CN105396561A - Preparation method for holocellulose/chitosan microsphere adsorbent - Google Patents

Preparation method for holocellulose/chitosan microsphere adsorbent Download PDF

Info

Publication number
CN105396561A
CN105396561A CN201510919579.6A CN201510919579A CN105396561A CN 105396561 A CN105396561 A CN 105396561A CN 201510919579 A CN201510919579 A CN 201510919579A CN 105396561 A CN105396561 A CN 105396561A
Authority
CN
China
Prior art keywords
holocellulose
subsequently
chitosan
solution
parts
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.)
Pending
Application number
CN201510919579.6A
Other languages
Chinese (zh)
Inventor
黄勇
薛红娟
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.)
Changzhou University
Original Assignee
Changzhou University
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 Changzhou University filed Critical Changzhou University
Priority to CN201510919579.6A priority Critical patent/CN105396561A/en
Publication of CN105396561A publication Critical patent/CN105396561A/en
Pending legal-status Critical Current

Links

Classifications

    • 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
    • B01J20/28Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties
    • B01J20/28014Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties characterised by their form
    • B01J20/28016Particle form
    • B01J20/28021Hollow particles, e.g. hollow spheres, microspheres or cenospheres
    • 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
    • B01J20/30Processes for preparing, regenerating, or reactivating
    • B01J20/3021Milling, crushing or grinding
    • 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
    • B01J20/30Processes for preparing, regenerating, or reactivating
    • B01J20/3071Washing or leaching
    • 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
    • B01J20/30Processes for preparing, regenerating, or reactivating
    • B01J20/3085Chemical treatments not covered by groups B01J20/3007 - B01J20/3078
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2220/00Aspects relating to sorbent materials
    • B01J2220/40Aspects relating to the composition of sorbent or filter aid materials
    • B01J2220/48Sorbents characterised by the starting material used for their preparation
    • B01J2220/4812Sorbents characterised by the starting material used for their preparation the starting material being of organic character
    • B01J2220/4825Polysaccharides or cellulose materials, e.g. starch, chitin, sawdust, wood, straw, cotton
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/28Treatment of water, waste water, or sewage by sorption
    • C02F1/286Treatment of water, waste water, or sewage by sorption using natural organic sorbents or derivatives thereof
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2101/00Nature of the contaminant
    • C02F2101/10Inorganic compounds
    • C02F2101/20Heavy metals or heavy metal compounds
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/30Wastewater or sewage treatment systems using renewable energies
    • Y02W10/37Wastewater or sewage treatment systems using renewable energies using solar energy

Landscapes

  • Chemical & Material Sciences (AREA)
  • Analytical Chemistry (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Solid-Sorbent Or Filter-Aiding Compositions (AREA)

Abstract

The invention relates to a preparation method for a holocellulose/chitosan microsphere adsorbent, belonging to the field of preparation of an adsorption material. The method is directed at the problems of poor adsorption capability and need for chemical modification and crosslinking of a conventional cellulose adsorbent and comprises the following steps: subjecting soybean straw to degreasing and decoloring and then to hydrolysis so as to prepare a chitosan microsphere particle; then compounding the chitosan microsphere particle with holocellulose; extracting a mixture obtained in the previous step with ethyl acetate in a Soxhlet extraction apparatus; and carrying out drying so as to prepare the holocellulose/chitosan microsphere adsorbent. Accordin gto the invention, the holocellulose/chitosan microsphere adsorbent prepared from the soybean straw has heavy metal ion adsorption capacity of more than 90%; and preparation of the adsorbent from the soybean straw reduces cost and is green, environment-friendly and pollution-free.

