CN103553371A - Method for preparing lime milk in alkaline process aluminium oxide production - Google Patents
Method for preparing lime milk in alkaline process aluminium oxide production Download PDFInfo
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- CN103553371A CN103553371A CN201310568038.4A CN201310568038A CN103553371A CN 103553371 A CN103553371 A CN 103553371A CN 201310568038 A CN201310568038 A CN 201310568038A CN 103553371 A CN103553371 A CN 103553371A
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- lime
- lime milk
- milk
- ashing
- aluminium oxide
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Abstract
The invention relates to a method for preparing lime milk for bayer process two-stage calcium preparation in alkaline process aluminium oxide production. The method is characterized in that the lime milk is prepared by adopting bayer process primary-washing liquefaction ash or/and sintering process coarse liquefaction ash in a lime milk preparation process. The method for preparing the lime milk in the alkaline process aluminium oxide production can be used for reducing the dilution of system concentration and the steam consumption of evaporation. The adopted ashing solutions are from production solutions in the working procedures, and the solution amount is not increased, so that the bayer process through capacity is not influenced, and the separation and washing indexes of the bayer process are not influenced.
Description
Technical field
The present invention relates to a kind of two sections of methods of joining calcium milk of lime preparation used of bayer's process of alkaline process alumina producing.
Background technology
At present, in alkaline process aluminum oxide production process, the blending process of milk of lime is all to adopt water or square position mother liquor to carry out ashing.The problem that this milk of lime blending process exists is: when bayer's process adopts two sections, join calcium, second segment will add milk of lime, and the milk of lime of now water preparation adds in flow process, can cause the water yield of bringing flow process into increase, system concentration is caused and watered down, steam consumption for evaporation is raise; With mother liquor (ak:3.2 left and right) ashing meeting, cause soltion viscosity to increase, lime is difficult to dissolve, and ashing weak effect, also easily causes line clogging.More seriously, with the solution outside bayer's process stripping, red mud separation, washing procedure or water ground, enter this operation, can cause system liquid measure to increase, handling capacity reduces, but also can affect the control of liquid amount balance and postorder index.
Summary of the invention
Object of the present invention is exactly the deficiency existing for above-mentioned prior art, provides a kind of and can effectively reduce the watering down of system concentration, and reduces steam consumption for evaporation, and ashing is effective, and liquid measure maintains the milk of lime compound method of the alkaline process alumina producing of original balance.
The object of the invention is to be achieved through the following technical solutions.
A milk of lime compound method for alumina producing, is characterized in that milk of lime process for preparation adopts Bayer process primary wash liquor ashing or/and crude liquor used sinter method ashing, preparing lime milk.
The milk of lime compound method of a kind of alkaline process alumina producing of the present invention, adopt Bayer process primary wash liquor ashing or crude liquor used sinter method ashing, avoided bringing into the water yield the watering down system concentration of Production Flow Chart completely, reduced steam consumption for evaporation, ashing effect is better, adopts with Bayer process primary wash liquor and crude liquor used sinter method and mixes rear ashing, can reduce watering down system concentration, reduce steam consumption for evaporation, ashing effect is better.The ashing solution adopting all comes from the production solution of this operation, does not increase any liquid measure, makes bayer's process handling capacity unaffected, and bayer's process is separated, washing index is unaffected.
Embodiment
A milk of lime compound method for alumina producing, milk of lime process for preparation adopts Bayer process primary wash liquor ashing or/and crude liquor used sinter method ashing, preparing lime milk.
During operation, send lime slaking machine to carry out ashing the mixed solution of Bayer process primary wash liquor, crude liquor used sinter method or Bayer process primary wash liquor and crude liquor used sinter method, ashing liquid measure used is unrestricted, can, according to carrying required amount allocate arbitrarily, be mixed with the milk of lime that concentration meets production requirement.
Embodiment 1
Send lime slaking machine to mix with lime Bayer process primary wash liquor and carry out ashing, the composition the active calcium ion content of the milk of lime being mixed with reaches 180g/l, enters into high pressure digestion dilution trap, and its system caustic sodium concentration maintains 160g/l; Reduced steam consumption for evaporation.
Embodiment 2
Send lime slaking machine to mix with lime crude liquor used sinter method and carry out ashing, the composition the active calcium ion content of the milk of lime being mixed with reaches 160g/l, enters into high pressure digestion dilution trap, and its system caustic sodium concentration maintains 162g/l; Reduced steam consumption for evaporation.
