CN104085898B - Method of preparing tubular clay by polar polymer intercalation - Google Patents

Method of preparing tubular clay by polar polymer intercalation Download PDF

Info

Publication number
CN104085898B
CN104085898B CN201410330738.4A CN201410330738A CN104085898B CN 104085898 B CN104085898 B CN 104085898B CN 201410330738 A CN201410330738 A CN 201410330738A CN 104085898 B CN104085898 B CN 104085898B
Authority
CN
China
Prior art keywords
clay
mud
tubulose
intercalation
slurry
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.)
Expired - Fee Related
Application number
CN201410330738.4A
Other languages
Chinese (zh)
Other versions
CN104085898A (en
Inventor
曾雄丰
张文丽
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
North China University of Science and Technology
Original Assignee
North China University of Science and Technology
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by North China University of Science and Technology filed Critical North China University of Science and Technology
Priority to CN201410330738.4A priority Critical patent/CN104085898B/en
Publication of CN104085898A publication Critical patent/CN104085898A/en
Application granted granted Critical
Publication of CN104085898B publication Critical patent/CN104085898B/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

  • Compositions Of Macromolecular Compounds (AREA)
  • Solid-Sorbent Or Filter-Aiding Compositions (AREA)
  • Water Treatment By Sorption (AREA)
  • Preparation Of Clay, And Manufacture Of Mixtures Containing Clay Or Cement (AREA)
  • Silicates, Zeolites, And Molecular Sieves (AREA)

Abstract

The invention relates to a method of preparing tubular clay by polar polymer intercalation and belongs to the field of functional ceramic materials. The clay used by the functional ceramic material is Suzhou soil which mainly comprises mineral compositions of millite and kaolinite; the intercalator is polar low molecular polyacrylic acid, of which the viscosity average molecular weigh is 1800-2400g/mol and the additive amount is 0.5-1wt%. The preparation method comprises the following steps: weighing a certain amount of Suzhou soil and mixing with a proper amount of distilled water to obtain slurry, wherein the distilled water is weighed in a mass ratio of distilled water to clay of 1 to 1; adding 0.5-1wt% of stronger ammonia water based on mass of slurry, wherein the mass fraction of NH3 in stronger ammonia water is 25.0-28.0%; pouring into a ball mill tank to grind for 12 hours; then, adding 0.5-1wt% of polyacrylic acid based on mass of slurry, and grinding for 24 hours to obtain intercalated slurry; grinding the intercalated slurry by a millstone mill for 1 hour; then, drying and dispersing to obtain the dry powder tubular clay. The clay provided by the invention can be used as a harmful substance adsorbent, a clarifying agent for turbid water and a sealant for radioactive wastes and toxic materials and has important meaning in the field of environmental protection, water safety and the like.

