CN109439023A - A technique for functional filler production is carried out using red mud - Google Patents

A technique for functional filler production is carried out using red mud Download PDF

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CN109439023A
CN109439023A CN201811315787.5A CN201811315787A CN109439023A CN 109439023 A CN109439023 A CN 109439023A CN 201811315787 A CN201811315787 A CN 201811315787A CN 109439023 A CN109439023 A CN 109439023A
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red mud
micro mist
powdery
mesh partial
partial size
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张勇
王玉军
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    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09CTREATMENT OF INORGANIC MATERIALS, OTHER THAN FIBROUS FILLERS, TO ENHANCE THEIR PIGMENTING OR FILLING PROPERTIES ; PREPARATION OF CARBON BLACK  ; PREPARATION OF INORGANIC MATERIALS WHICH ARE NO SINGLE CHEMICAL COMPOUNDS AND WHICH ARE MAINLY USED AS PIGMENTS OR FILLERS
    • C09C1/00Treatment of specific inorganic materials other than fibrous fillers; Preparation of carbon black
    • C09C1/40Compounds of aluminium
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K11/00Use of ingredients of unknown constitution, e.g. undefined reaction products
    • C08K11/005Waste materials, e.g. treated or untreated sewage sludge
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K13/00Use of mixtures of ingredients not covered by one single of the preceding main groups, each of these compounds being essential
    • C08K13/06Pretreated ingredients and ingredients covered by the main groups C08K3/00 - C08K7/00
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K9/00Use of pretreated ingredients
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L101/00Compositions of unspecified macromolecular compounds
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L21/00Compositions of unspecified rubbers
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09CTREATMENT OF INORGANIC MATERIALS, OTHER THAN FIBROUS FILLERS, TO ENHANCE THEIR PIGMENTING OR FILLING PROPERTIES ; PREPARATION OF CARBON BLACK  ; PREPARATION OF INORGANIC MATERIALS WHICH ARE NO SINGLE CHEMICAL COMPOUNDS AND WHICH ARE MAINLY USED AS PIGMENTS OR FILLERS
    • C09C3/00Treatment in general of inorganic materials, other than fibrous fillers, to enhance their pigmenting or filling properties
    • C09C3/08Treatment with low-molecular-weight non-polymer organic compounds
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09CTREATMENT OF INORGANIC MATERIALS, OTHER THAN FIBROUS FILLERS, TO ENHANCE THEIR PIGMENTING OR FILLING PROPERTIES ; PREPARATION OF CARBON BLACK  ; PREPARATION OF INORGANIC MATERIALS WHICH ARE NO SINGLE CHEMICAL COMPOUNDS AND WHICH ARE MAINLY USED AS PIGMENTS OR FILLERS
    • C09C3/00Treatment in general of inorganic materials, other than fibrous fillers, to enhance their pigmenting or filling properties
    • C09C3/10Treatment with macromolecular organic compounds

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Treatment Of Sludge (AREA)
  • Processing Of Solid Wastes (AREA)

Abstract

A technique for functional filler production is carried out using red mud, required process is as follows, A: using cyclosizer, surge-tank, Pulp pump, underflow slot, overflow launder, carries out cyclone classification processing to red mud raw material, obtains lower than 400 mesh partial size red mud micro mists and is higher than 400 mesh partial size raw materials;B: the aqueous red mud micro mist that process A is obtained is evaporated using scroll feeder, drying machine, hot-blast stove, drying obtains powdery red mud micro mist, it is handled for being higher than 400 mesh partial size raw materials using scroll feeder, crushing drying equipment, high pressure blower, more rotor vertical air flow graders, pneumatic conveying dryer, with powdery red mud micro mist together as the raw materials for production of rubber filling after progress powder processing;C: using height batch mixer as processing equipment, stearic acid, modified paraffin are used as auxiliary material, the powdery red mud micro mist that step B, C obtains is processed into rubber filling.The present invention all efficiently uses red mud resource, protects ecological environment, has saved soil.

