CN206008102U - Apparatus for purifying oil products peculiar to vessel - Google Patents
Apparatus for purifying oil products peculiar to vessel Download PDFInfo
- Publication number
- CN206008102U CN206008102U CN201620833630.1U CN201620833630U CN206008102U CN 206008102 U CN206008102 U CN 206008102U CN 201620833630 U CN201620833630 U CN 201620833630U CN 206008102 U CN206008102 U CN 206008102U
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- oil
- valve
- vacuum
- dehydrator
- vessel
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Abstract
The utility model discloses a kind of apparatus for purifying oil products peculiar to vessel, which includes inlet valve etc., oil inlet pipe connects inlet valve, inlet valve is connected with coarse filter, coarse filter is connected with heater, heater is provided with thermometer and is connected with dehydrator, dehydrator outer surface is provided with an observation window and inside is then provided with vacuum separation tank, dehydrator is provided with vacuum meter, it is connected with condenser after vacuum meter connection vacuum valve again, oil gas check valve is provided with below condenser, oil gas check valve is connected with water ring vacuum pump, drain valve is provided with below dehydrator, dehydrator connects fine filter by the pipeline of side, pressure gauge is provided with above fine filter and delivery valve and flowline are connected by pipeline, it is connected with oil outlet pump below fine filter.This utility model can reliably remove the harmful substances such as moisture in poor oil, impurity, gas, and the rapid performance for recovering oil reaches the oil after process and uses standard.
Description
Technical field
This utility model is related to a kind of purifier, more particularly to a kind of apparatus for purifying oil products peculiar to vessel.
Background technology
Oil product clearing machine peculiar to vessel is used for the purified treatment of ship oil product, predominantly makes in electromotor diesel oil and plant equipment
Lubricating oil.Marine diesel oil may be mixed into moisture and mechanical admixture in subpackage and transport, if any more moisture in diesel oil,
The calorific capacity of diesel oil will be reduced in burning, can be frozen at low temperature, so that the fuel feed system blocking of diesel engine, machinery
The presence of impurity may cause oil circuit to block.In plant equipment is used, major part can remain in equipment to marine lubricant
In, it is mixed into impurity, moisture, produces the quality that emulsified water etc. reduces oil, lubricant pollution normally cannot be transported by plant equipment
OK.As the use of ship lubricating oil has to comply with international standard regulation, oil product clearing machine peculiar to vessel has become the indispensability of ship's navigation
Facility.Often using traditional centrifugal oil product purification treatment apparatus, its shortcoming is existing oil product clearing machine peculiar to vessel:To oil
In product, the filtration result of moisture and impurity is poor;Oil after process is treated as waste oil discharge, it is impossible to is circulated recycling, causes
Waste;Noise and vibrations when centrifugal frame for movement runs which is larger.
Utility model content
Technical problem to be solved in the utility model is to provide a kind of apparatus for purifying oil products peculiar to vessel, and which reliably can take off
Except the harmful substances such as the moisture in poor oil, impurity, gas, the rapid performance for recovering oil, reach the oil after process
Using standard.
This utility model is to solve above-mentioned technical problem by following technical proposals:A kind of oil purification dress peculiar to vessel
Put, it is characterised in which includes inlet valve, oil inlet pipe, coarse filter, dehydrator, drain valve, heater, thermometer, vacuum separation
Tank, condenser, oil gas check valve, water ring vacuum pump, oil outlet pump, pressure gauge, fine filter, delivery valve, flowline, observation window, true
Empty table, vacuum valve, oil inlet pipe connect inlet valve, and inlet valve is connected with coarse filter, and coarse filter is connected with heater, is set on heater
There is thermometer and be connected with dehydrator, dehydrator outer surface is provided with an observation window and inside is then provided with vacuum separation tank, be dehydrated
Device is provided with vacuum meter, is connected with condenser again, is provided with oil gas check valve, oil gas below condenser after vacuum meter connection vacuum valve
Check valve is connected with water ring vacuum pump, is provided with drain valve below dehydrator, and dehydrator connects fine filter, essence by the pipeline of side
Pressure gauge is provided with above filter and delivery valve and flowline are connected by pipeline, be connected with oil outlet pump below fine filter.
Preferably, the condenser is provided with water inlet and outlet, and inlet seal is connected to above condenser, water outlet
Mouth is sealedly attached to condenser side.
Preferably, the vacuum separation tank is gathered using compound three-dimensional Steaming structure and by nebulizer, reactor, separation chamber
Fuel tank, aspirating chamber, observation window, fluid level control device composition, separation chamber and oil drain tank composition, the reactor are located at aspirating chamber
Interior, separation chamber is located between reactor and oil drain tank, and oil drain tank sealed bottom connects oil-drain pipe and oil outlet pump.