Description

The preparation method of a kind of holocellulose/chitosan microball adsorbent
Technical field
The present invention relates to the preparation method of a kind of holocellulose/chitosan microball adsorbent, belong to sorbing material preparation field.
Background technology
Cellulose is eco-friendly macromolecular material, take cellulose as matrix, replace synthesis macromolecule matrix expensive at present, carry out the research of cellulose base functional nanocomposite, significantly can reduce the preparation cost of composite, what promote this type of material applies that poor, the easy decomposition of organic antibacterial agent heat endurance, persistence are poor, toxicity is comparatively large and use harmful for a long time usually, and in order to overcome the shortcoming of organic antibacterial agent, research direction is turned to inorganic antiseptic by people gradually.
Modified natural fibers element ABSORBENTS ABSORPTION metal biosorption has lot of advantages, therefore, in recent years, resource scarcity modified cellulose is used widely in environmental improvement heavy metal process row, and the preparation synthesis adsorbent of high adsorption and the regenerative agent of high reproducibility become current particularly important research point.
Summary of the invention
Technical problem to be solved by this invention: for adopting cellulose as adsorbent at present, adsorption capacity is poor and need to its chemical modification and crosslinked problem, provide one and carry out degreasing and decolouring by soybean stalk, it is hydrolyzed and prepares chitosan microball particle, subsequently by chitosan microball particle and brown cellulose compound, in soxhlet type apparatus, extracting is carried out by ethyl acetate, to its dry preparation a kind of holocellulose/chitosan microball adsorbent, this adsorbent Be very effective and easy to make.
For solving the problems of the technologies described above, the present invention adopts technical scheme as described below to be:
(1) soybean stalk is rinsed through clear water, after being exposed to the sun under sunlight 3 ~ 5 days, be placed in high speed grinding mill and carry out pulverizing and sieving to it, collect 80 ~ 100 object soybean stalk particles, subsequently by the ratio of methyl alcohol and toluene 5:1 by volume, be uniformly mixed at 20 ~ 30 DEG C, be prepared into extract;
(2) be the ratio of 1:3 in solid-to-liquid ratio, by the soybean stalk particle of above-mentioned preparation and extract, be placed in Soxhlet extraction device, after its Soxhlet extraction 5 ~ 6h, decolouring paraffin removal is carried out 1 ~ 2 time repeatedly again by macroporous resin column, in micropore gel column, carry out secondary decolourization paraffin removal 1 ~ 2 time more subsequently, remove stalk particle pigment and wax;
(3) after Soxhlet extraction completes, 1:5 in mass ratio, the sodium hydroxide solution of the soybean stalk particle after extracting and 0.85mol/L is uniformly mixed, and 70 ~ 75 DEG C of insulated and stirred reaction 1 ~ 2h are warming up to it, subsequently acetic acid solution adjustment pH to 4.2 ~ 4.5 that mass fraction is 5% are added to it, and to its pressure filtration, collect filter cake and be placed on dry 6 ~ 8h in the baking oven of 60 ~ 70 DEG C, obtaining holocellulose for subsequent use;
(4) ratio of 1:250 in mass ratio, Chitosan powder being dissolved to mass concentration is in the acetum of 2%, regulate pH to 2.5 ~ 3.0, be prepared into chitosan solution, count by weight subsequently, choose the chitosan solution of 45 ~ 65 parts, 20 ~ 30 parts of mass concentrations are the sodium tripolyphosphate solution of the different thiophene of the methyl mile beautiful jade ketone solution of 10% and the 2g/L of 15 ~ 25 parts, are uniformly mixed formation crosslinker solution at 20 ~ 30 DEG C;
(5) after end to be crosslinked, washing crosslinker solution to pH by deionized water is 7, subsequently to its suction filtration, collect filter cake, and use ethyl acetate and acetone extracting 20 ~ 24h in Soxhlet extraction device respectively, take out filter cake dry 20 ~ 30min in 50 DEG C of baking ovens subsequently, be prepared into chitosan microball carrier;
(6) count by weight, choose the holocellulose of above-mentioned preparation of the chitosan microball carrier of 20 ~ 45 parts, the deionized water of 35 ~ 50 parts and 20 ~ 25 parts, be prepared into shitosan mixed liquor, be placed on subsequently in there-necked flask, reflux 1h under 80 ~ 90 DEG C of waters bath with thermostatic control, after backflow completes, decompress filter is carried out to it, collect filter cake, and distilled water washing is 7.0 to pH, in 55 ~ 60 DEG C of baking ovens, dry 6 ~ 10h can be prepared into a kind of holocellulose/chitosan microball adsorbent.
Application process of the present invention is: getting holocellulose/chitosan microball sorbent-loaded that 20 ~ 40g obtains is on the screen cloth of 20 μm in aperture, being holded up by screen cloth is placed in wastewater disposal basin, one is laid every 50 ~ 60cm, pass into the mercury-containing waste water that mass concentration is 20 ~ 200mg/L, stop 6 ~ 8h, recording mercury ion adsorption capacity is 18 ~ 190mg/g, and adsorption rate reaches more than 90%.
The present invention is compared with additive method, and Advantageous Effects is:
(1) the present invention prepares holocellulose/chitosan microball adsorbent by soybean stalk, and heavy metal ionic adsorption effect reaches more than 90%;
(2) prepare adsorbent by soybean stalk, reduce costs, environmental protection is pollution-free.
Detailed description of the invention
