CN108620400A - The method for exempting to accompany washing oil mechanical tank cleaning - Google Patents
The method for exempting to accompany washing oil mechanical tank cleaning Download PDFInfo
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- CN108620400A CN108620400A CN201810218290.5A CN201810218290A CN108620400A CN 108620400 A CN108620400 A CN 108620400A CN 201810218290 A CN201810218290 A CN 201810218290A CN 108620400 A CN108620400 A CN 108620400A
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- Prior art keywords
- oil
- tank
- cleaning
- exempting
- point temperature
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Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B08—CLEANING
- B08B—CLEANING IN GENERAL; PREVENTION OF FOULING IN GENERAL
- B08B9/00—Cleaning hollow articles by methods or apparatus specially adapted thereto
- B08B9/08—Cleaning containers, e.g. tanks
- B08B9/0804—Cleaning containers having tubular shape, e.g. casks, barrels, drums
- B08B9/0813—Cleaning containers having tubular shape, e.g. casks, barrels, drums by the force of jets or sprays
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B08—CLEANING
- B08B—CLEANING IN GENERAL; PREVENTION OF FOULING IN GENERAL
- B08B9/00—Cleaning hollow articles by methods or apparatus specially adapted thereto
- B08B9/08—Cleaning containers, e.g. tanks
- B08B9/083—Removing scrap from containers, e.g. removing labels
Abstract
The present invention relates to oil-refining chemical industry Large Oil Tank cleaning technique fields, disclose a kind of method for exempting to accompany washing oil mechanical tank cleaning, include the following steps:(1) heating tank base oil makes it have certain mobility, then vacuum suction out and the mechanical injection equipment sent to arranging on can body of boosting, action of forced stirring mixing;(2) continue heating tank base oil, make deep fat that there is 360 degree of flows without dead angle Hybrid Heating in tank;(3) each point temperature and liquid level in tank are checked, each point temperature, liquid level change curve are drawn out;(4) when each point temperature and liquid level tend to be steady, start, to oil is sent outside, to be carried out at the same time hot-oil circulation heat preservation;(5) after sending oil, the aqueous-base cleaning hot water circuit of largest loop flow is established, heavy oil is periodically skimmed into recycling, when no heavy oil skims, terminate aqueous-base cleaning.The invention avoids the uses for largely accompanying washing oil, reduce the consumption of cleaning supplies.
Description
Technical field
The present invention relates to oil-refining chemical industry Large Oil Tank cleaning technique fields, and in particular to one kind is exempted to accompany oil washer
The method of the clear tank of tool.
Background technology
With the promotion of oil-refining chemical enterprise production capacity, crude oil storage capacity greatly increases, and petroleum tank overhauls the need to mechanical tank cleaning
Ask growing.Currently, cleaning crude oil storage tank needs the light-weight fuel oil using 2-4 times of tank bottom oil sludge reserve as accompanying early period
Washing oil, these light-weight fuel oils are mostly product oil, are mixed just into sump oil with heavy dirty oil, tank bottom sludge after treatment.One
The prodigious waste of lightweight finished fuels oil is caused, a large amount of sump oils is accordingly generated, occupies huge stocks;Two increase device sump oil
Freshening rate, more important is some crude oil tank farms not to have this kind of light oil, more not the channel of dirty oil recycling, this just gives oil tank clear
It washes and increases very burden;Three carry out the processing production capacity that freshening sump oil occupies many valuable devices again, cause vicious circle, economical
Cost is also larger.Therefore, the large-scale oil depot for not light-weight fuel oil or do not have freshening sump oil ability enterprise, can only hope and
Step, has seriously affected the business development of mechanical tank cleaning, it would be highly desirable to develop a set of stronger method of mechanical tank cleaning Technological adaptability.
Invention content
The purpose of the invention is to overcome the prior art to exist to accompany washing oil cleaning to lead to follow-up complicated processes and accompany washing oil
A large amount of wastes the problems such as, a kind of method for exempting to accompany washing oil mechanical tank cleaning is provided.
