CN104646062A - Preparation method for bamboo pulp cellulose-based integrated Fenton catalyst Fe<3+>C2O4/R - Google Patents

Preparation method for bamboo pulp cellulose-based integrated Fenton catalyst Fe<3+>C2O4/R Download PDF

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Publication number
CN104646062A
CN104646062A CN201510074499.5A CN201510074499A CN104646062A CN 104646062 A CN104646062 A CN 104646062A CN 201510074499 A CN201510074499 A CN 201510074499A CN 104646062 A CN104646062 A CN 104646062A
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bamboo pulp
bamboo
preparation
fenton catalyst
pulp fiber
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张勇
杨梦梦
杨晓刚
姚菊明
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Zhejiang Sci Tech University ZSTU
Zhejiang University of Science and Technology ZUST
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Zhejiang Sci Tech University ZSTU
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Abstract

The invention discloses a preparation method for a bamboo pulp cellulose-based integrated Fenton catalyst Fe<3+>C2O4/R. The preparation method is characterized in that tri-valent iron and oxalic acid are subjected to coordination to form a complex Fe<3+>C2O4, and the complex Fe<3+>C2O4 is loaded on bamboo pulp cellulose-based porous resin R synthesized by bamboo pulp to form the integrated Fenton catalyst Fe<3+>C2O4/R; under visible light, hydrogen peroxide can be catalyzed in an acceleration manner to degrade dye type organic pollutants in printing and dyeing wastewater. A product prepared by the method is high in efficiency, environment-friendly and low in cost; the problems of secondary pollution, high oxidization cost, low degrading efficiency and the like which are caused by a fact that the Fenton reagent cannot be repeatedly used in the conventional dye type organic pollutant Fenton oxidization degrading are solved, and the creation concept of using bamboo resources in China in a high value is provided, and thus the preparation method has obvious environmental and social significance.

Description

A kind of bamboo pulp fiber element basis set becomes fenton catalyst Fe 3+c 2o 4the preparation method of/R
Technical field
The present invention relates to a kind of preparation method of integrated fenton catalyst, particularly a kind of bamboo pulp fiber element basis set becomes fenton catalyst Fe 3+c 2o 4the preparation method of/R, belongs to high-molecular organic material technical field.
Background technology
Fenton oxidation is one of important technology of advanced treatment of industrial waste water, is to utilize hydrogen peroxide, with ferrous strong oxidizing property, oxidation operation is become inorganic states, reaches the object of degradation of organic waste water.During organic pollution, there is Fenton reagent and can not reuse and then cause secondary pollution in tradition Fenton oxidation, the limitations such as oxidation cost is high, degradation efficiency is low in degrading waste water.In recent years, the light of iron or iron complex is utilized to help hardly degraded organic substance in multiphase-fenton Fenton degradation water to cause the extensive concern of researcher.In early-stage Study, although add oxalic acid can improve catalytic efficiency, catalyst is not recyclable and then cause oxidation cost high.Simple load class heterogeneous catalyst can realize reclaiming, but reaction rate is in reduced levels always, is dropped into industrial imagination and is difficult to realize.
