CN104971519B - Manufacturing method for regeneration heavy oil and manufacturing system thereof - Google Patents
Manufacturing method for regeneration heavy oil and manufacturing system thereof Download PDFInfo
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- CN104971519B CN104971519B CN201410510081.XA CN201410510081A CN104971519B CN 104971519 B CN104971519 B CN 104971519B CN 201410510081 A CN201410510081 A CN 201410510081A CN 104971519 B CN104971519 B CN 104971519B
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Abstract
The present invention provides a manufacturing method for regeneration heavy oil and a manufacturing system thereof. The completely moisture removed regeneration heavy oil with high purity can be obtained by processing the waste oil containing moisture. For processing the waste oil to become regeneration heavy oil containing water less than 1 % by weight, the steps are: a flotation separation process-heating the waste oil to 40DEG C to 60DEG C and extracting the liquid from the upper layer part of the two layers separated from the oil; a first solid-liquid separation process- removing the solid composition over 0,8mm from the liquid obtained through the flotation separation process and taking out the liquid; a second solid-liquid separation process- removing the solid composition over 5 Mum from the liquid obtained through the first solid-liquid separation process, and taking out the liquid; a heating centrifugal separation process- heating the liquid obtained through the second solid-liquid separation process to 80 DEG C to 100 DEG C and then separating the liquid into lighter fluid, heavy liquid and sludge; and a moisture evaporation process.
Description
Technical field
The present invention relates to become by carrying out Regeneration Treatment to waste oil regeneration heavy oil regeneration heavy oil manufacture method and
Manufacture system.
Background technology
Most waste oil can become regenerated resources.For example, except engine oil, gear oil, ATF (Automatic
Transmission Fluid), the lubricating oil such as bobbin oil, beyond working oil and cutting oil, also clean oil, from mineral oil
Processing oil, the heavy oil kind that gone out of use etc..It is being recovered and is taking care of in the state of sump tank, generally, various oil mixing, and
Foreign body containing solid constituent and moisture.
It has been suggested the technology that such waste oil becomes regenerated resources, for example patent documentation 1~3.
Waste oil reclaiming processing system is Patent Document 1 discloses, is possessed and roguing is removed from waste oil by centrifugation
The operation of matter and afterwards waste oil is heated and evaporated remove impurity operation.
Useless oil treatment process is patent document 2 discloses that, is that waste oil is carried out after heat treated, to carry out three phase centrifugation separation,
And further light liquid is heated so as to the method that upper strata oil is taken out as reclaimed oil.
Patent Document 3 discloses from waste oil and manufacture the reclaimed oil manufacture device of reclaimed oil, possess as centrifugal separator
Oil water separator, by standing the water separator that carries out at least 2 sections of oil-water separation and by being contained in the oil for separating oil
Mud (sludge) is crushed to improve the fuel improving apparatus for separating oil.
Patent documentation 1:Japanese Unexamined Patent Publication 2003-306682 publications
Patent documentation 2:Japanese Unexamined Patent Publication 2006-104233 publications
Patent documentation 3:Japanese Unexamined Patent Publication 2013-60573 publications
Patent documentation described above 1~3 like that, in the look-ahead technique for carrying out oil reclaiming process, heating, from
The modes such as the heart is separated, filtered, distillation are variedly combined.
However, large-scale equipment etc. is needed in order to almost remove moisture completely from the waste oil containing moisture, mesh
Before, it is difficult to highly purified reclaimed oil is obtained using simple equipment, especially regeneration weight of the moisture amount less than 1 weight %
Oil.
The content of the invention
It is an object of the invention to provide being obtained in that almost completely by water by processing to the waste oil containing moisture
Divide the manufacture method and manufacture system of the regeneration heavy oil of the highly purified regeneration heavy oil for eliminating.
In order to reach above-mentioned purpose, the present invention provides following structure.
