CN207632756U - Waste lubricating oil flocculation extraction and distillation combination kettle - Google Patents
Waste lubricating oil flocculation extraction and distillation combination kettle Download PDFInfo
- Publication number
- CN207632756U CN207632756U CN201721406988.7U CN201721406988U CN207632756U CN 207632756 U CN207632756 U CN 207632756U CN 201721406988 U CN201721406988 U CN 201721406988U CN 207632756 U CN207632756 U CN 207632756U
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- CN
- China
- Prior art keywords
- distillation
- chamber
- flocculation
- agitating shaft
- lubricating oil
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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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- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The utility model discloses a kind of waste lubricating oil flocculation extraction and distillation combination kettle, and combination autoclave body is divided into two chambers, is above flocculation stirring chamber, and lower for distillation chamber, agitating shaft is perpendicular to wear two chambers.Cleaning door is arranged in stir chamber side, is cleared up flocculate by the cleaning door.Separated by macromolecular filtering stratum reticulare between flocculation stirring chamber and distillation chamber, agitating shaft is mounted with that sealing rubber ring, agitating shaft can simultaneously be stirred two chambers at filtering meshes, improves machinery utilization efficiency.It distills cavity wall to be equipped with around heating tube, coil structure adds the effect of stirring blade, distillation intracavitary can be made to be heated evenly, and ensures work safety, improves distillation efficiency.Distillation chamber side lower end is equipped with level control return duct and is connected at the top of autoclave body, and oil pump is mounted on return duct, can be controlled the liquid level for distilling intracavitary by the device, ensures equipment safety, the balance to work in control kettle.The utility model flocculates solvent to refine extraction and distill to be completed by a combination kettle, is reduced equipment investment, is reduced production cost, simple in structure, easy to use.
Description
Technical field
The utility model is related to lubricant oil regeneration processing unit (plant) field more particularly to a kind of waste lubricating oil flocculation extraction and steam
Evaporate combination kettle.
Background technology
Currently, waste lubricating oil recycling has been the project that lubricating oil industry was given priority in recent years, many lubricating oil
It can intake due to exchange interaction or other reasons with air in use, can also invade the dust in environment, machinery mill
The iron rust that the metal powder damaged and ferrous metal corrosion generate, these not only increase friction, influence the lubricating function of oil, and
The autoxidation of lubricating oil can also be accelerated and to corrosion of metal.The lubricating oil for losing efficiency is set to change, if abandoned extremely
Serious pollution can be caused in environment, this just needs to carry out recycling reprocessing production to waste lubricating oil.For the place of waste lubricating oil
Reason, will use, process is after waste lubricant oil regeneration mostly both at home and abroad at present：Waste lubricating oil is through sedimentation, purification, filtering, absorption
After removing most of impurity, then through its water content of dehydration reduction, then processed waste lubricant oil by hydrogenation is refined useless to remove
The substances such as oxide, sulfur-containing compound, halogen compounds, nitride and heavy metal compound in oil, most afterwards after blending
Obtain workable reclaimed oil.The rectification flow of waste oil is the technological process for including chemical refining or adsorption refining, chemistry
Technological process including demetalization and chemical demulsification can be also included in reprocessing process flow.Not due to technology and emphasis
Together, promoted waste lubricating oil to re-refine processing technology in two different directions to develop, produce with traditional sulfuric acid-carclazyte
There are regeneration technology and the propane flocculation extracting of acid pollution as the environmental friendly regenerated technique of anacidity of representative for what is represented.Wherein, purification step
It is rapid to usually require to carry out in a distillation column, and flocculate and refine extraction step and need again with additional equipment, therefore increase equipment
Input, improves production cost.
Utility model content
The purpose of this utility model is to solve the defect of above-mentioned existing equipment, naturally heavy for waste lubricating oil in the prior art
The drawbacks described above of shallow lake equipment, provide a kind of can extract useful oil plant and extraction effect good waste lubricating oil sinks naturally compared with limits
Shallow lake device.
To solve the above problems, the utility model can be realized by technical solution below.
Waste lubricating oil flocculation extraction and distillation combination kettle, by solvent flocculate refined extraction and distill by a combination kettle come
It completes, reduces equipment investment, reduce production cost, it is simple in structure, it is easy to use.
