CN102559362A - Waste oil regeneration apparatus - Google Patents
Waste oil regeneration apparatus Download PDFInfo
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- CN102559362A CN102559362A CN2012100300191A CN201210030019A CN102559362A CN 102559362 A CN102559362 A CN 102559362A CN 2012100300191 A CN2012100300191 A CN 2012100300191A CN 201210030019 A CN201210030019 A CN 201210030019A CN 102559362 A CN102559362 A CN 102559362A
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- oil
- adsorption tanks
- well heater
- material taking
- taking mouth
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Abstract
The invention discloses a waste oil regeneration apparatus, an oil inlet (1) of the waste oil regeneration apparatus is communicated with the inlet of an oil pump (2) and the inlet of a heater (3) in order, the outlet of the heater (3) is shunted and then respectively communicated with a drawing port I (17) of an adsorption pot I (16) and a drawing port II (32) of an adsorption pot II (29), a discharge hatch I of the adsorption pot I (16) is connected with a pressure controller (13), a non return valve (12), a prefilter (10), a postfilter (8) and an oil outlet (7) in order, a discharge hatch II of the adsorption pot II (29) enables feedback and is communicated with the drawing port I (17) of the adsorption pot I (16) through a pipeline (37), a compass type heater I (34) and a compass type heater II (30) are respectively provided in the adsorption pot I (16) and the adsorption pot II (29), and a temperature controller I (35) and a temperature controller II (36) are respectively provided on the compass type heater I (34) and the compass type heater II (30).
Description
Technical field
The present invention relates to a kind of oil reclaimer.
Background technology
Present equipment uses oil after wearing out; Its acid number rises; Surpass the normal operation that 0.30 (mgKOH/g) will have influence on equipment, and adopt impurity, moisture content, the gas of physical filtering method in can only filtering oil, can not reduce the acid number in the oil; At this moment just need waste a large amount of energy to equipment renew oil more again.
Summary of the invention
The invention provides a kind of oil reclaimer, it can prolong its work-ing life for fluid regeneration.
The present invention has adopted following technical scheme: a kind of oil reclaimer; It comprises in-line, adsorption tanks I, adsorption tanks II and fuel-displaced pipeline; On in-line, be provided with oil-in, oil pump and well heater; Oil-in is communicated with the import of oil pump and well heater successively; Be connected with the material taking mouth I of adsorption tanks I and the material taking mouth II of adsorption tanks II respectively after the outlet shunting of well heater; Fuel-displaced pipeline comprises pressure controller, vacuum breaker, prime strainer, back level strainer and oil outlet, and the discharge port I of adsorption tanks I is connected with oil outlet with pressure controller, vacuum breaker, prime strainer, back level strainer successively, and the discharge port II of adsorption tanks II is communicated with the material taking mouth I of adsorption tanks I through pipeline feedback back; In adsorption tanks I and adsorption tanks II, be respectively equipped with compass formula well heater I and compass formula well heater II, on compass formula well heater I and compass formula well heater II, be respectively equipped with temp controlled meter I and temp controlled meter II.
The outside surface of described adsorption tanks I is provided with the dog-house I; Communicate in dog-house I and the adsorption tanks I; Be provided with oil-feed filter screen I in the adsorption tanks I and go out the oil screen I, oil-feed filter screen I is positioned at material taking mouth I place, goes out the oil screen I and is positioned at discharge port I place; Be provided with qi of chong channel ascending adversely valve I in the outside of material taking mouth I, be provided with qi of chong channel ascending adversely valve III in the outside of discharge port I.The outside surface of described adsorption tanks II is provided with the dog-house II; Communicate in dog-house II and the adsorption tanks II; Be provided with oil-feed filter screen II in the adsorption tanks II and go out the oil screen II, oil-feed filter screen II is positioned at material taking mouth II place, goes out the oil screen II and is positioned at discharge port II place; Be provided with qi of chong channel ascending adversely valve II in the outside of material taking mouth II, be provided with qi of chong channel ascending adversely valve IV in the outside of discharge port II.Be respectively equipped with duty valve I and duty valve II between the material taking mouth I of the outlet of described well heater and adsorption tanks I and the material taking mouth II of adsorption tanks II.Be connected with temperature controller on the described well heater.Described pipeline is provided with duty valve III and duty valve IV.Described prime strainer is respectively equipped with tensimeter I and tensimeter II with the ingress of back level strainer.