Embodiment 3
The Bayer process primary wash liquor that is 1:1 by volume ratio and crude liquor used sinter method mixed solution, send lime slaking machine to carry out ashing, and the active calcium ion content reaches 170g/l, enters into high pressure digestion dilution trap, and its system caustic sodium concentration maintains 161g/l; Reduced steam consumption for evaporation.
Claims (1)
1. a milk of lime compound method for alkaline process alumina producing, is characterized in that milk of lime process for preparation adopts Bayer process primary wash liquor ashing or/and crude liquor used sinter method ashing, preparing lime milk.
Priority Applications (1)
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CN201310568038.4A CN103553371A (en) | 2013-11-15 | 2013-11-15 | Method for preparing lime milk in alkaline process aluminium oxide production |
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CN201310568038.4A CN103553371A (en) | 2013-11-15 | 2013-11-15 | Method for preparing lime milk in alkaline process aluminium oxide production |
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CN103553371A true CN103553371A (en) | 2014-02-05 |
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CN201310568038.4A Pending CN103553371A (en) | 2013-11-15 | 2013-11-15 | Method for preparing lime milk in alkaline process aluminium oxide production |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107445182A (en) * | 2017-08-28 | 2017-12-08 | 中国铝业股份有限公司 | A kind of Liquor of Ore Dressing Bayer process matches somebody with somebody calcium method |
Citations (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1346799A (en) * | 2001-11-09 | 2002-05-01 | 天津渤海化工有限责任公司天津碱厂 | Process for turning waste solution from production of soda to lime |
CN1843920A (en) * | 2006-05-17 | 2006-10-11 | 中国铝业股份有限公司 | Ash conversion method in alumina preparation |
CN101100306A (en) * | 2007-07-12 | 2008-01-09 | 中国铝业股份有限公司 | Calcium added method for producing aluminum oxide by Bayer process |
CN101157466A (en) * | 2007-08-03 | 2008-04-09 | 中国铝业股份有限公司 | Method for improving confluence desilication silica index of sintering process crude liquor and bayer process digested pulp |
CN101723424A (en) * | 2009-12-09 | 2010-06-09 | 中国铝业股份有限公司 | Method for increasing concentration of causticized alkali liquor |
CN102259903A (en) * | 2011-06-20 | 2011-11-30 | 中国铝业股份有限公司 | Method for reducing content of sodium carbonate in alumina Bayer process solution |
CN102951666A (en) * | 2012-11-29 | 2013-03-06 | 中国铝业股份有限公司 | Crude-liquid filtering and refining method by Bayer process |
CN102976570A (en) * | 2012-11-26 | 2013-03-20 | 中国铝业股份有限公司 | Method for reducing alkali consumption in Bayer production process |
-
2013
- 2013-11-15 CN CN201310568038.4A patent/CN103553371A/en active Pending
Patent Citations (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1346799A (en) * | 2001-11-09 | 2002-05-01 | 天津渤海化工有限责任公司天津碱厂 | Process for turning waste solution from production of soda to lime |
CN1843920A (en) * | 2006-05-17 | 2006-10-11 | 中国铝业股份有限公司 | Ash conversion method in alumina preparation |
CN101100306A (en) * | 2007-07-12 | 2008-01-09 | 中国铝业股份有限公司 | Calcium added method for producing aluminum oxide by Bayer process |
CN101157466A (en) * | 2007-08-03 | 2008-04-09 | 中国铝业股份有限公司 | Method for improving confluence desilication silica index of sintering process crude liquor and bayer process digested pulp |
CN101723424A (en) * | 2009-12-09 | 2010-06-09 | 中国铝业股份有限公司 | Method for increasing concentration of causticized alkali liquor |
CN102259903A (en) * | 2011-06-20 | 2011-11-30 | 中国铝业股份有限公司 | Method for reducing content of sodium carbonate in alumina Bayer process solution |
CN102976570A (en) * | 2012-11-26 | 2013-03-20 | 中国铝业股份有限公司 | Method for reducing alkali consumption in Bayer production process |
CN102951666A (en) * | 2012-11-29 | 2013-03-06 | 中国铝业股份有限公司 | Crude-liquid filtering and refining method by Bayer process |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107445182A (en) * | 2017-08-28 | 2017-12-08 | 中国铝业股份有限公司 | A kind of Liquor of Ore Dressing Bayer process matches somebody with somebody calcium method |
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Application publication date: 20140205 |