Effects 0.000 claims description 3
- 239000006185 dispersion Substances 0.000 abstract description 4
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 9
- 239000002699 waste material Substances 0.000 description 8
- 101100408455 Arabidopsis thaliana PLC7 gene Proteins 0.000 description 2
- 239000002253 acid Substances 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 206010028980 Neoplasm Diseases 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000003225 biodiesel Substances 0.000 description 1
- 201000011510 cancer Diseases 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 235000014113 dietary fatty acids Nutrition 0.000 description 1
- 239000008157 edible vegetable oil Substances 0.000 description 1
- 229930195729 fatty acid Natural products 0.000 description 1
- 239000000194 fatty acid Substances 0.000 description 1
- 150000004665 fatty acids Chemical class 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000005086 pumping Methods 0.000 description 1
- 150000004671 saturated fatty acids Chemical class 0.000 description 1
- 235000003441 saturated fatty acids Nutrition 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 150000004670 unsaturated fatty acids Chemical class 0.000 description 1
- 235000021122 unsaturated fatty acids Nutrition 0.000 description 1
Images
Classifications
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- 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
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/10—Biofuels, e.g. bio-diesel
Abstract
The utility model relates to a trench oil-catalyst mixing dispersion devices, including catalyst dissolution reation kettle, trench oil input tube, flowmeter, catalyst adder and first PLC, catalyst dissolution reation kettle has the hybrid chamber that is used for mixing trench oil and catalyst, trench oil input tube intercommunication hybrid chamber, and the flowmeter sets up on the trench oil input tube, and catalyst adder intercommunication hybrid chamber, a PLC connect flowmeter and catalyst adder for control catalyst adder adds the catalyst according to the flow of trench oil. Compared with the prior art, the illegal cooking oil-catalyst mixing and dispersing device can control the addition amount of the catalyst according to the input flow of the illegal cooking oil, so that the illegal cooking oil and the catalyst are synchronously added into the mixing cavity according to a preset proportion, the illegal cooking oil and the catalyst are premixed when being added, the difficulty of mixing and dispersing is greatly reduced, and the catalyst is more uniformly distributed in the illegal cooking oil.
Description
Technical Field
The utility model relates to a trench oil treatment facility technical field especially relates to a trench oil-catalyst mixing dispersion devices.
Background
The illegal cooking oil, known as waste oil, generally refers to various inferior oils existing in life, such as recovered edible oil, repeatedly used frying oil, etc., and mainly contains fatty acids (including saturated fatty acids and unsaturated fatty acids). The largest source of the illegal cooking oil is an oil separation tank of a sewer of a large-scale urban restaurant. Cancer may be caused by long-term eating, and the harm to human body is great.
At present, the illegal cooking oil is generally esterified by using methanol, and the illegal cooking oil is converted into biodiesel with the help of a catalyst, so that the waste is changed into valuable. The illegal cooking oil needs to be mixed with the catalyst in advance before reacting with the methanol, and due to the fact that the viscosity of the illegal cooking oil is high, the phenomenon of uneven mixing is easy to occur in common stirring and mixing, the content of the local catalyst is too low, the part of illegal cooking oil is difficult to react with the methanol, and the conversion rate of the illegal cooking oil is reduced.
SUMMERY OF THE UTILITY MODEL
In view of the above, there is a need to provide a drainage oil-catalyst mixing and dispersing device, which is used to solve the technical problem in the prior art that the catalyst is not easily dispersed in the drainage oil uniformly.
The utility model provides a mixed dispersion devices of trench oil-catalyst, this mixed dispersion devices of trench oil-catalyst includes: catalyst dissolves reation kettle, the trench oil input tube, the flowmeter, catalyst adder and first PLC, catalyst dissolves reation kettle has the hybrid chamber that is used for mixing trench oil and catalyst, trench oil input tube intercommunication hybrid chamber supplies in to mixing intracavity input trench oil, the flowmeter sets up and supplies in the flow that detects trench oil on the trench oil input tube, catalyst adder intercommunication hybrid chamber supplies in adding the catalyst to the hybrid chamber, flowmeter and catalyst adder are connected to first PLC, supply to control catalyst adder and add the catalyst according to the flow of trench oil.
