CN106622672A - Float fine coal cell distribution treatment technique - Google Patents
Float fine coal cell distribution treatment technique Download PDFInfo
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- CN106622672A CN106622672A CN201710101285.1A CN201710101285A CN106622672A CN 106622672 A CN106622672 A CN 106622672A CN 201710101285 A CN201710101285 A CN 201710101285A CN 106622672 A CN106622672 A CN 106622672A
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- coal
- flotation
- fine coal
- ash content
- ash
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03D—FLOTATION; DIFFERENTIAL SEDIMENTATION
- B03D1/00—Flotation
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03D—FLOTATION; DIFFERENTIAL SEDIMENTATION
- B03D1/00—Flotation
- B03D1/14—Flotation machines
- B03D1/1406—Flotation machines with special arrangement of a plurality of flotation cells, e.g. positioning a flotation cell inside another
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- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Biotechnology (AREA)
- Processing Of Solid Wastes (AREA)
- Solid Fuels And Fuel-Associated Substances (AREA)
Abstract
The invention discloses a float fine coal cell distribution treatment technique. The float fine coal cell distribution treatment technique comprises the following steps that coal to be treated is subjected to primary flotation operation; the ash content of fine coal of flotation cells of a flotation machine of primary flotation operation is detected; the fine coal with the low ash content is directly conveyed to filter dehydration equipment through the corresponding flotation cells and subjected to dehydration, a fine coal product is obtained, and the fine coal with the high ash content is subjected to secondary flotation operation; and the fine coal which is separated through secondary flotation operation enters a fine coal filter press and is subjected to dehydration, and another fine coal product is obtained. According to the float fine coal cell distribution treatment technique, the problem that in the traditional technique, ash carrying is caused due to the fact that primary flotation low-ash fine coal is subjected to secondary flotation concentration is effectively avoided, the fine coal productive rate is effectively increased, the ash content of fine coal is decreased, and chemical consumption is reduced.
Description
Technical field
The invention belongs to flotation technology field, and in particular to a kind of floatation clean coal point groove handling process.
Background technology
In recent years, due to the increasing and the development of mechanical coal mining technology of coal mining degree, characteristics of coal slime is constantly disliked
Change, and market is higher to product quality requirement, traditional coal slime floating process is increasingly unsatisfactory for existing requirement, therefore improves biography
System floatation process is extremely urgent.
Traditional coal slime flotation process is that floatation feed is sent into flotation device, and by flotation device cleaned coal and tail are sub-elected
Coal, subsequently into respective subsequent processing operations.The floatation process is simple to operate, and disposal ability is big, with low cost, but is answering
There are problems that cleans ash height, reagent consumption with during.In recent years, domestic coal preparation plant prevalence de slime flotation technique and
Secondary flotation technique.De slime flotation technology process flow process be before ore pulp enters and floats using the desliming device such as desliming pond, desliming screen will-
The height ash thin mud of 0.03mm is removed in advance, and rest materials enter flotation operation, and the technique reduces flotation operation in application process
Operating pressure, reduce cleans ash, reduce reagent consumption, but it is excessive to there is desliming device floor space, production cost is high
The shortcomings of;Secondary flotation technology process flow process is to carry out recleaning to a floatation clean coal after a flotation in ore pulp,
The technique effectively reduces cleans ash, improves quality of cleaned coal, but has that clean coal yield is too low, secondary flotation work operations pressure
Excessive the problems such as.Therefore, a kind of raising clean coal yield how is developed, cleans ash is reduced and is reduced the floatation process of production cost
Become those skilled in the art's technical barrier urgently to be resolved hurrily.
The content of the invention
For disadvantages mentioned above, the present invention proposes a kind of floatation clean coal point groove handling process.
The present invention proposes a kind of floatation clean coal point groove handling process, comprises the steps:
S1, pending coal is delivered to a flotation operation;
The cleaned coal that S2, each flotation cell to a flotation operation flotation device are sub-elected carries out respectively ash content detection;
S3, according to the ash content testing result of S2, the low cleaned coal of ash content is directly transported into filter dewatering equipment by the flotation cell
Dehydration forms head coal product, and the high cleaned coal of ash content is transported into secondary flotation operation by its respective flotation cell;
S4, the cleaned coal that secondary flotation operation is sub-elected is transported to clean coal pressur filter carries out processed, obtain floatation clean coal
Product.
Preferably, ash content detection is carried out to the cleaned coal of each flotation cell using coal slurry ash content on-line detector in S2.
Preferably, the low cleaned coal of ash content is directly transported into centrifugal dehydrator dehydration, centrifugal dehydration by the flotation cell in S3
Machine filter cake directly forms head coal product, and filtrate enters secondary flotation operation.
