CN203384055U - Mechanical rotor vacuum pump system for one-way oil supply and lubricating sealing - Google Patents
Mechanical rotor vacuum pump system for one-way oil supply and lubricating sealing Download PDFInfo
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- CN203384055U CN203384055U CN201320475218.3U CN201320475218U CN203384055U CN 203384055 U CN203384055 U CN 203384055U CN 201320475218 U CN201320475218 U CN 201320475218U CN 203384055 U CN203384055 U CN 203384055U
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Abstract
The utility model relates to an oil-sealed or dry acting mechanical rotor vacuum pump for reduction vaporization, and particularly relates to a mechanical rotor vacuum pump system for one-way oil supply and lubricating sealing. The mechanical rotor vacuum pump system comprises a mechanical rotor vacuum pump, wherein the mechanical rotor vacuum pump comprises a rotor, a rotor cavity, a suction channel and an exhaust channel; the suction channel and the exhaust channel are respectively communicated with the rotor cavity; the mechanical rotor vacuum pump is provided with a clean oil tank and a slop tank; an oil outlet of the clean oil tank is communicated with the rotor cavity through an oil supply pipeline; an oil inlet of the slop tank is communicated with the rotor cavity through an oil discharge pipeline and a gas-liquid separator orderly; an exhaust port is formed in the upper part of the gas-liquid separator. By adopting the mechanical rotor vacuum pump system, the actual acting pumping rate of the one-way oil supply vacuum pump can be increased; the vacuum degree can be greatly improved, so that the work temperature of the one-way oil supply vacuum pump is kept within the optimal work temperature range; the damage of dirty lubricating oil to the function of the one-way oil supply vacuum pump is completely casted off.
Description
Technical field
The utility model relates to the mechanical rotor vacuum pump, particularly a kind of mechanical rotor vacuum pump system of one way fuel feeding lubrication and seal for the oil seal type of reduction vaporization or dry type acting.
Background technique
Reduction vaporization is the preferred option in current purification field, by the enforcement of this scheme, not only can save and heat energy, can also save the refrigeration energy, can also suppress the pyrolysis of feed liquid (material be distilled) simultaneously,
The urgent serious hope of people obtains the reduction vaporization vacuum technique that cost performance is higher thus.
The mechanical rotor vacuum pump of oil seal type or dry type acting, be rotated the cutting operation by rotor and make formed space between rotor and rotor cavity size occur or move to change and realize acting in the rotor cavity, but not by coordinate operation to realize the liquid-ring vacuum pump of acting with working solution.
The dry-type mechanical rotator vacuum pump is mainly by housing, be arranged at the rotor cavity within housing, the main acting such as air intake passage and the exhaust passage be communicated with the rotor cavity and the rotor that is placed in rotor inside cavity parts form, it only relies on rotor can realize acting with the relative running cutting operation between the rotor cavity, and at present typical dry-type mechanical rotator vacuum pump has Roots pump, screw vacuum pump etc.
Oil seal type mechanical rotor vacuum pump is on the dry-type mechanical rotator vacuum pump mainly does work the basis of parts, increased again gas-liquid separator (also claiming fuel reserve tank), gas-liquid separator is placed in the side of rotor cavity, inside is loaded with lubricant oil appropriate and periodic replacement, the gas-liquid separator bottom is provided with oil-feed port and communicates with the rotor cavity, inside communicates with the exhaust passage outlet, upper end is communicated with the exhaust outlet communicated with the external world, lower end is communicated with the oil drain out be isolated from the outside, it not only relies on rotor and moves and do work with the relative running cutting between the rotor cavity, also need the lubricant oil in gas-liquid separator both to serve as lubricant medium, also serve as sealing medium, running clearance between rotor and rotor cavity is sealed, the quality of lubricants performance not only is related to the working life of mechanical rotor vacuum pump thus, also be related to the size of the mechanical rotor vacuum pump speed of exhaust and the height of degree of vacuum, at present typical oil seal type mechanical rotor vacuum pump has sliding valve vacuum pump and trochoid vacuum pump etc.
If above-mentioned dry-type mechanical rotator vacuum pump is carried out to work for the vacuum field of reduction vaporization, because having sealing medium, the dry-type mechanical rotator vacuum pump do not participate in sealing so, so must keep less free gap between rotor and rotor cavity, certainly lead to thus following drawback:
Although 1. between rotor and rotor cavity, kept less free gap, leakage is caused in less gap at last, must sacrifice certain speed of exhaust and degree of vacuum thus.
