CN205398577U - Integration lubricating oil reclaimation equipment - Google Patents

Integration lubricating oil reclaimation equipment Download PDF

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Publication number
CN205398577U
CN205398577U CN201620155207.0U CN201620155207U CN205398577U CN 205398577 U CN205398577 U CN 205398577U CN 201620155207 U CN201620155207 U CN 201620155207U CN 205398577 U CN205398577 U CN 205398577U
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China
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heating
impurity
settling tank
chamber
integration
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Expired - Fee Related
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CN201620155207.0U
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Chinese (zh)
Inventor
杨成志
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Zhejiang Power Machinery Co Ltd
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Individual
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Abstract

The utility model relates to an integration lubricating oil reclaimation equipment, including impurity removing mechanism, heating mechanism, the fractionating tower, the condensing tower, mechanism and water cooling tower are retrieved to the fraction, impurity removing mechanism includes gunbarrel and reinforced mechanism, the gunbarrel includes hybrid chamber and sedimentation chamber, reinforced mechanism includes the charge pump, the conveying pipe, control valve and ejection of compact mouth, heating mechanism includes heating device and heater body, heater body includes the cavity, a plurality of impurity back flows and a plurality of heating pipe, the cavity both ends still are equipped with first baffle and second baffle, it is first, form the heating chamber with the heating device intercommunication between two baffles and a plurality of impurity back flow and heating pipe, the impurity back flow distributes in the outside of heating pipe, the upper end of impurity back flow is lower than the upper end of heating pipe, heater body's top is located to the fractionating tower, fractionating tower top and condensing tower intercommunication, be used for the mixed oil gas of condensation fractionating tower exhaust. The utility model discloses a lubricating oil reclaimation is efficient, and unharmful solid, the liquid of regenerative process, gaseous matter discharge.