Preferably, the clean coal pressur filter in S4 is fast opening pressure filter.
The beneficial effects of the present invention is:
(1) in the present invention, due to floatation feed, advanced first flotation cell is sorted in flotation device, cleaned coal emersion;Tail coal enters
Enter the sorting of the second flotation cell, cleaned coal emersion, tail coal is sorted into the 3rd flotation cell ..., the like, until last is floating
Groove tail coal is selected to discharge as a floating tail-coal, each flotation cell cleans ash becomes larger.Using coal slurry ash content on-line checking
Instrument detects to each flotation cell cleans ash, and the cleaned coal for meeting head coal product ash content standard is directly entered centrifugal dehydrator and takes off
Water forms head coal product, and the cleaned coal for not meeting head coal product ash content standard enters secondary flotation operation, it is to avoid the low ash of a flotation
Cleaned coal enters secondary flotation operation gravity treatment back of the body ash, improves clean coal yield, reduces cleans ash, reduces the work of secondary flotation operation
Pressure.
(2) in the present invention, the low ash extract coal product that a flotation is sub-elected enters centrifugal dehydrator processed, secondary floating
The head coal product that choosing is sub-elected is due to the higher entrance fast opening pressure filter processed of moisture, it is to avoid different head coal products enter same
One dewatering operation, improves dewatering efficiency.
(3) in the present invention, a floatation clean coal processes the filtrate for producing into centrifugal dehydrator and enters secondary flotation, it is to avoid
The loss of cleaned coal.
Description of the drawings
Fig. 1:A kind of floatation clean coal proposed by the present invention point groove processing technological flow figure.
Specific embodiment
Fig. 1 is a kind of floatation clean coal proposed by the present invention point groove processing technological flow figure.
Technical scheme is specifically described below by specific embodiment.Using four trough floatation machines, it is desirable to essence
Ash content of coal index is less than 10%.
Embodiment 1
S1, pending coal is delivered to a flotation operation;
S2, ash content detection is carried out respectively to the cleaned coal that four flotation cells of a flotation operation are sub-elected, its ash content index is shown in
Table 1;
The each groove ash content index/% of table 1 embodiment, 1 flotation
One groove cleaned coal | Two groove cleaned coal | Three groove cleaned coal | Four groove cleaned coal | |
Ash content/% | 5.60 | 6.92 | 8.64 | 9.81 |
S3, according to the ash content testing result of S2, four flotation cell cleans ash are below 10%, meet head coal product ash content
Require, being directly transported to centrifugal dehydrator carries out processed, and filter cake forms head coal product, and filtrate enters secondary flotation operation;
S4, the cleaned coal that secondary flotation operation is sub-elected is transported to clean coal pressur filter carries out processed, obtain floatation clean coal
Product.
Embodiment 2
S1, pending coal is delivered to a flotation operation;
S2, ash content detection is carried out respectively to the cleaned coal that four flotation cells of a flotation operation are sub-elected, its ash content index is shown in
Table 2;
The each groove ash content index/% of table 2 embodiment, 2 flotation
One groove cleaned coal | Two groove cleaned coal | Three groove cleaned coal | Four groove cleaned coal | |
Ash content/% | 7.38 | 8.77 | 10.44 | 13.27 |
S3, according to the ash content testing result of S2, a groove, two groove cleans ash are below 10%, meet head coal product ash content
Require, being directly transported to centrifugal dehydrator carries out processed, filter cake forms head coal product, filtrate enters secondary flotation operation, three
Groove, four groove cleans ash are above 10%, do not meet head coal product ash requirements, are transported to secondary flotation operation;
S4, the cleaned coal that secondary flotation operation is sub-elected is transported to clean coal pressur filter carries out processed, obtain floatation clean coal
Product.
Embodiment 3
S1, pending coal is delivered to a flotation operation;
S2, ash content detection is carried out respectively to the cleaned coal that four flotation cells of a flotation operation are sub-elected, its ash content index is shown in
Table 3;
The each groove ash content index/% of table 3 embodiment, 3 flotation
One groove cleaned coal | Two groove cleaned coal | Three groove cleaned coal | Four groove cleaned coal | |
Ash content/% | 10.12 | 11.28 | 12.56 | 14.11 |
S3, according to the ash content testing result of S2, four flotation cell cleans ash are above 10%, do not meet head coal product ash
Divide and require, be transported to secondary flotation operation;
S4, the cleaned coal that secondary flotation operation is sub-elected is transported to clean coal pressur filter carries out processed, obtain floatation clean coal
Product.
Above-described embodiment is only the present invention preferably specific embodiment, but protection scope of the present invention is not limited to
This, various modifications or equivalent that technology according to the present invention scheme is made all should fall within the scope of protection of the present invention.
