CN115557714A - Structure for comprehensively recycling lime slaking residues - Google Patents
Structure for comprehensively recycling lime slaking residues Download PDFInfo
- Publication number
- CN115557714A CN115557714A CN202110750113.3A CN202110750113A CN115557714A CN 115557714 A CN115557714 A CN 115557714A CN 202110750113 A CN202110750113 A CN 202110750113A CN 115557714 A CN115557714 A CN 115557714A
- Authority
- CN
- China
- Prior art keywords
- crusher
- ash
- residue
- residues
- lime
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
- 235000008733 Citrus aurantifolia Nutrition 0.000 title claims abstract description 26
- 235000011941 Tilia x europaea Nutrition 0.000 title claims abstract description 26
- 239000004571 lime Substances 0.000 title claims abstract description 26
- 238000004064 recycling Methods 0.000 title claims abstract description 13
- 238000002844 melting Methods 0.000 claims abstract description 19
- 230000008018 melting Effects 0.000 claims abstract description 19
- 239000000839 emulsion Substances 0.000 claims abstract description 10
- 230000029087 digestion Effects 0.000 claims abstract description 3
- 239000008267 milk Substances 0.000 claims description 17
- 210000004080 milk Anatomy 0.000 claims description 17
- 235000013336 milk Nutrition 0.000 claims description 17
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 13
- 238000005070 sampling Methods 0.000 claims description 7
- 238000001514 detection method Methods 0.000 claims description 6
- 239000007787 solid Substances 0.000 claims description 4
- 239000011148 porous material Substances 0.000 claims 1
- 238000004519 manufacturing process Methods 0.000 description 11
- 238000000034 method Methods 0.000 description 5
- 239000000843 powder Substances 0.000 description 4
- 239000000243 solution Substances 0.000 description 4
- 238000003756 stirring Methods 0.000 description 4
- 239000002699 waste material Substances 0.000 description 4
- 239000000428 dust Substances 0.000 description 3
- 239000002245 particle Substances 0.000 description 3
- 238000005406 washing Methods 0.000 description 3
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 238000002360 preparation method Methods 0.000 description 2
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 description 1
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 1
- BRPQOXSCLDDYGP-UHFFFAOYSA-N calcium oxide Chemical compound [O-2].[Ca+2] BRPQOXSCLDDYGP-UHFFFAOYSA-N 0.000 description 1
- 239000000292 calcium oxide Substances 0.000 description 1
- ODINCKMPIJJUCX-UHFFFAOYSA-N calcium oxide Inorganic materials [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000010790 dilution Methods 0.000 description 1
- 239000012895 dilution Substances 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000002349 favourable effect Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000012452 mother liquor Substances 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 239000002893 slag Substances 0.000 description 1
- 229910000029 sodium carbonate Inorganic materials 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B2/00—Lime, magnesia or dolomite
- C04B2/02—Lime
- C04B2/04—Slaking
- C04B2/08—Devices therefor
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C23/00—Auxiliary methods or auxiliary devices or accessories specially adapted for crushing or disintegrating not provided for in preceding groups or not specially adapted to apparatus covered by a single preceding group
- B02C23/08—Separating or sorting of material, associated with crushing or disintegrating
- B02C23/10—Separating or sorting of material, associated with crushing or disintegrating with separator arranged in discharge path of crushing or disintegrating zone
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Ceramic Engineering (AREA)
- Materials Engineering (AREA)
- Structural Engineering (AREA)
- Organic Chemistry (AREA)
- Food Science & Technology (AREA)
- Processing Of Solid Wastes (AREA)
Abstract
The invention discloses a structure for comprehensively recycling lime digestion residues, which comprises an ash melting machine and an ash emulsion tank, wherein the ash melting machine is provided with a residue outlet, the residue outlet is provided with a crusher, and the crusher is connected with the ash emulsion tank.
Description
Technical Field
The invention relates to a structure for comprehensively recycling lime slaking residues, and belongs to the technical field of lime slaking residue recycling.
Background
The traditional lime milk preparation mode in the alumina industry is to adopt an ash melting machine to mix water or mother liquor, washing liquor and the like to operate and melt ash to prepare lime milk, because the lime melting machine can discharge residues in the operation process due to the component and quality problems of lime, the residues can not be recycled and comprehensively utilized, the residues are all subjected to outer piling and then are transported into an ore yard to enter the front end of the production system flow, the red mud amount is increased, the stable operation of the system and the sedimentation and washing consumption are increased, a large amount of carbonate is also promoted to enter the front end flow of the production system, the causticization of sodium carbonate in the system is inhibited to form the anti-causticization effect, partial useful component calcium oxide is carried in the residues in the discharging process, the waste of lime consumption is discarded, the residues are subjected to outer piling, powder dust flying ash is formed after weathering, the environmental protection management is influenced, and the waste of the outer piling management and the transportation labor force are also caused.