Preferably, safety glass is adopted on the outside of the vacuum separation tank as observation window.
Preferably, the water ring vacuum pump is configured with vacuum pump bleeding point safety device, water ring vacuum pump and vacuum separation
Fluid level control device in tank forms interlock circuit.
Preferably, the water ring vacuum pump adopts compound three-dimensional Steaming structure.
Preferably, the oil outlet pump selects low-noise oil pump.
Positive effect of the present utility model is:This utility model reliably can remove moisture in poor oil,
The harmful substances such as impurity, gas, the rapid performance for recovering oil, reach the oil after process and use standard.
Description of the drawings
Fig. 1 is structural representation of the present utility model.
Specific embodiment
This utility model preferred embodiment is given below in conjunction with the accompanying drawings, to describe the technical solution of the utility model in detail.
As shown in figure 1, this utility model apparatus for purifying oil products peculiar to vessel includes inlet valve 1, oil inlet pipe 2, coarse filter 3, dehydration
Device 4, drain valve 5, heater 6, thermometer 7, vacuum separation tank 8, condenser 9, oil gas check valve 10, water ring vacuum pump 11, go out
Oil pump 12, pressure gauge 13, fine filter 14, delivery valve 15, flowline 16, observation window 17, vacuum meter 18, vacuum valve 19, oil inlet pipe 2
Connection inlet valve 1, inlet valve 1 is connected with coarse filter 3, and coarse filter 3 is connected with heater 6, heater 6 be provided with thermometer 7 and
It is connected with dehydrator 4,4 outer surface of dehydrator is provided with an observation window 17 and inside is then provided with vacuum separation tank 8, in dehydrator 4
Vacuum meter 18 is provided with, is connected with condenser 9 after the connection vacuum valve 19 of vacuum meter 18 again, below condenser 9, is provided with oil gas check valve
10, oil gas check valve 10 is connected with water ring vacuum pump 11, is provided with drain valve 5, pipe of the dehydrator 4 by side below dehydrator 4
Road connects fine filter 14, is provided with pressure gauge 13 and connects delivery valve 15 and flowline 16, fine straining by pipeline above fine filter 14
It is connected with oil outlet pump 12 below device 14.
Operation principle of the present utility model is as follows:, inlet valve is opened, pending oily under oil-feed pumping action, through coarse filtration
Entering dehydrator after device carries out dehydration pretreatment.Pretreated moisture is discharged through hydrodynamic(al) drain valve, draining pump motivation, and impurity is passed through
Coarse filter blowoff valve is discharged, and pretreated oil enters heater and heated, and impurity is discharged from heater blowoff valve, heat
Oil is changed into the vaporific entrance vacuum separation tank of coarse grain from nebulizer, and moisture starts to evaporate, falls on reactor, in tank under mist of oil
Solid is formed, multifaceted Steaming structure, by circulation in short-term, just can reach purification purpose.Through dehydration, the oil of degassing
Product pass through oil outlet one-way valve in the presence of oil outlet pump, then complete a cycle of operation through fine filter filtration, then by fuel-displaced
Valve is fuel-displaced.Pressure gauge and sampling valve is additionally provided with flowline, the quality condition of pressure and oil in pipeline can be examined
Survey.The water vapour that separates from vacuum separator is suctioned out by vacuum and enters condenser, and most of water vapor is condensed into water and deposits
Enter hydrops storehouse, outside discharge machine, part water vapour and oil dissolved gas then enter water ring vacuum pump by pumping check valve, then true by water ring
Empty pump is discharged.
Condenser 9 is provided with water inlet and outlet, and inlet seal is connected to above condenser 9, and outlet sealing connects
13 side of condenser is connected to, the water circulation in condenser 9 can so substituted, is prevented condenser 9 overheated.
Vacuum separation tank 8 is using compound three-dimensional Steaming structure and by nebulizer, reactor, separation chamber, oil drain tank, pumping
Room, observation window, fluid level control device composition, separation chamber and oil drain tank composition, can so improve evaporation rate, increase profit point
From efficiency;Reactor is located at pumping interior, and separation chamber is located between reactor and oil drain tank, and oil drain tank sealed bottom connects oil extraction
Pipeline and oil outlet pump 12, can so make oil dehydration, degassing, reach clean-up effect.
Pipe outlet is provided with nebulizer, and inflow pipeline exit seal connects into pumping interior, can so allow deep fat to be atomized,
Make oil-water separation.
Safety so ensure that as observation window 17 using safety glass on the outside of vacuum separation tank 8, prevent unexpected sending out
Raw.
Water ring vacuum pump 11 is configured with vacuum pump bleeding point safety device, water ring vacuum pump 11 and liquid in vacuum separation tank 8
Level control device forms interlock circuit, can so improve safety during pumping, increases oil-water separation efficiency.