Waste lubricating oil flocculation extraction and distillation combination kettle, characterized in that the waste lubricating oil flocculation extraction and distillation combination
The top of kettle is equipped with oil inlet, flocculation solvent feed mouth, level control return duct and motor, and stirring is connect under the motor
Axis is equipped with two groups of stirring blades on agitating shaft, and for blade helically up around agitating shaft, the combination autoclave body is divided into two chambers
Room is above flocculation stirring chamber, and lower to distill chamber, agitating shaft is perpendicular to wear two chambers, and cleaning door is arranged in the stir chamber side, described
It distills chamber top side and is equipped with gas outlet, lower part is equipped with sewage draining exit.
As a kind of improvement of the utility model, the flocculation stirring chamber and distillation chamber between by macromolecular filtering stratum reticulare every
Disconnected, agitating shaft is mounted with sealing rubber ring at filtering meshes.
As a kind of improvement of the utility model, the distillation cavity wall is equipped with around heating tube, distills chamber side lower end
It equipped with level control return duct and is connected at the top of autoclave body, oil pump is mounted on return duct.
The utility model possessed advantageous effect compared with existing equipment is：
Combination autoclave body described in the utility model is divided into two chambers, is above flocculation stirring chamber, and lower to distill chamber, agitating shaft is perpendicular
Two chambers are worn, two chambers are respectively equipped with one group of stirring blade, and blade helically up around agitating shaft, can improve stirring effect
Rate.Cleaning door is arranged in the stir chamber side, and when stream time is longer, flocculation stirring intracavitary can stockpile a large amount of flocculations
Object influences to work normally, and can be cleared up flocculate by the cleaning door.The flocculation stirring chamber and distillation chamber between by
Macromolecular filtering stratum reticulare separates, and agitating shaft is mounted with that sealing rubber ring, agitating shaft can be simultaneously to two chambers at filtering meshes
Room is stirred, and improves machinery utilization efficiency, and sealing rubber ring can ensure the leakproofness of two chambers partition, enable material
Effectively filtering.The distillation cavity wall is equipped with around heating tube, and coil structure adds the effect of stirring blade, can make distillation intracavitary
It is heated evenly, ensures work safety, improve distillation efficiency.Distillation chamber side lower end is equipped with level control return duct and is connected to kettle
At the top of body, oil pump is mounted on return duct, the liquid level for distilling intracavitary can be controlled by the device, when liquid level mistake
Oil plant can block gas outlet when high, cause distillation cavity pressure excessive, influence equipment safety, can will be more under the action of oil pump
Excess oil liquid is pumped into stir chamber, to control the balance to work in kettle.
Description of the drawings
Fig. 1 is the structural schematic diagram of the utility model structure.
Specific implementation mode
The utility model seat is further described below according to attached drawing.
As shown in Figure 1, waste lubricating oil flocculation extraction and distillation combination kettle, including autoclave body（18）, level control return duct
（1）, flocculation stirring chamber（2）, motor（3）, oil inlet（4）, flocculation solvent feed mouth（5）, flocculation stirring blade（6）, stirring
Axis（7）, cleaning door（8）, sealing rubber ring（9）, macromolecular filtering stratum reticulare（10）, gas outlet（11）, distillation cavity wall（12）, heating
Pipe（13）, blowdown valve（14）, sewage draining exit（15）, distillation stirring blade（16）, oil pump（17）.
The top of waste lubricating oil flocculation extraction and distillation combination kettle described in the utility model is equipped with oil inlet（4）, flocculation it is molten
Agent feed inlet（5）, level control return duct（1）And motor（3）, the motor（3）Under connect agitating shaft（7）, agitating shaft（7）
It is upper that two groups of stirring blades, flocculation stirring blade are housed（6）With distillation stirring blade（16）, blade is helically up around stirring
Axis, the combination autoclave body（18）It is divided into two chambers, is above flocculation stirring chamber, it is lower for distillation chamber, agitating shaft（7）It is perpendicular to wear two chambers
Cleaning door is arranged in room, the stir chamber side（8）, the distillation chamber top side is equipped with gas outlet（11）, lower part is equipped with blowdown
Mouthful（15）.
By macromolecular filtering stratum reticulare between the flocculation stirring chamber and distillation chamber（10）Partition, agitating shaft run through filtering meshes
Place is mounted with sealing rubber ring（9）.The distillation cavity wall（12）Equipped with around heating tube（13）, distillation chamber side lower end is equipped with liquid
Face controls return duct（1）And be connected at the top of autoclave body, it is mounted with oil pump on return duct（17）.
