CN106084102B - A kind of preparation method of spherical granular lithium ion sieve - Google Patents

A kind of preparation method of spherical granular lithium ion sieve Download PDF

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CN106084102B
CN106084102B CN201610383433.9A CN201610383433A CN106084102B CN 106084102 B CN106084102 B CN 106084102B CN 201610383433 A CN201610383433 A CN 201610383433A CN 106084102 B CN106084102 B CN 106084102B
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ion sieve
lithium ion
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spherical granular
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CN106084102A (en
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石西昌
王尚兴
李志伟
陈亚
徐徽
杨喜云
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Central South University
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    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F112/00Homopolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by an aromatic carbocyclic ring
    • C08F112/02Monomers containing only one unsaturated aliphatic radical
    • C08F112/04Monomers containing only one unsaturated aliphatic radical containing one ring
    • C08F112/06Hydrocarbons
    • C08F112/08Styrene
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/02Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/22Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising organic material
    • B01J20/26Synthetic macromolecular compounds
    • B01J20/264Synthetic macromolecular compounds derived from different types of monomers, e.g. linear or branched copolymers, block copolymers, graft copolymers
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    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F212/00Copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by an aromatic carbocyclic ring
    • C08F212/02Monomers containing only one unsaturated aliphatic radical
    • C08F212/04Monomers containing only one unsaturated aliphatic radical containing one ring
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    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F212/00Copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by an aromatic carbocyclic ring
    • C08F212/34Monomers containing two or more unsaturated aliphatic radicals
    • C08F212/36Divinylbenzene
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    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K3/00Use of inorganic substances as compounding ingredients
    • C08K3/18Oxygen-containing compounds, e.g. metal carbonyls
    • C08K3/24Acids; Salts thereof
    • 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
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Abstract

The invention discloses a kind of preparation methods of spherical granular lithium ion sieve, include the following steps:Step (1):Water phase is dissolved to obtain in dispersant and water mixing;Step (2):Powdery lithium ion sieve is added into the water phase of step (1), the oil phase comprising monomer and initiator, which is added, after stirring heating carries out suspension polymerization;The monomer includes styrene;Step (3):After the completion of step (2) reaction, continue to heat up, spherical particle made from suspension polymerization is made to harden, the particle after hardening obtains ball-shaped lithium-ion sieve after washing, drying, pickling, washing and drying successively.Spherical granular lithium ion sieve epigranular produced by the present invention, intensity are high;The oil phase rate of recovery is more than 95%, and the powdery ion sieve rate of recovery is 100%.

Description

A kind of preparation method of spherical granular lithium ion sieve
Technical field
The invention belongs to the preparation fields of ion sieve adsorbant, and in particular to a kind of preparation side of spherical granular lithium ion sieve Method.
Background technology
Lithium is a kind of metal that electro-chemical activity is high, and application field is extensive, lithium battery, controllable nuclear fusion reactor, Aerospace, glass, ceramics, medicine and other fields have important use, for the market demand rapid development of lithium.Solid in the world The reserves of lithium ore are increasingly exhausted, can not meet the market demand.And salt lake bittern, seawater, well halogen etc. are huge liquid lithiums Mineral reserve are attached great importance to extracting lithium from these liquid mines, the lithium salts for having nearly 80% at present is that brine carries lithium both at home and abroad in recent years Product, comprehensive exploitation and the mainstream that lithium industrial development is had become using brine lithium resource.China western part possesses abundant brine lithium Resource, but since Li contents are low in the most of salt lake bitterns in China, Mg/Li is than high, traditional " precipitation-crystallisation " is not appropriate for Lithium is carried in such salt lake, and absorption method is that the effective ways of lithium are extracted in a kind of lithium-containing solution from low concentration, absorption method carries lithium Main media is lithium ion sieve adsorbant.
Existing lithium ion sieve such as LiMn2O4、Li4Mn5O12、Li1.6Mn1.6O4、Li2Mn3O7、Li4Mn5O12Or Li2TiO3 Deng being superfine powder, mobility and permeability are all poor, and molten loss rate is higher, and in absorption-desorption, and bed is easy to collapse It collapses so that complete block fluid, so being not used to industrialized production.Granular adsorbent is only prepared, could realize suction Attached method puies forward the industrial applications of lithium.In view of the above reason, this superfine powder shape lithium ion sieve is made loose porous Graininess becomes one of the emphasis of this field scientist concern.