To achieve the goals above, one aspect of the present invention provides a kind of method for exempting to accompany washing oil mechanical tank cleaning, including following
Step:
(1) heating tank base oil makes it have certain mobility, and then vacuum suction out and on force feed to can body is arranged
Mechanical injection equipment, action of forced stirring mixing;
(2) continue heating tank base oil, make deep fat that there is 360 degree of flows without dead angle Hybrid Heating in tank;
(3) each point temperature and liquid level in tank are checked, each point temperature, liquid level change curve are drawn out, is machine
Tool spraying equipment provides data and supports;
(4) when each point temperature and liquid level tend to be steady, start, to oil is sent outside, to be carried out at the same time hot-oil circulation heat preservation;
(5) after sending oil, the aqueous-base cleaning hot water circuit of largest loop flow is established, heavy oil is periodically skimmed into recycling,
When no heavy oil skims, terminate aqueous-base cleaning.
Compared with prior art, the invention has the advantages that:
1) mechanical tank cleaning technique is eliminated to accompanying the source of washing oil and the misgivings in place to go;
2) consumption of cleaning supplies is reduced;
3) adaptability of mechanical tank cleaning is improved.
Specific implementation mode
The endpoint of disclosed range and any value are not limited to the accurate range or value herein, these ranges or
Value should be understood as comprising the value close to these ranges or value.For numberical range, between the endpoint value of each range, respectively
It can be combined with each other between the endpoint value of a range and individual point value, and individually between point value and obtain one or more
New numberical range, these numberical ranges should be considered as specific open herein.
The specific implementation mode of the present invention is described in detail below.It should be understood that described herein specific
Embodiment is merely to illustrate and explain the present invention, and is not intended to restrict the invention.
The present invention provides a kind of methods for exempting to accompany washing oil mechanical tank cleaning, include the following steps:
(1) heating tank base oil makes it have certain mobility, and then vacuum suction comes out and boosts and send to cloth on can body
The mechanical injection equipment set, action of forced stirring mixing;
(2) continue heating tank base oil, make deep fat that there is 360 degree of flows without dead angle Hybrid Heating in tank;
(3) each point temperature and liquid level in tank are checked, each point temperature, liquid level change curve are drawn out, is machine
Tool spraying equipment provides data and supports, for example, need to increase emitted dose in low-temperature region, high liquid level region, raising is stirred strong
Degree;
(4) when each point temperature and liquid level tend to be steady, start, to oil is sent outside, to be carried out at the same time hot-oil circulation heat preservation, with
Maintain it that there is relatively stronger mobility, guarantee to move back oily thorough;
(5) after sending oil, the aqueous-base cleaning hot water circuit of largest loop flow is established, heavy oil is periodically skimmed into recycling,
When no heavy oil skims, terminate aqueous-base cleaning.
The mechanical tank cleaning technique of the present invention can not only remove the use for accompanying washing oil from, but also significantly reduce cleaning adminicle
The use of material, while improving the adaptability of mechanical tank cleaning.
It is easy to aspirate to enable tank bottom oil preferably to flow according to the present invention, in step (1), the heating
Temperature is 50-70 DEG C, and the flow of the vacuum suction is 5-15t/h.
It is described in step (1) to make tank bottom oil be heated through mechanical injection equipment Forced Mixing, fully according to the present invention
Can body is tank deck and/or pot sidewall.
According to the present invention, in step (1), the mechanical injection equipment is rotating machinery spray gun, strong using high-pressure jet
Mixing liquid processed.
According to the present invention, it is the flowing of abundant heat cycles, thoroughly eliminates heating dead angle, in step (2), the temperature of the heating
Degree is 80-100 DEG C, and the flow of the deep fat is 50-100t/h.
It is thoroughly to eliminate heating dead angle according to the present invention, in step (2), the time of the heating is 70-75 hours.