2. the mechanical rotor vacuum pump is to rely on air-breathing acting and the exhaust of rotor in the rotor cavity to do work omnidistance acting, when carrying out the exhaust acting, pumped gas must be compressed, and pumped gas inevitable heat of compression that outwards discharges when compressed, when the heat of compression be released acts between rotor and rotor cavity, the outwards heat radiation simultaneously of rotor cavity, and the heat of rotor is difficult to outwards discharge, now the thermal expansion coefficient of rotor will be greater than the thermal expansion coefficient of rotor cavity, the less free gap of both maintenances is occupied by the rotor that is expanded thus, finally can not make rotor normally operation in the rotor cavity, otherwise can only be by adding the free gap between greater trochanter and rotor cavity or reducing operating pressure differential, can not make thus the mechanical rotor vacuum pump enter efficient working state.
3. the corrosion dirt (solid formation) that the free gap kept between rotor and rotor cavity is very easy to be carried secretly in pumped gas occupies, and can not make thus the mechanical rotor vacuum pump keep permanent clean running state.
If above-mentioned oil seal type mechanical rotor vacuum pump is carried out to work for the vacuum field of reduction vaporization, certainly leads to following drawback:
In exhaust acting process, because the rising of air pressure is very easy, coagulated both vapor compression in pumped gas is liquefied and sneaks in lubricant oil with other corrosion dirt (solid formation), because can not absorbing, lubricant oil appropriate and periodic replacement continues the heat of compression produced, not only make thus mechanical rotor vacuum pump temperature significantly raise, also will make the degree of purity of lubricant oil contaminated deteriorated rapidly, contaminated deteriorated lubricant oil not only affects its lubricity, in air-breathing acting process, because reducing, air pressure is very easy to make to sneak into the coagulated steam that is liquefied in lubricant oil vaporization again, significantly reduce the speed of exhaust and the degree of vacuum of mechanical rotor vacuum pump, and the corrosion dirt of sneaking in lubricant oil will forever retain in lubricant oil, toward and under the operating mode that renews, the vapourizing temperature of lubricant oil (being become the temperature of gas phase states of matter by the liquid phase states of matter) is not only more and more lower, moisture content in it and corrosion dirt are by cumulative, moisture content will constantly corrode various metals and continue to produce new corrosion dirt, cumulative corrosion dirt not only affects the mobility of lubricant oil, also be very easy to stop up oil circuit, thus, if can not keep the degree of purity of lubricant oil, the mechanical rotor vacuum pump is difficult to realize in the reduction vaporization field application efficiently so, although having installed cold-trap additional at the suction end of mechanical rotor vacuum pump, some technician can coagulate steam for catching, some technician has been installed gas ballast valve additional on the cavity of mechanical rotor vacuum pump can coagulate steam for discharge, but still can not thoroughly break away from the infringement of dirty lubricant oil for mechanical rotor vacuum pump function.
The model utility content
The utility model is intended to solve the described problem of background technique, and provide a kind of mechanical rotor vacuum pump and absolute oil tank and slop tank to support the use, thoroughly to break away from the mechanical rotor vacuum pump system of dirty lubricant oil to the one way fuel feeding lubrication and seal of vacuum pump function infringement.
Realize that the technological scheme that the utility model purpose adopts is:
A kind of mechanical rotor vacuum pump system of one way fuel feeding lubrication and seal, comprise the mechanical rotor vacuum pump, described mechanical rotor vacuum pump comprises rotor, rotor cavity, the air intake passage and the exhaust passage that are communicated with the rotor cavity respectively, described mechanical rotor vacuum pump disposes absolute oil tank and slop tank, the oil outlet of described absolute oil tank is communicated with the rotor cavity by oil supply line, the filler opening of described slop tank is communicated with the rotor cavity by delivery pipeline, gas-liquid separator successively, and described gas-liquid separator top is provided with relief opening.
Adopt the utility model of technique scheme, its outstanding effect is: in the rotor cavity and between each movable part, efficiently performance is lubricated not only to make pure lubricant oil, sealing, rust inhibition, can also ensure that the lubricant oil under high vacuum can not fill air-breathing acting space because being vaporized, performance is cleaned, after cooling effect, contaminated dirty lubricant oil is discharged into gas-liquid separator with pumped gas by the rotor cavity, not only can improve thus the actual acting speed of exhaust of one way for oil vacuum pump, gas clean-up significantly, one way is remained in best operating temperature range for the operating temperature of oil vacuum pump, thoroughly break away from the infringement for the oil vacuum pump function for one way of dirty lubricant oil.
The technological scheme that realizes the utility model purpose also can have following preferred version:
Described mechanical rotor vacuum pump is sliding valve vacuum pump.
Described mechanical rotor vacuum pump is sliding valve vacuum pump, and the oil outlet of described absolute oil tank passes through oil supply line and is communicated with the rotor cavity via the rotor bearing gap.