First soybean stalk is rinsed through clear water, after being exposed to the sun under sunlight 3 ~ 5 days, be placed in high speed grinding mill and carry out pulverizing and sieving to it, collect 80 ~ 100 object soybean stalk particles, subsequently by the ratio of methyl alcohol and toluene 5:1 by volume, be uniformly mixed at 20 ~ 30 DEG C, be prepared into extract; Be the ratio of 1:3 in solid-to-liquid ratio, by the soybean stalk particle of above-mentioned preparation and extract, be placed in Soxhlet extraction device, after its Soxhlet extraction 5 ~ 6h, decolouring paraffin removal is carried out 1 ~ 2 time repeatedly again by macroporous resin column, in micropore gel column, carry out secondary decolourization paraffin removal 1 ~ 2 time more subsequently, remove stalk particle pigment and wax; After Soxhlet extraction completes, 1:5 in mass ratio, the sodium hydroxide solution of the soybean stalk particle after extracting and 0.85mol/L is uniformly mixed, and 70 ~ 75 DEG C of insulated and stirred reaction 1 ~ 2h are warming up to it, subsequently acetic acid solution adjustment pH to 4.2 ~ 4.5 that mass fraction is 5% are added to it, and to its pressure filtration, collect filter cake and be placed on dry 6 ~ 8h in the baking oven of 60 ~ 70 DEG C, obtaining holocellulose for subsequent use; The ratio of 1:250 in mass ratio, Chitosan powder being dissolved to mass concentration is in the acetum of 2%, regulate pH to 2.5 ~ 3.0, be prepared into chitosan solution, count by weight subsequently, choose the chitosan solution of 45 ~ 65 parts, mass concentration is the different thiophene of the methyl mile beautiful jade ketone solution of 10% and the sodium tripolyphosphate solution of 2g/L, is uniformly mixed formation crosslinker solution at 20 ~ 30 DEG C; After end to be crosslinked, washing crosslinker solution to pH by deionized water is 7, subsequently to its suction filtration, collect filter cake, and use ethyl acetate and acetone extracting 20 ~ 24h in Soxhlet extraction device respectively, take out filter cake dry 20 ~ 30min in 50 DEG C of baking ovens subsequently, be prepared into chitosan microball carrier; Count by weight, choose the holocellulose of above-mentioned preparation of the chitosan microball carrier of 20 ~ 45 parts, the deionized water of 35 ~ 50 parts and 20 ~ 25 parts, be prepared into shitosan mixed liquor, be placed on subsequently in there-necked flask, reflux 1h under 80 ~ 90 DEG C of waters bath with thermostatic control, after backflow completes, decompress filter is carried out to it, collect filter cake, and distilled water washing is 7.0 to pH, in 55 ~ 60 DEG C of baking ovens, dry 6 ~ 10h can be prepared into a kind of holocellulose/chitosan microball adsorbent.
Example 1
First soybean stalk is rinsed through clear water, after being exposed to the sun under sunlight 3 days, being placed in high speed grinding mill and carrying out pulverizing and sieving to it, collect 80 object soybean stalk particles, subsequently by the ratio of methyl alcohol and toluene 5:1 by volume, be uniformly mixed at 20 DEG C, be prepared into extract; Be the ratio of 1:3 in solid-to-liquid ratio, by the soybean stalk particle of above-mentioned preparation and extract, be placed in Soxhlet extraction device, after its Soxhlet extraction 5h, decolouring paraffin removal is carried out 1 time repeatedly again by macroporous resin column, in micropore gel column, carry out secondary decolourization paraffin removal 1 time more subsequently, remove stalk particle pigment and wax; After Soxhlet extraction completes, 1:5 in mass ratio, the sodium hydroxide solution of the soybean stalk particle after extracting and 0.85mol/L is uniformly mixed, and 70 DEG C of insulated and stirred reaction 1h are warming up to it, subsequently the acetic acid solution adjustment pH to 4.2 that mass fraction is 5% is added to it, and to its pressure filtration, collect filter cake and be placed on dry 6h in the baking oven of 60 DEG C, obtaining holocellulose for subsequent use; The ratio of 1:250 in mass ratio, Chitosan powder being dissolved to mass concentration is in the acetum of 2%, regulate pH to 2.5 ~ 3.0, be prepared into chitosan solution, count by weight subsequently, choose the chitosan solution of 45 parts, 30 parts of mass concentrations are the sodium tripolyphosphate solution of the different thiophene of the methyl mile beautiful jade ketone solution of 10% and the 2g/L of 25 parts, are uniformly mixed formation crosslinker solution at 20 DEG C; After end to be crosslinked, washing crosslinker solution to pH by deionized water is 7, subsequently to its suction filtration, collect filter cake, and use ethyl acetate and acetone extracting 20h in Soxhlet extraction device respectively, take out filter cake dry 20min in 50 DEG C of baking ovens subsequently, be prepared into chitosan microball carrier; Count by weight, choose the holocellulose of above-mentioned preparation of the chitosan microball carrier of 20 parts, the deionized water of 50 parts and 25 parts, be prepared into shitosan mixed liquor, be placed on subsequently in there-necked flask, reflux 1h under 80 DEG C of waters bath with thermostatic control, after backflow completes, decompress filter is carried out to it, collect filter cake, and distilled water washing is 7.0 to pH, in 55 DEG C of baking ovens, dry 6h can be prepared into a kind of holocellulose/chitosan microball adsorbent.
Getting holocellulose/chitosan microball sorbent-loaded that 20g obtains is on the screen cloth of 20 μm in aperture, being holded up by screen cloth is placed in wastewater disposal basin, one is laid every 50cm, pass into the mercury-containing waste water that mass concentration is 20mg/L, stop 6h, recording mercury ion adsorption capacity is 18mg/g, and adsorption rate reaches 90%.
Example 2