People, which also studied, takes different methods, it is intended to be prepared into and prepare granulated sorbent or membranaceous adsorbent.At present The prilling process for powder ion sieve adsorbant go out, reported is broadly divided into two major classes:One is direct molding bonded, Another kind is organic polymer molding.
The method that direct molding bonded produces granulated sorbent has:(1) polyvinyl chloride and ion sieve powder mixture are utilized It is dissolved with organic solvent (such as DMF or NMP), then instills molding in water and prepare granular ion sieve (CN101898113A);(2) with Water-soluble salt such as KCl is pore creating material, and DMF or NMP is added in PVC, KCl and powdery ion sieve mixture, sizes mixing, is pressed into Sheet, crushed after being dried dissolve away KCl at graininess, through water logging and are known as granular ion sieve adsorbant;(3) polysaccharide and solvent are added Heat of solution mixes, then ion sieve presoma is added in solution, is uniformly mixing to obtain viscous solution, then viscous solution is instilled stone In the oil phases such as oily ether, the solid spherical adsorbent (CN103316623A) etc. that grain size is 2~5mm is obtained.
Have with organic polymer is molding:(1) acrylic monomer inverse suspension polymerization is used to form crosslinking polymer process It is middle that lithium ion sieve powder is coated in polymer and obtains granular lithium ion sieve (CN 101955210A);(2) with acrylamide For polymerization forming monomer, ion sieve powder is suspended in monomer solution, initiator and crosslinking agent is added, it is anti-to cause cross-linked polymeric It answers, pelletized polypropylene amide-lithium ion sieve (CN1511963) is made.
There is some as intensity is insufficient, granularity is difficult for the preparation method of these granular lithium ion sieve adsorbants reported at present With control, or obtained granulated sorbent is not spherical morphology, and the poor fluidity of solution, bed resistance is big, and therefore, it is difficult to full The requirement of sufficient industrial applications.
Invention content
To solve existing lithium ion sieve intensity deficiency, the technical problem of exterior appearance difference, the present invention provides a kind of suspensions The method that polymerization prepares spherical granular lithium ion sieve, lithium ion sieve intensity height made from this method, are suitable for work at epigranular The lithium adsorbent prilling process of industry production application.
A kind of preparation method of spherical granular lithium ion sieve, includes the following steps:
Step (1):Water phase is dissolved to obtain in dispersant and water mixing;
Step (2):Modified powdery lithium ion sieve is added into the water phase of step (1), stirring is added after heating up includes The oil phase of monomer and initiator carries out suspension polymerization;The monomer includes styrene;
Step (3):After the completion of step (2) reaction, continue to heat up, spherical particle made from suspension polymerization made to harden, Particle after hardening obtains ball-shaped lithium-ion sieve after washing, drying, pickling, washing and drying successively.
In the present invention, crosslinking polymer is formed in the process by powdery lithium ion sieve packet using styrene monomer suspension polymerisation It overlays in polymer and obtains spherical granular lithium ion sieve;Contribute to that product is made by styrene monomer and suspension polymerisation mode Intensity height, epigranular, good fluidity, the ball-shaped lithium-ion sieve for being conducive to industrialized multiple cycle applications, and this method Reaction system is easy to control, and oil phase and the powdery ion sieve rate of recovery are high.
The features of the present invention is exactly:During polymerizing styrene sill polymerize, lithium ion sieve powder and organic is allowed Object is copolymerized, and forms granular lithium ion sieve adsorbant spherical, that intensity is high.The lithium ion sieve adsorbant being prepared in this way Particle be have product strength height, epigranular, good fluidity sphere material.
In step (1), the dispersant is selected from sodium chloride, magnesium hydroxide, sodium hydroxide, magnesium chloride, potassium chloride, water glass At least one of glass, calgon, gelatin, sodium lignin sulfonate, polyvinyl alcohol, neopelex, calcium phosphate.
Preferably, in water phase, the w/v of dispersant and water is less than 10g/100mL water.