Description

A technique for functional filler production is carried out using red mud
Technical field
The present invention relates to red mud processing method field, especially a kind of skill that functional filler production is carried out using red mud Art.
Background technique
Red mud is the solid slag discharged during producing aluminium oxide etc., is gained the name because appearance is aobvious red.By production oxygen The difference for changing bauxitic feed materials composition of ores and alumina-producing method that aluminium uses, produces the chemistry and mine of red mud after aluminium oxide Object composition has big difference very much.Bauxite mainly has Indonesia, Malaysia, Ao Zhoukuang at present, produces in aluminium oxide process, and general use is visitd Ear method or sintering process, the type of red mud is divided into Bayer process red mud and two kinds of red mud from sintering process after production.Either use Bayer Method or sintering process produce aluminium oxide, and 1 ton of aluminium oxide of every production about gives off 1.0~1.8 tons of red mud.
Currently, byproduct red mud is in stockpiling state after most of manufacturers will produce aluminium oxide, red mud pilling can divide It is stored up for dry piling and wet type.Either dry piling or wet type stockpiling, the stacking processing of red mud not only need to expend big The soil of amount, while the construction and maintenance in stockyard are also required to spend a large amount of expense, a large amount of exposed red muds are long and long in stockyard Just will form dust, fly upward with the wind, pollute atmosphere, people's lives are caused to compare severely impact, also to animals and plants Existence causes immeasurable negative effect, deteriorates the ecological environment on periphery.Since red mud has, aqueous height, retentiveness is strong, contains Alkali height and the features such as partial size is smaller, bad dispersibility, up to the present, does not find an ideal processing mode still both at home and abroad. At present to the application of red mud, only handle lower than 400 mesh partial size red muds below, for the production as cement etc. Raw material uses, and is of limited application, research has shown that, the part on 400 mesh partial sizes is mainly red with siliceous minerals such as quartz sands Based on iron ore, the more difficult grinding processing of these hardness of mineral height, therefore the red mud for being actually higher than 400 mesh or more still can not be effectively big Amount utilizes, and causes the pollution of environment and the waste of resource.
Based on above-mentioned, a kind of production method is provided, raw materials for production of the red mud as other products, nothing can be all efficiently used Strong technical support can be provided to protection environment and resource reutilization by doubting.
Summary of the invention
In order to overcome during existing red mud processes, 400 mesh partial size red muds below can only be carried out using there are the drawbacks of, The present invention provides being handled using advanced processing equipment and technology red mud, at 400 mesh partial size above section crushing Raw materials for production (red mud filler) after partially being handled after reason and below 400 mesh partial sizes as rubber filling, rubber filling conduct The raw materials for production of plastics etc. all efficiently use red mud resource to reach, protect environment, and can obtain preferable economy A kind of technology that functional filler production is carried out using red mud of benefit.
The technical solution adopted by the present invention to solve the technical problems is:
A technique for functional filler production being carried out using red mud, it is characterised in that required process is as follows, A: using rotation Current classifier, surge-tank, Pulp pump, underflow slot, overflow launder carry out cyclone classification processing to red mud raw material, obtain lower than 400 mesh It sieves partial size red mud micro mist and is higher than 400 mesh partial size raw materials;B: process A is obtained using scroll feeder, drying machine, hot-blast stove Aqueous red mud micro mist evaporation, drying obtain powdery red mud micro mist, for be higher than 400 mesh partial size raw materials use screw feed Device, crushing drying equipment, high pressure blower, more rotor vertical air flow graders, pneumatic conveying dryer are handled, and are carried out powder and are added With powdery red mud micro mist together as the raw materials for production of rubber filling after work;C: using height batch mixer as processing equipment, make Stearic acid, modified paraffin are used as auxiliary material, the powdery red mud micro mist that step B, C obtains is processed into rubber filling, stearic acid Raw material can also use aluminate coupling agent.
In the step A, first the red mud raw material that stockyard is excavated is put into surge-tank, water is added to be slurried, admittedly contain concentration 17-18g/l is controlled, then raw material is squeezed into Pulp pump and carries out cyclone classification processing in cyclosizer, according to processing needs 400 mesh partial sizes, 500 mesh partial sizes can be used for classification circle's point, after cyclosizer classification, higher than of 400 mesh partial sizes Grain enters in underflow slot, individually handles after filters pressing separates, and filtrate returns in surge-tank as seasoning liquid and is recycled, and is lower than The particle of 400 mesh partial sizes enters overflow launder by overflow, obtains after filters pressing separation micro- lower than the aqueous red mud of 400 mesh partial sizes Powder.