According to the present invention, in order in due course to sending oil outside, in step (4), 5 DEG C of temperature difference <, each point between each point temperature
Mixing temperature >=90 DEG C of temperature, the liquid level difference < 5cm.
According to the present invention, to ensure the abundant recycling of heavy oil, in step (5), the aqueous-base cleaning hot water circuit 45-50 is small
When.
According to the present invention, in step (5), the method for the aqueous-base cleaning hot water circuit is added water to higher than steam into tank
Coil pipe height is added the cleaning agent of a concentration of 0.5-1 weight ‰, is heated to 80-100 DEG C.
According to the present invention, as long as cleaning agent can thoroughly clean the cleaning agent of grease.The cleaning agent is that RFC series is clear
Lotion, can thorough purge tank base oil.
According to the present invention, during the aqueous-base cleaning cycle, timing adjustment eject position and injection intensity make to be adhered to tank
Bottom and tank skin heavy oil come into full contact with cleaning agent, in dissolving stripping to water.
The present invention will be described in detail by way of examples below.In following embodiment, in the feelings being not particularly illustrated
It is raw materials used to be all made of commercial product under condition.
Embodiment 1
A method of exempt to accompany washing oil mechanical tank cleaning, include the following steps:
(1) tank bottom oil vapour coil pipe is heated to 60 DEG C, after making tank bottom oil that there is certain mobility, by mechanical clear
Vacuum (vacuum degree 70KPa) suction of tank equipment setting, is 10t/h with flow, tank bottom oil is pumped out, and boosts to
1.0MPa is sent to tank deck and the rotating machinery spray gun of pot sidewall arrangement, is mixed using high-pressure jet action of forced stirring so that coil pipe
Heat less than place can also heat, make tank bottom oil fully flow;
(2) it as tank bottom oil mobility enhances, is uniformly mixed, continues to be heated to 90 DEG C, hot-oil circulation flow reaches 80t/
H so that deep fat in tank 360 degree without dead angle Hybrid Heating, thoroughly eliminate heating dead angle, this process needs to be carried out continuously 72 small
When;
(3) each point temperature and liquid level in tank are checked, each point temperature, liquid level change curve are drawn out, for rotation
Tool spray gun of making a connection provides data and supports;
(4) when each point temperature and liquid level tend to be steady (5 DEG C of temperature difference < between each point temperature, each point temperature it is mixed
Temperature is closed up to 90 DEG C, liquid level difference < 5cm), start, to oil is sent outside, hot-oil circulation heat preservation to be carried out at the same time, to maintain it to have
Relatively stronger mobility, guarantee are moved back oily thorough;
(5) after sending oil, the RFC series that a concentration of 1 weight ‰ is added higher than steam pipe coil height is added water into tank
Cleaning agent of grease stain is heated to 90 DEG C, establishes the aqueous-base cleaning hot water circuit of largest loop flow, and recycle the phase in aqueous-base cleaning
Between, timing adjustment eject position and injection intensity make to be adhered to tank bottom and tank skin heavy oil come into full contact with cleaning agent, and dissolving stripping is arrived
In water, the heavy oil that cycle is taken out of is periodically skimmed by recycling using oil skimmer, when no heavy oil skims, terminates aqueous-base cleaning, by water
It exits, you can carry out clear tank according to other steps of normal wash tank, specially:High-pressure water jet agitator tank bed mud, works as tank bottom
Mud agitation and dilution is extracted out after having certain fluidity by slush pump (suction machine), and progress muddy water is mechanically decoupled outside tank, separates
Dry mud collected as solid waste, the water source of the clear water of recycling as high-pressure water jet, circulating and recovering is cleaned up up to tank bottom mud,
Until cleaning finishes.
After tested, chemical cleaning project does not influence construction speed because exempting from the due to of accompanying washing oil, the introducing of aqueous-base cleaning so that tube wall,
Oily fully penetrated diffusion dissolution, is come out by abundant recycling in tank bottom and the heavy oil stain and greasy filth of steam pipe coil attachment, cleaning effect
Fruit is ideal, and the heavy oil rate of recovery is up to 95.5%.