Autoclave body is combined described in utility model and is divided into two chambers, is above flocculation stirring chamber, and lower to distill chamber, agitating shaft is perpendicular to be worn
Two chambers, two chambers are respectively equipped with one group of stirring blade, and blade helically up around agitating shaft, can improve stirring effect
Rate.Cleaning door is arranged in the stir chamber side, and when stream time is longer, flocculation stirring intracavitary can stockpile a large amount of flocculations
Object influences to work normally, and can be cleared up flocculate by the cleaning door.The flocculation stirring chamber and distillation chamber between by
Macromolecular filtering stratum reticulare separates, and agitating shaft is mounted with that sealing rubber ring, agitating shaft can be simultaneously to two chambers at filtering meshes
Room is stirred, and improves machinery utilization efficiency, and sealing rubber ring can ensure the leakproofness of two chambers partition, enable material
Effectively filtering.The distillation cavity wall is equipped with around heating tube, and coil structure adds the effect of stirring blade, can make distillation intracavitary
It is heated evenly, ensures work safety, improve distillation efficiency.Distillation chamber side lower end is equipped with level control return duct and is connected to kettle
At the top of body, oil pump is mounted on return duct, the liquid level for distilling intracavitary can be controlled by the device, when liquid level mistake
Oil plant can block gas outlet when high, cause distillation cavity pressure excessive, influence equipment safety, can will be more under the action of oil pump
Excess oil liquid is pumped into stir chamber, to control the balance to work in kettle.
The prompt of book according to the above description can also carry out embodiment according to practical condition in use
Certain more change and modification meet the requirement of actual production.
Claims (3)
1. waste lubricating oil flocculation extraction and distillation combination kettle, which is characterized in that including combining autoclave body, the waste lubricating oil flocculation carries
The top for taking and distilling combination kettle is equipped with oil inlet, flocculation solvent feed mouth, level control return duct and motor, described electronic
Agitating shaft is connect under machine, two groups of stirring blades is housed, blade is helically up around agitating shaft, the combination autoclave body point on agitating shaft
It is above flocculation stirring chamber for two chambers, lower to distill chamber, agitating shaft is perpendicular to wear two chambers, and the stir chamber side setting is clear
Li Men, the distillation chamber top side are equipped with gas outlet, and lower part is equipped with sewage draining exit.
2. waste lubricating oil flocculation extraction according to claim 1 and distillation combination kettle, the flocculation stirring chamber and distillation chamber
Between separated by macromolecular filtering stratum reticulare, agitating shaft is mounted with sealing rubber ring at the filtering meshes.
3. waste lubricating oil flocculation extraction according to claim 1 and distillation combination kettle, the distillation cavity wall, which is equipped with, to be surround
Heating tube, distillation chamber side lower end is equipped with level control return duct and is connected at the top of autoclave body, and oil pump is mounted on return duct.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721406988.7U CN207632756U (en) | 2017-10-30 | 2017-10-30 | Waste lubricating oil flocculation extraction and distillation combination kettle |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721406988.7U CN207632756U (en) | 2017-10-30 | 2017-10-30 | Waste lubricating oil flocculation extraction and distillation combination kettle |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207632756U true CN207632756U (en) | 2018-07-20 |
Family
ID=62858987
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201721406988.7U Expired - Fee Related CN207632756U (en) | 2017-10-30 | 2017-10-30 | Waste lubricating oil flocculation extraction and distillation combination kettle |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN207632756U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111235364A (en) * | 2020-03-30 | 2020-06-05 | 盛瑞传动股份有限公司 | Quenching oil recovery device |
| CN113578230A (en) * | 2021-06-29 | 2021-11-02 | 浙江中科玖源新材料有限公司 | Violent exothermic reation kettle is prevented to integral type |
-
2017
- 2017-10-30 CN CN201721406988.7U patent/CN207632756U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111235364A (en) * | 2020-03-30 | 2020-06-05 | 盛瑞传动股份有限公司 | Quenching oil recovery device |
| CN113578230A (en) * | 2021-06-29 | 2021-11-02 | 浙江中科玖源新材料有限公司 | Violent exothermic reation kettle is prevented to integral type |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20180720 Termination date: 20191030 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |