CN205443223U - Refining equipment - Google Patents
Refining equipment Download PDFInfo
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- CN205443223U CN205443223U CN201620180771.8U CN201620180771U CN205443223U CN 205443223 U CN205443223 U CN 205443223U CN 201620180771 U CN201620180771 U CN 201620180771U CN 205443223 U CN205443223 U CN 205443223U
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- tank body
- fining
- deodorize
- deacidification
- pots
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Abstract
The utility model provides a refining equipment, including a fining pot that connects gradually the setting, no. Two fining pots, no. Three decoloration jars and no. Four deodorizing tanks, no. One the fining pot is water washing tank for wash the processing, and get rid of colloid phosphatide and impurity in the oil, no. Two the fining pot is the deacidification jar for remove the aliphatic acid in deoiling: no. Three fining pots are vacuum decoloration jar for eliminate the pigment in the oil: no. Four the fining pot is the deodorizing tank for remove the various pollution tastes in deoiling, the utility model discloses can avoid exhaust emission, again can the accurate control oil refining process, improve oil refining efficiency.
Description
Technical field
This utility model belongs to edible oil Technology in Pressing field, particularly to a kind of refining equipment.
Background technology
Current China table oil industry, required heat energy is all by coal-fired heating, conduction oil heats edible oil by circulating pump circulating heat conduction oil and completes each operation of refined oil, reach food and standard is installed, region boiler heating is allowed to carry out table oil in country, it is also necessary to the emission abatement device that configuration cost is high, some region (such as drinking water source place), national environmental protection department is not allow for the existence of boiler enterprise, thus constrains the development of manufacturing enterprise；Further, owing to utilizing boiler fired coal equipment, whole oil refining process is all difficult to control to, and has both wasted manpower and materials, under efficiency is the most at a fairly low.
Therefore, need now a kind of refining equipment badly, be not only able to avoid waste gas to discharge, can accurately control again oil refining process, improve oil refining efficiency.
Utility model content
The utility model proposes a kind of refining equipment, solve oil refining process in prior art and be all difficult to control to, waste manpower and materials, simultaneously the problem of inefficiency.
The technical solution of the utility model is achieved in that refining equipment, is sequentially connected with a fining pot of setting, No. two fining pots, No. three bleachers and No. four deodorizing tanks including by petroleum pipeline；
A number fining pot is water washing tank, is used for carrying out washing process, and removes the colloid phospholipid in oil removing and impurity；
No. two fining pots are deacidification tank, for removing the fatty acid in oil；
No. three fining pots are vacuum decoloration tank, for sloughing the pigment in oil；
No. four fining pots are vacuum deodorization tank, for removing the various pollution tastes in oil.
As one preferred embodiment, a number fining pot includes a washing tank body, being provided with washing charge door on washing tank body, be provided with some washing electrothermal tubes in water washing tank body, washing tank body top is provided with the washing blender stretching into washing tank body, washing electrothermal tube connects the automatically controlled electroplax of washing, wherein oil temperature controls to be 70 degree of-80 degree, washes water temperature 100 degree, stands 8-10 hour after mixing time 30-50 minute, then release colloid and impurity, washing tank body is provided with a valve.
As one preferred embodiment, No. two fining pots include a deacidification tank body, deacidification tank body is provided with deacidification charge door, is provided with some deacidification electrothermal tubes in deacidification tank body, and deacidification tank body top is provided with the deacidification blender stretching into deacidification tank body, deacidification electrothermal tube connects the automatically controlled electroplax of deacidification, wherein 70 degree of-80 degree of oil temperature, adds room temperature decolorising agent and stirs 1 hour, stand 5 hours, then release soap matter, deacidification tank body is provided with No. two valves.