The present invention has following beneficial effect: the present invention is provided with two adsorption tanks; One of them adsorption tanks is made fluid another adsorption tanks when giving birth to and is done the processing of sorbent material activating and regenerating; The activation temperature of aluminum oxide is 350-400 ℃, time 30-40 minute, and the sorbent material activating and regenerating can use repeatedly after handling repeatedly, and adsorption tanks are provided with two compass formula well heaters; The qi of chong channel ascending adversely of qi of chong channel ascending adversely valve is arranged at the adsorption tanks bottom when the activation adsorption agent is operated, and cooperates a jar top qi of chong channel ascending adversely valve to use and gets rid of moisture.There is gas flow that active oxidation filter sorbent material is heated evenly in jar, but the shortening of activated alumina recovery time, and loaded down with trivial details the feeding intake that also can remove from got material work.Utilize each duty valve before the sorbent material activating and regenerating is handled doing, the qi of chong channel ascending adversely valve that cooperates adsorption tanks top with pressurized air the emptying of adsorption tanks inner fluid.Regenerating unit of the present invention is furnished with heating system separately when fluid regeneration purifying treatment, this system comes design temperature according to the optimal adsorption working temperature of sorbent material.The optimal working temp of activated alumina is 50-60 ℃; Utilize in the activated alumina adsorbents with oil in acidic substance; Sorbent material is thrown in jar in adsorption tanks, and other free state material is with trickle aperture of the oxidized aluminium of fluid flow direction or polymer adsorbing material absorption that the gap stops in the while oil.From the fluid that regenerating unit comes out, sneak into fluid for preventing granule foreign, doing deeper purifying treatment through two strainers, the fluid after the purification is discharged from oil outlet.
Description of drawings
Fig. 1 is a structural representation of the present invention.
Embodiment
In Fig. 1, the invention provides a kind of oil reclaimer, it comprises in-line, adsorption tanks I 16, adsorption tanks II 29 and fuel-displaced pipeline; On in-line, be provided with oil-in 1, oil pump 2 and well heater 3; Oil-in 1 is communicated with the import of oil pump 2 and well heater 3 successively, is connected with the material taking mouth I 17 of adsorption tanks I 16 and the material taking mouth II 32 of adsorption tanks II 29 respectively after the outlet shunting of well heater 3, is connected with temperature controller 4 on the well heater 3; Be respectively equipped with duty valve I 22 and duty valve II 20 between the material taking mouth I 17 of the outlet of well heater 3 and adsorption tanks I 16 and the material taking mouth II 32 of adsorption tanks II 32; Fuel-displaced pipeline comprises pressure controller 13, vacuum breaker 12, prime strainer 10, back level strainer 8 and oil outlet 7, and the discharge port I of adsorption tanks I 16 is connected with oil outlet 7 with pressure controller 13, vacuum breaker 12, prime strainer 10, back level strainer 8 successively, and the discharge port II of adsorption tanks II 29 is communicated with the material taking mouth I 17 of adsorption tanks I 16 through pipeline 37 feedback backs; Pipeline 37 is provided with duty valve III 24 and duty valve IV 6; In adsorption tanks I 16 and adsorption tanks II 29, be respectively equipped with compass formula well heater I 34 and compass formula well heater II 30, on compass formula well heater I 34 and compass formula well heater II 30, be respectively equipped with temp controlled meter I 35 and temp controlled meter II 36, the outside surface of adsorption tanks I 16 is provided with dog-house I 15; Communicate in dog-house I 15 and the adsorption tanks I 16; Be provided with oil-feed filter screen I 18 in the adsorption tanks I 16 and go out oil screen I 19, oil-feed filter screen I 18 is positioned at material taking mouth I 17 places, goes out oil screen I 19 and is positioned at discharge port I place; Be provided with qi of chong channel ascending adversely valve I 21 in the outside of material taking mouth I 17; Be provided with qi of chong channel ascending adversely valve III 14 in the outside of discharge port I, the outside surface of adsorption tanks II 29 is provided with dog-house II 26, communicates in dog-house II 26 and the adsorption tanks II 29; Be provided with oil-feed filter screen II 31 in the adsorption tanks II 29 and go out oil screen II 27; Oil-feed filter screen II 31 is positioned at material taking mouth II 32 places, goes out oil screen II 27 and is positioned at discharge port II place, is provided with qi of chong channel ascending adversely valve II 33 in the outside of material taking mouth II 32; Be provided with qi of chong channel ascending adversely valve IV 25 in the outside of discharge port II, prime strainer 10 is respectively equipped with tensimeter I 11 and tensimeter II 9 with the ingress of back level strainer 8.
Claims (7)
1. oil reclaimer; It is characterized in that it comprises in-line, adsorption tanks I (16), adsorption tanks II (29) and fuel-displaced pipeline; On in-line, be provided with oil-in (1), oil pump (2) and well heater (3); Oil-in (1) is communicated with the import of oil pump (2) and well heater (3) successively; Be connected with the material taking mouth I (17) of adsorption tanks I (16) and the material taking mouth II (32) of adsorption tanks II (29) respectively after the outlet shunting of well heater (3); Fuel-displaced pipeline comprises pressure controller (13), vacuum breaker (12), prime strainer (10), back level strainer (8) and oil outlet (7); The discharge port I of adsorption tanks I (16) is connected with oil outlet (7) with pressure controller (13), vacuum breaker (12), prime strainer (10), back level strainer (8) successively; The discharge port II of adsorption tanks II (29) is communicated with the material taking mouth I (17) of adsorption tanks I (16) through pipeline (37) feedback back; In adsorption tanks I (16) and adsorption tanks II (29), be respectively equipped with compass formula well heater I (34) and compass formula well heater II (30), on compass formula well heater I (34) and compass formula well heater II (30), be respectively equipped with temp controlled meter I (35) and temp controlled meter II (36).