Its characteristic of technical scheme that we propose at this is, utilizes cellulose base porous resin load ferric oxalate on the one hand, realizes ferric iron Catalyzed by Oxalic Acid agent complex compound Fe 3+c 2o 4the recovery and reuse of/R, thus the processing cost reducing process Fenton oxidation, and minimizing flowing molten iron loses the secondary environmental pollution caused; On the other hand making part with iron forms ferric iron Catalyzed by Oxalic Acid agent complex compound by adding the oxalates with light sensitivity, can improve the defects such as the reaction rate caused due to heterogeneous catalyst is low, raising multiphase-fenton Fenton is degraded the speed of dyeing waste water and efficiency.In the preparation of multiphase-fenton fenton catalyst and application thereof, Chinese patent (CN201410465387) " surface-modified nano tri-iron tetroxide fenton catalyst and preparation method thereof " prepares high dispersancy nano tri-iron tetroxide by coprecipitation, then carries out surface modification by Hydrolyze method to nano ferriferrous oxide; Chinese patent (CN201410483397) " a kind of method preparing heterogeneous light Fenton catalyst " is by goethite-Graphene-mesoporous supports material triplicity, for the excellent catalytic effect of organic pollutants (particularly phenol, nitrogen heterocyclic ring etc.), pH is applied widely, repeat performance is good, effectively can reduce COD and TOC in waste water simultaneously; Chinese patent (CN201410448550) " a kind of take molecular sieve as heterogeneous fenton catalyst of Fe-Mn bimetallic of carrier and its preparation method and application " is by MnSO 4h 2o and FeSO 47H 2obtain mixed system after the mixing of O solution, in mixed system, add NaY molecular sieve, mix, in above-mentioned mixed system, add citric acid, water-bath, gained dope is dried, calcine, obtain the heterogeneous fenton catalyst of Fe-Mn/NaY support type; United States Patent (USP) (US 20060138057 A1) " Eco-friendly photo - fenton catalyst-immobilized Fe (III) over HY-zeolite " ferric ion is fixed on HY zeolite through methods such as dipping, calcinings obtains isomery iron (III)-HY catalyst; by evaluating its catalyst activity to the Fenton degraded of phenolic waste liquor, and study iron load capacity, H 2o 2concentration, the factors such as pH value are on the impact of catalyst light Fenton's reaction; United States Patent (USP) (US 20050274678 A1) " Integrated technology in sequential treatment of organics and heavy metal ions wastewater " provides a kind of integrated technology for the continuous complicated wastewater treatment process containing low biological degradability organic matter and heavy metal ion produced by process of surface treatment, is conducive to the ferrite quality reducing Fenton oxidation process iron mud generation and improve processing procedure generation.So far, yet there are no and utilize bamboo pulp fiber element as molecular skeleton matrix, become the related process technologies of fenton catalyst to occur in order to prepare bamboo pulp fiber element basis set.
Meanwhile, China is the country studying, cultivate and utilize bamboo in the world the earliest, and bamboo resource is very abundant, the important sources of bamboo Ye Shi China bamboo district peasant economy income.Bamboo belongs to rank vegetation resource, has fast growth, the cycle of becoming a useful person is short, fiber content advantages of higher, and fibre morphology and fibrocyte content are close to even higher than general leaf wood.Make full use of the bamboo resource of China's abundant, the renewable new material of preparation high added value, opens one's minds, meets national development circular economy policy, have important practical significance for one that becomes higher value application China bamboo resource.
Summary of the invention
In order to overcome in traditional Fenton oxidation process industrial wastewater process, Fenton reagent is difficult to reclaim and then cause secondary pollution, the problems such as oxidation cost is high, degradation efficiency is low, the bamboo resource of recycling China's abundant prepares the renewable new material of high added value simultaneously, the object of this invention is to provide a kind of bamboo pulp fiber element basis set and becomes fenton catalyst Fe 3+c 2o 4the preparation method of/R.