Described mechanical rotor vacuum pump is Roots pump, and the oil outlet of described absolute oil tank is communicated with the air intake passage of described rotor cavity by the external oil supply line of the pump housing, and the exhaust passage outlet of described rotor cavity is communicated with the oil and gas import of described gas-liquid separator.
Described mechanical rotor vacuum pump is screw vacuum pump, and the oil outlet of described absolute oil tank is communicated with the air intake passage of described rotor cavity by the external oil supply line of the pump housing, and the exhaust passage outlet of described rotor cavity is communicated with the oil and gas import of described gas-liquid separator.
Between described absolute oil tank and rotor cavity oil supply line on the metering charging pump is housed.
The outlet of described slop tank is communicated with the evaporation feed liquor mouth of decompression distillation device by the first discharge valve and the first discharge line.
The vaporizer bottom discharge gate of described decompression distillation device is communicated with the import of absolute oil tank via corrosion dirt decontaminating separator by the second discharge valve and the second discharge line.
Described corrosion dirt decontaminating separator is a kind of subsiding and purifying separator, and the container that it has respectively sump oil import and absolute oil outlet by a side forms, and described container bottom is provided with corrosion fouling products floss hole and vent valves.
Described corrosion dirt decontaminating separator is a kind of filtration, purification separator, the container that it has respectively sump oil import and absolute oil outlet by a side forms, described container bottom is provided with corrosion fouling products floss hole and vent valves, described internal tank is equipped with container intracavity is divided into to two-part screen filtration sheet, the part of container is communicated with sump oil import and corrosion fouling products floss hole respectively, and another part of container is communicated with the absolute oil outlet.
The accompanying drawing explanation
Fig. 1 is the utility model embodiment 1 structural representation.
Fig. 2 is the utility model embodiment 2 structural representations.
Fig. 3 is the utility model embodiment 3 structural representations.
Fig. 4 is the utility model embodiment 4 structural representations.
Fig. 5 is the utility model embodiment 5 structural representation.
Fig. 6 is the utility model embodiment 6 structural representation.
Fig. 7 is the utility model embodiment 7 structural representation.
Fig. 8 is the structural representation of subsiding and purifying separator in embodiment 7.
Fig. 9 is the structural representation of filtration, purification separator in embodiment 7.
In figure: sliding valve vacuum pump 1, rotor cavity 2, rotor 3, oil drain out 4, delivery pipeline 5, slop tank 6, absolute oil tank 7, external oil supply line 8, oil-feed port 9, built-in oil supply line 10, relief opening 11, gas-liquid separator 12, exhaust passage 13, air intake passage 14, rotor bearing 15, Roots pump 16, screw vacuum pump 17, metering charging pump 18, the first discharge valve 19, the first discharge line 20, the second discharge valve 21, vaporizer 22, condenser 23, fraction collecting tank 24, exhaust line 25, vacuum pump 26, corrosion dirt decontaminating separator 27, the second discharge line 28, sump oil import 29, corrosion fouling products floss hole 30, vent valves 31, absolute oil outlet 32, screen filtration sheet 33.
Oil supply line had herein both comprised external oil supply line 8, also comprised built-in oil supply line 10.
Embodiment
Further set forth the utility model below by embodiment, purpose only is to understand better the utility model content.
Embodiment 1:
Referring to Fig. 1, what the mechanical rotor vacuum pump in the present embodiment adopted is sliding valve vacuum pump 1.Sliding valve vacuum pump 1 has the gas-liquid separator 12 become one with it, air intake passage 14 the inners of sliding valve vacuum pump 1 have by inside the slide bar that hollow passageway and lower end have a through hole and are communicated with rotor cavity 2, its exhaust passage 13 imports are communicated with rotor cavity 2 upper ends, exhaust passage 13 outlets are placed in gas-liquid separator 12 inner chambers, are respectively arranged with oil drain out 4, oil-feed port 9 and relief opening 11 on gas-liquid separator 12 housings.
The oil outlet of absolute oil tank 7 is the built-in oil supply line 10 of the external oil supply line 8 by pump housing outside, the oil-feed port 9 on gas-liquid separator 12 housings, gas-liquid separator 12 inside successively, and via air intake passage 14 and rotor cavity 2 internal communication; Oil drain out 4 on gas-liquid separator 12 housings is communicated with slop tank 6 by the delivery pipeline 5 of pump housing outside.