The lime powder is used for preparing the lime milk, so that the cost is high, and the market competition of enterprise production is not facilitated.
Disclosure of Invention
The technical problem to be solved by the invention is to provide a structure for comprehensively recycling lime digestion residues, which can avoid the influence of the front end of the flow of the residues entering a production system on the production system, reduce the waste of lime consumption, avoid the influence of environmental protection treatment caused by the formation of powder flying dust due to the drying or weathering of part of components in the residues after the residues are piled outside due to external conditions, and simultaneously avoid the increase of labor force for the stockpiling management and transportation caused by the piling; the defects of the prior art can be overcome.
The technical scheme of the invention is as follows: a structure for comprehensively recycling lime slaking residues comprises an ash melting machine and an ash emulsion groove, wherein a residue outlet is formed in the ash melting machine, a crusher is arranged at the residue outlet, and the crusher is connected with the ash emulsion groove.
The feed opening of the crusher and the ash melting machine are both provided with hot water supply pipes, and the hot water supply main pipe is provided with a solid content index adjusting device.
A stirring device is arranged between the crusher and the lime milk tank, and a concentration detection device is arranged on the stirring device.
The ash melting machine is connected with the crusher, the crusher is connected with the stirring device, and the stirring device is connected with the ash emulsion tank through the transfer tank.
The screen mesh of the crusher is 5mm in aperture.
Compared with the prior art, the structure for comprehensively recycling the lime slaking residue has the following advantages:
(1) The method comprises the steps that a crusher is additionally arranged to crush residues, a slag discharge port of the ash melting machine is designed to be introduced into the crusher, the crusher is started to operate to crush the residues simultaneously in the ash melting machine ash crushing and ash emulsion preparing process, and the crushed lime residues are introduced into an ash emulsion groove to prepare the ash emulsion, so that the ash residues are prevented from being recycled in time to be comprehensively utilized after being stacked outside, transported into a mine storage yard and finally enter the front end of a production system flow again to cause influence on a production system; meanwhile, the consumption waste of lime milk preparation by lime and the formation of powder flying dust by residue outside the pile are avoided, and the increase of labor force for management and transportation caused by residue outside the pile is also avoided.
(2) Hot water supply pipes are arranged on a feed opening of the crusher and the ash melting machine, so that in the process of starting the crusher to operate and crush residues, a small part of water is led out from original hot water which is mixed with water by the ash melting machine to prepare ash emulsion and is used as dilution drainage washing water for crushing the residues, and the residues are prevented from being blocked at a screen after being crushed;
(3) Be equipped with sample detection granularity device between breaker and ash milk groove, add sample detection granularity device like this and can carry out first regulation granularity to the residue after the breakage, through the adjustment that contains index adjusting device admittedly, avoid influencing the quality of follow-up ash milk groove production ash milk, be favorable to further ensureing that production demand ash milk contains the index admittedly.
(4) The screen mesh aperture of the crusher is 5mm, the residue crushing test is carried out, a screen with the aperture of 5mm is selected as a screen, the granularity index is changed from 10-25mm of original particles to the granularity index larger than 5mm and not larger than 12 percent on the screen, and the granularity index of the residue meets the production requirement and is completely recycled to enter the production flow.
Drawings
In order to make the objects, technical solutions and advantages of the present invention more apparent, the present invention will be described in further detail with reference to the accompanying drawings, in which:
fig. 1 is a schematic view of the connection structure of the present invention.
Wherein, the ash melting machine 1; a milk tank 2; a crusher 3; a hot water supply pipe 4; a sampling and detecting granularity device 5; a solid content index adjusting device 6.
Detailed Description
Hereinafter, preferred embodiments of the present invention will be described in detail with reference to the accompanying drawings. It should be understood that the preferred embodiments are illustrative of the invention only and are not limiting upon the scope of the invention.
Embodiment 1. As shown in fig. 1, a structure for comprehensively recycling lime slaking residue comprises an ash melting machine 1 and an ash milk tank 2, wherein the ash melting machine 1 is provided with a residue outlet, the residue outlet is provided with a crusher 3, and the crusher 3 is connected with the ash milk tank 2; the screen mesh aperture of the crusher 3 is 5mm.