For achieving the above object, technical scheme of the present invention adopts following steps:
1) plant pulverizer is adopted to pulverize bamboo pulpboard, filter through 100 eye mesh screens, obtain particle diameter and be less than or equal to 0.15 mm bamboo pulp powder, add alkaline solution vigorous stirring 2 ~ 4 min of precooling to-10 ~-25 DEG C, leave standstill reaction 60 ~ 120 min, taking-up is placed in ice bath and stirs, and obtains the bamboo pulp fiber cellulose solution of homogeneous transparent;
2) under mechanical agitation, bamboo pulp fiber cellulose solution heating water bath to 50 ~ 70 DEG C that step 1) is obtained, pass into nitrogen 20 ~ 40 min, the ammonium persulfate adding 0.1 ~ 0.2 g/g bamboo pulp powder causes 10 ~ 20 min, add the acrylamide of 0.5 ~ 1.0 g/g bamboo pulp powder successively, the acrylic acid of 2.0 ~ 4.0 g/g bamboo pulp powder and the N-N '-methylene-bisacrylamide through NaOH neutralization of 15 ~ 25 mg/g bamboo pulp powder, continue logical nitrogen reaction 1 ~ 3 h, product deionized water is washed till neutrality, add absolute ethyl alcohol dehydration 12 ~ 24 h, freeze drying obtains bamboo pulp fiber element base porous resin R,
3) by 0.1 ~ 0.2 mol/L Na 2c 2o 4with Fe (NO 3) 3solution respectively gets 10 mL hybrid reaction 20 ~ 40 min, by 40 ~ 60 mg steps 2) bamboo pulp fiber that obtains element base porous resin R adds above-mentioned mixed solution, reaction 24 h is shaken under 20 ~ 40 DEG C, water bath with thermostatic control oscillator, 100 ~ 120 r/min conditions, product deionized water is washed till neutrality, and namely vacuum drying obtains integrated fenton catalyst Fe 3+c 2o 4/ R product.
Described alkaline solution is NaOH and urea mixed solution, wherein the mass percent of NaOH, urea and deionized water is respectively 4 ~ 6 wt%, 9 ~ 11 wt% and 83 ~ 87 wt%, and bamboo pulp powder carries out mixing and reacting with 2 g: 50 ~ 70 mL with this mixed solution.
Described bamboo pulpboard is the one in black bamboo pulpboard, square bamboo pulp plate, mao bamboon pulpboard and henon bamboo pulpboard.
Compared with background technology, the beneficial effect that the present invention has is:
The present invention introduces bamboo resource in the raw material of the integrated fenton catalyst of synthesis, has expanded the raw material range of the integrated fenton catalyst of preparation; The bamboo pulp fiber element basis set of preparing of the present invention's proposition becomes fenton catalyst Fe 3+c 2o 4the method of/R is conducive to solving in traditional Fenton oxidation degraded dyeing waste water dye class organic pollution process, Fenton reagent can not reuse and then cause secondary pollution, the problems such as oxidation cost is high, degradation efficiency is low, propose opening one's minds of higher value application China bamboo resource simultaneously, meet national development circular economy policy, be expected to the income conscientiously improving China bamboo district peasant.
Accompanying drawing explanation
Fig. 1 is integrated fenton catalyst Fe prepared by embodiment 1 3+c 2o 4the field emission scanning electron microscope photo of/R product.Wherein, Fig. 1 a is that cellulose base porous resin amplifies 10,000 times of photos, and Fig. 1 b is integrated fenton catalyst Fe 3+c 2o 4/ R amplifies 5,000 times of photos.
Detailed description of the invention
Below in conjunction with specific embodiment, the invention will be further described.
embodiment 1:
1) plant pulverizer is adopted to pulverize henon bamboo pulpboard, filter through 100 eye mesh screens, obtain particle diameter and be less than or equal to 0.15 mm bamboo pulp powder, add alkaline solution vigorous stirring 4 min of precooling to-10 DEG C, leave standstill reaction 120 min, wherein alkaline solution is NaOH and urea mixed solution, the mass percent of NaOH, urea and deionized water is respectively 6 wt%, 11 wt% and 83 wt%, bamboo pulp powder carries out mixing and reacting with 2 g: 70 mL with mixed solution, then take out and be placed in ice bath and stir, obtain homogeneous transparent bamboo pulp fiber cellulose solution;
2) under mechanical agitation, the bamboo pulp fiber cellulose solution heating water bath to 70 DEG C that step 1) is obtained, pass into nitrogen 20 min, the ammonium persulfate adding 0.1 g/g bamboo pulp powder causes 20 min, add the acrylamide of 0.5 g/g bamboo pulp powder successively, the acrylic acid of 2.0 g/g bamboo pulp powder and the N-N '-methylene-bisacrylamide through NaOH neutralization of 15 mg/g bamboo pulp powder, continue logical nitrogen and react 1 h, product deionized water is washed till neutrality, add absolute ethyl alcohol to dewater 12 h, freeze drying obtains bamboo pulp fiber element base porous resin R;
3) by 0.1 mol/L Na 2c 2o 4with Fe (NO 3) 3solution respectively gets 10 mL hybrid reaction 20 min, by 40 mg steps 2) bamboo pulp fiber that obtains element base porous resin R adds above-mentioned mixed solution, reaction 24 h is shaken under 40 DEG C, water bath with thermostatic control oscillator, 100 r/min conditions, product deionized water is washed till neutrality, and namely vacuum drying obtains integrated fenton catalyst Fe 3+c 2o 4/ R product (a).
