CN206613219U - Profit secondary separation device in molecular distillation technique - Google Patents
Profit secondary separation device in molecular distillation technique Download PDFInfo
- Publication number
- CN206613219U CN206613219U CN201720282718.3U CN201720282718U CN206613219U CN 206613219 U CN206613219 U CN 206613219U CN 201720282718 U CN201720282718 U CN 201720282718U CN 206613219 U CN206613219 U CN 206613219U
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- CN
- China
- Prior art keywords
- storage tank
- main storage
- drainpipe
- auxiliary storage
- molecular distillation
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- 238000000034 method Methods 0.000 title claims abstract description 22
- 238000000199 molecular distillation Methods 0.000 title claims abstract description 15
- 238000000926 separation method Methods 0.000 title claims abstract description 14
- 239000007788 liquid Substances 0.000 claims abstract description 6
- 239000003921 oil Substances 0.000 description 33
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 10
- 230000009286 beneficial effect Effects 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 230000008676 import Effects 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 230000000505 pernicious effect Effects 0.000 description 3
- 238000011084 recovery Methods 0.000 description 2
- 238000009825 accumulation Methods 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000004821 distillation Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000010687 lubricating oil Substances 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 239000013049 sediment Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Landscapes
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
Light oil ingress pipe is accessed outside profit secondary separation device in a kind of molecular distillation technique of the utility model, including main storage tank, the main storage tank, the main tank bottom is provided with the first drainpipe, and first drainpipe is provided with the first control valve；The main storage tank side is provided with auxiliary storage tank, and overflow pipe is provided between the main storage tank and auxiliary storage tank；The main storage tank is provided with liquid level gauge, and the auxiliary storage tank is provided with overfall and transparent windows, and the auxiliary tank bottom is provided with the second drainpipe；The second control valve is provided with second drainpipe.The utility model is separated again to moisture in the light oil that is generated in molecular distillation technique, can effectively improve oil quality, remarkable in economical benefits.
Description
Technical field
The utility model is related to drain oil recovery equipment, and in particular to profit secondary separation is filled in a kind of molecular distillation technique
Put.
Background technology
Molecular distillation waste lubricating oil recovery and reusing and recycling, both beneficial to economizing on resources, can also prevent the pollution of the environment, and its tool is considerable
Economic benefit and social benefit.Find, the light oil water content that the technique is collected is difficult to control to, directly reduce in production practices
The quality of product oil.
The content of the invention
Technical problem to be solved in the utility model is to provide a kind of simple in construction, is easy to technology controlling and process, can significantly drop
Profit secondary separation device in the molecular distillation technique of light oil water content in low molecule distillation technique.
In order to solve the above technical problems, profit secondary separation device in a kind of molecular distillation technique of the utility model, including
Light oil ingress pipe is accessed outside main storage tank, the main storage tank, the main tank bottom is provided with the first drainpipe, the first row
Water pipe is provided with the first control valve；The main storage tank side is provided with auxiliary storage tank, is provided between the main storage tank and auxiliary storage tank excessive
Flow tube；The main storage tank is provided with liquid level gauge, and the auxiliary storage tank is provided with overfall and transparent windows, the auxiliary tank bottom
It is provided with the second drainpipe；The second control valve is provided with second drainpipe.
The liquid level that the liquid level gauge that the utility model is set is easy to operating personnel to observe light oil in main storage tank carries out production control
System；The light oil persistently imported automatically flows into auxiliary storage tank by overflow pipe, and the separation of water component sinks down into bottom, and operating personnel are by transparent
Observation window checks auxiliary storage tank bottom whether there is layering, and judges whether light oil water content is qualified on this basis.Determine light oil
Water content is qualified, and technique continues, and light oil is exported by overfall and collected；When water-bearing layer is close to overflow pipe, main storage tank is emptied in time
Bottom ponding simultaneously is implemented to control to front-end process, so that profit is efficiently separated.In technique, operating personnel by the first control valve,
Second control valve discharge correspondence storage tank internal water accumulation.The utility model divides moisture in the light oil that is generated in molecular distillation technique again
From can effectively improve oil product, have distinct economic.
It is preferred that, the main storage tank, auxiliary tank top are provided with the gas eduction tube of connection.During operation, main storage tank, auxiliary storage
Pernicious gas, which is collected, in tank burns, pollution-free.
It is preferred that, the main storage tank, auxiliary storage tank are respectively arranged with infundibulate bottom.In technique, the moisture isolated exists respectively
Bucket shape bottom sediments, the technical scheme can avoid flowing the moisture that oil body disturbance standing is sunk to the bottom, it is ensured that optimal oil-water separation.
To sum up, the technical solution of the utility model has following beneficial effect：
1st, component is few, and equipment cost is low；
2nd, topology layout rationally, is easy to technology controlling and process；
3rd, pernicious gas is prevented in line, beneficial to environmental protection；
4th, efficiently, oil quality lifting is notable for water-oil separating.
Brief description of the drawings
Fig. 1 is working state schematic representation of the present utility model.