Claims (4)
1. a kind of floatation clean coal divides groove handling process, it is characterised in that comprise the steps:
S1, pending coal is delivered to a flotation operation;
The cleaned coal that S2, each flotation cell to a flotation operation flotation device are sub-elected carries out respectively ash content detection;
S3, according to the ash content testing result of S2, the low cleaned coal of ash content is directly transported into filter dewatering equipment dehydration by the flotation cell
Head coal product is formed, the high cleaned coal of ash content is transported into secondary flotation operation by its respective flotation cell;
S4, the cleaned coal that secondary flotation operation is sub-elected is transported to clean coal pressur filter carries out processed, obtain floatation clean coal product.
2. a kind of floatation clean coal according to claim 1 divides groove handling process, it is characterised in that using coal slurry ash in S2
On-line detector is divided to carry out ash content detection to the cleaned coal of each flotation cell.
3. a kind of floatation clean coal according to claim 1 divides groove handling process, it is characterised in that in S3 that ash content is low
Cleaned coal is directly transported to centrifugal dehydrator dehydration by the flotation cell, and centrifugal dehydrator filter cake directly forms head coal product, and filtrate enters
Secondary flotation operation.
4. a kind of floatation clean coal according to claim 1 divides groove handling process, it is characterised in that the cleaned coal press filtration in S4
Machine is fast opening pressure filter.
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CN201710101285.1A CN106622672A (en) | 2017-02-24 | 2017-02-24 | Float fine coal cell distribution treatment technique |
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Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN109078747A (en) * | 2018-06-26 | 2018-12-25 | 山西天地王坡煤业有限公司 | The method and device of coarse-fine coal classification production |
CN110899001A (en) * | 2019-10-24 | 2020-03-24 | 国家能源集团乌海能源有限责任公司 | Two-stage flotation process for difficult-to-float coal slime |
CN112371351A (en) * | 2020-09-21 | 2021-02-19 | 新汶矿业集团有限责任公司洗煤分公司 | Fine coal slime deep processing technology |
CN114643194A (en) * | 2022-03-21 | 2022-06-21 | 河南天元煤业有限公司 | Method for treating flotation concentrate by adopting fine screen |
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CN102430480A (en) * | 2011-10-19 | 2012-05-02 | 中国矿业大学 | Coarse clean coal regrinding recleaning separation technique |
CN104138808A (en) * | 2014-08-19 | 2014-11-12 | 四川达竹煤电(集团)有限责任公司渡市选煤发电厂 | Three-product flotation coal preparation technique |
CN105597940A (en) * | 2016-01-04 | 2016-05-25 | 淮北矿业股份有限公司 | Coal dressing flotation process for coal dressing plant |
CN205253375U (en) * | 2015-10-19 | 2016-05-25 | 中国矿业大学 | Column type flotation equipment |
WO2016135368A1 (en) * | 2015-02-26 | 2016-09-01 | Micropulva Ltd Oy | Method for refining of in power plants produced coal ash and coal containing ashes produced in other combustion processings |
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2017
- 2017-02-24 CN CN201710101285.1A patent/CN106622672A/en active Pending
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
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CN102430480A (en) * | 2011-10-19 | 2012-05-02 | 中国矿业大学 | Coarse clean coal regrinding recleaning separation technique |
CN104138808A (en) * | 2014-08-19 | 2014-11-12 | 四川达竹煤电(集团)有限责任公司渡市选煤发电厂 | Three-product flotation coal preparation technique |
WO2016135368A1 (en) * | 2015-02-26 | 2016-09-01 | Micropulva Ltd Oy | Method for refining of in power plants produced coal ash and coal containing ashes produced in other combustion processings |
CN205253375U (en) * | 2015-10-19 | 2016-05-25 | 中国矿业大学 | Column type flotation equipment |
CN105597940A (en) * | 2016-01-04 | 2016-05-25 | 淮北矿业股份有限公司 | Coal dressing flotation process for coal dressing plant |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN109078747A (en) * | 2018-06-26 | 2018-12-25 | 山西天地王坡煤业有限公司 | The method and device of coarse-fine coal classification production |
CN110899001A (en) * | 2019-10-24 | 2020-03-24 | 国家能源集团乌海能源有限责任公司 | Two-stage flotation process for difficult-to-float coal slime |
CN112371351A (en) * | 2020-09-21 | 2021-02-19 | 新汶矿业集团有限责任公司洗煤分公司 | Fine coal slime deep processing technology |
CN114643194A (en) * | 2022-03-21 | 2022-06-21 | 河南天元煤业有限公司 | Method for treating flotation concentrate by adopting fine screen |
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Application publication date: 20170510 |