embodiment 2:
1) plant pulverizer is adopted to pulverize black bamboo pulpboard, filter through 100 eye mesh screens, obtain particle diameter and be less than or equal to 0.15 mm bamboo pulp powder, add alkaline solution vigorous stirring 3 min of precooling to-15 DEG C, leave standstill reaction 90 min, wherein alkaline solution is NaOH and urea mixed solution, the mass percent of NaOH, urea and deionized water is respectively 5 wt%, 10 wt% and 85 wt%, bamboo pulp powder carries out mixing and reacting with 2 g: 60 mL with mixed solution, then take out and be placed in ice bath and stir, obtain homogeneous transparent bamboo pulp fiber cellulose solution;
2) under mechanical agitation, the bamboo pulp fiber cellulose solution heating water bath to 60 DEG C that step 1) is obtained, pass into nitrogen 30 min, the ammonium persulfate adding 0.15 g/g bamboo pulp powder causes 15 min, add the acrylamide of 0.75 g/g bamboo pulp powder successively, the acrylic acid of 3.0 g/g bamboo pulp powder and the N-N '-methylene-bisacrylamide through NaOH neutralization of 20 mg/g bamboo pulp powder, continue logical nitrogen and react 2 h, product deionized water is washed till neutrality, add absolute ethyl alcohol to dewater 18 h, freeze drying obtains bamboo pulp fiber element base porous resin R;
3) by 0.15 mol/L Na 2c 2o 4with Fe (NO 3) 3solution respectively gets 10 mL hybrid reaction 30 min, by 50 mg steps 2) bamboo pulp fiber that obtains element base porous resin R adds above-mentioned mixed solution, reaction 24 h is shaken under 30 DEG C, water bath with thermostatic control oscillator, 110 r/min conditions, product deionized water is washed till neutrality, and namely vacuum drying obtains integrated fenton catalyst Fe 3+c 2o 4/ R product (b).
embodiment 3:
1) plant pulverizer is adopted to pulverize black bamboo pulpboard, filter through 100 eye mesh screens, obtain particle diameter and be less than or equal to 0.15 mm bamboo pulp powder, add alkaline solution vigorous stirring 2 min of precooling to-25 DEG C, leave standstill reaction 60 min, wherein alkaline solution is NaOH and urea mixed solution, the mass percent of NaOH, urea and deionized water is respectively 4 wt%, 9 wt% and 87 wt%, bamboo pulp powder carries out mixing and reacting with 2 g: 50 mL with mixed solution, then take out and be placed in ice bath and stir, obtain homogeneous transparent bamboo pulp fiber cellulose solution;
2) under mechanical agitation, the bamboo pulp fiber cellulose solution heating water bath to 50 DEG C that step 1) is obtained, pass into nitrogen 40 min, the ammonium persulfate adding 0.2 g/g bamboo pulp powder causes 10 min, add the acrylamide of 1.0 g/g bamboo pulp powder successively, the acrylic acid of 4.0 g/g bamboo pulp powder and the N-N '-methylene-bisacrylamide through NaOH neutralization of 25 mg/g bamboo pulp powder, continue logical nitrogen and react 3 h, product deionized water is washed till neutrality, add absolute ethyl alcohol to dewater 24 h, freeze drying obtains bamboo pulp fiber element base porous resin R;
3) by 0.2 mol/L Na 2c 2o 4with Fe (NO 3) 3solution respectively gets 10 mL hybrid reaction 40 min, by 60 mg steps 2) bamboo pulp fiber that obtains element base porous resin R adds above-mentioned mixed solution, reaction 24 h is shaken under 20 DEG C, water bath with thermostatic control oscillator, 120 r/min conditions, product deionized water is washed till neutrality, and namely vacuum drying obtains integrated fenton catalyst Fe 3+c 2o 4/ R product (c).