Further, still including setting up the trench oil input pump on the trench oil input pipe, first PLC still is connected with the trench oil input pump for the flow of the trench oil in the control trench oil input pipe.
Furthermore, still include the swill-cooked dirty oil holding vessel that is used for storing the swill-cooked dirty oil, the one end intercommunication swill-cooked dirty oil holding vessel that the mixing chamber was kept away from to the swill-cooked dirty oil input tube.
Furthermore, the device also comprises a drainage oil output pipe communicated with the mixing cavity, and the drainage oil output pipe is used for guiding out the drainage oil mixed with the catalyst in the mixing cavity.
Furthermore, still including setting up the swill-cooked dirty oil delivery pump on the swill-cooked dirty oil output tube, the swill-cooked dirty oil delivery pump supplies to drive the swill-cooked dirty oil that mixes the catalyst in the swill-cooked dirty oil output tube and flows.
Furthermore, the device also comprises a liquid level detector arranged on the catalyst dissolution reaction kettle, and the liquid level detector is used for detecting the liquid level of the oil in the mixing cavity.
Further, still including the second PLC of connecting liquid level detector and trench oil delivery pump, the second PLC supplies to control the power of trench oil delivery pump according to the liquid level of fluid in the hybrid chamber.
Furthermore, the catalyst dissolution reaction kettle is provided with a stirring mechanism for stirring and mixing the catalyst and the illegal cooking oil.
Furthermore, the stirring mechanism comprises a stirring part and a power part, wherein the part of the stirring part is arranged in the mixing cavity, the power part is in transmission connection with the stirring part, and the power part is used for driving the stirring part to rotate.
Further, the catalyst adder is a spiral metering scale.
Compared with the prior art, the illegal cooking oil-catalyst mixing and dispersing device can control the addition amount of the catalyst according to the input flow of the illegal cooking oil, so that the illegal cooking oil and the catalyst are synchronously added into the mixing cavity according to a preset proportion, the illegal cooking oil and the catalyst are premixed when being added, the difficulty of mixing and dispersing is greatly reduced, and the catalyst is more uniformly distributed in the illegal cooking oil.
The foregoing description is only an overview of the technical solutions of the present invention, and in order to make the technical means of the present invention more clearly understood, and to implement the technical means according to the content of the description, the preferred embodiments of the present invention are described in detail below with reference to the accompanying drawings. The following examples and the accompanying drawings illustrate specific embodiments of the present invention.
Drawings
The accompanying drawings, which are included to provide a further understanding of the invention and are incorporated in and constitute a part of this application, illustrate embodiment(s) of the invention and together with the description serve to explain the invention without undue limitation to the invention. In the drawings:
fig. 1 is a schematic structural diagram of the illegal cooking oil-catalyst mixing and dispersing device provided by the present invention.
Detailed Description
The following detailed description of the preferred embodiments of the invention, which is to be read in connection with the accompanying drawings, forms a part of this application, and together with the embodiments of the invention, serve to explain the principles of the invention and not to limit its scope.
Referring to fig. 1, the local waste oil-catalyst mixing and dispersing device includes a waste oil storage tank 1, a waste oil input pipe 2, a catalyst dissolving reaction kettle 3, a waste oil input pump 4, a flow meter 5, a catalyst adder 6, a first PLC7, a waste oil output pipe 8, a waste oil output pump 9, a liquid level detector 10, and a second PLC 11.
The illegal cooking oil storage tank 1 is a device for temporarily storing the collected illegal cooking oil, the illegal cooking oil storage tank 1 is communicated with the catalyst dissolution reaction kettle 3 through an illegal cooking oil input pipe 2, and in other embodiments of the present application, an acid value detector may be disposed on the illegal cooking oil input pipe 2 to detect the acid value of the illegal cooking oil.