Description

A kind of method that polar polymer intercalation prepares tubulose clay
Technical field
The invention belongs to ceramic material field, and in particular to a kind of polar polymer intercalation prepares the side of tubulose clay Method.
Technical background
The industry such as textile printing and dyeing, papermaking, plastics and leather all produces substantial amounts of waste water from dyestuff every year, because many dyestuffs are Complicated organic matter containing azo bond, poly aromatic rings, can teratogenesis, carcinogenic, mutagenesis, therefore, the removal of this kind of Wastewater Dyes It is extremely important.Many dyestuffs are anti-oxidant, difficult degradation, have greater advantage using the dyestuff in adsorbent removal waste water.Activated carbon It is a kind of effective adsorbent, but it is expensive, limit its extensive use.
Clay mineral has the characteristics such as adsorptivity, ion exchangeable, dispersiveness, in terms of environmental improvement, clay pit with it Thing can be used as noxious substance agent, the fining agent of muddy water, sealant of radioactive waste and poisonous material etc..But, glue Adsorptivity, ion exchangeable, dispersiveness of soil particle etc. are influenceed very big by clay particle microscopic appearance.And natural clay mineral its More than the microscopic appearance of particle in the form of sheets, it is bar-shaped, particle size is generally tens microns, limit clay in environmental improvement should With.
The present invention is by the working process to natural clay mineral, increasing specific surface area, reduction particle size, change particle Pattern etc., obtains high adsorption, macroion exchangeability, the tubulose clay of polymolecularity, and the tubulose clay is in environmental protection and water The fields such as purified treatment have a good application prospect.
The content of the invention
It is an object of the invention to be directed to the deficiency that natural clay is applied in environmental improvement, there is provided a kind of high-ratio surface The preparation method of long-pending, low particle diameter, the tubulose clay of high absorption property.
Technical scheme is with technical characteristic:
It is intercalation object with clay, intercalator is polar low molecular polyacrylic acid, and polyacrylic acid viscosity average molecular weigh is 1800 ~2400g/mol, addition are ‰~10wt of 5wt ‰, weigh a certain amount of Suzhou soil and are mixed into mud with appropriate distilled water, are steamed The amount of distilled water is pressed with clay mass ratio as measure at 1: 1, adds the concentrated ammonia liquor of the ‰~10wt of 5wt ‰ of quality of mud fluid to pour into ball grinder In mill 12h.The polyacrylic acid for adding the ‰~10wt of 5wt ‰ of quality of mud fluid obtains intercalation mud through the 24h that mills, using disk Mill mills 1h intercalation mud, then dry powder tubulose clay is obtained after drying and dispersion.
Clay used is with raw clay that kaolinite and illite are main mineral composition.
Concentrated ammonia liquor used is the ‰~10wt of 5wt ‰ of quality of mud fluid, NH3 mass fractions content 25.0% in concentrated ammonia liquor~ 28.0%.
Low-molecular polypropylene acid viscosity average molecular weigh used is 1800~2400g/mol.
5~20 μm of the length of obtained tubulose clay, 100~200nm of diameter.
Specific embodiment
Embodiment 1
Selection is intercalation object with the Suzhou soil that illite and kaolinite are main mineral composition, weighs 150g Suzhou soils, 150ml distilled water is measured, the amount of distilled water is pressed with clay mass ratio as measure at 1: 1, in addition ball grinder.It is guiding with ammoniacal liquor Agent, measures 1.5ml concentrated ammonia liquors, in concentrated ammonia liquor, NH3Mass fraction is content 25.0%~28.0%, pours into ball grinder and mills 12h obtains mud, weighs the polyacrylic acid that 2g viscosity average molecular weighs are 1800g/mol and pours into ball grinder, then the 24h that mills is inserted Layer mud, using mill by the 1h that milled in intercalation mud, then obtains dry powder tubulose clay after drying and dispersion.
, through laser particle size analysis, clay particle differential volume median particle diameter is in 5.60 μm, differential volume peak for the tubulose clay Value particle diameter is 4.05 μm;Scanned electronic microscope photos and projection electronic microscope photos, length is 5~10 μm, directly more than clay particle in a tubular form 100~150nm of footpath.And the blank sample without intercalation processing, clay particle differential volume median particle diameter at 13.08 μm, differential Volumetric peak particle diameter is 34.58 μm;Scanned electronic microscope photos and projection electronic microscope photos, many stratiforms of clay particle, particle size is 30~50 μm.Therefore the method can effectively reduce clay particle diameter, form the effect of tubular structure.
Embodiment 2
Selection is intercalation object with the Suzhou soil that illite and kaolinite are main mineral composition, weighs 150g Suzhou soils, 150ml distilled water is measured, the amount of distilled water is pressed with clay mass ratio as measure at 1: 1, in addition ball grinder.It is guiding with ammoniacal liquor Agent, measures 1.5ml concentrated ammonia liquors, in concentrated ammonia liquor, NH3Mass fraction is content 25.0%~28.0%, pours into ball grinder and mills 12h obtains mud, weighs the polyacrylic acid that 2g viscosity average molecular weighs are 2400g/mol and pours into ball grinder, then the 24h that mills is inserted Layer mud, using mill by the 1h that milled in intercalation mud, then obtains dry powder tubulose clay after drying and dispersion.
, through laser particle size analysis, clay particle differential volume median particle diameter is in 9.03 μm, differential volume peak for the tubulose clay Value particle diameter is 5.37 μm;Scanned electronic microscope photos and projection electronic microscope photos, length is 8~15 μm, directly more than clay particle in a tubular form 130~200nm of footpath.Compare with the blank sample without intercalation processing, the method can effectively reduce clay particle diameter, form tubulose knot The effect of structure.And with intercalator molecular weight for 1800g/mol samples are contrasted, intercalator molecular weight is to clay particle particle diameter and tubulose Structure has a significant effect, and intercalator viscosity average molecular weigh is advisable for 1800g/mol.
Embodiment 3
Selection is intercalation object with the Suzhou soil that illite and kaolinite are main mineral composition, weighs 150g Suzhou soils, 150ml distilled water is measured, the amount of distilled water is pressed with clay mass ratio as measure at 1: 1, in addition ball grinder.It is guiding with ammoniacal liquor Agent, measures 1.5ml concentrated ammonia liquors, in concentrated ammonia liquor, NH3Mass fraction is content 25.0%~28.0%, pours into ball grinder and mills 12h obtains mud, weighs the polyacrylic acid that 3g viscosity average molecular weighs are 1800g/mol and pours into ball grinder, then the 24h that mills is inserted Layer mud, using mill by the 1h that milled in intercalation mud, then obtains dry powder tubulose clay after drying and dispersion.
, through laser particle size analysis, clay particle differential volume median particle diameter is in 5.89 μm, differential volume peak for the tubulose clay Value particle diameter is 4.43 μm;Scanned electronic microscope photos and projection electronic microscope photos, length is 10~20 μm more than clay particle in a tubular form, 150~200nm of diameter.Compare with the blank sample without slotting treatment, the method can effectively reduce clay particle diameter, form tubulose knot The effect of structure.And be 2g with intercalator addition, intercalator addition is contrasted for the sample of 5wt ‰, and intercalator addition is to right Clay particle particle diameter and tubular structure have a significant effect, and intercalator addition is advisable for 5wt ‰.
Embodiment 4
Selection is intercalation object with the Suzhou soil that illite and kaolinite are main mineral composition, weighs 150g Suzhou soils, 150ml distilled water is measured, the amount of distilled water is pressed with clay mass ratio as measure at 1: 1, in addition ball grinder.It is guiding with ammoniacal liquor Agent, measures 1.5ml concentrated ammonia liquors, in concentrated ammonia liquor, NH3Mass fraction is content 25.0%~28.0%, pours into ball grinder and mills 12h obtains mud, weighs the polyacrylic acid that 2g viscosity average molecular weighs are 1800g/mol and pours into ball grinder, then the 24h that mills is inserted Layer mud, using mill by the 1h that milled in intercalation mud, then obtains dry powder tubulose clay after drying and dispersion.
The tubulose clay, through the test of cation exchange specific surface area and volume test, test result is:Tubulose clay always than Surface area is 220m2/ g, cation exchange capacity is 86.3 milliequivalents/100g.And without the blank sample of slotting treatment, always than Surface area is 135m2/ g, cation exchange capacity is 59.6 milliequivalents/100g.Contrasted with the blank sample without slotting treatment, Tubulose clay its total specific surface area being obtained through intercalation processing and improve 63%, cation exchange capacity improves 45%, it is seen that The total specific surface area and cation exchange capacity for obtaining tubulose clay through intercalation processing are significantly improved.