Embodiment
The utility model is further described below in conjunction with the accompanying drawings：
As shown in figure 1, profit secondary separation device in a kind of molecular distillation technique of the utility model, including main storage tank 1, institute
The outer access light oil ingress pipe 3 of main storage tank 1 is stated, the main bottom of storage tank 1 is provided with the first drainpipe 1b, first drainpipe
1b is provided with the first control valve 1c；The side of main storage tank 1 is provided with auxiliary storage tank 2, is set between the main storage tank 1 and auxiliary storage tank 2
There is overflow pipe 5；The main storage tank 1 is provided with liquid level gauge 1a, and the auxiliary storage tank 2 is provided with overfall 2a and transparent windows 2d,
The bottom of auxiliary storage tank 2 is provided with the second drainpipe 2b；The second control valve 2c is provided with the second drainpipe 2b.
The main storage tank 1, the top of auxiliary storage tank 2 are provided with the gas eduction tube 4 of connection.
The main storage tank 1, auxiliary storage tank 2 are respectively arranged with infundibulate bottom.
The oil outlet end of the light oil ingress pipe 3 is placed in the main bottom of storage tank 1, and the oil outlet end of the overflow pipe 5 is placed in auxiliary storage
The bottom of tank 2.
Embodiment
A, aqueous light oil persistently import main storage tank 1 by light oil ingress pipe 3；
B, the light oil imported realize that profit is layered in main storage tank 1；
C, the upper strata light oil of main storage tank 1 are overflowed to auxiliary storage tank 2 naturally by overflow pipe 5, and contained humidity sinks in main storage tank 1
Bottom；
Light oil after d, moisture separation persistently imports auxiliary storage tank 2；
E, the light oil of 2 pairs of importings of auxiliary storage tank carry out water-oil separating again；
F, the upper strata lightweight oil level of auxiliary storage tank 2 continue lifting, until the qualified light oil of water content is natural by overfall 2a
Overflow and collect；
G, by transparent windows 2d observe the auxiliary bottom of storage tank 2 whether there is ponding, judge whether oil product is qualified with this；Qualified work
Skill continues；Unqualified main storage tank 1 then suspends the aqueous light oil of importing, the end production process before the main ponding of storage tank 1 and adjustment is emptied
Row water-oil separating again afterwards；
H, main storage tank 1, pernicious gas imports incinerator through gas eduction tube 4 and burned in auxiliary storage tank 2；
I, periodically empty auxiliary storage tank 2 and sink to the bottom ponding.
The utility model is separated again to moisture in the light oil that is generated in molecular distillation technique, can effectively improve oil quality
Amount, remarkable in economical benefits.
Claims (4)
1. profit secondary separation device in molecular distillation technique, including main storage tank（1）, the main storage tank（1）Outer access light oil
Ingress pipe（3）, the main storage tank（1）Bottom is provided with the first drainpipe（1b）, first drainpipe（1b）It is provided with first
Control valve（1c）；It is characterized in that：The main storage tank（1）Side is provided with auxiliary storage tank（2）, the main storage tank（1）With auxiliary storage tank
（2）Between be provided with overflow pipe（5）；The main storage tank（1）It is provided with liquid level gauge（1a）, the auxiliary storage tank（2）It is provided with overfall
（2a）And transparent windows（2d）, the auxiliary storage tank（2）Bottom is provided with the second drainpipe（2b）；Second drainpipe（2b）
On be provided with the second control valve（2c）.
2. profit secondary separation device in molecular distillation technique according to claim 1, it is characterised in that：The main storage tank
（1）, auxiliary storage tank（2）Top is provided with the gas eduction tube of connection（4）.
3. profit secondary separation device in molecular distillation technique according to claim 1, it is characterised in that：The main storage tank
（1）, auxiliary storage tank（2）It is respectively arranged with infundibulate bottom.
4. profit secondary separation device in molecular distillation technique according to claim 1, it is characterised in that：The light oil
Ingress pipe（3）Oil outlet end be placed in main storage tank（1）Bottom, the overflow pipe（5）Oil outlet end be placed in auxiliary storage tank（2）Bottom.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720282718.3U CN206613219U (en) | 2017-03-22 | 2017-03-22 | Profit secondary separation device in molecular distillation technique |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720282718.3U CN206613219U (en) | 2017-03-22 | 2017-03-22 | Profit secondary separation device in molecular distillation technique |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206613219U true CN206613219U (en) | 2017-11-07 |
Family
ID=60233551
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720282718.3U Active CN206613219U (en) | 2017-03-22 | 2017-03-22 | Profit secondary separation device in molecular distillation technique |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206613219U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112044157A (en) * | 2019-06-06 | 2020-12-08 | 陕西万宝隆科技实业发展有限公司 | Deslagging and oil-water decomposing system for oily wastewater |
-
2017
- 2017-03-22 CN CN201720282718.3U patent/CN206613219U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112044157A (en) * | 2019-06-06 | 2020-12-08 | 陕西万宝隆科技实业发展有限公司 | Deslagging and oil-water decomposing system for oily wastewater |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CP01 | Change in the name or title of a patent holder |
Address after: 246000 Anhui Guofu Lubricant Industry Co., Ltd., Xizhuang Group, Nongzhuang Village, Yangqiao Town, Yixiu District, Anqing City, Anhui Province Patentee after: Anhui Guofu Environmental Technology Co.,Ltd. Address before: 246000 Anhui Guofu Lubricant Industry Co., Ltd., Xizhuang Group, Nongzhuang Village, Yangqiao Town, Yixiu District, Anqing City, Anhui Province Patentee before: ANHUI GUOFU LUBRICANT INDUSTRY Co.,Ltd. |
|
| CP01 | Change in the name or title of a patent holder |