A mixing cavity is formed inside the catalyst dissolving reaction kettle 3 and used for mixing and dispersing the illegal cooking oil and the catalyst. In this embodiment, the illegal cooking oil input pipe 2 is communicated with the top of the mixing chamber, and the catalyst dissolution reaction kettle 3 further has a stirring mechanism 31, and the stirring mechanism 31 is used for stirring the catalyst and the illegal cooking oil to uniformly mix and disperse the catalyst and the illegal cooking oil. The stirring mechanism 31 includes a stirring portion 311 partially disposed in the mixing chamber, and a power portion 312 in transmission connection with the stirring portion 311, wherein the power portion 312 is generally disposed outside the mixing chamber and is used for driving the stirring portion 311 to rotate. The power portion 312 is usually a motor of a suitable type, and other structures may be adopted to realize the stirring function in other embodiments. The catalyst dissolving reaction kettle 3 also has a heating function, and the temperature in the reaction kettle is controlled by a heating module such as an electric heater and a temperature control module, so that the catalyst and the illegal cooking oil are mixed and dissolved at a proper temperature.
The illegal cooking oil input pipe 2 is provided with an illegal cooking oil input pump 4 which is used for pumping the illegal cooking oil in the illegal cooking oil storage tank 1 into the catalyst dissolution reaction kettle 3. The illegal cooking oil input pipe 2 is also provided with a flowmeter 5 for detecting the flow of illegal cooking oil in the illegal cooking oil input pipe 2.
The catalyst adder 6 is in communication with the mixing chamber for precise control of the amount of catalyst added. In this embodiment, the catalyst feeder 6 may be a screw weigher. A first PLC (Programmable Logic Controller) 7 is connected to the flow meter 5 and the catalyst adder 6, so as to realize the linked automatic control of the flow rate of the illegal cooking oil and the input amount of the catalyst, so as to ensure that the input amount of the catalyst matches the input amount of the illegal cooking oil, so that the catalyst and the illegal cooking oil are originally mixed and added according to a predetermined ratio, and then are stirred by the stirring mechanism 31 to be more easily and uniformly dispersed.
In other embodiments of the present application, the first PLC7 may also be connected to the illegal cooking oil inlet pump 4, so that the illegal cooking oil inlet flow rate and the catalyst addition amount are controlled in a linkage manner, and the illegal cooking oil inlet flow rate is actively adjusted to be better matched with the catalyst.
The catalyst dissolving reaction kettle 3 is also communicated with a illegal cooking oil output pipe 8, and is communicated with subsequent treatment equipment through the illegal cooking oil output pipe 8, and the illegal cooking oil mixed with the catalyst is conveyed to the subsequent treatment equipment. The illegal cooking oil output pipe 8 is provided with an illegal cooking oil output pump 9, and the illegal cooking oil output pump 9 drives the illegal cooking head mixed with the catalyst in the illegal cooking oil output pipe 8 to flow to the subsequent treatment equipment.
In other embodiments of the present application, a liquid level detector 10 may be further disposed on the catalyst dissolution reaction kettle 3, and the liquid level detector 10 is configured to detect a liquid level of the oil in the mixing chamber. Then, the second PLC11 is used for connecting the liquid level detector 10 and the illegal cooking oil output pump 9, so that the output quantity of the illegal cooking oil containing the catalyst and the storage quantity of the illegal cooking oil containing the catalyst in the catalyst dissolving reaction kettle 3 are automatically controlled in a linkage manner, and the illegal cooking oil containing the catalyst in the catalyst dissolving reaction kettle 3 is ensured to be maintained within a reasonable range.
Namely, when the liquid level in the catalyst dissolution reaction kettle 3 reaches the upper limit threshold, the working power of the illegal cooking oil output pump 9 is increased, the output flow of the illegal cooking oil containing the catalyst is increased, and the storage capacity of the illegal cooking oil containing the catalyst in the catalyst dissolution reaction kettle 3 is reduced. When the liquid level in the catalyst dissolution reaction kettle 3 reaches the lower limit threshold, the working power of the illegal cooking oil output pump 9 is reduced, the output flow of the illegal cooking oil containing the catalyst is reduced, and the storage capacity of the illegal cooking oil containing the catalyst in the catalyst dissolution reaction kettle 3 is increased.
Implement the embodiment of the utility model provides a, following beneficial effect has: the illegal cooking oil-catalyst mixing and dispersing device can control the addition amount of the catalyst according to the input flow of the illegal cooking oil, so that the illegal cooking oil and the catalyst are synchronously added into the mixing cavity according to a preset proportion, the illegal cooking oil and the catalyst are premixed when being added, the difficulty of mixing and dispersing is greatly reduced, and the catalyst is more uniformly distributed in the illegal cooking oil.
