CN202519227U - Oil residue treating and oil-extracting device - Google Patents
Oil residue treating and oil-extracting device Download PDFInfo
- Publication number
- CN202519227U CN202519227U CN2012201574550U CN201220157455U CN202519227U CN 202519227 U CN202519227 U CN 202519227U CN 2012201574550 U CN2012201574550 U CN 2012201574550U CN 201220157455 U CN201220157455 U CN 201220157455U CN 202519227 U CN202519227 U CN 202519227U
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- Prior art keywords
- oil
- tank
- dregs
- fat
- handled
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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.)
- Expired - Fee Related
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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
- 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
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Abstract
The utility model discloses an oil residue treating and oil-extracting device, which comprises an oil residue treating and oil-extracting tank with an inlet and an outlet, a hot saline tank, a sulfuric acid tank and a high-level oil storage tank, wherein the oil residue treating and oil-extracting tank is provided with a stirring device, and a tank body of the oil residue treating and oil-extracting tank is provided with an oil extracting tank heating device; the hot saline tank and the sulfuric acid tank are arranged above the oil residue treating and oil-extracting tank and is connected with an oil residue treating and oil-extracting pipe through an input pipeline, wherein a hot saline tank heating device is arranged in the hot saline tank, the lower end part of the input pipeline is connected with a material distributor arranged in the oil residue treating and oil-extracting tank, and the input pipeline is provided with two control valves for controlling the hot saline tank and the sulfuric acid tank; and the high-level oil storage tank is connected with the oil residue treating and oil-extracting tank through an output pipeline, wherein the high-level oil storage tank is provided with a leading-out port, and the output pipeline is provided with a chemical pump. The tank type oil-extracting device disclosed by the utility model has low power consumption and high oil residue treating and oil-extracting yield; acid liquor and hot saline are added in the oil residue treatment to ensure that impurities and oil can be effectively and rapidly separated; the oil residue treating and oil-extracting device disclosed by the utility model has small occupying area, low investment and low labor intensity; and the tank-type oil-extracting treatment capacity is large and the treating cost is saved.
Description
Technical field
The utility model relates to a kind of dregs of fat and handles oil extraction plant.
Background technology
The dregs of fat that oil chemistry factory produced have the value of second stage employ, and are more to the processing mode of the dregs of fat at present, but treatment facility exists following drawback: a, energy consumption bigger usually, and oil yield is lower; B, single treatment amount are less; C, treatment facility take up an area of increasing and invest higher.
The utility model content
The purpose of the utility model is exactly in order to address the above problem, and provides a kind of dregs of fat to handle oil extraction plant.
To achieve these goals, the utility model adopts following technical scheme:
A kind of dregs of fat are handled oil extraction plant, it is characterized in that, comprising:
The dregs of fat with entrance and exit are handled and to be carried oil tank, and it is provided with whipping appts, and the said dregs of fat are handled and carried oil tank body and be provided with and carry the oil tank heating unit;
Being located at dregs of fat processing carries the oil tank top and carries hot salt brine jar and the sulphuric acid tank that oil pipe links to each other through input channel with dregs of fat processing; Establish hot salt brine jar heating unit in the said hot salt brine jar; Said input channel bottom is handled the material sparger carry in the oil tank and is linked to each other with being located at the dregs of fat, said input channel be provided with two control hot salt brine jars and sulphuric acid tank by-pass valve control;
Carry the high-order oil tank that oil tank links to each other through output channel with dregs of fat processing, it is provided with export mouth, and said output channel is provided with chemical pump.
Preferably, the said oil tank heating unit of carrying is a heating jacket.
Preferably, said hot salt brine jar heating unit is a heating coil.
Preferably, said input channel is " Y " font.
Further improvement as the utility model is that the said chemical pump and the dregs of fat are handled the output channel of carrying between oil tank and are provided with first valve.
Further improvement as the utility model is that the said chemical pump and the dregs of fat are handled the output channel of carrying between oil tank and are provided with isocon, and this isocon is provided with second valve.
Further improvement as the utility model is that said isocon exit end is provided with the assorted geosyncline of water.
Further improvement as the utility model is that said chemical pump exit end is provided with the 3rd valve.
Further improvement as the utility model is that the nearly high-order oil tank end of said output channel is provided with the 4th valve.
Further improvement as the utility model is that the input channel that is " Y " font is provided with input channel overhead control valve.
