CN205435173U - High viscosity vacuum oil purifier system - Google Patents
High viscosity vacuum oil purifier system Download PDFInfo
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- CN205435173U CN205435173U CN201521108281.9U CN201521108281U CN205435173U CN 205435173 U CN205435173 U CN 205435173U CN 201521108281 U CN201521108281 U CN 201521108281U CN 205435173 U CN205435173 U CN 205435173U
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Abstract
The utility model provides a high viscosity vacuum oil purifier system, include that the lower extreme of flume is equipped with a drainage pipe through advancing oil feed flange, strainer, oil -feed pump, heater, oil water separation chamber and the vacuum separation tower that the oil pipe way links to each other, the row of being equipped with oil pipe says and the 2nd drainage pipe on the vacuum separation tower, is equipped with condensation chamber, water knockout drum, storage water tank and second drain valve on the 2nd drainage pipe in proper order, the utility model discloses simple structure, reasonable in design to high viscosity oil has been solved because higher, the flowable nature of viscosity surface tension poor and fluid is great for the principle to vacuum degassing and decompression evaporation, the technological difficult point of readily releasable not, and the evaporation of will reducing pressure simultaneously combines together with the vacuum separation, and a large amount of moisture in the oil are sloughed to the high efficiency, and the highest water content of fluid of processing can reach 25%.
Description
Technical field
This utility model relates to a kind of High-viscosity vacuum oil purifier system.
Background technology
All the time, the method that China's steel industry takes centrifugal separation method and gravitational settling from iron and steel designing institute to iron and steel enterprise user all the time for the purified treatment of high-viscosity oil, this kind of method can only be that the moisture etc. in oil is carried out preliminary process, not adapting to fluid soak in a large number and contain the requirement that mechanical admixture is many, each lubricating management personnel just take, when lubricating system oil is bad, process of changing oil.The most not only waste substantial amounts of available fluid, and useless oil handling is not had very good way yet, simultaneously with regard to environmental protection and energy-conservation aspect, also purification to high-viscosity oil is had higher requirement, therefore my company have studied lubricating system oil---the purifier of heavy oil for steel industry main equipment, the appearance of this device, not only solve the every pollution problem in original fluid, and fluid can be played maintaining effect, the service life of fluid can be extended simultaneously.Original in metallurgical system, the drain period of fluid is generally 1 year, and after using this device, fluid maybe need not be replaced by the service life that can be greatly prolonged fluid, it is only necessary to carry out simple supplementing when fluid is inadequate.For the development of this device, mainly have a key of the following aspects: 1, high-viscosity oil due to viscosity higher, flowable is poor, belongs to heavy oil one class, and the purification for fluid have to be relatively big in view of the surface tension of fluid, the feature being not readily separated；2, for vacuum separation, the domestic method usually having three types, it is volume shape, vaporific and film like, but these three method is for the process of high-viscosity oil, efficiency is the poorest.
Utility model content
For the problems referred to above, the utility model proposes a kind of High-viscosity vacuum oil purifier system.
For solving above technical problem, the technical scheme that this utility model provides is:
A kind of High-viscosity vacuum oil purifier system, it is characterized in that, including passing sequentially through the oil-feed flange that inflow pipeline is connected, coarse filter, oil-feed pump, heater, oil-water separation room and vacuum separation tower, described coarse filter is at least 2, described oil-feed pump and the first motor are connected, and driven by the first motor, described heater is far-infrared heater, the lower end of described oil-water separation room is linked with flume, described flume and oil-water separation room are externally connected with water-level gauge, the lower end of described vacuum separation tower is provided with 2 liquid level controllers, described liquid level controller is arranged one on the other, it is respectively upper liquid level controller and lower liquid level controller；
The lower end of described flume is provided with first row waterpipe, first row water valve on described first row waterpipe, described vacuum separation tower is provided with oil-drain pipe and second row waterpipe, described oil-drain pipe is positioned at the lower end of vacuum separation tower, oil drain pump, check-valves, fine filter and oil extraction flange it is sequentially provided with on oil-drain pipe, described second row waterpipe is positioned at the upper end of vacuum separation tower, and second row waterpipe is sequentially provided with condensation chamber, water knockout drum, storage tank and second row water valve；
Described lower liquid level controller is connected with the first motor, control oil-feed speed, described upper liquid level controller is connected with the second motor, control oil extraction speed, described fine filter is connected with the part inflow pipeline between oil-feed flange and coarse filter by overflow pipe, and overflow pipe is provided with overflow valve, is provided with condenser in described condensation chamber, and connect vacuum lead, described vacuum lead is sequentially provided with vacuum valve and vacuum pump；
Further, it is provided with observation window between described 2 liquid level controllers；
Further, diversion it is marked with in advance in described flume；
Further, being provided with sampling pipe between described fine filter and oil extraction flange, described sampling pipe is provided with sampling valve.