First soybean stalk is rinsed through clear water, after being exposed to the sun under sunlight 4 days, being placed in high speed grinding mill and carrying out pulverizing and sieving to it, collect 90 object soybean stalk particles, subsequently by the ratio of methyl alcohol and toluene 5:1 by volume, be uniformly mixed at 25 DEG C, be prepared into extract; Be the ratio of 1:3 in solid-to-liquid ratio, by the soybean stalk particle of above-mentioned preparation and extract, be placed in Soxhlet extraction device, after its Soxhlet extraction 5.5h, decolouring paraffin removal is carried out 1 time repeatedly again by macroporous resin column, in micropore gel column, carry out secondary decolourization paraffin removal 1 time more subsequently, remove stalk particle pigment and wax; After Soxhlet extraction completes, 1:5 in mass ratio, the sodium hydroxide solution of the soybean stalk particle after extracting and 0.85mol/L is uniformly mixed, and 72 DEG C of insulated and stirred reaction 1.5h are warming up to it, subsequently the acetic acid solution adjustment pH to 4.3 that mass fraction is 5% is added to it, and to its pressure filtration, collect filter cake and be placed on dry 7h in the baking oven of 65 DEG C, obtaining holocellulose for subsequent use; The ratio of 1:250 in mass ratio, Chitosan powder being dissolved to mass concentration is in the acetum of 2%, regulate pH to 2.7, be prepared into chitosan solution, count by weight subsequently, choose the chitosan solution of 50 parts, 25 parts of mass concentrations are the sodium tripolyphosphate solution of the different thiophene of the methyl mile beautiful jade ketone solution of 10% and the 2g/L of 25 parts, are uniformly mixed formation crosslinker solution at 25 DEG C; After end to be crosslinked, washing crosslinker solution to pH by deionized water is 7, subsequently to its suction filtration, collect filter cake, and use ethyl acetate and acetone extracting 22h in Soxhlet extraction device respectively, take out filter cake dry 25min in 50 DEG C of baking ovens subsequently, be prepared into chitosan microball carrier; Count by weight, choose the holocellulose of above-mentioned preparation of the chitosan microball carrier of 30 parts, the deionized water of 45 parts and 25 parts, be prepared into shitosan mixed liquor, be placed on subsequently in there-necked flask, reflux 1h under 85 DEG C of waters bath with thermostatic control, after backflow completes, decompress filter is carried out to it, collect filter cake, and distilled water washing is 7.0 to pH, in 58 DEG C of baking ovens, dry 8h can be prepared into a kind of holocellulose/chitosan microball adsorbent.
Getting holocellulose/chitosan microball sorbent-loaded that 30g obtains is on the screen cloth of 20 μm in aperture, being holded up by screen cloth is placed in wastewater disposal basin, one is laid every 55cm, pass into the mercury-containing waste water that mass concentration is 100mg/L, stop 7h, recording mercury ion adsorption capacity is 100mg/g, and adsorption rate reaches 92%.
Example 3
First soybean stalk is rinsed through clear water, after being exposed to the sun under sunlight 5 days, being placed in high speed grinding mill and carrying out pulverizing and sieving to it, collect 100 object soybean stalk particles, subsequently by the ratio of methyl alcohol and toluene 5:1 by volume, be uniformly mixed at 30 DEG C, be prepared into extract; Be the ratio of 1:3 in solid-to-liquid ratio, by the soybean stalk particle of above-mentioned preparation and extract, be placed in Soxhlet extraction device, after its Soxhlet extraction 6h, decolouring paraffin removal is carried out 2 times repeatedly again by macroporous resin column, in micropore gel column, carry out secondary decolourization paraffin removal 2 times more subsequently, remove stalk particle pigment and wax; After Soxhlet extraction completes, 1:5 in mass ratio, the sodium hydroxide solution of the soybean stalk particle after extracting and 0.85mol/L is uniformly mixed, and 75 DEG C of insulated and stirred reaction 2h are warming up to it, subsequently the acetic acid solution adjustment pH to 4.5 that mass fraction is 5% is added to it, and to its pressure filtration, collect filter cake and be placed on dry 8h in the baking oven of 70 DEG C, obtaining holocellulose for subsequent use; The ratio of 1:250 in mass ratio, Chitosan powder being dissolved to mass concentration is in the acetum of 2%, regulate pH to 3.0, be prepared into chitosan solution, count by weight subsequently, choose the chitosan solution of 65 parts, the mass concentration of 20 parts is the sodium tripolyphosphate solution of the different thiophene of the methyl mile beautiful jade ketone solution of 10% and the 2g/L of 15 parts, is uniformly mixed formation crosslinker solution at 30 DEG C; After end to be crosslinked, washing crosslinker solution to pH by deionized water is 7, subsequently to its suction filtration, collect filter cake, and use ethyl acetate and acetone extracting 24h in Soxhlet extraction device respectively, take out filter cake dry 30min in 50 DEG C of baking ovens subsequently, be prepared into chitosan microball carrier; Count by weight, choose the holocellulose of above-mentioned preparation of the chitosan microball carrier of 45 parts, the deionized water of 35 parts and 20 parts, be prepared into shitosan mixed liquor, be placed on subsequently in there-necked flask, reflux 1h under 90 DEG C of waters bath with thermostatic control, after backflow completes, decompress filter is carried out to it, collect filter cake, and distilled water washing is 7.0 to pH, in 60 DEG C of baking ovens, dry 10h can be prepared into a kind of holocellulose/chitosan microball adsorbent.
Getting holocellulose/chitosan microball sorbent-loaded that 40g obtains is on the screen cloth of 20 μm in aperture, being holded up by screen cloth is placed in wastewater disposal basin, one is laid every 60cm, pass into the mercury-containing waste water that mass concentration is 200mg/L, stop 8h, recording mercury ion adsorption capacity is 190mg/g, and adsorption rate reaches 95%.

