CN107349917A - Highly dissoluble aromatic solvent decolorizing adsorbent and preparation method thereof - Google Patents

Highly dissoluble aromatic solvent decolorizing adsorbent and preparation method thereof Download PDF

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Publication number
CN107349917A
CN107349917A CN201710596742.9A CN201710596742A CN107349917A CN 107349917 A CN107349917 A CN 107349917A CN 201710596742 A CN201710596742 A CN 201710596742A CN 107349917 A CN107349917 A CN 107349917A
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absorbent resin
parts
molecular screen
macroporous absorbent
screen primary
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CN201710596742.9A
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Inventor
苏仁秋
李凤娟
周宇锋
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CHANGSHU ALLIANCE CHEMICAL Co Ltd
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CHANGSHU ALLIANCE CHEMICAL Co Ltd
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Priority to CN201710596742.9A priority Critical patent/CN107349917A/en
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    • 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
    • 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
    • B01J20/10Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising silica or silicate
    • 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
    • B01J20/10Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising silica or silicate
    • B01J20/12Naturally occurring clays or bleaching earth
    • 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
    • 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
    • B01J20/223Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising organic material containing metals, e.g. organo-metallic compounds, coordination complexes
    • 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
    • B01J20/24Naturally occurring macromolecular compounds, e.g. humic acids or their derivatives
    • 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
    • B01J20/261Synthetic macromolecular compounds obtained by reactions only involving carbon to carbon unsaturated bonds

Abstract

The invention discloses a kind of highly dissoluble aromatic solvent decolorizing adsorbent and preparation method thereof, including macroporous absorbent resin, active coke powder, atlapulgite, molecular screen primary powder, carboxymethyl cellulose, sodium abietate, polyvinyl formal, hydrogenated rosin glyceride, polyvinyl alcohol resin, asbestos wool, retinal;Preparation method:Macroporous absorbent resin activates to be handled with filling;Prepare parcel intermediate layer;Prepare parcel outer layer.The present invention is by being reasonably formulated design and unique layering packaging type preparation technology, adsorbent is prepared into the multilayer packaging type structure using the macroporous absorbent resin of molecular screen primary powder filling as core, absorption outer layer is used as using active coke powder, intermediate barrier layer is used as using asbestos wool, using the macroporous absorbent resin of molecular screen primary powder filling as high efficiency filter sandwich layer, the effect of filtration, purification by different level is realized to aromatic solvent, effectively increase adsorption effect, and adsorbent amount can be saved, cost is reduced, there are wide market prospects.