Description

Integration lubricant oil regeneration equipment
Technical field
This utility model relates to a kind of regenerating waste oil equipment, more particularly to a kind of integration lubricant oil regeneration equipment.
Background technology
Lubricating oil is to reduce friction in engineering goods; the important means of protection parts; it is widely used in the various machinery equipments such as machinery, vehicle, boats and ships; in use owing to being mixed into dust, mechanical admixture, moisture by outside contamination; simultaneously because being produced multiple intermediate oxidation product, Organic substance and a large amount of colloid by effects such as high-temperature oxydations; make machine oil color blackening, decrease in viscosity, quality decline, thus reduce so lose its control friction, reduce wear and tear, cool, seal off, alleviate the effects such as vibration and have to replacing and become used oil.
If the used oil changed directly is abandoned, not only can serious environment pollution, and cause the great wasting of resources, therefore, lubricant oil regeneration becomes study hotspot, and of the prior art exist re-refining oil unit, but its separation efficiency is low, regeneration effect is not good, and this utility model aims to provide the integrated lubricant oil regeneration equipment that a kind of separation efficiency is high, regeneration effect is excellent.
Utility model content
The purpose of this utility model is in that to solve the deficiencies in the prior art, it is provided that a kind of integration lubricant oil regeneration equipment.
This utility model solves its technical problem and be the technical scheme is that
Integration lubricant oil regeneration equipment, including impurity removal mechanism, heating arrangements, fractionating column, condensing tower, fraction recovering mechanism and water cooling tower,
Described impurity removal mechanism includes settling tank and the charging mechanism of jacketed, settling tank includes hybrid chamber and precipitation chamber, charging mechanism includes charge pump, feed pipe, control valve and is positioned at the discharging gate of feed pipe end, the discharging direction of discharging gate is the tangential direction along hybrid chamber inwall, the bottom in precipitation chamber is provided with the first drainage conduit for getting rid of lubricating oil after remove impurity and the second drainage conduit for despumation, and the inlet height of the first drainage conduit is higher than the height of the second drainage conduit;
Described heating arrangements includes heating plant and heater body, heater body includes cavity, some impurity return ducts and some adds heat pipe, cavity two ends are additionally provided with the first baffle plate and second baffle, first and second baffle plate and some impurity return ducts with add the heating chamber that between heat pipe, formation connects with heating plant, impurity return duct is distributed in the outside adding heat pipe, the upper end of impurity return duct is lower than the upper end adding heat pipe, add heat pipe and the connection of the first drainage conduit, impurity return duct and the connection of the second drainage conduit, cavity top is additionally provided with the separator for intercepting impurity;
The top of heater body is located at by described fractionating column, fractionating column is provided with some fraction districts, fraction recovering mechanism includes fuel oil catcher and corresponding to evaporating some base oil catchers of number of partitions, each fraction district of fractionating column connects with base oil catcher, for collecting the base oil distillated, fractionating column top connects with condensing tower, for condensing the mixed oil and gas that fractionating column is discharged, fuel oil catcher connects with condensing tower oil-out, for collecting the fuel oil that the condensation of condensed tower obtains.
Preferably, described settling tank is at least arranged in parallel two groups, is additionally provided with floating discharge device in settling tank, and described floating discharge device is made up of ball float, discharge flexible pipe and connector, one end of discharge flexible pipe connects with the first drainage conduit, and the other end is connected by connector and ball float are fixing.
Preferably, described hybrid chamber is cylindrical, precipitation chamber is conical, it is uniformly provided with some fixtures along the intersection of hybrid chamber and precipitation chamber outside settling tank, it is fixing for settling tank is installed, settling tank top is provided with toxic emission mechanism, and settling tank is processed by stainless steel, and its capacity is 5-10m3
Preferably, described heating arrangements also includes automatic control of liquid level mechanism, and described automatic control of liquid level mechanism is loaded in the first drainage conduit, for automatically controlling the liquid level adding in heat pipe.
Preferably, described automatic control of liquid level mechanism is float valve chamber, and containment portion is provided with interlayer, for filling with insulation material, adds the equal diameters or unequal of heat pipe and impurity return duct, and adding heat pipe upper end beyond the height of the first baffle plate is more than 10cm.
Preferably, described heating plant is made up of industrial burner, heating tube and waste heat recovery pipe, and the outfan of industrial burner connects with heating tube, and heating tube all connects with heating chamber with waste heat recovery pipe.