Claims (1)

1. a preparation method for holocellulose/chitosan microball adsorbent, is characterized in that concrete preparation process is:
(1) soybean stalk is rinsed through clear water, after being exposed to the sun under sunlight 3 ~ 5 days, be placed in high speed grinding mill and carry out pulverizing and sieving to it, collect 80 ~ 100 object soybean stalk particles, subsequently by the ratio of methyl alcohol and toluene 5:1 by volume, be uniformly mixed at 20 ~ 30 DEG C, be prepared into extract;
(2) be the ratio of 1:3 in solid-to-liquid ratio, by the soybean stalk particle of above-mentioned preparation and extract, be placed in Soxhlet extraction device, after its Soxhlet extraction 5 ~ 6h, decolouring paraffin removal is carried out 1 ~ 2 time repeatedly again by macroporous resin column, in micropore gel column, carry out secondary decolourization paraffin removal 1 ~ 2 time more subsequently, remove stalk particle pigment and wax;
(3) after Soxhlet extraction completes, 1:5 in mass ratio, the sodium hydroxide solution of the soybean stalk particle after extracting and 0.85mol/L is uniformly mixed, and 70 ~ 75 DEG C of insulated and stirred reaction 1 ~ 2h are warming up to it, subsequently acetic acid solution adjustment pH to 4.2 ~ 4.5 that mass fraction is 5% are added to it, and to its pressure filtration, collect filter cake and be placed on dry 6 ~ 8h in the baking oven of 60 ~ 70 DEG C, obtaining holocellulose for subsequent use;
(4) ratio of 1:250 in mass ratio, Chitosan powder being dissolved to mass concentration is in the acetum of 2%, regulate pH to 2.5 ~ 3.0, be prepared into chitosan solution, count by weight subsequently, choose the chitosan solution of 45 ~ 65 parts, 20 ~ 30 parts of mass concentrations are the sodium tripolyphosphate solution of the different thiophene of the methyl mile beautiful jade ketone solution of 10% and the 2g/L of 15 ~ 25 parts, are uniformly mixed formation crosslinker solution at 20 ~ 30 DEG C;
(5) after end to be crosslinked, washing crosslinker solution to pH by deionized water is 7, subsequently to its suction filtration, collect filter cake, and use ethyl acetate and acetone extracting 20 ~ 24h in Soxhlet extraction device respectively, take out filter cake dry 20 ~ 30min in 50 DEG C of baking ovens subsequently, be prepared into chitosan microball carrier;
(6) count by weight, choose the holocellulose of above-mentioned preparation of the chitosan microball carrier of 20 ~ 45 parts, the deionized water of 35 ~ 50 parts and 20 ~ 25 parts, be prepared into shitosan mixed liquor, be placed on subsequently in there-necked flask, reflux 1h under 80 ~ 90 DEG C of waters bath with thermostatic control, after backflow completes, decompress filter is carried out to it, collect filter cake, and distilled water washing is 7.0 to pH, in 55 ~ 60 DEG C of baking ovens, dry 6 ~ 10h can be prepared into a kind of holocellulose/chitosan microball adsorbent.
CN201510919579.6A 2015-12-12 2015-12-12 Preparation method for holocellulose/chitosan microsphere adsorbent Pending CN105396561A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201510919579.6A CN105396561A (en) 2015-12-12 2015-12-12 Preparation method for holocellulose/chitosan microsphere adsorbent