Description

Highly dissoluble aromatic solvent decolorizing adsorbent and preparation method thereof
Technical field
The present invention relates to aromatic solvent preparing technical field, is inhaled more particularly to a kind of highly dissoluble aromatic solvent with decolourizing Attached dose and preparation method thereof, be particularly suitable for use in GF-S1500 aromatic solvents.
Background technology
GF-S series of aromatic hydrocarbon solvents are with C9、C10Heavy aromatics is raw material, with reference to special aromatic solvent standard development in the world Production, have the advantages that dissolving power is strong, toxicity is low, smell is small, not oxygen-containing and heavy metal, boiling point are high, volatility is slow, it is main to use In industries such as coating, agricultural chemicals, plastics, paint of coating.
Because GF-S series of aromatic hydrocarbon solvent has good gradient solubility property for most of agricultural chemicals, with farm chemical emulgent Monomer also has fabulous intersolubility, has the features such as flash-point is high, and evaporation rate is slow, and permeability is strong by the missible oil of its configuration, therefore, GF-S series of aromatic hydrocarbon solvent is often used as farm chemical emulgent, when dropping in the stagnation on plant or insect table body to extend pesticide liquid Between improve the drug effect of agricultural chemicals.
The colourity of aromatic solvent naphtha is the important indicator of aromatic solvent naphtha product quality, directly affects answering for aromatic solvent naphtha Use scope.If colourity is too high, use range with regard to being restricted, it is necessary to carry out decolorization significantly.
At present, conventional decoloring aromatic solvent oil method has absorption method and rectification method etc..Wherein, the decolorizing effect of rectification method It is undesirable, and observable index is higher, is unfavorable for cost-effective;And adsorbent amount to be present big, de- for the absorption method that generally uses at present The defects of color effect is undesirable.
The content of the invention
The present invention solves the technical problem of provide a kind of highly dissoluble aromatic solvent decolorizing adsorbent and its system Preparation Method, three-decker formula efficient decolorizing adsorbent can be formed, effectively improve decolorizing effect, reduce adsorbent amount.
In order to solve the above technical problems, one aspect of the present invention is:It is molten to provide a kind of highly dissoluble aromatic hydrocarbons Agent decolorizing adsorbent, including following parts by weight of component:10~15 parts of macroporous absorbent resin, 20~25 parts of active coke powder, activity 5~10 parts of carclazyte, 10~15 parts of molecular screen primary powder, 3~5 parts of carboxymethyl cellulose, 1~2 part of sodium abietate, polyvinyl alcohol contracting first 1~3 part of aldehyde, 1.5~2 parts of hydrogenated rosin glyceride, 4~5 parts of polyvinyl alcohol resin, 4~8 parts of asbestos wool, 2~3 parts of retinal.
In order to solve the above technical problems, another technical solution used in the present invention is:A kind of highly dissoluble aromatic hydrocarbons is provided The preparation method of solvent decolorizing adsorbent, comprises the following steps:
(1)Macroporous absorbent resin activates to be handled with filling:The macroporous absorbent resin of formula ratio and molecular screen primary powder are placed in 0~5 DEG C cold water in, be stirred to uniform, reflux state be heated to constant heating rate under stirring, fills both Point diffusion, then adds the hydrogenated rosin glyceride of formula ratio, and carries out microwave treatment, be then cooled to 0~5 DEG C stand 1~ 3h, then reflux state is heated to above-mentioned heating rate, filter, gained pellet frozen is dried, obtain molecular screen primary powder filling Macroporous absorbent resin;
(2)Prepare parcel intermediate layer:The retinal of half formula ratio, whole polyvinyl alcohol resins and atlapulgite are mixed equal It is even, 100~110 DEG C are then heated to, constant temperature keeps 5~8min, then adds the asbestos wool and sodium abietate of formula ratio while hot, stirs Mix and mix to uniform, finally by step(1)The macroporous absorbent resin of the molecular screen primary powder filling of middle preparation is added thereto, first Slurry is stirred into high speed dispersor, spray-drying installation is reused and granule materials is made, individual layer parcel is obtained after fully drying Molecular screen primary powder fills macroporous absorbent resin;
(3)Prepare parcel outer layer:By the retinal of remaining formula ratio, whole active coke powder, carboxymethyl cellulose and polyethylene Alcohol formal is well mixed, and is then heated to 50~70 DEG C of constant temperature and is kept 10~15min, adds step(2)The bag of middle gained Wrap up in material, after microwave treatment, be transferred to 1~3h of standing in 0~5 DEG C of environment, first stir into slurry with high speed dispersor, reuse spray Granule materials are made in mist drying device, after fully drying, obtain multilayer packaging type decolorizing adsorbent.