1st mode of the present invention is related to regenerate heavy oil manufacture method, and the waste oil containing moisture is processed, the waste oil is made
Become regeneration heavy oil of the moisture amount less than 1 weight %, above-mentioned regeneration heavy oil manufacture method is characterised by having:On floating
Waste oil, in above-mentioned floating separation procedure, is heated to 40 DEG C~60 DEG C of temperature, and will be separated into the upper of two-layer by separation circuit
The liquid of layer segment takes out;1st solid-liquid separation process, in above-mentioned 1st solid-liquid separation process, from by above-mentioned floating upper separation work
The solid constituent more than 0.8mm is removed in the liquid that sequence is obtained and liquid is taken out;2nd solid-liquid separation process, in above-mentioned 2nd solid-liquid
In separation circuit, the solid constituent more than 5 μm is removed from the liquid obtained by above-mentioned 1st solid-liquid separation process and take out liquid
Body;Heating and three phase centrifugation separation circuit, in above-mentioned heating and three phase centrifugation separation circuit, will be by the above-mentioned 2nd
After the liquid that solid-liquid separation process is obtained is heated to the temperature of 80 DEG C~100 DEG C of scopes, using three phase centrifugation seperator by the liquid
Body is separated into light liquid, heavy-fluid and greasy filth;And moisture evaporation operation, in above-mentioned moisture evaporation operation, will be added by above-mentioned
The light liquid that heat and three phase centrifugation separation circuit are obtained is heated to the temperature of 100 DEG C~110 DEG C of scopes and is stirred and makes water
Divide evaporation, remaining liquid is obtained as regeneration heavy oil.
Above-mentioned 1st mode is characterised by, above-mentioned floating separation procedure, above-mentioned heating centrifugal separation process and above-mentioned water
The heating divided in evaporization process, is carried out by with the heat exchange of vapor.
2nd mode of the present invention is related to regenerate heavy oil manufacture system, and the waste oil containing moisture is processed, the waste oil is made
Become regeneration heavy oil of the moisture amount less than 1 weight %, above-mentioned regeneration heavy oil manufacture system is characterised by having:1st adds
Thermal, above-mentioned 1st heater is in order that waste oil is separated into two-layer and takes out the liquid of top section and be heated to waste oil
40 DEG C~60 DEG C of temperature;1st equipment for separating liquid from solid, above-mentioned 1st equipment for separating liquid from solid is from being obtained by above-mentioned 1st heater
Liquid in remove solid constituent more than 0.8mm;2nd equipment for separating liquid from solid, above-mentioned 2nd equipment for separating liquid from solid is from by above-mentioned
The solid constituent more than 5 μm is removed in the liquid that 1st equipment for separating liquid from solid is obtained and liquid is taken out;2nd heater, above-mentioned
The liquid obtained by above-mentioned 2nd equipment for separating liquid from solid is heated to 2 heaters the temperature of 80 DEG C~100 DEG C of scopes;Three-phase
Liquid after above-mentioned 2nd heating devices heat is separated into light liquid, heavy-fluid and oil by seperator, above-mentioned three-phase separator
Mud;And the 3rd heater, the light liquid obtained by above-mentioned three phase centrifugation seperator is heated to 100 by above-mentioned 3rd heater
DEG C~temperature of 110 DEG C of scopes be stirred and make moisture evaporation, remaining liquid is obtained as regeneration heavy oil.
Above-mentioned 2nd mode is characterised by that above-mentioned 1st heater, above-mentioned 2nd heater and the above-mentioned 3rd are heated
Device is to carry out the heater with the heat exchange of vapor.
The manufacture method and manufacture system of regeneration heavy oil of the invention, can be with low cost manufacture moisture amount
Less than the regeneration heavy oil of 1 weight %.
Description of the drawings
Fig. 1 is the manufacture method and the flow process and composition of manufacture system of the regeneration heavy oil for schematically illustrating the present invention
Figure.
Description of reference numerals
Tl, T2, T3, T4, T5, T6, T7, T8, T9... tank;P1, P2, P3, P4, P5, P6, P7... pump;S1... filter
Net;S2... centrifugal separator;S3... three phase centrifugation seperator;Hl, H2, H3... heater.
Specific embodiment
Hereinafter, referring to the drawings embodiments of the present invention are illustrated.
Fig. 1 is the manufacture method and the flow process and composition of manufacture system of the regeneration heavy oil for schematically illustrating the present invention
Figure.
First, various waste oil are reclaimed and is stored in tank T1.Can advise for JIS as the waste oil of the process object of the present invention
Regeneration heavy oil suitable with the heavy oil from A heavy oil to heavy oil B in lattice.As such waste oil, except engine oil, gear oil, ATF
Beyond the lubricating oil such as (Automatic Transmission Fluid), bobbin oil, working oil and cutting oil, also clean
Oil, the processing oil from mineral oil, the heavy oil kind for going out of use etc..Usually contain in these waste oil considerable amount of moisture (average 6~
16 weight % or so).In addition, the also foreign body of the solid constituent containing all size.
In existing regeneration Heavy oil treatment method, heating evaporation, centrifugation are carried out to remove moisture, but in order to
Make moisture amount less than 1 weight %, need large-scale distillation equipment etc., so as to cost uprises.The present invention is provided and can be use up
Amount simply manufactures method and device of the moisture less than the regeneration heavy oil of 1 weight %.