Embodiment 2
A method of exempt to accompany washing oil mechanical tank cleaning, include the following steps:
(1) tank bottom oil vapour coil pipe is heated to 50 DEG C, after making tank bottom oil that there is certain mobility, by mechanical clear
The vacuum suction of tank equipment setting, is 5t/h with flow, tank bottom oil is pumped out, and boosts and send to tank deck and pot sidewall arrangement
Rotating machinery spray gun in, utilize high-pressure jet action of forced stirring mixing so that coil pipe heating less than place can also heat, make tank
Base oil fully flows;
(2) it as tank bottom oil mobility enhances, is uniformly mixed, continues to be heated to 100 DEG C, hot-oil circulation flow reaches
100t/h so that deep fat in tank 360 degree without dead angle Hybrid Heating, thoroughly eliminate heating dead angle, this process needs be carried out continuously
70 hours;
(3) each point temperature and liquid level in tank are checked, each point temperature, liquid level change curve are drawn out, for rotation
Tool spray gun of making a connection provides data and supports;
(4) (5 DEG C of temperature difference <, the mixing of each point temperature between each point temperature when each point temperature and liquid level tend to be steady
Temperature is up to 100 DEG C, the liquid level difference < 5cm), start, to oil is sent outside, hot-oil circulation heat preservation to be carried out at the same time, to maintain its tool
There are relatively stronger mobility, guarantee to move back oily thorough;
(5) it after sending oil, is added water into tank higher than steam pipe coil height, the RFC systems of a concentration of 0.5 weight ‰ is added
Row cleaning agent of grease stain is heated to 80 DEG C, establishes the aqueous-base cleaning hot water circuit of largest loop flow, and recycle the phase in aqueous-base cleaning
Between, timing adjustment eject position and injection intensity make to be adhered to tank bottom and tank skin heavy oil come into full contact with cleaning agent, and dissolving stripping is arrived
In water, the heavy oil that cycle is taken out of is periodically skimmed by recycling using oil skimmer, when no heavy oil skims, terminates aqueous-base cleaning, by water
It exits, you can carry out clear tank according to other steps of normal wash tank, specially:High-pressure water jet agitator tank bed mud, works as tank bottom
Mud agitation and dilution is extracted out after having certain fluidity by slush pump (suction machine), and progress muddy water is mechanically decoupled outside tank, separates
Dry mud collected as solid waste, the water source of the clear water of recycling as high-pressure water jet, circulating and recovering is cleaned up up to tank bottom mud,
Until cleaning finishes.
After tested, chemical cleaning project does not influence construction speed because exempting from the due to of accompanying washing oil, the introducing of aqueous-base cleaning so that tube wall,
Oily fully penetrated diffusion dissolution, is come out by abundant recycling in tank bottom and the heavy oil stain and greasy filth of steam pipe coil attachment, cleaning effect
Fruit is ideal, and the heavy oil rate of recovery is up to 95.5%.