In a preferred embodiment of the present invention, the step(1)In, the addition of the cold water is the macroporous absorption 10~15 times of resin and molecular screen primary powder gross weight;The constant heating rate is 8~10 DEG C/min;The microwave treatment Process conditions be:Frequency 2500MHz, power 1000W, 15~30min of time.
In a preferred embodiment of the present invention, the step(1)In, the molecular screen primary powder fills macroporous absorbent resin Filling rate be more than 75%.
In a preferred embodiment of the present invention, the step(2)In, the outlet temperature of the spray-drying installation is 100~110 DEG C, the thickness of gained integument is 10~100 μm.
In a preferred embodiment of the present invention, the step(3)In, the microwave treatment conditions are:Frequency 2550MHz, power 800W, 10~20min of time;The outlet temperature of the spray-drying installation is 80~100 DEG C, gained parcel The thickness of layer is 10~100 μm.
The beneficial effects of the invention are as follows:A kind of highly dissoluble aromatic solvent decolorizing adsorbent of the present invention, by rational Formula design and unique layering packaging type preparation technology, adsorbent are prepared into the macroporous absorption tree filled with molecular screen primary powder Fat is the multilayer packaging type structure of core, and the adsorbent of the multilayer packaging type structure is using active coke powder as absorption outer layer, with stone Velveteen is real to aromatic solvent using the macroporous absorbent resin of molecular screen primary powder filling as high efficiency filter sandwich layer as intermediate barrier layer The effect of filtration, purification is by different level showed, has effectively increased adsorption effect, and adsorbent amount can be saved, reduced cost, have Wide market prospects.
Embodiment
Presently preferred embodiments of the present invention is described in detail below so that advantages and features of the invention can be easier to by It will be appreciated by those skilled in the art that apparent clearly defined so as to be made to protection scope of the present invention.
The embodiment of the present invention includes:
Embodiment 1
A kind of highly dissoluble aromatic solvent decolorizing adsorbent, including following parts by weight of component:10 parts of macroporous absorbent resin, activity 20 parts of coke powder, 5 parts of atlapulgite, 10 parts of molecular screen primary powder, 3 parts of carboxymethyl cellulose, 1 part of sodium abietate, polyvinyl alcohol contracting first 1 part of aldehyde, 1.5 parts of hydrogenated rosin glyceride, 4 parts of polyvinyl alcohol resin, 4 parts of asbestos wool, 2 parts of retinal.
The each component of above-mentioned decolorizing adsorbent uses layering packaging type to be prepared into the macroporous absorption filled with molecular screen primary powder Resin is the multilayer packaging type structure of core, so as to realize the effect to aromatic solvent filtration, purification by different level, is decolourized with improving Effect, saves adsorbent amount, and specific preparation method is as follows:
(1)Macroporous absorbent resin activates to be handled with filling:The macroporous absorbent resin of formula ratio and molecular screen primary powder are placed in and accounted for greatly In 10 times of 0~5 DEG C of cold water of macroporous adsorbent resin and molecular screen primary powder gross weight, it is stirred to uniform, in stirring Under to be heated to reflux state under 8 DEG C/min constant heating rate, both is fully spread, then add the hydrogenation of formula ratio Rosin glyceride, and be 2500MHz in frequency, power is microwave treatment 15min under conditions of 1000W, then with 15 DEG C/min Speed be cooled to 0~5 DEG C, stand 1h, then reflux state is heated to 8 DEG C/min constant heating rate, filter, by gained Pellet frozen is dried, and obtains the macroporous absorbent resin of molecular screen primary powder filling;
After tested, the filling rate of molecular screen primary powder is more than 75% in gained macroporous absorbent resin;
(2)Prepare parcel intermediate layer:The retinal of half formula ratio, whole polyvinyl alcohol resins and atlapulgite are mixed equal It is even, be then heated to 100 DEG C, constant temperature keeps 8min, then adds the asbestos wool and sodium abietate of formula ratio while hot, be stirred to Uniformly, added material is made all to melt for uniform mixture, finally by step(1)The macropore of the molecular screen primary powder filling of middle preparation Polymeric adsorbent is added thereto, then stirs into slurry with high speed dispersor, is 100 DEG C in outlet temperature using spray-drying installation Under the conditions of macroporous absorbent resin granule materials of the surface with integument are made in slurry, after fully drying, obtain individual layer parcel Molecular screen primary powder fills macroporous absorbent resin, and after tested, the thickness of integument is 10~100 μm;