The beneficial effects of the utility model are:
A kind of High-viscosity vacuum oil purifier system that the utility model proposes, including the oil-feed flange being connected by inflow pipeline, coarse filter, oil-feed pump, heater, oil-water separation room and vacuum separation tower, the lower end of flume is provided with first row waterpipe, vacuum separation tower is provided with oil-drain pipe and second row waterpipe, it is sequentially provided with condensation chamber on second row waterpipe, water knockout drum, storage tank and second row water valve, this utility model simple in construction, reasonable in design, with vacuum outgas be evaporated under reduced pressure as principle, solve high-viscosity oil due to viscosity higher, the surface tension of flowable difference and fluid is bigger, the technological difficulties being not readily separated, reduction vaporization is combined with vacuum separation simultaneously, efficiently slough large quantity of moisture in oil, the fluid maximum water content processed is up to 25%.
Accompanying drawing explanation
Fig. 1 this utility model schematic diagram.
Detailed description of the invention
A kind of High-viscosity vacuum oil purifier system as depicted, it is characterized in that, including passing sequentially through the oil-feed flange 2 that inflow pipeline 1 is connected, coarse filter 3, oil-feed pump 4, heater 5, oil-water separation room 6 and vacuum separation tower 7, described coarse filter 3 at least 2, described oil-feed pump 4 is connected with the first motor 8, and driven by the first motor 8, described heater 5 is far-infrared heater, the lower end of described oil-water separation room 6 is linked with flume 9, described flume 9 is externally connected with water-level gauge 10 with oil-water separation room 6, the lower end of described vacuum separation tower 7 is provided with 2 liquid level controllers 11, described liquid level controller 11 is arranged one on the other, it is respectively upper liquid level controller 12 and lower liquid level controller 13；
The lower end of described flume 9 is provided with first row waterpipe 14, first row water valve 15 on described first row waterpipe 14, described vacuum separation tower 7 is provided with oil-drain pipe 16 and second row waterpipe 17, described oil-drain pipe 16 is positioned at the lower end of vacuum separation tower 7, oil drain pump 18 it is sequentially provided with on oil-drain pipe 16, check-valves 19, fine filter 20 and oil extraction flange 21, described oil drain pump 18 is connected with the second motor 26, and driven by the second motor 26, described second row waterpipe 17 is positioned at the upper end of vacuum separation tower 7, condensation chamber 22 it is sequentially provided with on second row waterpipe 17, water knockout drum 23, storage tank 24 and second row water valve 25；
Described lower liquid level controller 13 is connected with the first motor 8, control oil-feed speed, described upper liquid level controller 12 is connected with the second motor 26, control oil extraction speed, described fine filter 20 is connected with the part inflow pipeline 1 between oil-feed flange 2 and coarse filter 3 by overflow pipe 27, and overflow pipe 27 is provided with overflow valve 28, is provided with condenser 29 in described condensation chamber 22, and connect vacuum lead 30, described vacuum lead 30 is sequentially provided with vacuum valve 31 and vacuum pump 32；
Further, it is provided with observation window 33 between described 2 liquid level controllers 11；
Further, diversion it is marked with in advance in described flume 9；
Further, being provided with sampling pipe 34 between described fine filter 20 and oil extraction flange 21, described sampling pipe 34 is provided with sampling valve 35.
Simultaneously, the filter element of coarse filter of the present utility model is for make for stainless steel cloth, filter element aperture is 200 mesh, vacuum pump is the original-pack pump using Siemens Company, performance, effect are all greatly improved than domestic pump, oil-feed pump and oil drain pump are purchased in Sino-Japan joint quay gear pump factory, the filter element of fine filter then have employed the stainless steel cloth felt of current domestic blank and folds formula filter element, energy repeated washing, filtering traffic is big, pollutant holding capability is big, and filtering accuracy is high, and after this filter element filtering, oil cleanliness factor is up to NAS standard 6 grades.