A hot water supply pipe 4 is arranged on a feed opening of the crusher 3 and the ash melting machine 1, and a solid content index adjusting device 6 is arranged on the hot water supply pipe 4; a sampling and granularity detecting device 5 is arranged between the crusher 3 and the milk tank 2; the ash melting machine 1 is connected with the crusher 3, the crusher 3 is connected with the sampling and particle size detecting device 5, and the sampling and particle size detecting device 5 is connected with the ash milk tank 2 through transfer tanks.
Finally, the above embodiments are only intended to illustrate the technical solutions of the present invention and not to limit the present invention, and although the present invention has been described in detail with reference to the preferred embodiments, it will be understood by those skilled in the art that modifications or equivalent substitutions may be made on the technical solutions of the present invention without departing from the spirit and scope of the technical solutions, and all of them should be covered by the claims of the present invention.
Claims (5)
1. The utility model provides a lime digestion residue synthesizes recycle's structure, it includes changes ash machine (1) and ash emulsion groove (2), is equipped with the residue export on changing ash machine (1), its characterized in that: and a crusher (3) is arranged at the residue outlet, and the crusher (3) is connected with the milk ash groove (2).
2. The structure for comprehensively recycling lime slaked residue according to claim 1, characterized in that: the feed opening of the crusher (3) and the ash melting machine (1) are both provided with hot water supply pipes (4), and the hot water supply pipes (4) are provided with solid content index adjusting devices (6).
3. The structure for comprehensively recycling lime slaked residue according to claim 1, characterized in that: a sampling granularity detection device (5) is arranged between the crusher (3) and the milk tank (2).
4. The structure for comprehensively recycling lime slake residue according to claim 3, wherein: the ash melting machine is connected with the crusher (3) through a transfer groove, the crusher (3) is connected with the sampling granularity detection device (5), and the sampling granularity detection device (5) is connected with the ash milk groove (2).
5. The structure for comprehensively recycling lime slaked residue according to any one of claims 1 to 4, characterized in that: the screen mesh of the crusher (3) has a pore size of 5mm.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202110750113.3A CN115557714A (en) | 2021-07-02 | 2021-07-02 | Structure for comprehensively recycling lime slaking residues |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202110750113.3A CN115557714A (en) | 2021-07-02 | 2021-07-02 | Structure for comprehensively recycling lime slaking residues |
Publications (1)
Publication Number | Publication Date |
---|---|
CN115557714A true CN115557714A (en) | 2023-01-03 |
Family
ID=84736721
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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CN202110750113.3A Pending CN115557714A (en) | 2021-07-02 | 2021-07-02 | Structure for comprehensively recycling lime slaking residues |
Country Status (1)
Country | Link |
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CN (1) | CN115557714A (en) |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1194236A (en) * | 1998-03-13 | 1998-09-30 | 山东海化集团有限公司 | Method of recovering waste slag |
JP2011147854A (en) * | 2010-01-19 | 2011-08-04 | Yanagida Sangyo Kk | Method and system for treating marine shellfish |
CN204039264U (en) * | 2014-08-26 | 2014-12-24 | 荆门市五三五江消石灰有限责任公司 | With the calcium hydroxide production line of secondary digestion machine |
CN105541136A (en) * | 2016-01-20 | 2016-05-04 | 湖州浙宝冶金辅料有限公司 | Production process and system of calcium hydroxide |
CN208120984U (en) * | 2018-03-27 | 2018-11-20 | 山东海天生物化工有限公司 | A kind of ashing device improving the newborn concentration of ash |
-
2021
- 2021-07-02 CN CN202110750113.3A patent/CN115557714A/en active Pending
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1194236A (en) * | 1998-03-13 | 1998-09-30 | 山东海化集团有限公司 | Method of recovering waste slag |
JP2011147854A (en) * | 2010-01-19 | 2011-08-04 | Yanagida Sangyo Kk | Method and system for treating marine shellfish |
CN204039264U (en) * | 2014-08-26 | 2014-12-24 | 荆门市五三五江消石灰有限责任公司 | With the calcium hydroxide production line of secondary digestion machine |
CN105541136A (en) * | 2016-01-20 | 2016-05-04 | 湖州浙宝冶金辅料有限公司 | Production process and system of calcium hydroxide |
CN208120984U (en) * | 2018-03-27 | 2018-11-20 | 山东海天生物化工有限公司 | A kind of ashing device improving the newborn concentration of ash |
Non-Patent Citations (1)
Title |
---|
刘家兴,李国英: "集装箱式石灰提升机", 纸和造纸 * |
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PB01 | Publication | ||
PB01 | Publication | ||
SE01 | Entry into force of request for substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
RJ01 | Rejection of invention patent application after publication |
Application publication date: 20230103 |