The effect of above-mentioned slop tank 6 is in fact the volume that increases gas-liquid separator 12, in specific embodiments, can omit slop tank 6 by the gas-liquid separator 12 that uses larger volume.In the technological scheme of omitting slop tank 6, the oil drain out 4 that gas-liquid separator 12 lower ends arrange is equivalent to the sump oil outlet of slop tank 6, therefore, omit the technological scheme of slop tank 6 at the gas-liquid separator 12 that uses larger volume, should be considered as within the technical solution of the utility model category.
As shown in Figure 1, rotor 3 moves in the direction of the clock in rotor cavity 2, when slide bar runs to lower dead center in the guiding valve guide rail, space in rotor cavity 2 is divided into two equal portions by rotor 3, a copy of it is the air-breathing acting space communicated with air intake passage 14 by guiding valve, wherein another part is the exhaust acting space communicated with gas-liquid separator 12 by exhaust passage 13, when slide bar runs to top dead center in the guiding valve guide rail, exhaust acting space in rotor cavity 2 will realize maximizing, air-breathing acting space in rotor cavity 2 will produce thus simultaneously, make rotor 3 move and realize continuing acting by circumgyration incision within rotor cavity 2.
When rotor 3 during in the interior lasting acting of rotor cavity 2, the pure lubricant oil of absolute oil tank 7 interior fillings will supply in rotor cavity 2 via oil-feed port 9 continuously, not only make between pure lubricant oil each movable part in rotor cavity 2 that efficient performance is lubricated, sealing, rust inhibition, can also ensure that lubricant oil under high vacuum can not be vaporized and fills air-breathing acting space.After performance cleaning, cooling effect, contaminated dirty lubricant oil is discharged into gas-liquid separator 12 with pumped gas by rotor cavity 2, not only can improve thus the actual acting speed of exhaust of one way for oil vacuum pump, gas clean-up significantly, one way is remained in best operating temperature range for the operating temperature of oil vacuum pump, thoroughly break away from the infringement for the oil vacuum pump function for one way of dirty lubricant oil.
Pure lubricant oil by oil-feed port 9 inputs carries out work in pumped gas, necessarily can coagulate steam and other corrosion dirt (solid formation) from containing in the pumped gas of reduction vaporization, the lubricant oil participated in after air-breathing acting participates in the exhaust acting then, now the residing air pressure environment of lubricant oil becomes malleation by negative pressure, the coagulated both vapor compression liquefaction of the coagulated steam contained in pumped gas in being very easy to it under positive pressure is also sneaked into lubricant oil with other corrosion dirt, under the effect that dirty lubricant oil after contaminated does work for oil vacuum pump in one way, with pumped gas, by rotor cavity 2, via exhaust passage 13, be discharged in gas-liquid separator 12, dirty lubricant oil is under the effect of self gravitation, by gas-liquid separator 12 collected and be discharged into slop tank 6 via oil drain out 4 within, pumped gas is discharged into the external world by the relief opening 11 of gas-liquid separator 12 upper ends.
In order to prevent that the interior dirty lubricant oil after contaminated in exhaust passage 13 from flowing back to rotor cavity 2 again, can be in exhaust passage 13 import part one-way valve is installed or is changed the exhaust angle.
In above-mentioned working procedure, the pure lubricant oil of constantly being inputted by oil-feed port 9, not only can guarantee can not fill air-breathing acting space and bring into play lubricated, seal action because being vaporized under the high vacuum of air-breathing acting, it can also can coagulate the liquefaction produced under the positive pressure environment of exhaust acting steam, the heat of compression and other corrosion dirt and be absorbed and bring into play cleaning, cooling, the effect such as antirust, the final cleaning inside of one way for oil vacuum pump that not only can keep, can also make it keep efficient acting under best state.
Embodiment 2:
Referring to Fig. 2, embodiment 2 only is with embodiment 1 difference, the oil outlet of absolute oil tank 7 is the built-in oil supply line 10 of the external oil supply line 8 by pump housing outside, the oil-feed port 9 on gas-liquid separator 12 housings, gas-liquid separator 12 inside successively, and be communicated with rotor cavity 2 via rotor bearing 15 gaps, exhaust passage 13 outlets are placed in described gas-liquid separator 12 inner chambers.
Based on said structure, lubricant oil is preferentially to the rotor bearing 15 at rotor 3 two ends, to supply oil lubrication by built-in oil supply line 10, not only further improved thus the lubricated environment of rotor bearing 15, also make lubricant oil be entered the inside of rotor cavity 2 by the two ends of rotor cavity 2, from and further improved lubricant oil in rotor cavity 2 and the distributivity between each movable part.