In the step B, cyclone classification is dewatered to be lower than 400 mesh partial size red mud particles, feeds through scroll feeder Drying machine, red mud material are mixed in drying machine with the hot wind that hot-blast stove provides, and are evaporated moisture and are broken up and obtain powdery in powdery Red mud micro mist;When for being higher than 400 mesh partial size feedstock processing, raw material, which enters to crush in drying equipment through scroll feeder, to be carried out Processing, the hot-air air distribution plate of pneumatic conveying dryer it is the allocated enter crush drying equipment hothouse in, and high speed rotation to Upper movement, in the case where crushing the grinder of drying equipment, the collective effect of high pressure blower swirling eddy, material is pulverized, refines, point Fluidization is dissipated, is dried simultaneously, material is dried to as powdery product, and it is vertical then to ascend into more rotors with gas spiral It is screened in formula gas flow sizing machine, according to the red mud micro mist for requiring gradable each particle size range out, more rotor vertical gas flow points Particle after grade machine classification is collected through loading head, and dusty gas is filtered through bag collector and emptied, and the dust of collection is as high level-one Red mud micro mist, can be obtained after processing using 800 mesh partial sizes as leading products micro mist two, quantum of output 75%, while output grain Spend 400-800 mesh partial size micro mist one, quantum of output 20%;The above micro mist three of 2500 mesh partial size of granularity, quantum of output 5%;? To the obtained powdery red mud micro mist of red mud micro mist one, red mud micro mist two, red mud micro mist three, high level-one red mud micro mist and process B Together as the raw materials for production of rubber filling.
In the step C, using in height batch mixer be used as processing equipment, red mud micro mist one, the red mud that step B is obtained The powdery red mud micro mist that micro mist two, red mud micro mist three, high level-one red mud micro mist and process B obtain first pours into high mixing machine, so Stearic acid, modified paraffin are added thereto in 1% to 3% ratio afterwards, be sufficiently mixed uniformly, temperature does not surpass when height is mixed 120 degree are crossed, being cool below 25 degree by water when low mixed can discharge, and produce functional red mud filler, and red mud filler has Dispersibility, compatibility well.
The medicine have the advantages that the present invention is handled red mud using advanced processing equipment and technology, 400 meshes Raw materials for production (red mud after partially being handled after partial size above section pulverization process and below 400 mesh partial sizes as rubber filling Filler), raw materials for production of the rubber filling as plastics etc., what is obtained can also directly dry progress higher than 400 mesh partial size raw materials High iron ore sale.After the present invention is used as the filler of plastics-production, the alkali in red mud is released when can thermally decompose with PVC (plastics) HCl (hydrogen chloride) gas react, to inhibit the degradation and decomposition of PVC, common PVC product uses 8 Nian Houqiang outdoor Degree safety loses, and the plastics for adding red mud still remain good mechanical property for a long time, has no aging phenomenon, or even strong Degree is increased, this also embodies excellent function of the red mud as plastic filler.The present invention reaches all effective to red mud resource It utilizes, protects ecological environment, saved soil, both had an economic benefit or have a social benefit.Based on above-mentioned, so the present invention has The application prospect having had.
Detailed description of the invention
The present invention is described further with reference to the accompanying drawings and examples.
Fig. 1 is flow diagram of the present invention.
Specific embodiment
Shown in Fig. 1, a technique for functional filler production being carried out using red mud, required process is as follows, A: using rotation Current classifier, surge-tank, Pulp pump, underflow slot, overflow launder carry out cyclone classification processing to red mud raw material, obtain lower than 400 mesh It sieves partial size red mud micro mist and is higher than 400 mesh partial size raw materials;B: using scroll feeder, strong drying machine, hot-blast stove by process A The obtained evaporation of aqueous red mud micro mist, drying obtains powdery red mud micro mist, is fed for being higher than 400 mesh partial size raw materials using spiral Glassware, powerful smashing drying equipment, high pressure blower, more rotor vertical air flow graders, forced airflow drying equipment are handled, With powdery red mud micro mist together as the raw materials for production of rubber filling after progress powder processing;C: using height batch mixer as at Equipment is managed, uses stearic acid, modified paraffin that the powdery red mud micro mist that step B, C obtains is processed into rubber and plastic as auxiliary material and fills out Material, stearic acid raw material can also use aluminate coupling agent.
Shown in Fig. 1, in step A, first the red mud raw material that stockyard is excavated is put into surge-tank, water is added to be slurried, Gu 17-18g/l is controlled containing concentration, then raw material is squeezed into Pulp pump and carries out cyclone classification processing in cyclosizer, according to adding Work needs can be used 400 mesh partial sizes, 500 mesh partial sizes and is higher than 400 mesh grains after cyclosizer classification for classification circle's point The particle of diameter enters in underflow slot, individually handles after filters pressing separates, and filtrate returns in surge-tank as seasoning liquid and is recycled, Particle lower than 400 mesh partial sizes enters overflow launder by overflow, obtains after filters pressing separation aqueous red lower than 400 mesh partial sizes Mud micro mist.
Shown in Fig. 1, in step B, cyclone classification is dewatered to be lower than 400 mesh partial size red mud particles, through screw feed Device feeds strong drying machine, and red mud material mixes with the hot wind that hot-blast stove provides in strong drying machine, evaporates moisture and break up Powdery red mud micro mist is obtained in powdery;When for being higher than 400 mesh partial size feedstock processing, raw material enters strength through scroll feeder It crushes and is handled in drying equipment, the hot-air of forced airflow drying equipment enters powerful smashing drying through air distribution plate distribution and sets In standby hothouse, and high speed rotation moves upwards, in the grinder of powerful smashing drying equipment, high pressure blower swirling eddy Under collective effect, material is dispersed fluidization, is dried simultaneously, material is dried to as powdered products by powerful smashing, refinement Product are then ascended into more rotor vertical air flow graders with gas spiral and are screened, according to require it is gradable go out each grain The red mud micro mist of diameter range, the particle after more rotor vertical air flow grader classifications are collected through loading head, and dusty gas is received through bag The filtering emptying of dirt device, the dust of collection can be obtained as higher leveled red mud micro mist after processing with 800 mesh partial sizes as main artificial delivery Product micro mist two, quantum of output 75%, while output granularity 400-800 mesh partial size micro mist one, quantum of output 20%;Granularity 2500 The above micro mist three of mesh partial size, quantum of output 5%;Obtained red mud micro mist one, red mud micro mist two, red mud micro mist three, high level-one are red The raw materials for production of mud micro mist and powdery red mud micro mist together as rubber filling.