The above description is only for the preferred embodiment of the present invention, but the 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 by the present invention.
Claims (10)
1. A gutter oil-catalyst mixing and dispersing device is characterized by comprising: the device comprises a catalyst dissolving reaction kettle, a trench oil input pipe, a flow meter, a catalyst adder and a first PLC, wherein the catalyst dissolving reaction kettle is provided with a mixing cavity, the trench oil input pipe is communicated with the mixing cavity and is used for inputting trench oil into the mixing cavity, the flow meter is arranged on the trench oil input pipe and is used for detecting the flow of the trench oil, the catalyst adder is communicated with the mixing cavity and is used for adding a catalyst into the mixing cavity, and the first PLC is connected with the flow meter and the catalyst adder and is used for controlling the catalyst adder to add the catalyst according to the flow of the trench oil.
2. The illegal cooking oil-catalyst mixing and dispersing device according to claim 1, further comprising an illegal cooking oil input pump disposed on the illegal cooking oil input pipe, wherein the first PLC is further connected to the illegal cooking oil input pump for controlling a flow rate of illegal cooking oil in the illegal cooking oil input pipe.
3. The illegal cooking oil-catalyst mixing and dispersing device of claim 2, further comprising an illegal cooking oil storage tank for storing illegal cooking oil, wherein one end of the illegal cooking oil input pipe, which is far away from the mixing cavity, is communicated with the illegal cooking oil storage tank.
4. The illegal cooking oil-catalyst mixing and dispersing device of claim 1, further comprising an illegal cooking oil output pipe communicating with the mixing chamber.
5. The illegal cooking oil-catalyst mixing and dispersing device of claim 4, further comprising an illegal cooking oil output pump disposed on the illegal cooking oil output pipe.
6. The illegal cooking oil-catalyst mixing and dispersing device according to claim 5, further comprising a liquid level detector disposed in the catalyst dissolution reaction kettle, wherein the liquid level detector is used for detecting the liquid level of the oil in the mixing cavity.
7. The illegal cooking oil-catalyst mixing and dispersing device according to claim 6, further comprising a second PLC connected to the liquid level detector and the illegal cooking oil output pump, wherein the second PLC is configured to control power of the illegal cooking oil output pump according to the liquid level of the oil in the mixing chamber.
8. The illegal cooking oil-catalyst mixing and dispersing device according to claim 1, wherein the catalyst dissolution reaction kettle is provided with a stirring mechanism.
9. The illegal cooking oil-catalyst mixing and dispersing device according to claim 8, wherein the stirring mechanism comprises a stirring part partially disposed in the mixing chamber and a power part in transmission connection with the stirring part, and the power part is used for driving the stirring part to rotate.
10. The illegal cooking oil-catalyst mixing and dispersing device of claim 1, wherein the catalyst adder is a screw scale.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202220092312.XU CN217324003U (en) | 2022-01-14 | 2022-01-14 | Illegal cooking oil-catalyst mixing and dispersing device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202220092312.XU CN217324003U (en) | 2022-01-14 | 2022-01-14 | Illegal cooking oil-catalyst mixing and dispersing device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN217324003U true CN217324003U (en) | 2022-08-30 |
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ID=82993147
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202220092312.XU Active CN217324003U (en) | 2022-01-14 | 2022-01-14 | Illegal cooking oil-catalyst mixing and dispersing device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN217324003U (en) |
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2022
- 2022-01-14 CN CN202220092312.XU patent/CN217324003U/en active Active
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CP03 | Change of name, title or address | ||
| CP03 | Change of name, title or address |
Address after: 431600 Kaifa 2nd Road, Hanchuan economic and Technological Development Zone, Xiaogan City, Hubei Province Patentee after: Hubei Tianji Bioenergy Co.,Ltd. Country or region after: China Address before: 431600 Kaifa 2nd Road, Hanchuan economic and Technological Development Zone, Xiaogan City, Hubei Province Patentee before: HUBEI TIANJI NEW ENERGY LIMITED BY SHARE LTD. Country or region before: China |