Preferably, described waste heat recovery pipe also connects with the chuck of settling tank, for the waste heat by reclaiming, settling tank is heated.
Preferably, described fraction recovering mechanism also includes compressor, liquefying plant and liquefied gas storage, and the isolated on-condensible gas of condensing tower is through compressor compresses, and is liquefied by liquefying plant, is stored in liquefied gas storage.
The used oil of the replacing of separate sources pumps in precipitation mechanism via charging mechanism, used oil is fully rotatable mix homogeneously after entering along hybrid chamber tangential direction in hybrid chamber, under the influence of centrifugal force simultaneously, impurity and used oil relative motion in used oil and separated, after entering precipitation chamber, impurity sinks to bottom precipitation chamber, gone out by the second discharge bank of tubes, used oil through remove impurity is precipitating top, chamber, next operation is entered via discharge flexible pipe and the first discharge bank of tubes, design by floating discharge mechanism, ensure that discharge flexible pipe is always discharged near precipitation top, chamber, Impurity removal compares used oil thoroughly.
Heating plant is to adding heat pipe body heating, pump into through feed pipe through the waste lubricating oil of pretreatment and add in heat pipe heated gasification, rise along adding heat pipe, after touching separator, foam and the heavy relatively larger material of impurity geometric ratio are blocked, drop back in cavity, assemble a certain amount of after through being automatically drained out by impurity return duct, the fraction through separator enters fractionating column and processes further.
Design an automatic control of liquid level mechanism (float valve chamber), the liquid level that can control to add in heat pipe is to suitable height, when the conveying of waste lubricating oil feed lines is broken down, float valve chamber can control the waste lubricating oil of indoor storage and supplement toward adding heat pipe, it is to avoid adds heat pipe dry combustion method and damages.
A kind of lubricant oil regeneration method, based on lubricant oil regeneration equipment of the present utility model, described method carries out as follows:
(1) waste lubricating oil adds settling tank by charging mechanism, heating, Spin precipitate, remove impurity in settling tank;
(2) waste lubricating oil after removing impurity by means of precipitation is delivered to heating arrangements, to technological temperature, waste lubricating oil heating is produced mixed oil and gas and isolates greasy filth, and mixed oil and gas enters fractionating column, and greasy filth is settled down to greasy filth outlet through impurity return duct;
(3) mixed oil and gas slips out different base oils in the different fractions district of fractionating column and is respectively fed to base oil catcher, residue mixed oil and gas is conveyed into condensing tower, isolate fuel oil and fixed gas, fuel oil is sent into fuel oil catcher, fixed gas delivers to compressor, fixed gas is pressurizeed by compressor and delivers to liquefying plant and is condensed into liquefied gas loading storage tank, supplies heating arrangements once again and use after decompressor reduces pressure.
The beneficial effects of the utility model are: reasonable in design, process easy for installation, lubricant oil regeneration efficiency is high, favorable regeneration effect, automatic continuous production can be realized, being readily put into industrialization, the solid, liquid, gas body mass emissions that whole regenerative process is not harmful to, greasy filth can be reused as heating fuel.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model;
Fig. 2 is the structural representation precipitating mechanism in Fig. 1;
Fig. 3 is the structural representation of heating arrangements and fractionating column in Fig. 1.
In figure: 01, settling tank, 011, hybrid chamber, 012, precipitation chamber, 02, charging mechanism, 021, charge pump, 022, feed pipe, 023, control valve, 024, discharging gate, 03, the first drainage conduit, the 04, second drainage conduit, 05, cavity, 06, impurity return duct, 07, heat pipe is added, 08, separator, 09, fractionating column, 10, condensing tower, 11, fixture, 12, toxic emission mechanism, 13, float valve chamber, 14, industrial combustion machine, 15, heating tube, 16, waste heat recovery pipe.
Detailed description of the invention
Below by specific embodiment, and in conjunction with accompanying drawing, the technical solution of the utility model is described in further detail.
Embodiment:
Integrated lubricant oil regeneration equipment as shown in Figure 1, including impurity removal mechanism, heating arrangements, fractionating column, condensing tower, fraction recovering mechanism and water cooling tower,
Described impurity removal mechanism includes settling tank 01 and the charging mechanism 02 of jacketed, settling tank 01 includes hybrid chamber 011 and precipitation chamber 012, charging mechanism 01 includes charge pump 021, feed pipe 022, controls valve 023 and be positioned at the discharging gate 024 of feed pipe 022 end, the discharging direction of discharging gate 024 is the tangential direction along hybrid chamber 011 inwall, the bottom in precipitation chamber 012 is provided with the first drainage conduit 03 for getting rid of lubricating oil after remove impurity and the second drainage conduit 04 for despumation, and the inlet height of the first drainage conduit 03 is higher than the height of the second drainage conduit 04;
