CN218435030U - Oil boiling device - Google Patents
Oil boiling device Download PDFInfo
- Publication number
- CN218435030U CN218435030U CN202222074795.3U CN202222074795U CN218435030U CN 218435030 U CN218435030 U CN 218435030U CN 202222074795 U CN202222074795 U CN 202222074795U CN 218435030 U CN218435030 U CN 218435030U
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- CN
- China
- Prior art keywords
- oil
- pipe
- tank
- storage tank
- temporary storage
- Prior art date
- 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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- 238000009835 boiling Methods 0.000 title claims description 10
- 238000003860 storage Methods 0.000 claims abstract description 55
- 238000010438 heat treatment Methods 0.000 claims abstract description 18
- 238000003756 stirring Methods 0.000 claims description 18
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 13
- 238000007790 scraping Methods 0.000 claims description 9
- 230000009467 reduction Effects 0.000 claims description 6
- 238000005086 pumping Methods 0.000 claims description 4
- 239000000126 substance Substances 0.000 claims description 4
- 238000004519 manufacturing process Methods 0.000 abstract description 11
- 239000010865 sewage Substances 0.000 abstract description 11
- 108010010803 Gelatin Proteins 0.000 abstract description 10
- 239000008273 gelatin Substances 0.000 abstract description 10
- 229920000159 gelatin Polymers 0.000 abstract description 10
- 235000019322 gelatine Nutrition 0.000 abstract description 10
- 235000011852 gelatine desserts Nutrition 0.000 abstract description 10
- 239000002351 wastewater Substances 0.000 abstract description 9
- 239000004519 grease Substances 0.000 abstract description 7
- 238000011084 recovery Methods 0.000 abstract description 4
- 230000002349 favourable effect Effects 0.000 abstract description 3
- 239000007788 liquid Substances 0.000 description 5
- 239000006185 dispersion Substances 0.000 description 4
- 239000003925 fat Substances 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 239000000843 powder Substances 0.000 description 3
- 230000008569 process Effects 0.000 description 3
- 239000002994 raw material Substances 0.000 description 3
- 238000007710 freezing Methods 0.000 description 2
- 230000008014 freezing Effects 0.000 description 2
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
- 230000002378 acidificating effect Effects 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 239000000853 adhesive Substances 0.000 description 1
- 230000001070 adhesive effect Effects 0.000 description 1
- 230000004075 alteration Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000006229 carbon black Substances 0.000 description 1
- 239000011362 coarse particle Substances 0.000 description 1
- 239000003431 cross linking reagent Substances 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000007667 floating Methods 0.000 description 1
- 239000000499 gel Substances 0.000 description 1
- 239000003292 glue Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 230000007935 neutral effect Effects 0.000 description 1
- 108090000623 proteins and genes Proteins 0.000 description 1
- 102000004169 proteins and genes Human genes 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 229920002545 silicone oil Polymers 0.000 description 1
- 239000002002 slurry Substances 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- QAOWNCQODCNURD-UHFFFAOYSA-N sulfuric acid Substances OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 1
- 238000004065 wastewater treatment Methods 0.000 description 1
Images
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- Mixers Of The Rotary Stirring Type (AREA)
Abstract
The utility model discloses an oil decocting device, include: spiral delivery mechanism, spiral delivery mechanism's feed inlet and sump pit intercommunication, and spiral delivery mechanism's discharge gate is installed directly over the hopper, and the screw pump is installed on the right side of hopper simultaneously to the hopper passes through the screw pump, the conveyer pipe sets up with oil decocting jar intercommunication, and oil storage temporary storage tank is installed on oil decocting jar's right side, and oil storage temporary storage tank inside fixed mounting has heating coil, and oil storage temporary storage tank sets up through oil pumper and conveyer pipe and oil storage tank intercommunication simultaneously. This oil decocting device realizes carrying out recovery processing work again in the waste water to the production process production of gelatin, and the grease in the waste water can draw the back and sell, improves the economic benefits of gelatin production line, reduces the treatment pressure of sewage treatment system to gelatin sewage simultaneously, is favorable to subsequent sewage treatment work.
Description
Technical Field
The utility model relates to a chemical industry equipment field specifically is an oil decocting device.