Claims (4)

1. a kind of method that polar polymer intercalation prepares tubulose clay, it is characterised in that with principal component as illite and kaolinite Clay be intercalation object, in clay essential mineral composition for kaolinite content be 70wt%~80wt%, illite content is 5wt%~10wt%, other compositions are 10wt%~25wt%, and particle diameter is 30~50 μm, is with polar low molecular polyacrylic acid Intercalator, the preparation method of the tubulose clay is comprised the following steps:Slurrying;Clay intercalated treatment;Machine-shaping;Dry and divide Dissipate;
The method of clay intercalated treatment be by viscosity average molecular weigh for 1800g/mol polyacrylic acid by quality of mud fluid 5wt ‰~ 10wt ‰ is added in mud, then by mud in ball mill ball milling 24h, obtain intercalation clay mud;
The scattered method of drying be by tubulose clay mortar in toasting 12h at 80 DEG C, then through ball milling 1h, obtain length of tube be 5~ 20 μm, the tubulose clay of a diameter of 100~200nm.
2. the method that a kind of polar polymer intercalation as claimed in claim 1 prepares tubulose clay, it is characterised in that pole used Property low-molecular polypropylene acid viscosity average molecular weigh be 1800g/mol, addition for quality of mud fluid ‰~10wt of 5wt ‰.
3. the method that a kind of polar polymer intercalation as claimed in claim 1 prepares tubulose clay, it is characterised in that mud system Standby method be clay account for the 49.5wt%~49.75wt% of quality of mud fluid, distilled water account for the 49.5wt% of quality of mud fluid~ 49.75wt%, ammoniacal liquor account for the ‰~10wt of 5wt ‰ of quality of mud fluid, and NH3 mass fractions content 25.0wt% in ammoniacal liquor~ 28.0wt%, above-mentioned three kinds of raw materials are milled 12h in ball mill.
4. the method that a kind of polar polymer intercalation as claimed in claim 1 prepares tubulose clay, it is characterised in that be processed into The method of type is that intercalation mud is milled 1h through mill, obtains tubulose clay mortar.
CN201410330738.4A 2014-07-08 2014-07-08 Method of preparing tubular clay by polar polymer intercalation Expired - Fee Related CN104085898B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201410330738.4A CN104085898B (en) 2014-07-08 2014-07-08 Method of preparing tubular clay by polar polymer intercalation