2. oil reclaimer according to claim 1; The outside surface that it is characterized in that described adsorption tanks I (16) is provided with dog-house I (15); Communicate in dog-house I (15) and the adsorption tanks I (16); Be provided with oil-feed filter screen I (18) in the adsorption tanks I (16) and go out oil screen I (19), oil-feed filter screen I (18) is positioned at material taking mouth I (17) to be located, and goes out oil screen I (19) and is positioned at discharge port I place; Be provided with qi of chong channel ascending adversely valve I (21) in the outside of material taking mouth I (17), be provided with qi of chong channel ascending adversely valve III (14) in the outside of discharge port I.
3. oil reclaimer according to claim 1; The outside surface that it is characterized in that described adsorption tanks II (29) is provided with dog-house II (26); Communicate in dog-house II (26) and the adsorption tanks II (29); Be provided with oil-feed filter screen II (31) in the adsorption tanks II (29) and go out oil screen II (27), oil-feed filter screen II (31) is positioned at material taking mouth II (32) to be located, and goes out oil screen II (27) and is positioned at discharge port II place; Be provided with qi of chong channel ascending adversely valve II (33) in the outside of material taking mouth II (32), be provided with qi of chong channel ascending adversely valve IV (25) in the outside of discharge port II.
4. oil reclaimer according to claim 1 is characterized in that being respectively equipped with duty valve I (22) and duty valve II (20) between the material taking mouth II (32) of material taking mouth I (17) and adsorption tanks II (32) of outlet and adsorption tanks I (16) of described well heater (3).
5. oil reclaimer according to claim 1 is characterized in that being connected with on the described well heater (3) temperature controller (4).
6. oil reclaimer according to claim 1 is characterized in that described pipeline (37) is provided with duty valve III (24) and duty valve IV (6).
7. oil reclaimer according to claim 1 is characterized in that the ingress of described prime strainer (10) and back level strainer (8) is respectively equipped with tensimeter I (11) and tensimeter II (9).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2012100300191A CN102559362A (en) | 2012-02-12 | 2012-02-12 | Waste oil regeneration apparatus |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2012100300191A CN102559362A (en) | 2012-02-12 | 2012-02-12 | Waste oil regeneration apparatus |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN102559362A true CN102559362A (en) | 2012-07-11 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2012100300191A Pending CN102559362A (en) | 2012-02-12 | 2012-02-12 | Waste oil regeneration apparatus |
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| Country | Link |
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| CN (1) | CN102559362A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102900942A (en) * | 2012-10-30 | 2013-01-30 | 西安勤业石油设备有限责任公司 | Purification system and purification method of lubricating engineering truck |
| CN109731369A (en) * | 2019-02-19 | 2019-05-10 | 安徽国孚凤凰科技有限公司 | A kind of multi-stage absorption extracting II class base oil device of production |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN201978536U (en) * | 2011-01-24 | 2011-09-21 | 重庆市沙坪坝区锋渝滤油机厂 | Reverse-flow type device for regeneration of waste oil |
| CN102295980A (en) * | 2011-07-22 | 2011-12-28 | 重庆大学 | Regeneration method for waste engine oil |
| CN202446858U (en) * | 2012-02-12 | 2012-09-26 | 戚纪锁 | Waste oil reclaiming device |
-
2012
- 2012-02-12 CN CN2012100300191A patent/CN102559362A/en active Pending
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN201978536U (en) * | 2011-01-24 | 2011-09-21 | 重庆市沙坪坝区锋渝滤油机厂 | Reverse-flow type device for regeneration of waste oil |
| CN102295980A (en) * | 2011-07-22 | 2011-12-28 | 重庆大学 | Regeneration method for waste engine oil |
| CN202446858U (en) * | 2012-02-12 | 2012-09-26 | 戚纪锁 | Waste oil reclaiming device |
Non-Patent Citations (1)
| Title |
|---|
| 郭雷等: "机油再生装置的研制", 《内燃机车》 * |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102900942A (en) * | 2012-10-30 | 2013-01-30 | 西安勤业石油设备有限责任公司 | Purification system and purification method of lubricating engineering truck |
| CN109731369A (en) * | 2019-02-19 | 2019-05-10 | 安徽国孚凤凰科技有限公司 | A kind of multi-stage absorption extracting II class base oil device of production |
| CN109731369B (en) * | 2019-02-19 | 2024-05-14 | 安徽国孚凤凰科技有限公司 | Device for producing II-type base oil through multistage adsorption extraction |
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Application publication date: 20120711 |