The water phase of step (1) adds powdery lithium ion sieve after the completion of preparing.
Preferably, the add weight and oil phase volume ratio of powdery ion sieve are 10-100g: 100mL.
Spheric granules can be made using the method for the present invention in existing lithium ion sieve, preferably, the lithium ion screening From LiMn2O4、Li4Mn5O12、Li1.6Mn1.6O4、Li2Mn3O7、Li4Mn5O12Or Li2TiO3
Powdery ion sieve first carries out surface modification treatment before adding to powdery lithium ion sieve adsorbant.At modified Reason makes inorganic lithium ion sieve powder surface have lipophile.
During surface modification treatment, powdery lithium ion sieve to be modified is immersed in containing the organic solution in surfactant In.The surfactant is but is not limited to coupling agent, aliphatic acid.
Preferably, the surfactant is silane coupling agent, titanate coupling agent, hexadecylic acid, palmate, ten At least one of eight acid, octadecanoate.
Further preferably, the surfactant is stearic acid.
During surface modification treatment, in the ethanol solution that powdery lithium ion sieve to be modified is impregnated to stearic acid.It is molten at this In liquid, the concentration of stearic acid does not influence surface modification treatment effect.
Powdery lithium ion sieve after surface treatment is added into the water phase of step (1), is heated up under stiring;Then add Oil phase carries out suspension polymerization.
In suspension polymerization, oil phase is 1~10: 10 with water phase volume ratio.
In step (2), temperature when oil phase adds, the stir speed (S.S.) and polymeric reaction temperature in polymerization process and monomer class Type etc. can all influence the intensity and granularity of spheric granules obtained.
Preferably, in step (2), the oil described in being added at 40 DEG C~75 DEG C is warming up to after powdery lithium ion sieve is added Phase is warming up to 80 DEG C of -85 DEG C of progress suspension polymerizations after the completion of feeding intake;The stir speed (S.S.) of suspension polymerization is 100- 500r/min;Time is 1h-5h.
In the present invention, the oil phase includes styrene monomer and initiator.
Existing oil-soluble initiator can be used as initiator of the present invention.
Preferably, the initiator is azo-initiator and/or peroxide initiator.
Azo-initiator has azodiisobutyronitrile (AIBN), azobisisoheptonitrile (ABVN) etc.;Peroxide initiator For example, benzoyl peroxide, the benzoyl peroxide tert-butyl ester, methyl ethyl ketone peroxide etc..
Further preferably, the initiator be azodiisobutyronitrile, azobisisoheptonitrile, azo diisopropyl imidazoline hydrochloride, At least one of benzoyl peroxide.
The weight ratio of initiator and monomer is 1%-8%.
In suspension polymerization, the monomer can be styrene single monomer;In order to further increase suspension polymerisation system The intensity of the ball-shaped lithium-ion sieve obtained, particle size uniformity, the monomer is in addition to comprising styrene, and also selectivity includes other lists Body, such as alternative includes other vinyl monomers, acrylic monomer.
Preferably, the monomer also includes divinylbenzene, acrylonitrile, vinyl chloride, vinylidene chloride, methyl methacrylate It is one or more in ester.
Preferably, in the monomer, the weight of styrene is the 20-100% of total monomer weight.
In the present invention, also selectivity includes perforating agent in the oil phase, and the perforating agent is selected from toluene, hexane, heptan At least one of alkane, octane, normal heptane, 12 carbon alkane, aliphatic acid, polystyrene, polyvinylacetate.
Further preferably, in step (2), the temperature that adds of the oil phase is 40 DEG C~75 DEG C, is carried out after the completion of feeding intake Suspension polymerization temperature is 80 DEG C -85 DEG C;The stir speed (S.S.) of suspension polymerization is 100-500r/min;Time is 1h-5h.
After the completion of suspension polymerisation, 85 DEG C~100 DEG C are continuously heating to, spherical particle made from suspension polymerization is carried out Cure process;The cure process time is greater than or equal to 0.5h.
In step (3), after the completion of cure process, filtering obtains spherical granular lithium ion sieve presoma, the spherical granular lithium Ion sieve presoma obtains object i.e. after 80 DEG C of warm water washings, baking oven drying, mordant pickling, washing and drying successively Spherical granular lithium ion sieve.