As one preferred embodiment, No. three fining pots include a decolouring tank body, for vacuum tank, decolouring tank body is provided with decolouring charge door, is provided with some decolouring electrothermal tubes in bleacher body, decolouring tank body top is provided with the decolouring blender stretching into decolouring tank body, decolouring electrothermal tube connects the automatically controlled electroplax of decolouring, wherein 105 degree of-110 degree of oil temperature, adds decolorising agent and stirs 1 hour, filter at once, slough the pigment in oil.
As one preferred embodiment, No. four fining pots include a deodorize tank body, deodorize tank body is provided with deodorize charge door, some deodorize electrothermal tubes it are provided with in deodorizing tank body, deodorize tank body top is provided with the deodorize blender stretching into deodorize tank body, deodorize electrothermal tube connects the automatically controlled electroplax of deodorize, deodorize tank body connects cooling pump and vacuum pump, deodorize tank base is provided with nitrogen tube, deodorize tank base is provided with fine filter, oil temperature is heated to 220 degree of-245 degree, continuous vacuum 3 hours, then cold filtration.
As one preferred embodiment, oil refining required theoretical heat=refined oil specific heat × refined oil weight × (initial temperature of the final temperature-oil of oil), theoretical budget power=oil refining theoretical institute calorific requirement/theory estimated time.
As one preferred embodiment, theoretical budget power/predetermined power factor obtains actually required power.
As one preferred embodiment, power factor is 0.7-0.85.
As one preferred embodiment, the quantity of washing electrothermal tube, deacidification electrothermal tube, decolouring electrothermal tube and deodorize electrothermal tube is 3-5 group.
As one preferred embodiment, washing automatically controlled electroplax, decolouring electric control panel, the automatically controlled electroplax of deacidification and deodorize electric control panel uses split be arranged on corresponding tank body or use integrally disposed.
After have employed technique scheme, the beneficial effects of the utility model are:
1. environmental protection, utilizes electric energy to heat, and decreases the waste gas discharge that fire coal causes；
2. safety coefficient is high, and whole oil refining process need not arrange work at each valve and operates, it is only necessary to utilizes control electroplax to realize oil refining and controls, reduces the risk brought to operator due to high temperature；Meanwhile, when conduction oil at high temperature circulates, dangerous at a relatively high, the application then effectively prevent the potential safety hazard therefore brought；
3. using manpower and material resources sparingly, whole process can realize control by electric control dish, and labor intensity is little, decreases labour force and puts into；
4. low cost, it is not necessary to additionally carrying out waste gas emission treatment or reduction of discharging processes, the investment producing equipment is substantially reduced；
5. can accurately control production time, time according to actual needs, utilize electric control dish to control to run power, reach accurately to control, it is ensured that the oil of oil refining.
Accompanying drawing explanation
In order to be illustrated more clearly that this utility model embodiment or technical scheme of the prior art, the accompanying drawing used required in embodiment or description of the prior art will be briefly described below, apparently, accompanying drawing in describing below is only embodiments more of the present utility model, for those of ordinary skill in the art, on the premise of not paying creative work, it is also possible to obtain other accompanying drawing according to these accompanying drawings.
Fig. 1 is the structural representation of this utility model refining equipment.
In figure, number fining pot of 1-, 2-blender；3-washes electrothermal tube；4-washes automatically controlled electroplax；No. bis-fining pots of 5-；6-deacidification electrothermal tube；The automatically controlled electroplax of 7-deacidification；No. tri-fining pots of 8-；9-decolours electrothermal tube；10-decolours automatically controlled electroplax；11-filter；12-temporary storage tank；No. tetra-fining pots of 13-；14-vacuum pump；15-deodorize electrothermal tube；16-cooling pump；The automatically controlled electroplax of 17-deodorize；18-nitrogen tube；19-petroleum pipeline；Number valve of 20-；No. bis-valves of 21-；22-fine filter.
Detailed description of the invention
Below in conjunction with the accompanying drawing in this utility model embodiment, the technical scheme in this utility model embodiment is clearly and completely described, it is clear that described embodiment is only a part of embodiment of this utility model rather than whole embodiments.Based on the embodiment in this utility model, the every other embodiment that those of ordinary skill in the art are obtained under not making creative work premise, broadly fall into the scope of this utility model protection.