Embodiment 3:
Referring to Fig. 3, the mechanical rotor vacuum pump in the present embodiment adopts Roots pump 16.The rotor 3 of Roots pump 16 is by two synchronous operated concave-convex shape rotor 3 mix proportions, in the process of running, left side rotor 3 turns round in the counterclockwise direction, right side rotor 3 turns round along clockwise direction, unlatching by two rotor 3 male and fomale(M&F)s realizes air-breathing acting, the space that concave surface by rotor 3 and rotor cavity 2 the form transition operation that realizes bleeding, closure by two rotor 3 male and fomale(M&F)s realizes the exhaust acting, being rotated cutting operation in rotor cavity 2 by rotor 3 makes between rotor 3 and rotor cavity 2 formed space that size occurs and mobile the variation realized what whole process was done work.
The air intake passage 14 of Roots pump 16 (being positioned at pump housing upper end) sidepiece arranges oil-feed port 9, and the oil outlet of absolute oil tank 7 is communicated with oil-feed port 9 by the external oil supply line 8 of pump housing outside, and is communicated with rotor cavity 2 via air intake passage 14; The exhaust passage 13 of Roots pump 16 (being positioned at pump housing lower end) outlet is communicated with the oil and gas import of external gas-liquid separator 12, gas-liquid separator 12 case top are provided with oil and gas import, case top one side arranges relief opening 11, housing bottom arranges oil drain out 4, and is communicated with slop tank 6 by delivery pipeline 5.
Based on said structure, enter rotor cavity 2 by the pure lubricant oil of oil-feed port 9 input by pump housing upper end, the dirty lubricant oil after contaminated enters gas-liquid separator 12 by pump housing lower end.The lubricant oil that enters rotor cavity 2 not only can guarantee can not fill air-breathing acting space and bring into play lubricated, seal action because being vaporized under the high vacuum of air-breathing acting, it can also can coagulate the liquefaction produced under the positive pressure environment of exhaust acting steam, the heat of compression and other corrosion dirt and be absorbed and bring into play cleaning, cooling, the effect such as antirust, the final cleaning inside of one way for oil vacuum pump that not only can keep, can also make it keep efficient acting under best state, widen therefrom the adaptability for working condition of this pump type.
Embodiment 4:
Referring to Fig. 4, mechanical rotor vacuum pump in the present embodiment is screw vacuum pump 17, the rotor 3 of screw vacuum pump 17 is by two mutual meshing, synchronous operated screw rod mix proportions, one of them screw flight be dextrorotation to, another screw flight is counterclockwise rotation direction, two screw rods are in the process of running, and a screw rod turns round in the counterclockwise direction, and another screw rod turns round along clockwise direction.Between two screw flights, formed gap space is the space of bleeding, and the mutual meshing point between two screw rods is the cutting sealing point of bleeding, and the mutual meshing line between two screw rods is the cutting sealing line of bleeding.
The air intake passage 14 of screw vacuum pump 17 (being positioned at pump housing right-hand member) sidepiece arranges oil-feed port 9, and the oil outlet of absolute oil tank 7 is communicated with oil-feed port 9 by the external oil supply line 8 of pump housing outside, and is communicated with rotor cavity 2 via air intake passage 14; The exhaust passage 13 of screw vacuum pump 17 (being positioned at pump housing left end) outlet is communicated with the oil and gas import of external gas-liquid separator 12, gas-liquid separator 12 case top are provided with oil and gas import, case top one side arranges relief opening 11, housing bottom arranges oil drain out 4, and is communicated with slop tank 6 by delivery pipeline 5.
Based on said structure, pumped gas, in the space of bleeding, under the shutoff of the cutting sealing line of bleeding, moves the inside that carries over rotor cavity 2 from right to left, and air-breathing acting is that the right-hand part at the pump housing completes, and the exhaust acting is what in the left side of the pump housing, to complete.Pure lubricant oil by oil-feed port 9 input enters rotor cavity 2 by pump housing right-hand member, and the dirty lubricant oil after contaminated enters gas-liquid separator 11 by pump housing lower end.The lubricant oil that enters rotor cavity 2 not only can guarantee can not fill air-breathing acting space and bring into play lubricated, seal action because being vaporized under the high vacuum of air-breathing acting, it can also can coagulate the liquefaction produced under the positive pressure environment of exhaust acting steam, the heat of compression and other corrosion dirt and be absorbed and bring into play cleaning, cooling, the effect such as antirust, the final cleaning inside of one way for oil vacuum pump that not only can keep, can also make it keep efficient acting under best state, widen therefrom the adaptability for working condition of this pump type.
Embodiment 5:
Referring to Fig. 5, embodiment 5 is on embodiment 1 basic structure, between absolute oil tank 7 and rotor cavity 2 oil supply line on be equipped with the metering charging pump 18.Specifically at absolute oil tank 7, to the external oil supply line 8 between oil-feed port 9, metering charging pump 18 is housed.