Shown in Fig. 1, using processing equipment is used as in height batch mixer, red mud micro mist one, the red mud that step B is obtained are micro- The powdery red mud micro mist that powder two, red mud micro mist three, high level-one red mud micro mist and process B obtain first pours into high mixing machine, then Stearic acid, modified paraffin are added thereto in 1% to 3% ratio, be sufficiently mixed uniformly, temperature is no more than when height is mixed 120 degree, being cool below 25 degree by water when low mixed can discharge, and produce functional red mud filler, and red mud filler has very Dispersibility well, compatibility.Red mud micro mist as rubber filling key be solve red mud micro mist dispersibility and with rubber, plastics The surface activation techniques of the compatibility of equal basis materials, red mud micro mist carry out table using stearic acid or aluminate coupling agent material Face activation, plays surface oleophylic not hydrophilic interaction, conducive to the Quality advance of plastics;Using modified paraffin as special lubrication And (modified paraffin is the improved maleic anhydride of crosslinking technology to dispersant material, and grafting rate is higher than 1%, is better than same kind of products at abroad Grafting rate) as a variety of combination inorganic material hydroxyl, the carboxyls being easy to itself contained in matrix and red mud, play sufficiently Compatible role, while neutralizing the free alkali in red mud, therefore, the rigidity and other characteristics of red mud can be given full play of, And do not influence the toughness of plastic matrix material.
Shown in Fig. 1, the powerful smashing drying equipment that the present invention uses, working principle is granular material by screw feeding Hothouse is added in device, and the hot-air of forced airflow drying equipment enters the drying of powerful smashing drying equipment through air distribution plate distribution Room, and after high speed rotation moves upwards, in the collective effect of the grinder of powerful smashing drying equipment, high pressure blower swirling eddy Under, material is dispersed fluidization, is dried simultaneously by powerful smashing, refinement.Forced airflow drying equipment is set in rotary flash distillation It is improved on the basis of standby, the spreading disk of flashing apparatus is changed to high speed rotor, has certain pulverization that can beat red mud More disperse, more preferable with the effect of hot air, to reduce the energy consumption of crushing, drying, comparing than flashing apparatus can be reduced 30% or so.More rotor vertical air flow graders, general grader separate 400 mesh of fineness highest, are unable to satisfy micron order powder The production of body, it is domestic at present for the above micro mist production of 2000 mesh, mostly use horizontal scroll gas flow sizing machine.The present invention uses Vertical more rotor gas flow sizing machines, can be used for the production of 5000 mesh powder body materials, can be realized the life of high mesh number powder body material It produces, compared to horizontal more rotor gas flow sizing machines of same rotor bank, production capacity improves 30%, and power consumption reduces by 30%.
Shown in Fig. 1, the present invention is handled red mud using advanced processing equipment and technology, 400 mesh partial sizes with Raw materials for production (red mud filler) after partially being handled after upper part pulverization process and below 400 mesh partial sizes as rubber filling, Raw materials for production of the rubber filling as plastics etc., can also directly drying higher than 400 mesh partial size raw materials for obtaining carry out high iron ore Sale.After the present invention is used as the filler of plastics-production, HCl that alkali in red mud is released when can thermally decompose with PVC (plastics) (hydrogen chloride) gas reacts, thus inhibit the degradation and decomposition of PVC, common PVC product Strength Safety after outdoor use 8 years It loses, and the plastics for adding red mud still remain good mechanical property for a long time, have had no aging phenomenon or even intensity Increase, this also embodies excellent function of the red mud as plastic filler.The present invention, which reaches, all efficiently uses red mud resource, protects Ecological environment has been protected, soil has been saved, both had an economic benefit or has had a social benefit.Based on above-mentioned, so what the present invention had had Application prospect.
Basic principles and main features and advantages of the present invention of the invention have been shown and described above, for this field skill For art personnel, it is clear that the present invention is limited to the details of above-mentioned exemplary embodiment, and without departing substantially from spirit or base of the invention In the case where eigen, the present invention can be realized in other specific forms.It therefore, in all respects, should all be by reality Apply example and regard exemplary as, and be non-limiting, the scope of the present invention by appended claims rather than above description It limits, it is intended that including all changes that fall within the meaning and scope of the equivalent elements of the claims in the present invention. Any reference signs in the claims should not be construed as limiting the involved claims.
In addition, it should be understood that although this specification is described in terms of embodiments, but not each embodiment is only wrapped Containing an independent technical solution, this description of the specification is merely for the sake of clarity, and those skilled in the art should It considers the specification as a whole, the technical solutions in the various embodiments may also be suitably combined, forms those skilled in the art The other embodiments being understood that.