Operation principle of the present utility model is:
nullContaminated oil enters inflow pipeline，First pass around at least two group coarse filters and remove the mechanical admixture of larger particles，Internal fluid is heated by heater via，When fluid is heated to uniform temperature，Because oil is different with the coefficient of expansion of water，Density contrast can quickly increase，Thus accelerate " water-in-oil type "、The destruction of " oil-in-water type " liquid film，Heating simultaneously makes oil viscosity reduce，Be conducive to gathering and the sedimentation of the globule，Deep fat enters oil-water separation room unhurried current subsequently、Off-load，And in the centrifugal chamber of oil-water separation room, carry out slight being centrifuged in rotating eccentricity mode，Slight centrifugal action only makes fluid film deform，Tapered，And do not make fluid stir and make muddy，Owing to the adhesion of oil with water declines，And oil is different from the proportion of water，Oil-water separation indoor tiny scattered water droplet combination accumulates the increasing globule，Under vortex and gravity act on jointly，The conical surface tapered by fluid film collects to the vertex of a cone，Finally it is deposited to the bottom of oil-water separation room，Owing to flume being marked with diversion in advance，Under affinity effect，Coil neutralization moisture can be made to converge with the water in flume，Vortex-like fluid enters vacuum separation tower the most step by step，The fluid of preliminary purification enters vacuum separation tower，And under it acts on，Remaining aqueous in oil is carried out vacuum degree of depth separation，The fluid being relatively dried is discharged through oil drain pump，And further filter out trickle solid impurity by fine filter.
The above; it is only this utility model preferably detailed description of the invention; but protection domain of the present utility model is not limited thereto; any those familiar with the art is in the technical scope that this utility model discloses; the change that can readily occur in or replacement, all should contain in protection domain of the present utility model.Therefore, protection domain of the present utility model should be as the criterion with the protection domain of claims.
Claims (4)
1. a High-viscosity vacuum oil purifier system, it is characterized in that, including passing sequentially through the oil-feed flange that inflow pipeline is connected, coarse filter, oil-feed pump, heater, oil-water separation room and vacuum separation tower, described coarse filter is at least 2, described oil-feed pump and the first motor are connected, and driven by the first motor, described heater is far-infrared heater, the lower end of described oil-water separation room is linked with flume, described flume and oil-water separation room are externally connected with water-level gauge, the lower end of described vacuum separation tower is provided with 2 liquid level controllers, described liquid level controller is arranged one on the other, it is respectively upper liquid level controller and lower liquid level controller；
The lower end of described flume is provided with first row waterpipe, first row water valve on described first row waterpipe, described vacuum separation tower is provided with oil-drain pipe and second row waterpipe, described oil-drain pipe is positioned at the lower end of vacuum separation tower, oil drain pump, check-valves, fine filter and oil extraction flange it is sequentially provided with on oil-drain pipe, described second row waterpipe is positioned at the upper end of vacuum separation tower, and second row waterpipe is sequentially provided with condensation chamber, water knockout drum, storage tank and second row water valve；
Described lower liquid level controller is connected with the first motor, control oil-feed speed, described upper liquid level controller is connected with the second motor, control oil extraction speed, described fine filter is connected with the part inflow pipeline between oil-feed flange and coarse filter by overflow pipe, and overflow pipe is provided with overflow valve, is provided with condenser in described condensation chamber, and connect vacuum lead, described vacuum lead is sequentially provided with vacuum valve and vacuum pump.
A kind of High-viscosity vacuum oil purifier system the most according to claim 1, it is characterised in that be provided with observation window between described 2 liquid level controllers.
A kind of High-viscosity vacuum oil purifier system the most according to claim 1, it is characterised in that be marked with diversion in described flume in advance.
A kind of High-viscosity vacuum oil purifier system the most according to claim 1, it is characterised in that being provided with sampling pipe between described fine filter and oil extraction flange, described sampling pipe is provided with sampling valve.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201521108281.9U CN205435173U (en) | 2015-12-29 | 2015-12-29 | High viscosity vacuum oil purifier system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201521108281.9U CN205435173U (en) | 2015-12-29 | 2015-12-29 | High viscosity vacuum oil purifier system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205435173U true CN205435173U (en) | 2016-08-10 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201521108281.9U Expired - Fee Related CN205435173U (en) | 2015-12-29 | 2015-12-29 | High viscosity vacuum oil purifier system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205435173U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115228189A (en) * | 2022-07-08 | 2022-10-25 | 中天钢铁集团有限公司 | Steel rolling wire thin oil station oil purification device and control method thereof |
-
2015
- 2015-12-29 CN CN201521108281.9U patent/CN205435173U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115228189A (en) * | 2022-07-08 | 2022-10-25 | 中天钢铁集团有限公司 | Steel rolling wire thin oil station oil purification device and control method thereof |
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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: 20211229 |