The beneficial effect of the utility model is:
(1) pot type oil extraction plant, power consumption is low, and the dregs of fat are handled and are carried oily yield height.
(2) dregs of fat are handled and are added acid solution and hot salt brine, and impurity can be separated with grease fast and effectively.
(3) floor space is little, less investment, and labour intensity is low.
(4) to put forward the oil treatment amount big for pot type, practices thrift processing cost.
(5) this device can be applicable to the oil and fat chemical field, the dregs of fat that various oil chemistry factory produced is handled carried oil.
Description of drawings
Fig. 1 is the utility model structural representation.
Embodiment
For technique means, creation characteristic that the utility model is realized, reach purpose and be easy to understand understanding with effect, below in conjunction with concrete diagram, further set forth the utility model.
Need to prove, the word that uses in describing below " on " with orientation such as D score refer in the accompanying drawing upper and lower to, word " interior " and " outward " refer to respectively towards or specific features geometric centre direction away from drawing or in scheming.
As shown in Figure 1, a kind of dregs of fat are handled oil extraction plant, comprising: oil tank 5 is carried in the dregs of fat processing with entrance and exit, and it is provided with whipping appts 6, and said dregs of fat processing is carried oil tank body and is provided with heating jacket 8; Being located at dregs of fat processing carries the oil tank top and carries the hot salt brine jar 1 and sulphuric acid tank 3 that oil pipe links to each other through the input channel that roughly is " Y " font with dregs of fat processing; Brine tank 1 and sulphuric acid tank 3 are higher than the dregs of fat to be handled and carries oil tank 5 and be provided with to be beneficial to and directly the medium in two tank bodies flowed into the dregs of fat by action of gravity and handle and carry oil tank 5; Establish heating coil 2 in the said hot salt brine jar 1; Said input channel bottom be located at the dregs of fat and handle the material sparger 7 carry in the oil tank and link to each other; Said input channel is provided with the by-pass valve control of two control hot salt brine jars 1 and sulphuric acid tank 3; Said by-pass valve control is located at respectively on the introduction pipe of hot salt brine jar 1 and sulphuric acid tank 3 settings separately, and the input channel that is " Y " font is provided with input channel overhead control valve 4; Carry the high-order oil tank 11 that oil tank links to each other through output channel with dregs of fat processing; It has export mouth; This high position oil tank 11 is located at dregs of fat processing and is carried oil tank 5 position highly about equally; Said output channel is provided with chemical pump 10, and said chemical pump exit end is provided with the 3rd valve, with the output flow of control chemical pump.
As shown in Figure 1, the said chemical pump and the dregs of fat are handled the output channel of carrying between oil tank and are provided with first valve.
As shown in Figure 1, the said chemical pump and the dregs of fat are handled the output channel of carrying between oil tank and are provided with isocon, and this isocon is provided with second valve, and said isocon exit end is provided with the assorted geosyncline 9 of water.
As shown in Figure 1, the nearly high-order oil tank end of said output channel is provided with the 4th valve.
The principle of this device is: utilize the effective bonded principle of some non-oily impurity and acid in the dregs of fat; Remove the impurity in the dregs of fat, and can play the breakdown of emulsion carburetion and accelerate oil and grease that the isolating principle of impurity is carried out in the dregs of fat separates with impurity fast and effectively according to hot salt brine.
The workflow of this device: after the dregs of fat are handled the material process whipping appts 6 and heating jacket 8 heating of carrying oil tank 5 in this device; Add the sulfuric acid in the sulphuric acid tank 3 again; After material distributes 7 devices, fully contact, thereby the impurity in the oil is effectively combined with acid with the dregs of fat.The hot salt brine that then adds in the hot salt brine jar 1 that has prepared mixes static then back layering with a jar interior mixture.The water of telling is assorted to enter into the assorted geosyncline 9 of water, and the oil of telling is transported in the high-order oil tank 11 through chemical pump 10.
The above is merely the preferred implementation of the utility model, and the protection domain of the utility model is not limited in above-mentioned embodiment, and every technical scheme that belongs to the utility model principle all belongs to the protection domain of the utility model.For a person skilled in the art, some improvement of under the prerequisite of the principle that does not break away from the utility model, carrying out, these improve the protection domain that also should be regarded as the utility model.