Described heating arrangements includes heating plant and heater body, heater body includes cavity 05, some impurity return ducts 06 and some add heat pipe 07, cavity 05 two ends are additionally provided with the first baffle plate and second baffle, first, two baffle plates and some impurity return ducts 06 with add the heating chamber that between heat pipe 07, formation connects with heating plant, impurity return duct 06 is distributed in the outside adding heat pipe 07, the upper end of impurity return duct 06 is lower than the upper end adding heat pipe 07, add heat pipe 07 to connect with the first drainage conduit 03, impurity return duct 06 connects with the second drainage conduit 04, cavity 05 top is additionally provided with the separator 08 for intercepting impurity;
The top of heater body is located at by described fractionating column 09, fractionating column 09 is provided with some fraction districts, fraction recovering mechanism includes fuel oil catcher and corresponding to evaporating some base oil catchers of number of partitions, each fraction district of fractionating column 09 connects with base oil catcher, for collecting the base oil distillated, fractionating column 09 top connects with condensing tower 10, for condensing the mixed oil and gas that fractionating column 09 is discharged, fuel oil catcher connects with condensing tower 10 oil-out, for collecting the fuel oil that the condensation of condensed tower 10 obtains.
Specific to the present embodiment, as shown in Figure 2, described settling tank 01 is at least arranged in parallel two groups, floating discharge device it is additionally provided with in settling tank 01, described floating discharge device is made up of ball float, discharge flexible pipe and connector, one end of discharge flexible pipe connects with the first drainage conduit, and the other end is connected by connector and ball float are fixing.
In the present embodiment, described hybrid chamber 011 is cylindrical, precipitation chamber 012 is conical, the outside intersection along hybrid chamber 011 and precipitation chamber 012 of settling tank 01 is uniformly provided with some fixtures 11, it is fixing for settling tank 01 is installed, settling tank 01 top is provided with toxic emission mechanism 12, and settling tank 01 is processed by stainless steel, and its capacity is 5m3
In the present embodiment, described heating arrangements also includes automatic control of liquid level mechanism, described automatic control of liquid level mechanism is loaded in the first drainage conduit 03, for automatically controlling the liquid level added in heat pipe 07, described automatic control of liquid level mechanism is float valve chamber 13, and cavity 05 is provided externally with interlayer, for filling with insulation material, adding the equal diameters of heat pipe 07 and impurity return duct 06, adding heat pipe 07 upper end beyond the height of the first baffle plate is more than 10cm.
In the present embodiment, described heating plant is made up of industrial burner 14, heating tube 15 and waste heat recovery pipe 16, the outfan of industrial burner 14 connects with heating tube 15, heating tube 15 all connects with heating chamber with waste heat recovery pipe 16, described waste heat recovery pipe 16 also connects with the chuck of settling tank 01, settling tank 01 is heated by the waste heat for passing through to reclaim, described fraction recovering mechanism also includes compressor, liquefying plant and liquefied gas storage, the isolated on-condensible gas of condensing tower 10 is through compressor compresses, and liquefied by liquefying plant, it is stored in liquefied gas storage.
Lubricant oil regeneration equipment of the present utility model carries out as follows for the method for lubricant oil regeneration:
(1) waste lubricating oil adds settling tank by charging mechanism, heating, Spin precipitate, remove impurity in settling tank;
(2) waste lubricating oil after removing impurity by means of precipitation is delivered to heating arrangements, waste lubricating oil heating is produced mixed oil and gas to technological temperature and isolates greasy filth, mixed oil and gas enters fractionating column, greasy filth is settled down to greasy filth outlet through impurity return duct, automatic control of liquid level mechanism (float valve chamber) controls the liquid level adding in heat pipe, it is to avoid dry combustion method;
(3) mixed oil and gas slips out different base oils in the different fractions district of fractionating column and is respectively fed to base oil catcher, residue mixed oil and gas is conveyed into condensing tower, isolate fuel oil and fixed gas, fuel oil is sent into fuel oil catcher, fixed gas delivers to compressor, fixed gas is pressurizeed by compressor and delivers to liquefying plant and is condensed into liquefied gas loading storage tank, after decompressor reduces pressure, supply heating arrangements once again use, the solid, liquid, gas body mass emissions that whole regenerative process is not harmful to, greasy filth can be reused as heating fuel.
Embodiment described above is one of the present utility model preferably scheme, not this utility model is done any pro forma restriction, also has other variant and remodeling under the premise without departing from the technical scheme described in claim.