Background
The patent with the publication number of CN202462833U discloses a production line of neutral and acidic transparent adhesive through retrieval, wherein the production line comprises a first screw machine, a second screw machine, a transfer tank, a mixing dispersion machine, a side feeding machine and a cooler, the first screw machine is provided with an inlet for adding 107 glue, a cross-linking agent, white oil and silicone oil, an outlet of the first screw machine is connected with the transfer tank, the transfer tank is connected with the mixing dispersion machine, the mixing dispersion machine is connected with the side feeding machine, the side feeding machine is connected with the cooler, the cooler is connected with the second screw machine, the mixing dispersion machine is connected with a powder conveying device, and the powder conveying device conveys white carbon black powder; "
During the production of gelatin or the pretreatment of raw materials for oil products, gels, animal fats and large amounts of waste water are formed; the water is rich in protein and fat, and before the wastewater is treated, if the grease in the water can be extracted, the subsequent wastewater treatment is facilitated, and meanwhile, a lot of economic values can be generated; the present case is produced based on this.
SUMMERY OF THE UTILITY MODEL
An object of the utility model is to provide an oil decocting device to solve the defect mentioned in the above-mentioned background art.
In order to realize the above-mentioned purpose, provide an oil decocting device, include:
screw conveyer, screw conveyer's feed inlet and sump pit intercommunication, and screw conveyer's discharge gate is installed directly over the hopper, and the screw pump is installed on the right side of hopper simultaneously to the hopper passes through screw pump, conveyer pipe and the setting of oil decocting jar intercommunication, and the oil storage tank of keeping in is installed on the right side of oil decocting jar, and oil storage tank fixed mounting has heating coil, and oil storage tank of keeping in simultaneously sets up through oil pumper and conveyer pipe and oil storage tank intercommunication.
Preferably, the oil decocting tank comprises a tank body, an oil scraping plate, a feeding pipe, a speed reducing motor, a stirring device and an overflow pipe, wherein the speed reducing motor is installed at the top of the tank body through a base, an output shaft of the speed reducing motor is fixedly connected with the stirring device, a heat exchange jacket is installed on the outer side of the tank body, and the heat exchange jacket is communicated with an external steam pipe.
Preferably, five groups of feed pipes are respectively installed at the top of the tank body, and the tank body is respectively communicated with an external hot water pipe, an output pipe of a screw pump, an oil residue pipe and a chemical product pipe through the four groups of feed pipes.
Preferably, the overflow pipe is installed to the upper right side of the jar body, and the overflow pipe passes through the pipeline and keeps in the oil inlet intercommunication of jar, and the overflow pipe highly is greater than the height that the jar was kept in to the oil storage.
Preferably, the stirring device is driven by a speed reduction motor, a stirring shaft on the stirring device is welded and fixed with the oil scraping plate, and the end part of the oil scraping plate is in contact with the inner wall of the tank body.
Preferably, the oil storage temporary storage tank comprises a horizontal tank, a heating coil, a steam outlet pipe and a steam inlet pipe, one end of the heating coil is fixedly connected with the steam outlet pipe, the other end of the heating coil is fixedly connected with the steam inlet pipe, and the steam inlet pipe is communicated with an external steam pipe.
Compared with the prior art, the beneficial effects of the utility model are that: a heating coil is arranged in the oil storage temporary storage tank to prevent oil in the tank from freezing in winter, the oil storage temporary storage tank conveys the oil into the oil storage tank through an oil pumping pump, and the oil is sold; can realize carrying out recovery processing work again in the waste water to the production process production of gelatin, the grease in the waste water can be drawed the back and sell, improves the economic benefits of gelatin production line, reduces the treatment pressure of sewage treatment system to gelatin sewage simultaneously, is favorable to subsequent sewage treatment work.
Drawings
FIG. 1 is a schematic view of the technological process of the oil boiling device of the structure of the utility model;
FIG. 2 is a schematic view of the oil boiling tank of the present invention;
FIG. 3 is a schematic view of the oil storage temporary storage tank of the present invention;
fig. 4 is a sectional view of the oil storage temporary storage tank of the structure of the present invention.
Reference numbers in the figures: 1. a screw conveyor; 2. a hopper; 3. a screw pump; 4. an oil boiling tank; 41. a tank body; 42. a scraper plate; 43. a feed tube; 44. a reduction motor; 45. a stirring device; 46. an overflow pipe; 5. an oil storage temporary storage tank; 51. a horizontal tank; 52. a heating coil; 53. a vapor outlet pipe; 54. a steam inlet pipe; 6. pumping an oil pump; 7. an oil storage tank.
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 work belong to the protection scope of the present invention.