(floating separation procedure)
The waste oil for being stored in tank T1 is sent to the 1st heater H1 using pump P1.1st heater H1 possesses following knot
Structure:Heat-exchange pump is equipped with can container, heat-exchange pump is connected with the steam generator outside can container.It is filled into and carries
Waste oil in the tank of the heat exchanger is heated to the appropriate temperature of 40~60 DEG C of scopes, preferably from about 50 DEG C.After the heating
Under state, the time of regulation is waited until waste oil is separated into two-layer.After waste oil is separated into two-layer, the top section that will only float
Liquid takes out and is sent to subsequent processing.The underclad portion being removed in the floating separation procedure is almost moisture.
(the 1st solid-liquid separation process)
Make the drainage screen by the segregation apparatuss as the 1st solid-liquid separation process by the liquid of floating separation procedure acquisition
S1.In the 1st solid-liquid separation process, the foreign body of the solid constituent more than about 0.8mm is removed.Liquid after drainage screen S1
Body is recycled to tank T2.
(the 2nd solid-liquid separation process)
Make to be recovered to the centrifugation of the liquid by the segregation apparatuss as the 2nd solid-liquid separation process of tank T2 by the use of pump P2
Machine S2.The tiny segregator CF150 that centrifugal separator S2 is made for such as Dongdu separator industry (strain).In the 2nd solid-liquid separation work
In sequence, the foreign body of the solid constituent more than about 5 μm is removed.Liquid after tiny segregator S2 is recycled to tank T3.
(heating and three phase centrifugation separation circuit)
The liquid for being recovered to tank T3 is sent to the 2nd of the leading portion as heating and three phase centrifugation separation circuit by the use of pump P3
Heater H2.2nd heater H2 is identical with the 1st heater H1 by for the can container structure of heat exchange is carried out with vapor
Into.The liquid being filled in the tank with heat exchanger is heated to the appropriate temperature of 80 DEG C~100 DEG C of scopes, preferably from about
90℃.Liquid after heating is imported into the three phase centrifugation seperator S3 of back segment.
Autojector (セ Le Off ジ エs of the three phase centrifugation seperator S3 of back segment for such as mitsubishi chemical industry machine (strain) society
Network タ mono-) SJ150J.The liquid of waste oil is separated into light liquid, heavy-fluid and greasy filth by three phase centrifugation seperator S3.Thus, oily conduct
Light liquid is separated, and water is separated as heavy-fluid, and the solid constituent of 0.1~5 μ m is separated as greasy filth (also containing moisture).
Light liquid is recycled to tank T4, and heavy-fluid is recycled to tank T5, and greasy filth is recycled to tank T6.Additionally, heavy-fluid is sent to tank using pump P5
T8 is simultaneously processed in incinerator.Greasy filth is sent to tank T9 using pump P6 and is processed in incinerator.
(moisture evaporation operation)
The light liquid for being obtained and be recovered to by heating and three phase centrifugation separation circuit tank T4 is sent to the 3rd heating using pump P4
Device H3.3rd heater H3 is identical with l and the 2nd heater H1, H2 by for the tank of heat exchange is carried out with vapor
Container is constituted.The light liquid being filled in the can container with heat exchanger is heated to the temperature of 100 DEG C~110 DEG C of scopes,
It is preferred that the temperature of 103 DEG C~105 DEG C of scopes.Circumferentially it is stirred using blender in can container, also, under can container
Portion is provided with mixing pump, carries out the stirring of above-below direction.Thereby, it is possible to the light liquid being uniformly heated up in can container, water can be made
Divide from light liquid and evaporate with integrally not staying omission.And, it is preferable that by the pressure in can container is adjusted to malleation, suitably press down
The intrusion of air processed.Thus, even if the evaporation of low volatile oil can also suppress to ignite and on fire.
In the case where the treating capacity of light liquid is more, the temperature of the 3rd heater H3 is set to higher.In addition, for oil
Water separates the situation of waste oil being difficult to, can by be combined as reducing 1 treating capacity, by temperature be set as it is higher,
Extend process time and reinforcing mixing power in 1 or it is multiple, improve moisture evaporation ability.
Moisture evaporation is made by the process of the operation is carried out to light liquid, and the moisture amount of remaining liquid can be made
Less than 1 weight %.Tank T7 is sent to using pump P7 through the liquid of moisture evaporation operation, is stored as regeneration heavy oil.