Claims (10)
1. dregs of fat are handled oil extraction plant, it is characterized in that, comprising:
The dregs of fat with entrance and exit are handled and to be carried oil tank, and it is provided with whipping appts, and the said dregs of fat are handled and carried oil tank body and be provided with and carry the oil tank heating unit;
Being located at dregs of fat processing carries the oil tank top and carries hot salt brine jar and the sulphuric acid tank that oil pipe links to each other through input channel with dregs of fat processing; Establish hot salt brine jar heating unit in the said hot salt brine jar; Said input channel bottom is handled the material sparger carry in the oil tank and is linked to each other with being located at the dregs of fat, said input channel be provided with two control hot salt brine jars and sulphuric acid tank by-pass valve control;
Carry the high-order oil tank that oil tank links to each other through output channel with dregs of fat processing, it is provided with export mouth, and said output channel is provided with chemical pump.
2. a kind of dregs of fat according to claim 1 are handled oil extraction plant, it is characterized in that the said oil tank heating unit of carrying is a heating jacket.
3. a kind of dregs of fat according to claim 1 are handled oil extraction plant, it is characterized in that said hot salt brine jar heating unit is a heating coil.
4. a kind of dregs of fat according to claim 1 are handled oil extraction plant, it is characterized in that said input channel is " Y " font.
5. a kind of dregs of fat according to claim 1 are handled oil extraction plant, it is characterized in that, the said chemical pump and the dregs of fat are handled the output channel of carrying between oil tank and are provided with first valve.
6. a kind of dregs of fat according to claim 1 are handled oil extraction plant, it is characterized in that, the said chemical pump and the dregs of fat are handled the output channel of carrying between oil tank and are provided with isocon, and this isocon is provided with second valve.
7. a kind of dregs of fat according to claim 6 are handled oil extraction plant, it is characterized in that, said isocon exit end is provided with the assorted geosyncline of water.
8. a kind of dregs of fat according to claim 1 are handled oil extraction plant, it is characterized in that said chemical pump exit end is provided with the 3rd valve.
9. a kind of dregs of fat according to claim 1 are handled oil extraction plant, it is characterized in that the nearly high-order oil tank end of said output channel is provided with the 4th valve.
10. a kind of dregs of fat according to claim 4 are handled oil extraction plant, it is characterized in that the input channel that is " Y " font is provided with input channel overhead control valve.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN2012201574550U CN202519227U (en) | 2012-04-10 | 2012-04-10 | Oil residue treating and oil-extracting device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
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CN2012201574550U CN202519227U (en) | 2012-04-10 | 2012-04-10 | Oil residue treating and oil-extracting device |
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CN202519227U true CN202519227U (en) | 2012-11-07 |
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CN2012201574550U Expired - Fee Related CN202519227U (en) | 2012-04-10 | 2012-04-10 | Oil residue treating and oil-extracting device |
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Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103084133A (en) * | 2013-02-20 | 2013-05-08 | 安徽天意环保科技有限公司 | Acidification reaction device |
CN103111251A (en) * | 2013-02-20 | 2013-05-22 | 安徽天意环保科技有限公司 | Waste acid utilization device of acidification kettle |
CN108587796A (en) * | 2018-03-21 | 2018-09-28 | 安徽工程大学 | A kind of intelligence fish oil soap stock high-efficiency sedimentation processing unit |
CN108949336A (en) * | 2018-07-25 | 2018-12-07 | 中国农业科学院农产品加工研究所 | Animal oil Slag treatment device and method |
-
2012
- 2012-04-10 CN CN2012201574550U patent/CN202519227U/en not_active Expired - Fee Related
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103084133A (en) * | 2013-02-20 | 2013-05-08 | 安徽天意环保科技有限公司 | Acidification reaction device |
CN103111251A (en) * | 2013-02-20 | 2013-05-22 | 安徽天意环保科技有限公司 | Waste acid utilization device of acidification kettle |
CN103111251B (en) * | 2013-02-20 | 2015-05-27 | 安徽天意环保科技有限公司 | Waste acid utilization device of acidification kettle |
CN108587796A (en) * | 2018-03-21 | 2018-09-28 | 安徽工程大学 | A kind of intelligence fish oil soap stock high-efficiency sedimentation processing unit |
CN108949336A (en) * | 2018-07-25 | 2018-12-07 | 中国农业科学院农产品加工研究所 | Animal oil Slag treatment device and method |
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C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20121107 Termination date: 20150410 |
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EXPY | Termination of patent right or utility model |