As it is shown in figure 1, this refining equipment, it is sequentially connected with a fining pot of setting, No. two fining pots, No. three bleachers and No. four deodorizing tanks including by petroleum pipeline 19；
A number fining pot 1 is water washing tank, is used for carrying out washing process, and removes the colloid phospholipid in oil removing and impurity；
No. two fining pots 5 are deacidification tank, for removing the fatty acid in oil；
No. three fining pots 8 are vacuum decoloration tank, for sloughing the pigment in oil；
No. four fining pots 13 are vacuum deodorization tank, for removing the various pollution tastes in oil.
A number fining pot 1 includes a washing tank body, it is provided with washing charge door on washing tank body, some washing electrothermal tubes 3 it are provided with in water washing tank body, washing tank body top is provided with the washing blender 2 stretching into washing tank body, washing electrothermal tube 3 connects the automatically controlled electroplax 4 of washing, and wherein oil temperature controls to be 70 degree of-80 degree, washes water temperature 100 degree, stand 8-10 hour after 30-50 minute time, washing tank body is provided with a valve 20.
No. two fining pots 5 include a deacidification tank body, deacidification tank body is provided with deacidification charge door, some deacidification electrothermal tubes 6 it are provided with in deacidification tank body, deacidification tank body top is provided with the deacidification blender 2 stretching into deacidification tank body, deacidification electrothermal tube 6 connects the automatically controlled electroplax of deacidification 7, wherein 70 degree of-80 degree of oil temperature, adds room temperature decolorising agent and stirs 1 hour, stand 5 hours, deacidification tank body is provided with No. two valves 21.
No. three fining pots 8 include a decolouring tank body, for vacuum tank, decolouring tank body is provided with decolouring charge door, being provided with some decolouring electrothermal tubes 9 in bleacher body, decolouring tank body top is provided with the decolouring blender 2 stretching into decolouring tank body, and decolouring electrothermal tube 9 connects the automatically controlled electroplax 10 of decolouring, wherein 105 degree of-110 degree of oil temperature, add decolorising agent to stir 1 hour, filter at once, slough the pigment in oil.
No. four fining pots 5 include a deodorize tank body, deodorize tank body is provided with deodorize charge door, some deodorize electrothermal tubes 15 it are provided with in deodorizing tank body, deodorize tank body top is provided with the deodorize blender 2 stretching into deodorize tank body, deodorize electrothermal tube 15 connects the automatically controlled electroplax of deodorize 17, deodorize tank body connects cooling pump 16 and vacuum pump 14, oil temperature is heated to 220 degree of-245 degree, continuous vacuum 3 hours, then cold filtration, deodorize tank base is provided with nitrogen tube 18, and deodorize tank base is provided with fine filter 22.
Oil refining required theoretical heat=refined oil specific heat × refined oil weight × (initial temperature of the final temperature-oil of oil), theoretical budget power=oil refining theoretical institute calorific requirement/theory estimated time.
Theoretical budget power/predetermined power factor obtains actually required power.
Power factor is 0.7-0.85.
The quantity of washing electrothermal tube 3, deacidification electrothermal tube 6, decolouring electrothermal tube 9 and deodorize electrothermal tube 15 is 3-5 group.
Washing automatically controlled electroplax 4, decolouring electric control panel, the automatically controlled electroplax of deacidification 7 and deodorize electric control panel uses split be arranged on corresponding tank body or use integrally disposed.
It is provided with filter 11 and temporary storage tank 12 between No. three fining pots 8 and No. four fining pots 13.
