CN107541329A - Waste oil regeneration production process - Google Patents

Waste oil regeneration production process Download PDF

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Publication number
CN107541329A
CN107541329A CN201610487230.4A CN201610487230A CN107541329A CN 107541329 A CN107541329 A CN 107541329A CN 201610487230 A CN201610487230 A CN 201610487230A CN 107541329 A CN107541329 A CN 107541329A
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CN
China
Prior art keywords
waste oil
oil
filter
light component
pans
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Pending
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CN201610487230.4A
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Chinese (zh)
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不公告发明人
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Individual
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Individual
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Priority to CN201610487230.4A priority Critical patent/CN107541329A/en
Publication of CN107541329A publication Critical patent/CN107541329A/en
Pending legal-status Critical Current

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  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)

Abstract

A kind of waste oil regeneration production process, its production craft step are:Cross and filter out metal impurities;Cross and filter out large granular impurity;Decompression dehydration;Molecular distillation purifies;Filtering polishing.Advantage is:This technique uses pure physical separation, and product quality is stable, non-secondary pollution.Good separating effect, product purity are high.Product can pass through addition various additives and be mixed into the various finished lubes such as industrial equipment, vehicular traffic.

Description

Waste oil regeneration production process
Technical field
Present invention relates to a kind of waste oil regeneration production process, and the oil quality particularly regenerated is good, belongs to waste oil regeneration Production technology field.
Background technology
At present, most of waste oil is purchased by small oil plant and processes inferior mixing with waste oil regeneration production process of poor quality Petrol and diesel oil or the oil that makes a fire, these illegal small oil plants are the illegal enterprises that country prohibites, and are sternly controlled.It is existing The oil quality for the regeneration that waste oil regeneration production process has is not good enough, some complex process, and production cost is high.
The content of the invention
The oil quality for the regeneration that the purpose of the present invention has aiming at current existing waste oil regeneration production process is inadequate Good, some complex process, equipment investment is big, the deficiency of production cost height, and provides a kind of waste oil regeneration production process.
Its production craft step is:
1)Cross and filter out metal impurities:By waste oil under conditions of pressure 0.1-0. 4Mpa, waste oil is set to pass through magnetic filter mistake Filter, the metal impurities in waste oil are removed;
2)Cross and filter out large granular impurity:By the waste oil for removing metal impurities under conditions of pressure 0.1-0. 4Mpa, make removing golden Belong to the waste oil of impurity by blue formula filter, the large granular impurity in waste oil is removed;
3)Decompression dehydration:The waste oil of above-mentioned removing large granular impurity is delivered to after preheater is preheated to 100-120 DEG C with pump, then sent Enter in thin film evaporator, after thin film evaporator is handled;
Lower boiling water therein, gasoline, diesel oil enter in light component pans after plate-type condenser condenses, when light component connects When being reached high level by the liquid level of tank, by being pumped into oil water separator, moisture therein is removed, reclaims gasoline therein, bavin Oil, the material therein not evaporated then enter in heavy constituent tank;
4)Molecular distillation purifies:Material in heavy constituent tank is delivered to after reheater is heated up to 280-320 DEG C, is sent into a fraction Sub- distiller, after the processing of first order molecular distiller, wherein entering after the base oil that can be utilized condenser condensation built in Light component pans, heavy constituent enter heavy constituent pans;
5)Filtering polishing:The base oils of above-mentioned light component pans is sent into polishing filter, is filtrated to get that colourity is relatively low, clarification Transparent lube base oil.
It is an advantage of the invention that:This technique uses pure physical separation, and product quality is stable, non-secondary pollution;Separating effect Good, product purity is high;Product can pass through addition various additives and be mixed into the various finished product lubrications such as industrial equipment, vehicular traffic Oil.
Embodiment
A kind of waste oil regeneration production process, it is characterised in that its production craft step is:
1)Cross and filter out metal impurities:By waste oil under conditions of pressure 0.1-0. 4Mpa, waste oil is set to pass through magnetic filter mistake Filter, the metal impurities in waste oil are removed;2)Cross and filter out large granular impurity:The waste oil of metal impurities will be removed in pressure 0.1-0. Under conditions of 4Mpa, the waste oil of removing metal impurities is set to remove the large granular impurity in waste oil by basket filter;3)Drop Press-dehydrating:The waste oil of above-mentioned removing large granular impurity is delivered to after preheater is preheated to 100-120 DEG C with pump, is re-fed into film steaming Send out in device, after thin film evaporator is handled;Lower boiling water therein, gasoline, diesel oil enter light after plate-type condenser condenses In component pans, when the liquid level of light component pans reaches high level, by being pumped into oil water separator, remove therein Moisture, reclaims gasoline therein, diesel oil, and the material therein not evaporated then enters in heavy constituent tank;Purpose is by used oil In the lower boiling material and diesel oil such as moisture remove, raw material is carried out being dehydrated pretreatment and improves the flash-point of base oil;4)Point Sub- distilation:Material in heavy constituent tank is delivered to after reheater is heated up to 280-320 DEG C, is sent into first order molecular distillation Device, after the processing of first order molecular distiller.The base oil that can be wherein utilized enters light component after the condenser condensation built in Pans, heavy constituent enter heavy constituent pans.Purpose is to separate the base oil in material;5)Filtering polishing:Will be upper The base oil for stating light component pans is sent into polishing filter, is filtrated to get that colourity is relatively low, lube base oil of clear.