Water ring vacuum pump 11 increases disengagement area using compound three-dimensional Steaming structure, and very big limit increases oil product in vacuum
Open-assembly time in system.
Test point on flowline installs water content detection unit, detects that fuel-displaced water is dirty using capacitance principle real-time online
Whether dye degree is exceeded.
Oil outlet pump 12 selects low-noise oil pump, and which has good suction capacity, and uniform flow, pulse free, noise are low, make
Use life-span length.
Heater 6 is designed for U-shaped, is wherein configured with automatic thermostatic controller, heating protecting device, can adjust oil
Temperature, prevents heating tank surface paint from damaging, it is ensured that the safety of heating system.
Fine filter 14 and coarse filter 3 improve filtering for moisture and impurity in oil product using vacuum type lubricating oil purifying system
Effect.
In sum, this utility model can reliably remove the harmful substances such as moisture in poor oil, impurity, gas,
The rapid performance for recovering oil, reaches the oil after process and uses standard.
Particular embodiments described above, to the technical problem of solution of the present utility model, technical scheme and beneficial effect
Further described, be should be understood that the foregoing is only specific embodiment of the utility model, not
For limiting this utility model, all within spirit of the present utility model and principle, any modification for being made, equivalent, change
Enter, should be included within protection domain of the present utility model.
Claims (7)
1. a kind of apparatus for purifying oil products peculiar to vessel, it is characterised in which includes inlet valve, oil inlet pipe, coarse filter, dehydrator, draining
Valve, heater, thermometer, vacuum separation tank, condenser, oil gas check valve, water ring vacuum pump, oil outlet pump, pressure gauge, fine straining
Device, delivery valve, flowline, observation window, vacuum meter, vacuum valve, oil inlet pipe connect inlet valve, and inlet valve is connected with coarse filter, slightly
Filter is connected with heater, and heater is provided with thermometer and is connected with dehydrator, and dehydrator outer surface is provided with an observation window
And inside is then provided with vacuum separation tank, dehydrator is provided with vacuum meter, is connected with condenser after vacuum meter connection vacuum valve again, cold
Oil gas check valve is provided with below condenser, and oil gas check valve is connected with water ring vacuum pump, is provided with drain valve, dehydrator below dehydrator
Fine filter is connected by the pipeline of side, pressure gauge is provided with above fine filter and delivery valve and flowline, essence are connected by pipeline
It is connected with oil outlet pump below filter.
2. apparatus for purifying oil products peculiar to vessel as claimed in claim 1, it is characterised in that the condenser is provided with water inlet and goes out
The mouth of a river, inlet seal are connected to above condenser, and outlet is sealedly attached to condenser side.
3. apparatus for purifying oil products peculiar to vessel as claimed in claim 1, it is characterised in that the vacuum separation tank adopts compound solid
Steaming structure by nebulizer, reactor, separation chamber, oil drain tank, aspirating chamber, observation window, fluid level control device composition, separation chamber
Constitute with oil drain tank, the reactor is located at pumping interior, separation chamber is located between reactor and oil drain tank, and oil drain tank bottom is close
Envelope connection oil-drain pipe and oil outlet pump.
4. apparatus for purifying oil products peculiar to vessel as claimed in claim 1, it is characterised in that adopt tempering on the outside of the vacuum separation tank
Glass is used as observation window.
5. apparatus for purifying oil products peculiar to vessel as claimed in claim 1, it is characterised in that the water ring vacuum pump is configured with vacuum pump
Bleeding point safety device, water ring vacuum pump form interlock circuit with the fluid level control device in vacuum separation tank.
6. apparatus for purifying oil products peculiar to vessel as claimed in claim 1, it is characterised in that the water ring vacuum pump adopts compound solid
Steaming structure.
7. apparatus for purifying oil products peculiar to vessel as claimed in claim 1, it is characterised in that the oil outlet pump selects low-noise oil pump.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201620833630.1U CN206008102U (en) | 2016-08-03 | 2016-08-03 | Apparatus for purifying oil products peculiar to vessel |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201620833630.1U CN206008102U (en) | 2016-08-03 | 2016-08-03 | Apparatus for purifying oil products peculiar to vessel |
Publications (1)
Publication Number | Publication Date |
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CN206008102U true CN206008102U (en) | 2017-03-15 |
Family
ID=58245512
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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CN201620833630.1U Active CN206008102U (en) | 2016-08-03 | 2016-08-03 | Apparatus for purifying oil products peculiar to vessel |
Country Status (1)
Country | Link |
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CN (1) | CN206008102U (en) |
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2016
- 2016-08-03 CN CN201620833630.1U patent/CN206008102U/en active Active
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