The particle of the granularity 20-80 mesh of lithium ion sieve made from suspension polymerization through the invention accounts for 95% or more, Granule strength is high, mobility is preferable, can preferably recycle.
Spherical granular lithium ion sieve epigranular produced by the present invention, intensity are high;The oil phase rate of recovery be more than 95%, powdery from The son sieve rate of recovery is 100%.In addition, this method technical process is simple, granulation time is short, production efficiency is high and of low cost.
Description of the drawings
Fig. 1 is the preparation technology flow chart of spherical granular lithium ion sieve of the present invention;
Fig. 2 is the SEM figures of spherical granular lithium ion sieve particle surface made from embodiment 1;
Fig. 3 is the spherical granular lithium ion sieve particle photo of granularity 20-40 mesh made from embodiment 4;
Fig. 4 is the spherical granular lithium ion sieve particle photo of granularity 40-80 mesh made from embodiment 4.
Specific implementation mode
Following embodiment is implemented by aforesaid operations method:
Technical scheme of the present invention is described in detail below in conjunction with specific embodiments of the present invention, certainly, is retouched The embodiment stated is only a portion embodiment of the present invention, rather than whole.
Following embodiment prepares spherical granular lithium ion sieve by Fig. 1 preparation process flows.
Embodiment 1
Sodium chloride 2.5g, polyvinyl alcohol 0.05g, gelatin 0.25g are weighed, is dissolved in 50mL pure water and is configured to water phase.It measures Styrene 1.65mL, divinylbenzene 5.45mL, methyl methacrylate 4.77mL, normal heptane 10mL, benzoyl peroxide 0.3g, Oil phase is obtained after mixed dissolution.First water phase is added in the three-necked flask with reflux condenser, stirring is to being completely dissolved;It is stirring It is slowly added to the modified powdery ion sieve in the surfaces 5g (being modified through stearic acid alcohol solution dipping) under state, begins to warm up, etc. After temperature rises to 60 DEG C, oil phase is added.80 DEG C are to slowly warm up to, constant temperature polymerisation 3h;90 DEG C are then heated to, ball 2h is boiled. Filtering obtains the ion sieve sphere being granulated, and is washed 2-3 times with 80 DEG C of hot water, washes away Granular gelatin.Then sphere is placed in rope In family name's extractor, except the normal heptane in degranulation, before then particle is dried to obtain porous spherical granular ion sieve at 60 DEG C Drive body.
Granular lithium ion sieve presoma is put in a certain amount of 0.5mol/l hydrochloric acid solutions, is mixed slowly at 30 DEG C, instead 1.5-2h is answered, spherical granular lithium ion sieve adsorbant is obtained.
The oil phase rate of recovery is 95%, and the powdery ion sieve rate of recovery is 100%.The granular lithium ion sieve adsorbant being prepared For spherical shape, grain graininess is uniform, and 20-80 mesh particles account for 95.5%.
Fig. 2 is the SEM photograph for the granular lithium ion sieve adsorbant that embodiment 1 is prepared;Fig. 2 (a) partly be the lithium from Son sieve particle SEM photograph, it can be seen from the figure that particle is spheric granules;Fig. 2 (b) is partly particle table after 1000 times of amplification The photo in face, as can be seen from the figure particle surface is vesicular texture.
Embodiment 2
Weigh NaOH 0.1g, MgCl2·6H2O 0.25g are separately added into 50ml deionized water dissolvings, then this two solution is mixed It closes;Gelatin 0.5g, polyvinyl alcohol 0.1g are weighed again, and it is in mixed liquor to be added above-mentioned, and heating for dissolving obtains water phase.Measure styrene 9mL, methyl methacrylate 1mL, benzoyl peroxide 0.45g obtain oil phase after mixed dissolution.Band reflux first is added in water phase It in the three-necked flask of condenser, stirs and heats, after temperature rises to 60 DEG C, the modification of the surfaces 6g is slowly added under stirring Powdery ion sieve (being modified through stearic acid alcohol solution dipping) afterwards, is then slowly added into oil phase.80 DEG C are to slowly warm up to, constant temperature Polymerisation 3h;90 DEG C are then heated to, ball 1h is boiled.Filtering obtains the ion sieve sphere being granulated, and 2-3 is washed with 80 DEG C of hot water Time, wash away Granular gelatin.Then particle is dried to obtain spherical granular ion sieve presoma at 60 DEG C, and spherical grain is obtained after pickling Shape lithium ion sieve adsorbant.
