CN2934235Y - Device for regeneration of lubrication oil fuel by oiliness waste slag waste oil - Google Patents
Device for regeneration of lubrication oil fuel by oiliness waste slag waste oil Download PDFInfo
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- CN2934235Y CN2934235Y CN 200620024911 CN200620024911U CN2934235Y CN 2934235 Y CN2934235 Y CN 2934235Y CN 200620024911 CN200620024911 CN 200620024911 CN 200620024911 U CN200620024911 U CN 200620024911U CN 2934235 Y CN2934235 Y CN 2934235Y
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- waste
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- oily
- waste oil
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Abstract
The utility model relates to a renewable fuel processing mechanism, in particular to an oily waste residue and waste oil renewing lubricating oil and fuel mechanism, including an oily waste residue waste oil evaporator, a condensator and a renewable fuel fractionation pot. The condensator is arranged on the oily waste residue waste oil evaporator and an evaporation and condensation pipeline which connects with the renewable fuel fractionation pot; The utility model also has a heat carrier boiler, the delivery outlet of the heat carrier of the heat carrier boiler is connected with a heat exchanger which is arranged in the oily waste residue waste oil evaporator by heating pipeline; the exhaust emission outlet of the renewable fuel fractionation pot is connected with a firebox of the heat carrier boiler by exhaust gas pipeline. When the heat carrier boiler is compared with the traditional renewable fuel processing mechanisms, the utility model has the advantages that: owing to the device has no wastewater and exhaust emission, therefore accords with the environmental protection requirements; the utility model also has the advantages of indirect heating, convenient control, safe operation; the waste heat in the boiler can be used to preheat or pre-treat the waste oil residues, and thus saving energy; evaporator preheating, heating, cooling can be artificially effective controlled with a high rate of oil; because of various oily solid, liquid waste can be taken as the raw materials, therefore the raw materials sources is extensive.
Description
Technical field:
The utility model relates to the recovered oil processing unit (plant), particularly a kind of device of oily waste kesiduum waste oil regeneration lubricating oil fuel oil.
Background technology:
Traditional recovered oil processing unit (plant) can only carry out the regeneration of used oil, and can not be by evaporation mode to waste residue rerefined oil, fuel oil.The regenerating waste oil processing unit (plant) is made of vaporizer, condenser, fractionating tank, its renovation process is: in the vaporizer of 1. used oil being packed into, the evaporation pipeline on vaporizer top is passed through in condenser, will feed through the pipeline of condenser in the fractionating tank, waste line feeds extraneous the most at last; 2. the heating cooking stove of vaporizer bottom is lighted to vaporizer heat directly is provided.There are following drawback in said apparatus and the method that relates to: the 1. flue dust of cooking stove discharging and distillation waste gas, can not purifying treatment, and environmental protection is not up to standard; 2. because of burning things which may cause a fire disaster and distilland zero distance almost, so easily waste gas is lighted, it is not up to standard to keep the safety in production; When 3. evaporation work is about to finish, following contradiction must occur: all evaporation is clean if i is with the fluid oil in the used oil, and then the drain pan of vaporizer might be burnt; All evaporation is clean if ii is not with the fluid oil in the used oil, then will waste energy, and improves tooling cost; Iii, above operation are difficult to identification, are difficult to control.4. waste heat can not reclaim, and wastes energy.
Summary of the invention:
Goal of the invention of the present utility model is intended to overcome the described drawback of background technology, and the device of a kind of environmental protection, safe, energy-conservation, the lubricating oil of oily waste kesiduum waste oil regeneration efficiently fuel oil is provided.
The technical scheme that realizes the foregoing invention purpose is: the device of this oily waste kesiduum waste oil regeneration lubricating oil fuel oil comprises waste residue waste oil vaporizer, condenser, recovered oil fractionating tank, on this waste residue waste oil vaporizer and tank connected evaporation of recovered oil fractionation and the condensate line condenser is housed, it also comprises a thermophore boiler, this thermophore pot interchanger connects, and the outlet port of described fractionating tank is connected by the combustion chamber of waste line with this thermophore boiler.
According to the device of this described this oily waste kesiduum waste oil regeneration lubricating oil fuel oil, compare with traditional regenerating waste oil processing unit (plant) and to have the following advantages:
1. environmental protection: boiler heating, non-wastewater discharge, the waste gas after the fractionation is delivered to boiler furnace by waste line it is thoroughly burnouted, and boiler smoke can discharge after by the environmental requirement dedusting by fly-ash separator;
2. safety: indirect heating, various phenomenon data presented such as heat supply temperature, backheat temperature, operating pressure, free air delivery can be controlled;
3. energy-conservation: as can to utilize boiler afterheat to carry out the preheating of waste residue waste oil, pre-treatment, utilize boiler master heat to be used for the evaporation of waste residue waste oil again;
4. efficient: the preheating of vaporizer, intensification, cooling all can artificially effectively be controlled, and the problem that does not exist the vaporizer drain pan to be burnt, and therefore can make residue be exsiccant powder or cellular, so high oil yield is arranged the thorough evaporate to dryness of the oil in the distilland;
5. raw material sources are extensive: various solid-state, the liquid rubbish of every butyraceous all can be raw material.
Description of drawings:
Fig. 1 is a structural representation of the present utility model.
Embodiment:
Provide a specific embodiment of the present utility model below in conjunction with accompanying drawing.