Claims (4)

1. a kind of technology for carrying out functional filler production using red mud, it is characterised in that required process is as follows, A: using eddy flow Grader, surge-tank, Pulp pump, underflow slot, overflow launder carry out cyclone classification processing to red mud raw material, obtain lower than 400 meshes Partial size red mud micro mist and be higher than 400 mesh partial size raw materials;B: process A is obtained using scroll feeder, drying machine, hot-blast stove The evaporation of aqueous red mud micro mist, drying obtain powdery red mud micro mist, for be higher than 400 mesh partial size raw materials using scroll feeder, It crushes drying equipment, high pressure blower, more rotor vertical air flow graders, pneumatic conveying dryer to be handled, carries out powder processing Afterwards with powdery red mud micro mist together as the raw materials for production of rubber filling;C: it using height batch mixer as processing equipment, uses The powdery red mud micro mist that step B, C obtains is processed into rubber filling as auxiliary material by stearic acid, modified paraffin, and stearic acid is former Material can also use aluminate coupling agent.
2. a kind of technology for carrying out functional filler production using red mud according to claim 1, it is characterised in that step A In, first the red mud raw material that stockyard is excavated is put into surge-tank, water is added to be slurried, admittedly 17-18g/l is controlled containing concentration, then Raw material is squeezed into Pulp pump and carries out cyclone classification processing in cyclosizer, according to processing need can be used 400 mesh partial sizes, 500 mesh partial sizes are classification circle's point, and after cyclosizer classification, the particle higher than 400 mesh partial sizes enters in underflow slot, through pressing It is individually handled after filter separation, filtrate returns in surge-tank as seasoning liquid and is recycled, and the particle lower than 400 mesh partial sizes passes through Overflow enters overflow launder, obtains the aqueous red mud micro mist lower than 400 mesh partial sizes after filters pressing separation.
3. a kind of technology for carrying out functional filler production using red mud according to claim 1, it is characterised in that step B In, cyclone classification is dewatered to be lower than 400 mesh partial size red mud particles, feeds drying machine through scroll feeder, red mud material exists Drying machine is mixed with the hot wind that hot-blast stove provides, and is evaporated moisture and is broken up and obtains powdery red mud micro mist in powdery;For being higher than When 400 mesh partial size feedstock processing, raw material, which enters to crush in drying equipment through scroll feeder, to be handled, pneumatic conveying dryer Hot-air air distribution plate it is the allocated enter in the hothouse for crushing drying equipment, and high speed rotation moves upwards, and is crushing drying Under the grinder of equipment, the collective effect of high pressure blower swirling eddy, material is pulverized, refines, and disperses fluidization, carries out simultaneously Dry, material is dried to as powdery product, then with gas spiral ascend into more rotor vertical air flow graders into Row screening, the particle according to the red mud micro mist for requiring gradable each particle size range out, after more rotor vertical air flow graders classifications It is collected through loading head, dusty gas is filtered through bag collector and emptied, and the dust of collection is as higher leveled red mud micro mist, after processing It can be obtained using 800 mesh partial sizes as leading products micro mist two, quantum of output 75%, while output granularity 400-800 mesh partial size Micro mist one, quantum of output 20%;The above micro mist three of 2500 mesh partial size of granularity, quantum of output 5%;It is obtained red mud micro mist one, red The powdery red mud micro mist that mud micro mist two, red mud micro mist three, high level-one red mud micro mist and process B obtain is together as rubber filling Raw materials for production.
4. a kind of technology for carrying out functional filler production using red mud according to claim 1, it is characterised in that step C In, using in height batch mixer be used as processing equipment, the red mud micro mist one that step B is obtained, red mud micro mist two, red mud micro mist Three, the powdery red mud micro mist that high level-one red mud micro mist and process B obtain first pours into high mixing machine, then by stearic acid, modification Paraffin is added thereto in 1% to 3% ratio, be sufficiently mixed uniformly, when height is mixed, temperature is no more than 120 degree, when low mixed Being cool below 25 degree by water can discharge, and produce functional red mud filler, and red mud filler has dispersibility, phase well Capacitive.
CN201811315787.5A 2018-11-07 2018-11-07 A technique for functional filler production is carried out using red mud Pending CN109439023A (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN114031898A (en) * 2021-06-09 2022-02-11 中国科学院兰州化学物理研究所 Aminated dealkalized red mud material, aminated dealkalized red mud toughened epoxy resin composite material and preparation method