The oil phase rate of recovery is 98%, and the powdery ion sieve rate of recovery is 100%.The granular lithium ion sieve adsorbant being prepared For spherical shape, grain graininess is uniform, and 20-80 mesh particles account for 96%.
Embodiment 3
Sodium chloride 3g, polyvinyl alcohol 0.2g, gelatin 0.5g are weighed, is dissolved in 100mL pure water and is configured to water phase.Measure benzene second Alkene 10mL, benzoyl peroxide 0.45g obtain oil phase after mixed dissolution.First water phase is added three mouthfuls of burnings with reflux condenser In bottle, stirs and heat, after temperature rises to 70 DEG C, the modified powdery ion sieve in the surfaces 6g is slowly added under stirring (being modified through stearic acid alcohol solution dipping), is then slowly added into oil phase.80 DEG C are to slowly warm up to, constant temperature polymerisation 3h;So After be warming up to 90 DEG C, boil ball 1h.Filtering obtains the ion sieve sphere being granulated, and is washed 2-3 times with 80 DEG C of hot water, it is bright to wash away particle Glue.Then particle is dried to obtain spherical granular ion sieve presoma at 60 DEG C, and the suction of spherical granular lithium ion sieve is obtained after pickling Attached dose.
The oil phase rate of recovery is 97.5%, and the powdery ion sieve rate of recovery is 100%.The granular lithium ion sieve absorption being prepared Agent is spherical shape, and grain graininess is uniform, and 20-80 mesh particles account for 83.5%.
Embodiment 4
Weigh NaOH 0.416g, MgCl2·6H2O 1.03g are dissolved in respectively in 250mL pure water, successively by NaOH solution and MgCl2Solution is added in the three-necked flask with reflux condenser.Gelatin 2.5g, polyvinyl alcohol 0.45g are weighed, three-necked flask is added In, stirring dissolves by heating.After being warming up to 75 DEG C, it is (molten through stearic acid ethyl alcohol to weigh the modified powdery lithium ion sieve in the surfaces 10g Liquid, which impregnates, to be modified), it is slowly added in three-necked flask.Then the 50mL dissolved with 4.5g benzoyl peroxides is added into three-necked flask Styrene adds 5ml methyl methacrylates.90 DEG C are continuously heating to after reaction 3h, spherical lithium has just been made after hardening 1h Ion sieve precursor particle.Then particle is filtered, with being put into drying box (60 DEG C) after 80 DEG C of pure water 2-3 times Spherical granular lithium ion sieve presoma is obtained after drying, and granular lithium ion sieve adsorbant is obtained through pickling.
The oil phase rate of recovery is 98%, and the powdery ion sieve rate of recovery is 100%.The granular lithium ion sieve adsorbant being prepared For spherical shape, grain graininess is uniform, and the particle that the particle of 20-40 mesh accounts for 62%, 40-80 mesh accounts for 33.5%.
Fig. 3 and Fig. 4 is the photo for the granular lithium ion sieve adsorbant that embodiment 4 is prepared;Wherein Fig. 3 is that granularity is The photo of the particle of 20-40 mesh, Fig. 4 are the photo for the particle that granularity is 40-80 mesh.It can be seen from the figure that particle is ball Shape particle.
Comparative example 1
Weigh NaOH 0.1g, MgCl2·6H2O 0.25g are separately added into 50ml deionized water dissolvings, then this two solution is mixed It closes;Gelatin 0.5g, polyvinyl alcohol 0.1g are weighed again, and it is in mixed liquor to be added above-mentioned, and heating for dissolving obtains water phase.Measure styrene 9mL, methyl methacrylate 1mL, benzoyl peroxide 0.45g obtain oil phase after mixed dissolution.Band reflux first is added in water phase It in the three-necked flask of condenser, stirs and heats, after temperature rises to 60 DEG C, the unmodified places 6g are slowly added under stirring The powdery ion sieve of reason (being modified without stearic acid alcohol solution dipping), is then slowly added into oil phase.80 DEG C are to slowly warm up to, perseverance Temperature polymerization;Polymerisation 3h;90 DEG C are then heated to, ball 1h is boiled.Filtering obtains spherical polymer beads, with 80 DEG C of hot water Washing 2-3 times, washes away Granular gelatin.Then particle is dried to obtain polymer beads at 60 DEG C.