In the regeneration heavy oil manufacture method and manufacture system of the above-mentioned present invention, the 1st~the 3rd heater is respective
Steam generator can have a steam generator without the need for separately arranging.General vapor is produced
Device can produce 0.1~5MPa, 110~250 DEG C of vapor.As steam generator (or vapor heat exchange
Device) can be using the oily-water seperating equipment of such as (strain) group paulownia industry.
The regeneration heavy oil manufacture method and manufacture system of the present invention is by steaming by general equipment for separating liquid from solid, based on water
The heater and three phase centrifugation seperator of gas is most combined as and obtains, can with low cost manufacture moisture amount less than
The regeneration heavy oil of 1 weight %.
The result after above-mentioned embodiments of the present invention are repeatedly implemented is summarized, it is as follows.
Waste oil:55~70kL
Regeneration heavy oil:45~60kL
The water quantities of the waste oil of before processing:6~12 weight %
The water quantities of the regeneration heavy oil after process:0.6~0.8 weight %
Claims (4)
- It is 1. a kind of to regenerate heavy oil manufacture method,Waste oil containing moisture is processed, makes the waste oil become regeneration heavy oil of the moisture amount less than 1 weight %,Above-mentioned regeneration heavy oil manufacture method is characterised by,Have:Waste oil, in above-mentioned floating separation procedure, is heated to 40 DEG C~60 DEG C of temperature, and will be separated into by floating separation procedure The liquid of the top section of two-layer takes out;1st solid-liquid separation process, in above-mentioned 1st solid-liquid separation process, from the liquid obtained by above-mentioned floating separation procedure Solid constituent of the middle removing more than 0.8mm simultaneously takes out liquid;2nd solid-liquid separation process, in above-mentioned 2nd solid-liquid separation process, from the liquid obtained by above-mentioned 1st solid-liquid separation process The solid constituent more than 5 μm is removed in body and liquid is taken out;Heating and three phase centrifugation separation circuit, in above-mentioned heating and three phase centrifugation separation circuit, will be by the above-mentioned 2nd After the liquid that solid-liquid separation process is obtained is heated to the temperature of 80 DEG C~100 DEG C of scopes, using three phase centrifugation seperator by the liquid Body is separated into the greasy filth of light liquid, heavy-fluid and the solid constituent containing 0.1~5 μ m;AndMoisture evaporation operation, in above-mentioned moisture evaporation operation, will be obtained by above-mentioned heating and three phase centrifugation separation circuit Light liquid be heated to the temperature of 103 DEG C~105 DEG C of scopes and be stirred and make moisture evaporation, thus make remaining liquid conduct Regenerate heavy oil and obtain.
- It is 2. according to claim 1 to regenerate heavy oil manufacture method, it is characterised in thatHeating in above-mentioned floating separation procedure, above-mentioned heating centrifugal separation process and above-mentioned moisture evaporation operation, by with The heat exchange of vapor is carrying out.
- It is 3. a kind of to regenerate heavy oil manufacture system,Waste oil containing moisture is processed, makes the waste oil become regeneration heavy oil of the moisture amount less than 1 weight %,Above-mentioned regeneration heavy oil manufacture system is characterised by,Have:1st heater, above-mentioned 1st heater is in order that waste oil is separated into two-layer and takes out the liquid of top section and will give up Oil is heated to 40 DEG C~60 DEG C of temperature;1st equipment for separating liquid from solid, above-mentioned 1st equipment for separating liquid from solid are removed from the liquid obtained by above-mentioned 1st heater More than the solid constituent of 0.8mm;2nd equipment for separating liquid from solid, above-mentioned 2nd equipment for separating liquid from solid is from the liquid obtained by above-mentioned 1st equipment for separating liquid from solid Remove the solid constituent more than 5 μm and take out liquid;The liquid obtained by above-mentioned 2nd equipment for separating liquid from solid is heated to 80 DEG C by the 2nd heater, above-mentioned 2nd heater The temperature of~100 DEG C of scopes;Liquid after above-mentioned 2nd heating devices heat is separated into light liquid, heavy-fluid by three-phase separator, above-mentioned three-phase separator And the greasy filth of the solid constituent containing 0.1~5 μ m;AndThe light liquid obtained by above-mentioned three phase centrifugation seperator is heated to 103 DEG C by the 3rd heater, above-mentioned 3rd heater The temperature of~105 DEG C of scopes is simultaneously stirred and makes moisture evaporation, remaining liquid is obtained as regeneration heavy oil.