The device of the described oily waste kesiduum waste oil regeneration of present embodiment lubricating oil fuel oil is by waste residue waste oil pre-treatment jar 1, interchanger 2, waste residue waste oil vaporizer 3, evaporation and condensate line 4, condenser 5, recovered oil fractionating tank 6, waste line 7, heat supply pipeline 8, thermophore boiler 9, fly-ash separator 10, waste residue waste oil transfer lime 11 is formed, on evaporation that this waste residue waste oil vaporizer 3 is connected with recovered oil fractionating tank 6 and the condensate line 4 condenser 5 is housed, the thermophore delivery port of this thermophore boiler 9 is connected with interchanger 2 in being arranged on described vaporizer 3 by heat supply pipeline 8, and the outlet port of described fractionating tank 6 passes through waste line 7 and is connected with the combustion chamber of this thermophore boiler 9.
The combustion chamber connects.
Present embodiment is provided with a waste residue waste oil pre-treatment jar 1, be provided with interchanger 2 in the described pre-treatment jar 1, this interchanger 2 is connected with the thermophore delivery port of described thermophore boiler 9 by heat supply pipeline 8, and described pre-treatment jar 1 is connected by waste residue waste oil line of pipes 11 with described vaporizer 3.
Present embodiment also is provided with a fly-ash separator 10, and the gas approach of this fly-ash separator 10 is connected with the exhanst gas outlet of described thermophore boiler 9.
Interchanger 2 in waste residue waste oil pre-treatment jar 1 in the present embodiment and the waste residue waste oil vaporizer 3 can be provided with single group or many groups as required, is used for receiving, distributing the boiler heat, to satisfy recovered oil evaporation conditions in the waste residue waste oil.When evaporation conditions was satisfied, gasification recovered oil entered condenser 5 by the outlet of vaporizer 3.
Condenser 5 in the present embodiment is built-in with air-cooled or water cooling heat exchanger, and when gasification recovered oil passed through, the recovered oil that just will gasify was condensed into liquefaction recovered oil.
This device passes through 9 heat supplies of thermophore boiler, and self-service instrument can be installed, and distributes, controls the heat supply state automatically; Can utilize waste heat that every defective of waste residue waste oil is finished processing in pre-treatment jar 1.
Claims (3)
1, a kind of device of oily waste kesiduum waste oil regeneration lubricating oil fuel oil, comprise waste residue waste oil vaporizer, condenser, recovered oil fractionating tank, on this waste residue waste oil vaporizer and tank connected evaporation of recovered oil fractionation and the condensate line condenser is housed, it is characterized in that it also comprises a thermophore boiler, the thermophore delivery port of this thermophore boiler is connected with interchanger in being arranged on described vaporizer by heat supply pipeline, and the outlet port of described fractionating tank is connected by the combustion chamber of waste line with this thermophore boiler.
2, the device of oily waste kesiduum waste oil regeneration lubricating oil fuel oil according to claim 1, it is characterized in that it also comprises a waste residue waste oil pre-treatment jar, be provided with interchanger in the described pre-treatment jar, this interchanger is connected with the thermophore delivery port of described thermophore boiler by heat supply pipeline, and described pre-treatment jar is connected by waste residue waste oil line of pipes with described vaporizer.
3, the device of oily waste kesiduum waste oil regeneration lubricating oil fuel oil according to claim 1 is characterized in that it also comprises a fly-ash separator, and the gas approach of this fly-ash separator is connected with the exhanst gas outlet of described thermophore boiler.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200620024911 CN2934235Y (en) | 2006-07-07 | 2006-07-07 | Device for regeneration of lubrication oil fuel by oiliness waste slag waste oil |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200620024911 CN2934235Y (en) | 2006-07-07 | 2006-07-07 | Device for regeneration of lubrication oil fuel by oiliness waste slag waste oil |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2934235Y true CN2934235Y (en) | 2007-08-15 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 200620024911 Expired - Fee Related CN2934235Y (en) | 2006-07-07 | 2006-07-07 | Device for regeneration of lubrication oil fuel by oiliness waste slag waste oil |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN2934235Y (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101804263A (en) * | 2009-05-08 | 2010-08-18 | 吴国存 | Waste oil continuous distilling device |
| CN101829434A (en) * | 2010-06-11 | 2010-09-15 | 吴国存 | Convective heat exchange fractionation device |
| CN101858646A (en) * | 2010-06-02 | 2010-10-13 | 吴国存 | Energy-saving and environment-protection heating device for distillation of oily waste materials |
| CN102538392A (en) * | 2011-11-23 | 2012-07-04 | 吴国存 | Oiliness waste gas compression, condensation and collection device |
| CN102851064A (en) * | 2012-08-30 | 2013-01-02 | 刘建波 | Continuous purification and distillation apparatus for combustible waste oil |
-
2006
- 2006-07-07 CN CN 200620024911 patent/CN2934235Y/en not_active Expired - Fee Related
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101804263A (en) * | 2009-05-08 | 2010-08-18 | 吴国存 | Waste oil continuous distilling device |
| CN101804263B (en) * | 2009-05-08 | 2011-12-07 | 唐山山岛石油化学有限公司 | Waste oil continuous distilling device |
| CN101858646A (en) * | 2010-06-02 | 2010-10-13 | 吴国存 | Energy-saving and environment-protection heating device for distillation of oily waste materials |
| CN101858646B (en) * | 2010-06-02 | 2012-07-18 | 唐山山岛石油化学有限公司 | Energy-saving and environment-protection heating device for distillation of oily waste materials |
| CN101829434A (en) * | 2010-06-11 | 2010-09-15 | 吴国存 | Convective heat exchange fractionation device |
| CN102538392A (en) * | 2011-11-23 | 2012-07-04 | 吴国存 | Oiliness waste gas compression, condensation and collection device |
| CN102851064A (en) * | 2012-08-30 | 2013-01-02 | 刘建波 | Continuous purification and distillation apparatus for combustible waste oil |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20070815 Termination date: 20100707 |