Claims (8)

1. integration lubricant oil regeneration equipment, including impurity removal mechanism, heating arrangements, fractionating column, condensing tower, fraction recovering mechanism and water cooling tower, it is characterised in that
Described impurity removal mechanism includes settling tank (01) and the charging mechanism (02) of jacketed, settling tank (01) includes hybrid chamber (011) and precipitation chamber (012), charging mechanism (02) includes charge pump (021), feed pipe (022), control valve (023) and be positioned at the discharging gate (024) of feed pipe (022) end, the discharging direction of discharging gate (024) is the tangential direction along hybrid chamber (011) inwall, the bottom of precipitation chamber (012) is provided with the first drainage conduit (03) for getting rid of lubricating oil after remove impurity and the second drainage conduit (04) for despumation, the inlet height of the first drainage conduit (03) is higher than the height of the second drainage conduit (04);
Described heating arrangements includes heating plant and heater body, heater body includes cavity (05), some impurity return ducts (06) and some add heat pipe (07), cavity (05) two ends are additionally provided with the first baffle plate and second baffle, first, two baffle plates and some impurity return ducts (06) with add the heating chamber that between heat pipe (07), formation connects with heating plant, impurity return duct (06) is distributed in the outside adding heat pipe (07), the upper end that the upper end ratio of impurity return duct (06) adds heat pipe (07) is low, add heat pipe (07) to connect with the first drainage conduit (03), impurity return duct (06) connects with the second drainage conduit (04), cavity (05) top is additionally provided with the separator (08) for intercepting impurity;
The top of heater body is located at by described fractionating column (09), fractionating column (09) is provided with some fraction districts, fraction recovering mechanism includes fuel oil catcher and corresponding to evaporating some base oil catchers of number of partitions, each fraction district of fractionating column (09) connects with base oil catcher, for collecting the base oil distillated, fractionating column (09) top connects with condensing tower (10), for condensing the mixed oil and gas that fractionating column (09) is discharged, fuel oil catcher connects with condensing tower (10) oil-out, for collecting the fuel oil that condensed tower (10) condensation obtains.
2. integration lubricant oil regeneration equipment according to claim 1, it is characterized in that: described settling tank (01) is at least arranged in parallel two groups, settling tank is additionally provided with floating discharge device in (01), described floating discharge device is made up of ball float, discharge flexible pipe and connector, one end of discharge flexible pipe connects with the first drainage conduit (04), and the other end is connected by connector and ball float are fixing.
3. integration lubricant oil regeneration equipment according to claim 1, it is characterized in that: described hybrid chamber (011) is cylindrical, precipitation chamber (012) is conical, the outside intersection along hybrid chamber (011) and precipitation chamber (012) of settling tank (01) is uniformly provided with some fixtures (11), it is fixing for settling tank (01) is installed, settling tank (01) top is provided with toxic emission mechanism (12), settling tank (01) is processed by stainless steel, and its capacity is 5-10m3
4. integration lubricant oil regeneration equipment according to claim 1, it is characterized in that: described heating arrangements also includes automatic control of liquid level mechanism, described automatic control of liquid level mechanism is loaded in the first drainage conduit (04), is used for automatically controlling the liquid level added in heat pipe (07).
5. integration lubricant oil regeneration equipment according to claim 4, it is characterized in that: described automatic control of liquid level mechanism is float valve chamber (13), cavity (05) is provided externally with interlayer, for filling with insulation material, adding the equal diameters or unequal of heat pipe (07) and impurity return duct (06), adding heat pipe (07) upper end beyond the height of the first baffle plate is more than 10cm.
6. integration lubricant oil regeneration equipment according to claim 1, it is characterized in that: described heating plant is made up of industrial burner (14), heating tube (15) and waste heat recovery pipe (16), the outfan of industrial burner (14) connects with heating tube (15), and heating tube (15) all connects with heating chamber with waste heat recovery pipe (16).
7. integration lubricant oil regeneration equipment according to claim 6, it is characterised in that: described waste heat recovery pipe (16) also connects with the chuck of settling tank (01), for the waste heat by reclaiming, settling tank (01) is heated.
8. integration lubricant oil regeneration equipment according to claim 1, it is characterized in that: described fraction recovering mechanism also includes compressor, liquefying plant and liquefied gas storage, the isolated on-condensible gas of condensing tower is through compressor compresses, and is liquefied by liquefying plant, is stored in liquefied gas storage.
CN201620155207.0U 2016-02-25 2016-02-25 Integration lubricating oil reclaimation equipment Expired - Fee Related CN205398577U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201620155207.0U CN205398577U (en) 2016-02-25 2016-02-25 Integration lubricating oil reclaimation equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201620155207.0U CN205398577U (en) 2016-02-25 2016-02-25 Integration lubricating oil reclaimation equipment

Publications (1)

Publication Number Publication Date
CN205398577U true CN205398577U (en) 2016-07-27

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ID=56948322

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201620155207.0U Expired - Fee Related CN205398577U (en) 2016-02-25 2016-02-25 Integration lubricating oil reclaimation equipment

Country Status (1)

Country Link
CN (1) CN205398577U (en)

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Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
C41 Transfer of patent application or patent right or utility model
TR01 Transfer of patent right

Effective date of registration: 20170109

Address after: 324000 Donggang Road, Qujiang, Zhejiang, No. nine, No. 2, No.

Patentee after: Zhejiang Power Machinery Co., Ltd.

Address before: Xi'an road 324000 in Zhejiang Province, Quzhou City Kecheng District No. 23 Building 1 unit 9 Dou Tan room 09

Patentee before: Zheng Liqing

CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20160727

Termination date: 20200225

CF01 Termination of patent right due to non-payment of annual fee