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201410330738.4A CN104085898B (en) 2014-07-08 2014-07-08 Method of preparing tubular clay by polar polymer intercalation

Publications (2)

Publication Number Publication Date
CN104085898A CN104085898A (en) 2014-10-08
CN104085898B true CN104085898B (en) 2017-05-24

Family

ID=51633696

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201410330738.4A Expired - Fee Related CN104085898B (en) 2014-07-08 2014-07-08 Method of preparing tubular clay by polar polymer intercalation

Country Status (1)

Country Link
CN (1) CN104085898B (en)

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1401566A (en) * 2002-09-24 2003-03-12 华南理工大学 Intercalation type or amorphous kaoline and preparing process thereof
CN103880032A (en) * 2014-04-13 2014-06-25 北京化工大学 Thiourea intercalation modified kaolin and preparation method thereof

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7273899B2 (en) * 2002-09-25 2007-09-25 Eastman Kodak Company Materials and method for making splayed layered materials
US20060122309A1 (en) * 2004-12-02 2006-06-08 Grah Michael D Intercalated layered silicate

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1401566A (en) * 2002-09-24 2003-03-12 华南理工大学 Intercalation type or amorphous kaoline and preparing process thereof
CN103880032A (en) * 2014-04-13 2014-06-25 北京化工大学 Thiourea intercalation modified kaolin and preparation method thereof

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
插层改性粘土的可加工性能研究;曾雄丰等;《中国陶瓷》;20140630;第60页"1 实验过程" *

Also Published As

Publication number Publication date
CN104085898A (en) 2014-10-08

Similar Documents

Publication Publication Date Title
Lian et al. Adsorption of Congo red from aqueous solutions onto Ca-bentonite
Thakur et al. Use of Tannin based natural coagulants for water treatment: An alternative to inorganic chemicals
CN100349652C (en) Bentonite base composite material for water treatment and its preparation method
Iakovleva et al. Manufacturing of novel low-cost adsorbent: Co-granulation of limestone and coffee waste
Nageeb Rashed et al. Adsorption of methylene blue using modified adsorbents from drinking water treatment sludge
CN102897783A (en) Preparation method of bentonite for slurry
CN107057710A (en) A kind of heavy metal-polluted soil eluent, preparation method, application method and method for treating waste liquid
CN106623400A (en) Method for remedying heavy metal contaminated soil through passivation
CN105126779A (en) Porous modified bentonite with foaming effect and preparation method thereof
CN106807882A (en) Inorganic precoated sand antiquated sand regeneration decomposition helps liquid and antiquated sand renovation process
Duraisamy et al. Adsorption of azure B dye on rice husk activated carbon: equilibrium, kinetic and thermodynamic studies
Ismail et al. Evaluation of a naturally derived tannin extracts biopolymer additive in drilling muds for high-temperature well applications
CN105907383B (en) The method of drilling fluid is prepared after a kind of water-based drilling wastewater treatment again
CN103073239A (en) Asphalt mixture applied to micro-surfacing of asphalt pavement and preparation method thereof
CN105289495B (en) Using adsorbing the method that the useless clay mineral reaction in-situ after dyestuff prepares multifunctional composite
CN104085898B (en) Method of preparing tubular clay by polar polymer intercalation
Niyungeko et al. Synergistic effects of anionic polyacrylamide and gypsum to control phosphorus losses from biogas slurry applied soils
CN102516782B (en) Emulsified bitumen and preparation method thereof
CN107473251A (en) A kind of preparation method of nanoscale calcium hydroxide
Huang et al. Remediation of lead-contaminated soil by washing with choline chloride-based deep eutectic solvents
Mahmud et al. Investigation on the workability and compressive strength of concrete by using bagasse ash from sugar mill
Mohamed et al. Permeability and tensile strength of concrete with Arabic gum biopolymer
CN104445338A (en) Waste drilling mud treatment method
Tolkou et al. Simultaneous removal of anionic and cationic dyes on quaternary mixtures by adsorption onto banana, orange and pomegranate peels
Haq et al. Adsorption of Crystal violet dye from synthetic textile effluents by utilizing wheat bran (Triticum aestivum)

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
CB02 Change of applicant information

Address after: Xinhua Xidao 063009 Hebei province Tangshan City Lunan District No. 46

Applicant after: North China Polytechnics

Address before: Xinhua Xidao 063009 Hebei province Tangshan City Lunan District No. 46

Applicant before: Hebei United University

COR Change of bibliographic data
GR01 Patent grant
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20170524

Termination date: 20180708

CF01 Termination of patent right due to non-payment of annual fee