This refining equipment: 1. environmental protection, utilizes electric energy to heat, and decreases the waste gas discharge that fire coal causes；
2. safety coefficient is high, and whole oil refining process need not arrange work at each valve and operates, it is only necessary to utilizes control electroplax to realize oil refining and controls, reduces the risk brought to operator due to high temperature；Meanwhile, when conduction oil at high temperature circulates, dangerous at a relatively high, the application then effectively prevent the potential safety hazard therefore brought；
3. using manpower and material resources sparingly, whole process can realize control by electric control dish, and labor intensity is little, decreases labour force and puts into；
4. low cost, it is not necessary to additionally carrying out waste gas emission treatment or reduction of discharging processes, the investment producing equipment is substantially reduced；
5. can accurately control production time, time according to actual needs, utilize electric control dish to control to run power, reach accurately to control, it is ensured that the oil of oil refining.
The foregoing is only preferred embodiment of the present utility model; not in order to limit this utility model; all within spirit of the present utility model and principle, any modification, equivalent substitution and improvement etc. made, within should be included in protection domain of the present utility model.
Claims (7)
1. a refining equipment, it is characterised in that include being sequentially connected with a fining pot of setting, No. two fining pots, No. three fining pots and No. four fining pots by petroleum pipeline；
A number fining pot is water washing tank, is used for carrying out washing process, and removes the colloid phospholipid in oil removing and impurity；
No. two fining pots are deacidification tank, for removing the fatty acid in oil；
No. three fining pots are vacuum decoloration tank, for sloughing the pigment in oil；
No. four fining pots are vacuum deodorization tank, for removing the various pollution tastes in oil.
Refining equipment the most according to claim 1, it is characterized in that, a number fining pot includes a washing tank body, it is provided with washing charge door on washing tank body, some washing electrothermal tubes it are provided with in water washing tank body, washing tank body top is provided with the washing blender stretching into washing tank body, and washing electrothermal tube connects the automatically controlled electroplax of washing.
Refining equipment the most according to claim 2, it is characterized in that, No. two fining pots include a deacidification tank body, deacidification tank body is provided with deacidification charge door, some deacidification electrothermal tubes it are provided with in deacidification tank body, deacidification tank body top is provided with the deacidification blender stretching into deacidification tank body, and deacidification electrothermal tube connects the automatically controlled electroplax of deacidification.
Refining equipment the most according to claim 3, it is characterized in that, No. three fining pots include a decolouring tank body, decolouring tank body is provided with decolouring charge door, some decolouring electrothermal tubes it are provided with in bleacher body, decolouring tank body top is provided with the decolouring blender stretching into decolouring tank body, and decolouring electrothermal tube connects the automatically controlled electroplax of decolouring.
Refining equipment the most according to claim 4, it is characterized in that, No. four fining pots include a deodorize tank body, deodorize tank body is provided with deodorize charge door, is provided with some deodorize electrothermal tubes in deodorizing tank body, and deodorize tank body top is provided with the deodorize blender stretching into deodorize tank body, deodorize electrothermal tube connects the automatically controlled electroplax of deodorize, described deodorize tank body connects has cooling pump and vacuum pump, deodorize tank base to be provided with nitrogen tube, and deodorize tank base is provided with fine filter.
Refining equipment the most according to claim 5, it is characterised in that the quantity of described washing electrothermal tube, deacidification electrothermal tube, decolouring electrothermal tube and deodorize electrothermal tube is 3-5 group.
Refining equipment the most according to claim 1, it is characterised in that be provided with filter and temporary storage tank between described No. three fining pots and No. four fining pots.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620180771.8U CN205443223U (en) | 2016-03-09 | 2016-03-09 | Refining equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620180771.8U CN205443223U (en) | 2016-03-09 | 2016-03-09 | Refining equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205443223U true CN205443223U (en) | 2016-08-10 |
Family
ID=56602120
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620180771.8U Expired - Fee Related CN205443223U (en) | 2016-03-09 | 2016-03-09 | Refining equipment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205443223U (en) |
-
2016
- 2016-03-09 CN CN201620180771.8U patent/CN205443223U/en not_active Expired - Fee Related
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160810 Termination date: 20180309 |