- It is 4. according to claim 3 to regenerate heavy oil manufacture system, it is characterised in thatAbove-mentioned 1st heater, above-mentioned 2nd heater and above-mentioned 3rd heater are to carry out the heat exchange with vapor Heater.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
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JP2014079835A JP5685663B1 (en) | 2014-04-09 | 2014-04-09 | Recycled heavy oil production method and production system |
JP2014-079835 | 2014-04-09 |
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CN104971519A CN104971519A (en) | 2015-10-14 |
CN104971519B true CN104971519B (en) | 2017-04-12 |
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JP (1) | JP5685663B1 (en) |
CN (1) | CN104971519B (en) |
PH (1) | PH12014000272A1 (en) |
TW (1) | TW201538709A (en) |
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WO2024047742A1 (en) * | 2022-08-30 | 2024-03-07 | 清水建設株式会社 | Method for treating oil-containing sludge, method for recovering oil from oil-containing sludge, apparatus for treating oil-containing sludge, apparatus for recovering oil from oil- containing sludge, system for treating oil-containing sludge, and system for recovering oil from oil-containing sludge |
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JPH0398601A (en) * | 1989-09-11 | 1991-04-24 | Hitachi Zosen Corp | Oil recovery device |
CN1458247A (en) * | 2003-04-30 | 2003-11-26 | 石建芳 | Process for preparing oil sludge containing blending residual |
CN1616615A (en) * | 2004-09-29 | 2005-05-18 | 上海宝钢废旧油处理站 | Parifying and regenerating process for high and medium viscosity waste oils |
CN102627381A (en) * | 2012-04-26 | 2012-08-08 | 陕西科技大学 | Two-step method resource treatment process for sludge containing oil |
CN103820200A (en) * | 2014-01-28 | 2014-05-28 | 连力生 | Process for regenerating base oil from waste lubricating oil |
Family Cites Families (8)
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JPH01275692A (en) * | 1988-04-27 | 1989-11-06 | Mitsubishi Kakoki Kaisha Ltd | Method of treating waste engine oil |
JPH0832891B2 (en) * | 1988-05-30 | 1996-03-29 | トヨタ自動車株式会社 | Method for removing sulfur from waste oil |
JPH0810509A (en) * | 1994-06-30 | 1996-01-16 | Mitsubishi Kakoki Kaisha Ltd | Vessel waste oil treatment |
JPH1190490A (en) * | 1997-09-19 | 1999-04-06 | Mishima Kosan Co Ltd | Regeneration of oil-containing sludge |
JP3944352B2 (en) * | 2000-11-01 | 2007-07-11 | 株式会社ジェイテクト | Waste liquid separation and recovery method and separation and recovery apparatus |
JP2003306682A (en) * | 2002-04-16 | 2003-10-31 | Kanto Kankyo Service Kk | Waste oil-collecting and regenerating system and waste oil-regenerating apparatus |
JP2006104233A (en) * | 2004-09-30 | 2006-04-20 | Nippon Mining & Metals Co Ltd | Method for treating waste oil |
CN201300008Y (en) * | 2008-10-31 | 2009-09-02 | 易治吉 | Oil filter system for reclaiming waste oil |
-
2014
- 2014-04-09 JP JP2014079835A patent/JP5685663B1/en active Active
- 2014-09-23 TW TW103132845A patent/TW201538709A/en not_active IP Right Cessation
- 2014-09-26 PH PH12014000272A patent/PH12014000272A1/en unknown
- 2014-09-28 CN CN201410510081.XA patent/CN104971519B/en active Active
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0398601A (en) * | 1989-09-11 | 1991-04-24 | Hitachi Zosen Corp | Oil recovery device |
CN1458247A (en) * | 2003-04-30 | 2003-11-26 | 石建芳 | Process for preparing oil sludge containing blending residual |
CN1616615A (en) * | 2004-09-29 | 2005-05-18 | 上海宝钢废旧油处理站 | Parifying and regenerating process for high and medium viscosity waste oils |
CN102627381A (en) * | 2012-04-26 | 2012-08-08 | 陕西科技大学 | Two-step method resource treatment process for sludge containing oil |
CN103820200A (en) * | 2014-01-28 | 2014-05-28 | 连力生 | Process for regenerating base oil from waste lubricating oil |
Also Published As
Publication number | Publication date |
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TWI561627B (en) | 2016-12-11 |
CN104971519A (en) | 2015-10-14 |
TW201538709A (en) | 2015-10-16 |
PH12014000272B1 (en) | 2016-04-04 |
JP5685663B1 (en) | 2015-03-18 |
PH12014000272A1 (en) | 2016-04-04 |
JP2015199848A (en) | 2015-11-12 |
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