When being granulated using the lithium ion sieve powder for not carrying out surface modification, obtained polymer beads are to be translucent Spheric granules, only a small amount of powdery lithium ion sieve has been aggregated in spheric granules, most of to remain in water phase.Oil phase The rate of recovery is 98%, and it is less than 15% that powdery ion sieve, which is granulated Percentage bound,.

Claims (10)

1. a kind of preparation method of spherical granular lithium ion sieve, which is characterized in that include the following steps:
Step (1):Water phase is dissolved to obtain in dispersant and water mixing;
Step (2):Surface modification treatment is carried out to powdery lithium ion sieve adsorbant, inorganic lithium ion sieve powder is made by modification Body surface face has lipophile;
Modified powdery lithium ion sieve is added into the water phase of step (1), it includes monomer and initiator to be added after stirring heating Oil phase carry out suspension polymerization;The monomer includes styrene;
Step (3):After the completion of step (2) reaction, continue to heat up, spherical particle made from suspension polymerization is made to harden, hardening Particle afterwards obtains ball-shaped lithium-ion sieve after washing, drying, pickling, washing and drying successively.
2. the preparation method of spherical granular lithium ion sieve as described in claim 1, which is characterized in that the monomer also includes It is one or more in divinylbenzene, acrylonitrile, vinyl chloride, vinylidene chloride, methyl methacrylate.
3. the preparation method of spherical granular lithium ion sieve as claimed in claim 2, which is characterized in that in the monomer, benzene The weight of ethylene is the 20-100% of total monomer weight.
4. the preparation method of spherical granular lithium ion sieve as claimed in claim 1 or 2, which is characterized in that the dispersant Selected from sodium chloride, magnesium hydroxide, sodium hydroxide, magnesium chloride, potassium chloride, waterglass, calgon, gelatin, lignin sulfonic acid At least one of sodium, polyvinyl alcohol, neopelex, calcium phosphate.
5. the preparation method of spherical granular lithium ion sieve as claimed in claim 4, which is characterized in that in water phase, dispersant and The w/v of water is less than 10g/100mL.
6. the preparation method of spherical granular lithium ion sieve as described in claim 1, which is characterized in that in step (2), powdery from The add weight and oil phase volume ratio of son sieve are 10-100g:100mL.
7. the preparation method of spherical granular lithium ion sieve as described in claim 1, which is characterized in that the initiator is even Nitrogen class initiator and/or peroxide initiator.
8. the preparation method of spherical granular lithium ion sieve as described in claim 1, which is characterized in that in suspension polymerization, Oil phase is 1~10 with water phase volume ratio:10.
9. the preparation method of spherical granular lithium ion sieve as described in claim 1, which is characterized in that in step (2), powder is added It is warming up to after shape lithium ion sieve and adds the oil phase at 40 DEG C~75 DEG C, being warming up to 80 DEG C -85 DEG C after the completion of feeding intake is hanged Floating polymerisation;The stir speed (S.S.) of suspension polymerization is 100-500r/min;Time is 1h-5h.
10. the preparation method of spherical granular lithium ion sieve as claimed in claim 9, which is characterized in that in step (3), suspend After the completion of polymerization, 85 DEG C~100 DEG C are continuously heating to, cure process is carried out to spherical particle made from suspension polymerization;Firmly Change processing time more than or equal to 0.5h.
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CN108435143B (en) * 2018-04-23 2020-11-13 陕西省膜分离技术研究院有限公司 High-hydrophilicity adsorbent, preparation and application of adsorbent in adsorbing rubidium ions or lithium ions
CN108435142B (en) * 2018-04-23 2020-11-13 陕西省膜分离技术研究院有限公司 Granular ion exchange type adsorbent, preparation and application of granular ion exchange type adsorbent in adsorbing rubidium or lithium
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