Embodiment 3
A kind of process for exempting to accompany washing oil mechanical tank cleaning, includes the following steps:
(1) tank bottom oil vapour coil pipe is heated to 70 DEG C, after making tank bottom oil that there is certain mobility, by mechanical clear
The vacuum suction of tank equipment setting, is 15t/h with flow, tank bottom oil is pumped out, and boosts and send to tank deck and pot sidewall cloth
In the rotating machinery spray gun set, utilize high-pressure jet action of forced stirring mixing so that coil pipe heating less than place can also heat, make
Tank bottom oil fully flows;
(2) it as tank bottom oil mobility enhances, is uniformly mixed, continues to be heated to 80 DEG C, hot-oil circulation flow reaches 60t/
H so that deep fat in tank 360 degree without dead angle Hybrid Heating, thoroughly eliminate heating dead angle, this process needs to be carried out continuously 75 small
When;
(3) each point temperature and liquid level in tank are checked, each point temperature, liquid level change curve are drawn out, for rotation
Tool spray gun of making a connection provides data and supports;
(4) (the mixing of 5 DEG C of temperature difference <, each point temperature between each point temperature when each point temperature and liquid level tend to be steady
Temperature is up to 95 DEG C, liquid level difference < 5cm), start, to oil is sent outside, hot-oil circulation heat preservation to be carried out at the same time, to maintain it with phase
To stronger mobility, guarantee is moved back oily thorough;
(5) it after sending oil, is added water into tank higher than steam pipe coil height, the RFC systems of a concentration of 0.8 weight ‰ is added
Row cleaning agent of grease stain is heated to 100 DEG C, establishes the aqueous-base cleaning hot water circuit of largest loop flow, and recycle in aqueous-base cleaning
Period, timing adjustment eject position and injection intensity make to be adhered to tank bottom and tank skin heavy oil come into full contact with cleaning agent, dissolving stripping
Into water, the heavy oil that cycle is taken out of is periodically skimmed by recycling using oil skimmer, when no heavy oil skims, terminates aqueous-base cleaning, it will
Water exits, you can carries out clear tank according to other steps of normal wash tank, specially:High-pressure water jet agitator tank bed mud, works as tank
Bed mud agitation and dilution is extracted out after having certain fluidity by slush pump (suction machine), and progress muddy water is mechanically decoupled outside tank, point
The dry mud gone out is collected as solid waste, the water source of the clear water of recycling as high-pressure water jet, and circulating and recovering is until the cleaning of tank bottom mud is done
Only, until cleaning finishes.
After tested, chemical cleaning project does not influence construction speed because exempting from the due to of accompanying washing oil, the introducing of aqueous-base cleaning so that tube wall,
Oily fully penetrated diffusion dissolution, is come out by abundant recycling in tank bottom and the heavy oil stain and greasy filth of steam pipe coil attachment, cleaning effect
Fruit is ideal, and the heavy oil rate of recovery is up to 95.3%.
Embodiment 4
A kind of process for exempting to accompany washing oil mechanical tank cleaning, includes the following steps:
(1) tank bottom oil vapour coil pipe is heated to 60 DEG C, after making tank bottom oil that there is certain mobility, by mechanical clear
Vacuum (vacuum degree 70KPa) suction of tank equipment setting, is 10t/h with flow, tank bottom oil is pumped out, and boosts to
1.0MPa is sent in the rotating machinery spray gun arranged to pot sidewall, is mixed using high-pressure jet action of forced stirring so that coil pipe heats not
To place can also heat, make tank bottom oil fully flow;
(2) it as tank bottom oil mobility enhances, is uniformly mixed, continues to be heated to 90 DEG C, hot-oil circulation flow reaches 90t/
H so that deep fat in tank 360 degree without dead angle Hybrid Heating, thoroughly eliminate heating dead angle, this process needs to be carried out continuously 73 small
When;
(3) each point temperature and liquid level in tank are checked, each point temperature, liquid level change curve are drawn out, for rotation
Tool spray gun of making a connection provides data and supports;
(4) when each point temperature and liquid level tend to be steady (5 DEG C of temperature difference < between each point temperature, each point temperature it is mixed
Temperature is closed up to 93 DEG C, liquid level difference < 5cm), start, to oil is sent outside, hot-oil circulation heat preservation to be carried out at the same time, to maintain it to have
Relatively stronger mobility, guarantee are moved back oily thorough;
(5) it after sending oil, is added water into tank higher than steam pipe coil height, the RFC systems of a concentration of 0.6 weight ‰ is added
Row cleaning agent of grease stain is heated to 90 DEG C, establishes the aqueous-base cleaning hot water circuit of largest loop flow, and recycle the phase in aqueous-base cleaning
Between, timing adjustment eject position and injection intensity make to be adhered to tank bottom and tank skin heavy oil come into full contact with cleaning agent, and dissolving stripping is arrived
In water, the heavy oil that cycle is taken out of is periodically skimmed by recycling using oil skimmer, when no heavy oil skims, terminates aqueous-base cleaning, by water
It exits, you can carry out clear tank according to other steps of normal wash tank.