Citations (16)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5385586A (en) * 1993-03-24 1995-01-31 Nalco Chemical Company Liquor oxalate stabilizers
CN2536572Y (en) * 2002-03-26 2003-02-19 中国铝业股份有限公司 Red mud separator for production of aluminum oxide by sintering process
CN1743077A (en) * 2005-09-22 2006-03-08 贵阳铝镁设计研究院 Coarse-fine red mud grading method
CN1772617A (en) * 2005-09-28 2006-05-17 中国铝业股份有限公司 Sintering process of separating red mud for alumina production
CN100998964A (en) * 2007-01-13 2007-07-18 沈阳铝镁设计研究院 Series red mud clinker dissolving out and red mud separation technology
CN101787227A (en) * 2010-01-19 2010-07-28 王立通 Production method of red mud filler
CN102120595A (en) * 2010-01-07 2011-07-13 贵阳铝镁设计研究院 Red mud separating and washing method
CN102492234A (en) * 2011-11-22 2012-06-13 中国铝业股份有限公司 Production method of red mud complexed polyvinyl chloride colorized rigid plastic
CN102642854A (en) * 2012-05-21 2012-08-22 修武县钜龙科技有限公司 Treatment method of red mud in Bayer process production flow of aluminum oxide
CN103483880A (en) * 2013-10-09 2014-01-01 张釜维 Production method of red mud filler
CN203842820U (en) * 2014-03-26 2014-09-24 合肥中亚建材装备有限责任公司 Vertical multi-rotor superfine micro-powder grader
CN104261361A (en) * 2014-09-11 2015-01-07 云南红富化肥有限公司 Washing and direct flotation method of low-grade refractory argillaceous phosphorite
CN105214832A (en) * 2015-10-28 2016-01-06 山东科技大学 A kind of gravity separation method red mud efficiently selects iron system and technique
CN108031546A (en) * 2017-12-27 2018-05-15 大连地拓环境科技有限公司 A kind of method of red mud recycling iron
CN108484983A (en) * 2018-04-19 2018-09-04 安徽工业大学 A kind of red mud with high efficiency flame retardance-SILICA FUME compounded rubber filler and preparation method thereof
CN108686828A (en) * 2018-05-29 2018-10-23 湖南埃铝环保科技有限公司 A method of sorting carries iron and removes sodium from red mud