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201510919579.6A CN105396561A (en) 2015-12-12 2015-12-12 Preparation method for holocellulose/chitosan microsphere adsorbent

Publications (1)

Publication Number Publication Date
CN105396561A true CN105396561A (en) 2016-03-16

Family

ID=55462512

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201510919579.6A Pending CN105396561A (en) 2015-12-12 2015-12-12 Preparation method for holocellulose/chitosan microsphere adsorbent

Country Status (1)

Country Link
CN (1) CN105396561A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108514868A (en) * 2018-05-11 2018-09-11 武汉轻工大学 The method of pigment in the preparation method and separation grease of magnetic cellulose microsphere
CN109201020A (en) * 2018-11-17 2019-01-15 管敏富 A kind of preparation method of cellulose microsphere adsorbent
CN109464510A (en) * 2018-10-25 2019-03-15 方林 A kind of preparation method of rose sleep-helpful capsule
CN113145080A (en) * 2021-05-21 2021-07-23 安徽农业大学 Preparation method of TEMPO oxidized holocellulose-chitosan adsorption material, prepared adsorption material and application

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20080190321A1 (en) * 2005-04-15 2008-08-14 Basf Aktiengesellschaft Cellulose Solutions in Ionic Liquids
CN103183832A (en) * 2011-12-28 2013-07-03 中国科学院青岛生物能源与过程研究所 Preparation method for magnetic cellulose-chitosan composite microsphere
CN103521150A (en) * 2013-10-16 2014-01-22 青岛大学 Method for preparing cellulose microspheres and chitosan-coated cellulose composite microspheres
CN104451941A (en) * 2014-12-01 2015-03-25 恒天海龙股份有限公司 Carboxymethyl chitosan/cellulose composite material and preparation method thereof
CN104558677A (en) * 2015-02-05 2015-04-29 东北林业大学 Preparation method of nano cellulose/chitosan composite foam