Referring to fig. 1-4, the present invention provides an oil boiling device, comprising: a screw conveyor 1;
feed inlet and sump pit intercommunication of screw conveyor 1, and screw conveyor 1's discharge gate is installed directly over hopper 2, while screw pump 3 is installed on hopper 2's right side, and hopper 2 is through screw pump 3, conveyer pipe and the setting of oil decocting jar 4 intercommunication, oil storage tank 5 of keeping in is installed on oil decocting jar 4's right side, and the inside fixed mounting of oil storage tank 5 of keeping in has heating coil 52, oil storage tank 5 of keeping in simultaneously sets up through oil pumper 6 and conveyer pipe and oil storage tank 7 intercommunication.
The process comprises the following steps:
1. all the wastewater directly enters a water collecting well through a sewage pipe, and coarse particles and animal raw materials are removed through a coarse-fine grid, so that equipment damage and biological slurry accumulation are prevented; transferring the materials in the water collecting well to the interior of a hopper 2 through a spiral conveying device 1;
2. when the oil decocting tank 4 has a feeding condition, turning on a switch of the screw pump 3, transferring skin, residue, floating oil and the like in sewage in the hopper 2 into the oil decocting tank 4, starting the speed reducing motor 44, raising the temperature in the oil decocting tank 4 to 92-96 ℃ through the jacket, and preserving the heat for 1-2 hours so as to better boil out oil and fat and facilitate residue-water separation;
3. before the steam is opened, quantitative concentrated sulfuric acid needs to be added into the oil boiling tank 4 to prevent the oil from being saponified in the oil boiling process;
4. standing for a period of time, after the grease and water in the oil boiling tank 4 are layered, opening a valve on a hot water recovery pipeline, adding hot water into the tank, and paying attention to the arrangement of a water adding port at the bottom of the tank, so that the grease slowly floats upwards and flows into the temporary oil storage tank 5 through an overflow pipe 46 on the wall of the tank;
5. a heating coil 52 is arranged in the oil storage temporary storage tank 5 to prevent oil in the tank from freezing in winter, and the oil storage temporary storage tank 5 conveys the oil into the oil storage tank 7 through an oil pumping pump 6;
6. the oil is sold for the outside.
Can realize carrying out recovery processing work again at the waste water that the production process to gelatin produced, oil in the waste water can draw the back and sell, improves the economic benefits of gelatin production line, reduces the treatment pressure of sewage treatment system to gelatin sewage simultaneously, is favorable to subsequent sewage treatment work.
As a preferred embodiment, the oil decocting tank 4 includes a tank 41, an oil scraping plate 42, a feeding pipe 43, a speed reducing motor 44, a stirring device 45 and an overflow pipe 46, the speed reducing motor 44 is installed on the top of the tank 41 through a base, an output shaft of the speed reducing motor 44 is fixedly connected with the stirring device 45, a heat exchange jacket is installed on the outer side of the tank 41, and the heat exchange jacket is communicated with an external steam pipe.
As shown in fig. 1-2: the heat exchange jacket is arranged on the outer side of the tank body 41 and communicated with an external steam pipe, so that high-temperature steam is introduced into the heat exchange jacket, and the tank body 41 is heated.
As a preferred embodiment, five sets of feed pipes 43 are respectively installed on the top of the tank 41, and the tank 41 is respectively communicated with the external hot water pipe, the output pipe of the screw pump 3, the oil residue pipe and the chemical pipe through the four sets of feed pipes 43.
As shown in fig. 2: the top of the tank 41 is respectively provided with five groups of feed pipes 43 which can be used for adding different additives and raw materials.
As a preferred embodiment, an overflow pipe 46 is installed at the upper right side of the tank 41, and the overflow pipe 46 is communicated with the oil inlet of the oil storage temporary storage tank 5 through a pipeline, and the height of the overflow pipe 46 is greater than that of the oil storage temporary storage tank 5.
As shown in fig. 1: along with this, the liquid level of the material in the tank body 41 is higher and higher, and because the density of the water body is different from that of the oil liquid, the oil liquid floats upwards, and when the liquid level of the oil liquid exceeds the inside of the overflow pipe 46, the oil layer is injected into the inside of the overflow pipe 46 along with the overflow pipe 46.
In a preferred embodiment, the stirring device 45 is driven by the speed reduction motor 44, and the stirring shaft of the stirring device 45 is welded and fixed to the oil scraper 42, and the end of the oil scraper 42 is in contact with the inner wall of the tank 41.
When the gear motor 44 drives the stirring device 45 to stir and mix different materials, the oil scraping plate 42 can be driven to move, so that the oil scraping plate 42 can scrape off oil stains attached to the inner wall of the tank body 41.