Based on said structure, not only do not limit the fuel feeding drop of absolute oil tank 7 and mechanical rotor vacuum pump, also can provide required optimum oil feeding for the mechanical rotor vacuum pump by metering charging pump 18.
According to embodiment 5, in embodiment 2, embodiment 3 and embodiment 4, metering charging pump 18 all can be housed on oil supply line, to realize the best fuel feeding control to vacuum pump, above-mentioned oil supply line had both comprised external oil supply line 8, also comprised built-in oil supply line 10.
Embodiment 6:
Referring to Fig. 6, embodiment 6 is on embodiment 1 basic structure, and the outlet of slop tank 6 is communicated with vaporizer 22 material feeding mouths of decompression distillation device by the first discharge valve 19 and the first discharge line 20.
The distilation device that decompression distillation device in the present embodiment is comprised of the second discharge valve 21, vaporizer 22, condenser 23, fraction collecting tank 24, exhaust line 25 and vacuum pump 26.
Under the effect of vacuum pump 26 suctions, absorb under positive pressure liquefaction and can coagulate steam, the dirty lubricant oil of the heat of compression and other corrosion dirt, outlet via slop tank 6 enters in the vaporizer 22 of decompression distillation device by the first discharge valve 19 and the first discharge line 20, when reaching 3/5ths left and right of vaporizer 22 volumes, the dirty lubricant oil in entering vaporizer 22 closes the first discharge valve 19, the radiator body of opening in vaporizer 22 carries out heat release and makes it carry out vaporization under the air pressure of vacuum to the dirty lubricant oil in vaporizer 22, under the effect of condenser 23, the gas phase distillate that is vaporized evaporation is cooled into liquid phase distillate collected by fraction collecting tank 24, the waste gas liquefied that can not be cooled is discharged into the external world via exhaust line 25 by vacuum pump 26.
Preferential evaporation and collected by fraction collecting tank 24 be the light components of low-boiling-point substance such as coagulated steam in dirty lubricant oil, moisture.
Later stage evaporation and collected by fraction collecting tank 24 be the lubricant oil component in dirty lubricant oil.
Component remaining after evaporation is the corrosion dirt in dirty lubricant oil.
Based on said structure, not only can utilize in dirty lubricant oil the heat of compression absorbed and save the part of heat energy energy consumption, the low-boiling-point substance in dirty lubricant oil can also be distilled and realizes efficiently separation by whole process light component, lubricant oil component and corrosion dirt.
Embodiment 7:
Referring to Fig. 7, embodiment 7 is on embodiment 6 basic structure, and the vaporizer of decompression distillation device 22 bottom discharge gates are communicated with the import of absolute oil tank 7 via corrosion dirt decontaminating separator 27 by the second discharge valve 21 and the second discharge line 28.
Under the effect of vacuum pump 26 suctions, absorb under positive pressure liquefaction and can coagulate steam, the dirty lubricant oil of the heat of compression and other corrosion dirt, outlet via slop tank 6 enters in the vaporizer 22 of decompression distillation device by the first discharge valve 19 and the first discharge line 20, when reaching 3/5ths left and right of vaporizer 22 volumes, the dirty lubricant oil in entering vaporizer 22 closes the first discharge valve 19, the radiator body of opening in vaporizer 22 carries out heat release to the dirty lubricant oil in vaporizer 22, make the coagulated steam in it, the light component of the low-boiling-point substances such as moisture carries out vaporization under the air pressure of vacuum, under the effect of condenser 23, the gas phase distillate that is vaporized evaporation is cooled into liquid phase distillate collected by fraction collecting tank 24, the waste gas liquefied that can not be cooled is discharged into the external world via exhaust line 25 by vacuum pump 26.
The light components of low-boiling-point substance such as the coagulated steam in dirty lubricant oil, moisture are evaporated when complete, stop the radiator body heat release, open the second discharge valve 21, make the dirty lubricant oil that removes the light component of low-boiling-point substance enter corrosion dirt decontaminating separator 27 by the second discharge line 28, corrosion dirt in dirty lubricant oil is collected by corrosion dirt decontaminating separator 27, and pure lubricant oil is flowed in absolute oil tank 7 by the import of absolute oil tank 7.
Based on said structure, not only can utilize the heat of compression absorbed in dirty lubricant oil and save the part of heat energy energy consumption, also can remove the light component of low-boiling-point substance in dirty lubricant oil by partial distillation, remove dirty lubricant oil internal corrosion dirt by corrosion dirt decontaminating separator 27, thereby under energy-efficient prerequisite and obtain the lubricant oil of reusable edible, and can reduce the pyrolysis that lubricant oil suffers in purification process and destroy.