After tested, chemical cleaning project does not influence construction speed because exempting from the due to of accompanying washing oil, the introducing of aqueous-base cleaning so that tube wall,
Oily fully penetrated diffusion dissolution, is come out by abundant recycling in tank bottom and the heavy oil stain and greasy filth of steam pipe coil attachment, cleaning effect
Fruit is ideal, and the heavy oil rate of recovery is up to 95.1%.
Comparative example 1
Different from embodiment 1 is only in that, the cleaning agent used is conventional oil based cleaning agent.After tested, oil base cleans
Agent is added before heating, after heat cycles, sends oil mass outside and does not obviously increase, and follow-up hot water oil skimming efficiency is just lower, heavy oil
It is adhered in tank bottom and tank skin with grease, can not climb up on top of the water and skim, the heavy oil in greasy filth, which goes out to skim, not to be come out, oil and mud after oil skimming
It still mixes, the heavy oil rate of recovery is less than 70%.
Comparative example 2
Different from embodiment 1 is only in that, lacks and checks each point temperature and liquid level in tank, draws out each point temperature
Degree, liquid level change curve provide data for rotating machinery spray gun and support, to also be not concerned with each point temperature and liquid level
Whether height tends to be steady, and directs out and send oil.
After tested, dissolubility oily in the heavy oil stain and greasy filth of tube wall, tank bottom and steam pipe coil attachment is poor, cannot be filled
Recycling is divided to come out, the heavy oil rate of recovery is less than 70%.
The preferred embodiment of the present invention has been described above in detail, and still, the present invention is not limited thereto.In the skill of the present invention
In art conception range, technical scheme of the present invention can be carried out a variety of simple variants, including each technical characteristic with it is any its
Its suitable method is combined, and it should also be regarded as the disclosure of the present invention for these simple variants and combination, belongs to
Protection scope of the present invention.
Claims (11)
1. a kind of method for exempting to accompany washing oil mechanical tank cleaning, which is characterized in that include the following steps:
(1) heating tank base oil makes it have certain mobility, the machine that then vacuum suction out and on force feed to can body is arranged
Tool spraying equipment, action of forced stirring mixing;
(2) continue heating tank base oil, make deep fat that there is 360 degree of flows without dead angle Hybrid Heating in tank;
(3) each point temperature and liquid level in tank are checked, each point temperature, liquid level change curve are drawn out;
(4) when each point temperature and liquid level tend to be steady, start, to oil is sent outside, to be carried out at the same time hot-oil circulation heat preservation;
(5) after sending oil, the aqueous-base cleaning hot water circuit of largest loop flow is established, heavy oil is periodically skimmed into recycling, until
When no heavy oil skims, terminate aqueous-base cleaning.
2. the method according to claim 1 for exempting to accompany washing oil mechanical tank cleaning, which is characterized in that in step (1), the heating
Temperature be 50-70 DEG C, the flow of the vacuum suction is 5-15t/h.
3. the method according to claim 1 for exempting to accompany washing oil mechanical tank cleaning, which is characterized in that in step (1), the can body
For tank deck and/or pot sidewall.
4. the method according to claim 1 for exempting to accompany washing oil mechanical tank cleaning, which is characterized in that in step (1), the machinery
Spraying equipment is rotating machinery spray gun.
5. the method for exempting to accompany washing oil mechanical tank cleaning according to any one of claim 1-4, which is characterized in that step
(2) in, the temperature of the heating is 80-100 DEG C, and the flow of the deep fat is 50-100t/h.
6. the method for exempting to accompany washing oil mechanical tank cleaning according to any one of claim 1-4, which is characterized in that step
(2) in, the time of the heating is 70-75 hours.