(3)Prepare parcel outer layer:By the retinal of remaining formula ratio, whole active coke powder, carboxymethyl cellulose and polyethylene Alcohol formal is well mixed, and is then heated to 50 DEG C of constant temperature and is kept 15min, adds step(2)The parcel material of middle gained, Frequency is 2550MHz, under conditions of power is 800W after microwave treatment 10min, is transferred in 0~5 DEG C of environment and stands 1h, then use High speed dispersor stirs into slurry, and uses spray-drying installation, by above-mentioned slurry under conditions of being 80~100 DEG C in outlet temperature Granule materials are made, after fully drying, obtain multilayer packaging type decolorizing adsorbent, after tested, the thickness of gained integument is 10 ~100 μm.
Embodiment 2
Difference with embodiment 1 is, highly dissoluble aromatic solvent decolorizing adsorbent of the invention, including following parts by weight group Point:15 parts of macroporous absorbent resin, 25 parts of active coke powder, 10 parts of atlapulgite, 15 parts of molecular screen primary powder, 5 parts of carboxymethyl cellulose, 2 parts of sodium abietate, 3 parts of polyvinyl formal, 2 parts of hydrogenated rosin glyceride, 5 parts of polyvinyl alcohol resin, 8 parts of asbestos wool, pine 3 parts of sesame oil.
The each component of above-mentioned decolorizing adsorbent uses layering packaging type to be prepared into the macroporous absorption filled with molecular screen primary powder Resin is the multilayer packaging type structure of core, so as to realize the effect to aromatic solvent filtration, purification by different level, is decolourized with improving Effect, saves adsorbent amount, and specific preparation method is as follows:
(1)Macroporous absorbent resin activates to be handled with filling:The macroporous absorbent resin of formula ratio and molecular screen primary powder are placed in and accounted for greatly In 15 times of 0~5 DEG C of cold water of macroporous adsorbent resin and molecular screen primary powder gross weight, it is stirred to uniform, in stirring Under to be heated to reflux state under 10 DEG C/min constant heating rate, both is fully spread, then add the hydrogen of formula ratio Change rosin glyceride, and be 2500MHz in frequency, power is microwave treatment 30min under conditions of 1000W, then with 20 DEG C/ Min speed is cooled to 0~5 DEG C, stands 3h, then is heated to reflux state with 10 DEG C/min constant heating rate, filters, will Gained pellet frozen is dried, and obtains the macroporous absorbent resin of molecular screen primary powder filling;
After tested, the filling rate of molecular screen primary powder is more than 75% in gained macroporous absorbent resin;
(2)Prepare parcel intermediate layer:The retinal of half formula ratio, whole polyvinyl alcohol resins and atlapulgite are mixed equal It is even, be then heated to 110 DEG C, constant temperature keeps 8min, then adds the asbestos wool and sodium abietate of formula ratio while hot, be stirred to Uniformly, added material is made all to melt for uniform mixture, finally by step(1)The macropore of the molecular screen primary powder filling of middle preparation Polymeric adsorbent is added thereto, then stirs into slurry with high speed dispersor, is 110 DEG C in outlet temperature using spray-drying installation Under the conditions of macroporous absorbent resin granule materials of the surface with integument are made in slurry, after fully drying, obtain individual layer parcel Molecular screen primary powder fills macroporous absorbent resin, and after tested, the thickness of integument is 10~100 μm;
(3)Prepare parcel outer layer:By the retinal of remaining formula ratio, whole active coke powder, carboxymethyl cellulose and polyethylene Alcohol formal is well mixed, and is then heated to 70 DEG C of constant temperature and is kept 10min, adds step(2)The parcel material of middle gained, Frequency is 2550MHz, under conditions of power is 800W after microwave treatment 20min, is transferred in 0~5 DEG C of environment and stands 3h, then use High speed dispersor stirs into slurry, and uses spray-drying installation, and above-mentioned slurry is made under conditions of outlet temperature is by 100 DEG C Granule materials, after fully drying, multilayer packaging type decolorizing adsorbent is obtained, after tested, the thickness of gained integument is 10~100 μm。
Decolorizing adsorbent prepared by the above method, using active coke powder as absorption outer layer, obstructed using asbestos wool among Layer, using the macroporous absorbent resin of molecular screen primary powder filling as high efficiency filter sandwich layer, for highly dissoluble aromatic solvent GF- During S1500 decolorization, have the effect that:Existing adsorbent product is contrasted, its decolouring degree lifts 2~3 grades, adsorbent Consumption saves more than 30%.
Embodiments of the invention are the foregoing is only, are not intended to limit the scope of the invention, it is every to utilize this hair The equivalent structure or equivalent flow conversion that bright description is made, or directly or indirectly it is used in other related technology necks Domain, it is included within the scope of the present invention.