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20080190321A1 (en) * 2005-04-15 2008-08-14 Basf Aktiengesellschaft Cellulose Solutions in Ionic Liquids
CN103183832A (en) * 2011-12-28 2013-07-03 中国科学院青岛生物能源与过程研究所 Preparation method for magnetic cellulose-chitosan composite microsphere
CN103521150A (en) * 2013-10-16 2014-01-22 青岛大学 Method for preparing cellulose microspheres and chitosan-coated cellulose composite microspheres
CN104451941A (en) * 2014-12-01 2015-03-25 恒天海龙股份有限公司 Carboxymethyl chitosan/cellulose composite material and preparation method thereof
CN104558677A (en) * 2015-02-05 2015-04-29 东北林业大学 Preparation method of nano cellulose/chitosan composite foam

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108514868A (en) * 2018-05-11 2018-09-11 武汉轻工大学 The method of pigment in the preparation method and separation grease of magnetic cellulose microsphere
CN108514868B (en) * 2018-05-11 2021-02-26 武汉轻工大学 Preparation method of magnetic cellulose microspheres and method for separating pigment in oil
CN109464510A (en) * 2018-10-25 2019-03-15 方林 A kind of preparation method of rose sleep-helpful capsule
CN109201020A (en) * 2018-11-17 2019-01-15 管敏富 A kind of preparation method of cellulose microsphere adsorbent
CN113145080A (en) * 2021-05-21 2021-07-23 安徽农业大学 Preparation method of TEMPO oxidized holocellulose-chitosan adsorption material, prepared adsorption material and application

Similar Documents

Publication Publication Date Title
CN105396561A (en) Preparation method for holocellulose/chitosan microsphere adsorbent
CN107383115B (en) The method for extracting flower color glycosides
CN103894396B (en) A kind of method of administering heavy-metal contaminated soil
CN103657600B (en) A kind of modification water treatment absorbent and its preparation method and application
CN103752280B (en) Composite modified walnut shell adsorbent and its preparation method and application
CN102179228A (en) Method for preparing carbon adsorbing material used for efficiently removing harmful ions from waste water
CN104059167A (en) Preparation method of polyamine compound-modified magnetic chitosan and application thereof
CN104759252A (en) A method of preparing porous carbon by adopting spherical zinc oxide as a template and applications of the porous carbon
CN103819934A (en) Method for preparing coated rare earth sulfide pigment
CN107638872B (en) Fly ash/magnetic straw composite material and preparation method and application thereof
CN105268418A (en) Preparation method of cross-linked chitosan modified shaddock peel adsorption material for removing low-concentration heavy metals in waste water
CN105251452A (en) Chitosan-silica gel hybridized magnetic adsorbent as well as preparation method and application thereof
CN113134339A (en) Preparation of zirconium-doped hydrotalcite-like adsorbent and application of zirconium-doped hydrotalcite-like adsorbent in treatment of phosphorus-containing wastewater
CN107383930B (en) The method for extracting plant brown pigment
CN102872831A (en) Compound adsorption material capable of removing cadmium ions in native water and preparation method thereof
CN102120790A (en) Methods for preparing high-hydrophilcity macroporous absorption resin and removing caffeine in crude tea extracts
CN103949226A (en) Preparation and application methods of magnetic polyvinyl alcohol-chitosan particles
CN105111654A (en) Preparation method of biomass film agent for shielding and reducing pollution
CN105561943A (en) Preparation method for magnetic rape stalk adsorbing material and application
CN107899554A (en) A kind of tealeaf residue compound adsorbent and preparation method thereof
CN104645942A (en) Method for preparing bamboo shoot shell adsorbing material
CN110665466A (en) Magnetic composite material for adsorbing Cd in water and preparation method thereof
CN105080485A (en) Method for preparing carbon bio-adsorbent from Chinese parasol fallen leaves
CN103007899B (en) Preparation method of heavy metal ion absorption resin
CN103007900B (en) Preparation method of kieselguhr modified absorbent resin

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
WD01 Invention patent application deemed withdrawn after publication
WD01 Invention patent application deemed withdrawn after publication

Application publication date: 20160316