Claims (1)

1. a kind of waste oil regeneration production process, it is characterised in that its production craft step is:
1)Cross and filter out metal impurities:By waste oil under conditions of pressure 0.1-0. 5Mpa, waste oil is set to pass through magnetic filter mistake Filter, the metal impurities in waste oil are removed;
2)Cross and filter out large granular impurity;By the waste oil for removing metal impurities under conditions of pressure 0.1-0. 5MPa, make removing golden Belong to the waste oil of impurity by blue formula filter, the large granular impurity in waste oil is removed;
3)Decompression dehydration:The waste oil of above-mentioned removing large granular impurity is delivered to after preheater is preheated to 100-120 DEG C with pump, then sent Enter in thin film evaporator, after thin film evaporator is handled;Lower boiling water therein, gasoline, diesel oil condense through plate-type condenser Enter afterwards in light component pans, when the liquid level of light component pans reaches high level, by being pumped into oil water separator, remove Moisture therein is removed, reclaims gasoline therein, diesel oil, the material therein not evaporated then enters in heavy constituent tank;
4)Molecular distillation purifies:Material in heavy constituent tank is delivered to after reheater is heated up to 300-320 DEG C, is sent into one-level Molecular still, after the processing of first order molecular distiller, wherein condenser condensation built in the base oil warp that can be utilized is laggard Enter light component pans, heavy constituent enters heavy constituent pans;
5)Filtering polishing:The base oils of above-mentioned light component pans is sent into polishing filter, is filtrated to get that colourity is relatively low, clarification Transparent lube base oil.
CN201610487230.4A 2016-06-29 2016-06-29 Waste oil regeneration production process Pending CN107541329A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201610487230.4A CN107541329A (en) 2016-06-29 2016-06-29 Waste oil regeneration production process

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201610487230.4A CN107541329A (en) 2016-06-29 2016-06-29 Waste oil regeneration production process

Publications (1)

Publication Number Publication Date
CN107541329A true CN107541329A (en) 2018-01-05

Family

ID=60962361

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201610487230.4A Pending CN107541329A (en) 2016-06-29 2016-06-29 Waste oil regeneration production process

Country Status (1)

Country Link
CN (1) CN107541329A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN115353928A (en) * 2022-08-19 2022-11-18 唐亮 Regenerated lubricating oil based on chemical method treatment

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN115353928A (en) * 2022-08-19 2022-11-18 唐亮 Regenerated lubricating oil based on chemical method treatment

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PB01 Publication
WD01 Invention patent application deemed withdrawn after publication

Application publication date: 20180105

WD01 Invention patent application deemed withdrawn after publication