Claims (6)

1. a kind of highly dissoluble aromatic solvent decolorizing adsorbent, it is characterised in that including following parts by weight of component:Macroporous absorption 10~15 parts of resin, 20~25 parts of active coke powder, 5~10 parts of atlapulgite, 10~15 parts of molecular screen primary powder, carboxymethyl cellulose 3~5 parts, 1~2 part of sodium abietate, 1~3 part of polyvinyl formal, 1.5~2 parts of hydrogenated rosin glyceride, polyvinyl alcohol tree 4~5 parts of fat, 4~8 parts of asbestos wool, 2~3 parts of retinal.
A kind of 2. preparation method of highly dissoluble aromatic solvent decolorizing adsorbent as claimed in claim 1, it is characterised in that Comprise the following steps:
(1)Macroporous absorbent resin activates to be handled with filling:The macroporous absorbent resin of formula ratio and molecular screen primary powder are placed in 0~5 DEG C cold water in, be stirred to uniform, reflux state be heated to constant heating rate under stirring, fills both Point diffusion, then adds the hydrogenated rosin glyceride of formula ratio, and carries out microwave treatment, be then cooled to 0~5 DEG C stand 1~ 3h, then reflux state is heated to above-mentioned heating rate, filter, gained pellet frozen is dried, obtain molecular screen primary powder filling Macroporous absorbent resin;
(2)Prepare parcel intermediate layer:The retinal of half formula ratio, whole polyvinyl alcohol resins and atlapulgite are mixed equal It is even, 100~110 DEG C are then heated to, constant temperature keeps 5~8min, then adds the asbestos wool and sodium abietate of formula ratio while hot, stirs Mix and mix to uniform, finally by step(1)The macroporous absorbent resin of the molecular screen primary powder filling of middle preparation is added thereto, first Slurry is stirred into high speed dispersor, spray-drying installation is reused and granule materials is made, individual layer parcel is obtained after fully drying Molecular screen primary powder fills macroporous absorbent resin;
(3)Prepare parcel outer layer:By the retinal of remaining formula ratio, whole active coke powder, carboxymethyl cellulose and polyethylene Alcohol formal is well mixed, and is then heated to 50~70 DEG C of constant temperature and is kept 10~15min, adds step(2)The bag of middle gained Wrap up in material, after microwave treatment, be transferred to 1~3h of standing in 0~5 DEG C of environment, first stir into slurry with high speed dispersor, reuse spray Granule materials are made in mist drying device, after fully drying, obtain multilayer packaging type decolorizing adsorbent.
3. the preparation method of highly dissoluble aromatic solvent decolorizing adsorbent according to claim 2, it is characterised in that institute State step(1)In, the addition of the cold water is 10~15 times of the macroporous absorbent resin and molecular screen primary powder gross weight;Institute It is 8~10 DEG C/min to state constant heating rate;The process conditions of the microwave treatment are:Frequency 2500MHz, power 1000W, 15~30min of time.
4. the preparation method of highly dissoluble aromatic solvent decolorizing adsorbent according to claim 2, it is characterised in that institute State step(1)In, the filling rate of the molecular screen primary powder filling macroporous absorbent resin is more than 75%.
5. the preparation method of highly dissoluble aromatic solvent decolorizing adsorbent according to claim 2, it is characterised in that institute State step(2)In, the outlet temperature of the spray-drying installation is 100~110 DEG C, and the thickness of gained integument is 10~100 μ m。
6. the preparation method of highly dissoluble aromatic solvent decolorizing adsorbent according to claim 2, it is characterised in that institute State step(3)In, the microwave treatment conditions are:Frequency 2550MHz, power 800W, 10~20min of time;The spraying is dry The outlet temperature of dry device is 80~100 DEG C, and the thickness of gained integument is 10~100 μm.
CN201710596742.9A 2017-07-20 2017-07-20 Highly dissoluble aromatic solvent decolorizing adsorbent and preparation method thereof Pending CN107349917A (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN115487780A (en) * 2022-08-02 2022-12-20 山东省农业科学院作物研究所 Comprehensive utilization method of wheat bran

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1184001A (en) * 1996-11-29 1998-06-10 浙江临安力生化工厂 Production technology of bentone adsorbent
CN1280877A (en) * 1999-07-20 2001-01-24 中国石化集团洛阳石油化工总厂 Process for regeneration of decolouring argil
CN102205230A (en) * 2011-05-14 2011-10-05 山西大学 Method for processing atlapulgite for decolorizing grease
CN102924659A (en) * 2012-11-12 2013-02-13 中国石油化工股份有限公司 Preparation method for C9 hydrogenation petroleum resin
CN106902770A (en) * 2017-03-14 2017-06-30 安徽海德石油化工有限公司 Adsorbent for decoloring aromatic solvent oil and preparation method thereof

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1184001A (en) * 1996-11-29 1998-06-10 浙江临安力生化工厂 Production technology of bentone adsorbent
CN1280877A (en) * 1999-07-20 2001-01-24 中国石化集团洛阳石油化工总厂 Process for regeneration of decolouring argil
CN102205230A (en) * 2011-05-14 2011-10-05 山西大学 Method for processing atlapulgite for decolorizing grease
CN102924659A (en) * 2012-11-12 2013-02-13 中国石油化工股份有限公司 Preparation method for C9 hydrogenation petroleum resin
CN106902770A (en) * 2017-03-14 2017-06-30 安徽海德石油化工有限公司 Adsorbent for decoloring aromatic solvent oil and preparation method thereof

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN115487780A (en) * 2022-08-02 2022-12-20 山东省农业科学院作物研究所 Comprehensive utilization method of wheat bran
CN115487780B (en) * 2022-08-02 2023-09-22 山东省农业科学院作物研究所 Comprehensive utilization method of wheat bran

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Inventor after: Su Renqiu

Inventor after: Li Fengjuan

Inventor after: Zhou Yufeng

Inventor before: Su Renqiu

Inventor before: Li Fengjuan

Inventor before: Zhou Yufeng

RJ01 Rejection of invention patent application after publication
RJ01 Rejection of invention patent application after publication

Application publication date: 20171117