Patent Citations (16)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5385586A (en) * 1993-03-24 1995-01-31 Nalco Chemical Company Liquor oxalate stabilizers
CN2536572Y (en) * 2002-03-26 2003-02-19 中国铝业股份有限公司 Red mud separator for production of aluminum oxide by sintering process
CN1743077A (en) * 2005-09-22 2006-03-08 贵阳铝镁设计研究院 Coarse-fine red mud grading method
CN1772617A (en) * 2005-09-28 2006-05-17 中国铝业股份有限公司 Sintering process of separating red mud for alumina production
CN100998964A (en) * 2007-01-13 2007-07-18 沈阳铝镁设计研究院 Series red mud clinker dissolving out and red mud separation technology
CN102120595A (en) * 2010-01-07 2011-07-13 贵阳铝镁设计研究院 Red mud separating and washing method
CN101787227A (en) * 2010-01-19 2010-07-28 王立通 Production method of red mud filler
CN102492234A (en) * 2011-11-22 2012-06-13 中国铝业股份有限公司 Production method of red mud complexed polyvinyl chloride colorized rigid plastic
CN102642854A (en) * 2012-05-21 2012-08-22 修武县钜龙科技有限公司 Treatment method of red mud in Bayer process production flow of aluminum oxide
CN103483880A (en) * 2013-10-09 2014-01-01 张釜维 Production method of red mud filler
CN203842820U (en) * 2014-03-26 2014-09-24 合肥中亚建材装备有限责任公司 Vertical multi-rotor superfine micro-powder grader
CN104261361A (en) * 2014-09-11 2015-01-07 云南红富化肥有限公司 Washing and direct flotation method of low-grade refractory argillaceous phosphorite
CN105214832A (en) * 2015-10-28 2016-01-06 山东科技大学 A kind of gravity separation method red mud efficiently selects iron system and technique
CN108031546A (en) * 2017-12-27 2018-05-15 大连地拓环境科技有限公司 A kind of method of red mud recycling iron
CN108484983A (en) * 2018-04-19 2018-09-04 安徽工业大学 A kind of red mud with high efficiency flame retardance-SILICA FUME compounded rubber filler and preparation method thereof
CN108686828A (en) * 2018-05-29 2018-10-23 湖南埃铝环保科技有限公司 A method of sorting carries iron and removes sodium from red mud

Non-Patent Citations (4)

* Cited by examiner, † Cited by third party
Title
侯炳毅等: "除砂工艺在拜尔法氧化铝生产中的应用", 《山西冶金》 *
樊文贞: "降低拜耳法赤泥含水率的工业实践", 《轻金属》 *
解竹柏等: "赤泥填充CPE防水卷材的研究", 《山东建材》 *
赵勇: "旋流器在氧化铝溶出赤泥分离中的应用", 《世界有色金属》 *

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN114031898A (en) * 2021-06-09 2022-02-11 中国科学院兰州化学物理研究所 Aminated dealkalized red mud material, aminated dealkalized red mud toughened epoxy resin composite material and preparation method

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Application publication date: 20190308