7. the method for exempting to accompany washing oil mechanical tank cleaning according to any one of claim 1-4, which is characterized in that step
(4) in, 5 DEG C of temperature difference < between each point temperature, mixing temperature >=90 DEG C of each point temperature, the liquid level difference < 5cm.
8. the method for exempting to accompany washing oil mechanical tank cleaning according to any one of claim 1-4, which is characterized in that step
(5) in, aqueous-base cleaning hot water circuit 45-50 hours.
9. the method for exempting to accompany washing oil mechanical tank cleaning according to any one of claim 1-4, which is characterized in that step
(5) in, the method for the aqueous-base cleaning hot water circuit is added water into tank higher than steam pipe coil height, and a concentration of 0.5- is added
The cleaning agent of 1 weight ‰, is heated to 80-100 DEG C.
10. the method according to claim 9 for exempting to accompany washing oil mechanical tank cleaning, which is characterized in that the cleaning agent is RFC systems
Row cleaning agent.
11. the method for exempting to accompany washing oil mechanical tank cleaning according to any one of claim 1-4, which is characterized in that described
During aqueous-base cleaning recycles, timing adjustment eject position and injection intensity.
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CN201810218290.5A CN108620400A (en) | 2018-03-16 | 2018-03-16 | The method for exempting to accompany washing oil mechanical tank cleaning |
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CN201810218290.5A CN108620400A (en) | 2018-03-16 | 2018-03-16 | The method for exempting to accompany washing oil mechanical tank cleaning |
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Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN112718736A (en) * | 2020-12-11 | 2021-04-30 | 辽阳科瑞特石油化工有限公司 | Water-based cleaning method for refining and chemical device |
CN114210676A (en) * | 2021-12-14 | 2022-03-22 | 张家港中远海运金港化工物流有限公司 | Cleaning method for tank box for transporting lubricating oil |
CN114408397A (en) * | 2021-12-14 | 2022-04-29 | 张家港中远海运金港化工物流有限公司 | Tank cleaning method |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102825039A (en) * | 2012-09-25 | 2012-12-19 | 杰瑞能源服务有限公司 | Method for cleaning oil tank |
CN104291542B (en) * | 2014-09-24 | 2016-05-25 | 北京蓝星清洗有限公司 | Silt displacement reclaimer and method at the bottom of a kind of Plates of Oil Storage Tank |
CN205289162U (en) * | 2015-11-19 | 2016-06-08 | 黄河裕泰(宁夏)环保科技有限公司 | Oil storage tank machinery self - cleaning system |
-
2018
- 2018-03-16 CN CN201810218290.5A patent/CN108620400A/en active Pending
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102825039A (en) * | 2012-09-25 | 2012-12-19 | 杰瑞能源服务有限公司 | Method for cleaning oil tank |
CN104291542B (en) * | 2014-09-24 | 2016-05-25 | 北京蓝星清洗有限公司 | Silt displacement reclaimer and method at the bottom of a kind of Plates of Oil Storage Tank |
CN205289162U (en) * | 2015-11-19 | 2016-06-08 | 黄河裕泰(宁夏)环保科技有限公司 | Oil storage tank machinery self - cleaning system |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN112718736A (en) * | 2020-12-11 | 2021-04-30 | 辽阳科瑞特石油化工有限公司 | Water-based cleaning method for refining and chemical device |
CN112718736B (en) * | 2020-12-11 | 2022-08-05 | 辽宁科瑞特石油化工有限公司 | Water-based cleaning method for refining and chemical device |
CN114210676A (en) * | 2021-12-14 | 2022-03-22 | 张家港中远海运金港化工物流有限公司 | Cleaning method for tank box for transporting lubricating oil |
CN114408397A (en) * | 2021-12-14 | 2022-04-29 | 张家港中远海运金港化工物流有限公司 | Tank cleaning method |
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Application publication date: 20181009 |
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