In a preferred embodiment, the oil storage temporary storage tank 5 comprises a horizontal tank 51, a heating coil 52, a steam outlet pipe 53 and a steam inlet pipe 54, wherein one end of the heating coil 52 is fixedly connected with the steam outlet pipe 53, the other end of the heating coil 52 is fixedly connected with the steam inlet pipe 54, and a steam pipe externally connected with the steam inlet pipe 54 is arranged in a communicating manner.
As shown in fig. 3-4: in winter: the high-temperature steam enters the heating coil 52 from the steam inlet 54, and the grease inside the horizontal tank 51 is heated by the heating coil 52, so that the grease is prevented from being frozen.
Although embodiments of the present invention have been shown and described, it will be appreciated by those skilled in the art that various changes, modifications, substitutions and alterations can be made in these embodiments without departing from the principles and spirit of the invention, the scope of which is defined in the appended claims and their equivalents.
Claims (6)
1. An oil decocting device, comprising: screw conveyer (1), a serial communication port, the feed inlet and the sump pit intercommunication of screw conveyer (1), and the discharge gate of screw conveyer (1) is installed directly over hopper (2), while screw pump (3) are installed on the right side of hopper (2), and hopper (2) are through screw pump (3), the conveyer pipe sets up with oil decocting tank (4) intercommunication, oil storage temporary storage tank (5) are installed on the right side of oil decocting tank (4), and oil storage temporary storage tank (5) inside fixed mounting has heating coil (52), oil storage temporary storage tank (5) set up through oil-pumping pump (6) and conveyer pipe and oil storage tank (7) intercommunication simultaneously.
2. The oil decocting device of claim 1, wherein: the oil boiling tank (4) comprises a tank body (41), an oil scraping plate (42), a feeding pipe (43), a speed reduction motor (44), a stirring device (45) and an overflow pipe (46), wherein the speed reduction motor (44) is installed at the top of the tank body (41) through a base, an output shaft of the speed reduction motor (44) is fixedly connected with the stirring device (45), a heat exchange jacket is installed on the outer side of the tank body (41), and the heat exchange jacket is communicated with an external steam pipe.
3. The oil decocting device of claim 2, wherein: five groups of feed pipes (43) are respectively installed at the top of the tank body (41), and the tank body (41) is respectively communicated with an external hot water pipe, an output pipe of the screw pump (3), an oil residue pipe and a chemical pipe through the four groups of feed pipes (43).
4. The oil decocting device of claim 2, wherein: an overflow pipe (46) is installed on the upper right side of the tank body (41), the overflow pipe (46) is communicated with an oil inlet of the oil storage temporary storage tank (5) through a pipeline, and the height of the overflow pipe (46) is larger than that of the oil storage temporary storage tank (5).
5. The oil decocting device of claim 2, wherein: the stirring device (45) is driven by a speed reducing motor (44), a stirring shaft on the stirring device (45) is welded and fixed with the oil scraping plate (42), and meanwhile, the end part of the oil scraping plate (42) is arranged in contact with the inner wall of the tank body (41).
6. The oil decocting device of claim 1, wherein: oil storage temporary storage tank (5) advances pipe (54) including horizontal tank (51), heating coil (52), steam exit tube (53) and steam, and the one end and the steam exit tube (53) fixed connection of heating coil (52), and the other end and the steam of heating coil (52) advance pipe (54) fixed connection simultaneously to steam advances the external steam pipe intercommunication setting of pipe (54).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202222074795.3U CN218435030U (en) | 2022-08-08 | 2022-08-08 | Oil boiling device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202222074795.3U CN218435030U (en) | 2022-08-08 | 2022-08-08 | Oil boiling device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN218435030U true CN218435030U (en) | 2023-02-03 |
Family
ID=85093030
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202222074795.3U Active CN218435030U (en) | 2022-08-08 | 2022-08-08 | Oil boiling device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN218435030U (en) |
-
2022
- 2022-08-08 CN CN202222074795.3U patent/CN218435030U/en active Active
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20240304 Address after: 355100 no.1-10, Wenpu Road, Yacheng Town, Xiapu County, Ningde City, Fujian Province Patentee after: Fujian Funingpu Biotechnology Co.,Ltd. Country or region after: China Address before: 355100 no.1-10, Wenpu Road, Yacheng Town, Xiapu County, Ningde City, Fujian Province Patentee before: Fujian funingpu gelatin Co.,Ltd. Country or region before: China |