Referring to Fig. 8, what at the corrosion dirt decontaminating separator 27 described in embodiment 7, adopt is a kind of subsiding and purifying separator.The container that it has respectively sump oil import 29 and absolute oil outlet 32 by a side forms, and described container bottom is provided with corrosion fouling products floss hole 30 and vent valves 31.
The purification mechanism of subsiding and purifying separator is: utilize the physical feature that between corrosion dirt and lubricant oil, proportion has larger difference, under the condition with suitable circulation subsiding and purifying space, corrosion dirt certainty and lubricant oil generation sedimentation separation in dirty lubricant oil, dirty lubricant oil is entered in corrosion dirt decontaminating separator 27 by sump oil import 29, pure lubricant oil is discharged into absolute oil tank 7 via absolute oil outlet 32, and the corrosion dirt is discharged into the external world via corrosion fouling products floss hole 30 and vent valves 31.
Based on said structure, under the prerequisite that does not consume any energy source and power, can make dirty lubricant oil realize solid-liquid separation.
Referring to Fig. 9, what at the corrosion dirt decontaminating separator 27 described in embodiment 7, adopt is a kind of filtration, purification separator.The container that it has respectively sump oil import 29 and absolute oil outlet 32 by a side forms, described container bottom is provided with corrosion fouling products floss hole 30 and vent valves 31, described internal tank is equipped with container intracavity is divided into to two-part screen filtration sheet 33, the part of container is communicated with sump oil import 29 and corrosion fouling products floss hole 30 respectively, and another part of container is communicated with absolute oil outlet 32.Screen filtration sheet 33 can be comprised of the steel mesh filtering material, can also be comprised of the filter-cloth filtering material, also can be comprised of the Filter paper filtering material.
The purification mechanism of filtration, purification separator is: utilize the physical feature that between corrosion dirt and lubricant oil, form has larger difference, under the effect of screen filtration sheet 33, corrosion dirt in dirty lubricant oil will occur to force to separate with lubricant oil, dirty lubricant oil is entered in corrosion dirt purification separation mechanism 27 by sump oil import 29, within pure lubricant oil is discharged into absolute oil tank 7 via absolute oil outlet 32, the corrosion dirt is discharged into the external world via corrosion fouling products floss hole 30 and vent valves 31.
Based on the said apparatus structure, in less space reaches the shorter time, can realize efficient solid-liquid separation.
The description of the various embodiments described above is not all the restriction to technical solutions of the utility model, any according to the utility model design, done only for pro forma but not substantial equivalent transformation all should be considered as the technical solution of the utility model category.
Claims (10)
1. the mechanical rotor vacuum pump system of an one way fuel feeding lubrication and seal, comprise the mechanical rotor vacuum pump, described mechanical rotor vacuum pump comprises rotor, rotor cavity, the air intake passage and the exhaust passage that are communicated with the rotor cavity respectively, it is characterized in that, described mechanical rotor vacuum pump disposes absolute oil tank and slop tank, the oil outlet of described absolute oil tank is communicated with the rotor cavity by oil supply line, the filler opening of described slop tank is communicated with the rotor cavity by delivery pipeline, gas-liquid separator successively, and described gas-liquid separator top is provided with relief opening.
2. the mechanical rotor vacuum pump system of one way fuel feeding lubrication and seal according to claim 1, is characterized in that, described mechanical rotor vacuum pump is sliding valve vacuum pump.
3. the mechanical rotor vacuum pump system of one way fuel feeding lubrication and seal according to claim 1 and 2, it is characterized in that, described mechanical rotor vacuum pump is sliding valve vacuum pump, and the oil outlet of described absolute oil tank passes through oil supply line and is communicated with the rotor cavity via the rotor bearing gap.
4. the mechanical rotor vacuum pump system of one way fuel feeding lubrication and seal according to claim 1, it is characterized in that, described mechanical rotor vacuum pump is Roots pump, the oil outlet of described absolute oil tank is communicated with the air intake passage of described rotor cavity by the external oil supply line of the pump housing, and the exhaust passage outlet of described rotor cavity is communicated with the oil and gas import of described gas-liquid separator.
5. the mechanical rotor vacuum pump system of one way fuel feeding lubrication and seal according to claim 1, it is characterized in that, described mechanical rotor vacuum pump is screw vacuum pump, the oil outlet of described absolute oil tank is communicated with the air intake passage of described rotor cavity by the external oil supply line of the pump housing, and the exhaust passage outlet of described rotor cavity is communicated with the oil and gas import of described gas-liquid separator.
6. the mechanical rotor vacuum pump system of one way fuel feeding lubrication and seal according to claim 1, is characterized in that, between described absolute oil tank and rotor cavity oil supply line on the metering charging pump is housed.
7. the mechanical rotor vacuum pump system of one way fuel feeding lubrication and seal according to claim 1, is characterized in that, the outlet of described slop tank is communicated with the evaporation feed liquor mouth of decompression distillation device by the first discharge valve and the first discharge line.
8. the mechanical rotor vacuum pump system of one way fuel feeding lubrication and seal according to claim 7, it is characterized in that, the vaporizer bottom discharge gate of described decompression distillation device is communicated with the import of absolute oil tank via corrosion dirt decontaminating separator by the second discharge valve and the second discharge line.
9. the mechanical rotor vacuum pump system of one way fuel feeding lubrication and seal according to claim 7, it is characterized in that, described corrosion dirt decontaminating separator is a kind of subsiding and purifying separator, the container that it has respectively sump oil import and absolute oil outlet by a side forms, and described container bottom is provided with corrosion fouling products floss hole and vent valves.
10. the mechanical rotor vacuum pump system of one way fuel feeding lubrication and seal according to claim 7, it is characterized in that, described corrosion dirt decontaminating separator is a kind of filtration, purification separator, the container that it has respectively sump oil import and absolute oil outlet by a side forms, described container bottom is provided with corrosion fouling products floss hole and vent valves, described internal tank is equipped with container intracavity is divided into to two-part screen filtration sheet, the part of container is communicated with sump oil import and corrosion fouling products floss hole respectively, and another part of container is communicated with the absolute oil outlet.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320475218.3U CN203384055U (en) | 2013-04-22 | 2013-08-06 | Mechanical rotor vacuum pump system for one-way oil supply and lubricating sealing |
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201310138583.X | 2013-04-22 | ||
| CN 201310138583 CN103195717A (en) | 2013-04-22 | 2013-04-22 | One-way oil supply and lubrication sealing mechanical rotor vacuum pump system |
| CN201320475218.3U CN203384055U (en) | 2013-04-22 | 2013-08-06 | Mechanical rotor vacuum pump system for one-way oil supply and lubricating sealing |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203384055U true CN203384055U (en) | 2014-01-08 |
Family
ID=48718459
Family Applications (2)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201310138583 Pending CN103195717A (en) | 2013-04-22 | 2013-04-22 | One-way oil supply and lubrication sealing mechanical rotor vacuum pump system |
| CN201320475218.3U Expired - Lifetime CN203384055U (en) | 2013-04-22 | 2013-08-06 | Mechanical rotor vacuum pump system for one-way oil supply and lubricating sealing |
Family Applications Before (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201310138583 Pending CN103195717A (en) | 2013-04-22 | 2013-04-22 | One-way oil supply and lubrication sealing mechanical rotor vacuum pump system |
Country Status (1)
| Country | Link |
|---|---|
| CN (2) | CN103195717A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103352853A (en) * | 2013-04-22 | 2013-10-16 | 吴国存 | One-way oil supply lubricating and sealing mechanical rotor vacuum pump system |
| CN109268268A (en) * | 2018-11-27 | 2019-01-25 | 中国船舶重工集团公司第七0四研究所 | Marine turbing integral type integrates water ring vacuum pump |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111520371B (en) * | 2020-04-30 | 2021-12-21 | 浙江肯特科技股份有限公司 | Self-air-source-control-based oil-supplementing lubricating preparation structure for label washing machine |
-
2013
- 2013-04-22 CN CN 201310138583 patent/CN103195717A/en active Pending
- 2013-08-06 CN CN201320475218.3U patent/CN203384055U/en not_active Expired - Lifetime
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103352853A (en) * | 2013-04-22 | 2013-10-16 | 吴国存 | One-way oil supply lubricating and sealing mechanical rotor vacuum pump system |
| CN103352853B (en) * | 2013-04-22 | 2016-06-29 | 唐山山岛石油化学有限公司 | The mechanical rotor vacuum pump system that one way feed lubrication seals |
| CN109268268A (en) * | 2018-11-27 | 2019-01-25 | 中国船舶重工集团公司第七0四研究所 | Marine turbing integral type integrates water ring vacuum pump |
| CN109268268B (en) * | 2018-11-27 | 2023-09-19 | 中国船舶重工集团公司第七0四研究所 | Integrated water ring vacuum pump of marine steam turbine |
Also Published As
| Publication number | Publication date |
|---|---|
| CN103195717A (en) | 2013-07-10 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20140108 Effective date of abandoning: 20160629 |
|
| C25 | Abandonment of patent right or utility model to avoid double patenting |