Measure water absorbent rate and the ferric iron load factor of the cellulose base porous resin R that embodiment 1,2,3 prepares.Table 1 is for being prepared the measurement result of ferric iron load factor on the water absorbent rate of cellulose base porous resin R, cellulose base porous resin R by embodiment 1,2,3.From data in table 1, a kind of bamboo pulp fiber element basis set of the present invention is adopted to become fenton catalyst Fe 3+c 2o 4integrated fenton catalyst Fe prepared by the preparation method of/R 3+c 2o 4/ R has higher ferric iron load factor.
As Fig. 1, from integrated fenton catalyst Fe prepared by embodiment 1 3+c 2o 4the field emission scanning electron microscope photo of/R product can be found out, it is loose porous that Fig. 1 a shows cellulose base porous resin pattern, is conducive to a large amount of loads of later stage ferric ion, and Fig. 1 b shows the integrated fenton catalyst Fe of preparation 3+c 2o 4its individual size of/R and specific area are suitable for, and are suitable for carrying out efficient light and help Fenton catalytic oxidation.
Table 1
What more than enumerate is only specific embodiments of the invention.The invention is not restricted to above embodiment, many distortion can also be had.All distortion that those of ordinary skill in the art can directly derive from content disclosed by the invention or associate, all should think protection scope of the present invention.

Claims (3)

1. a bamboo pulp fiber element basis set becomes fenton catalyst Fe 3+c 2o 4the preparation method of/R, is characterized in that, comprises the following steps:
1) plant pulverizer is adopted to pulverize bamboo pulpboard, filter through 100 eye mesh screens, obtain particle diameter and be less than or equal to 0.15 mm bamboo pulp powder, add alkaline solution vigorous stirring 2 ~ 4 min of precooling to-10 ~-25 DEG C, leave standstill reaction 60 ~ 120 min, taking-up is placed in ice bath and stirs, and obtains the bamboo pulp fiber cellulose solution of homogeneous transparent;
2) under mechanical agitation, bamboo pulp fiber cellulose solution heating water bath to 50 ~ 70 DEG C that step 1) is obtained, pass into nitrogen 20 ~ 40 min, the ammonium persulfate adding 0.1 ~ 0.2 g/g bamboo pulp powder causes 10 ~ 20 min, add the acrylamide of 0.5 ~ 1.0 g/g bamboo pulp powder successively, the acrylic acid of 2.0 ~ 4.0 g/g bamboo pulp powder and the N-N '-methylene-bisacrylamide through NaOH neutralization of 15 ~ 25 mg/g bamboo pulp powder, continue logical nitrogen reaction 1 ~ 3 h, product deionized water is washed till neutrality, add absolute ethyl alcohol dehydration 12 ~ 24 h, freeze drying obtains bamboo pulp fiber element base porous resin R,
3) by 0.1 ~ 0.2 mol/L Na 2c 2o 4with Fe (NO 3) 3solution respectively gets 10 mL hybrid reaction 20 ~ 40 min, by 40 ~ 60 mg steps 2) bamboo pulp fiber that obtains element base porous resin R adds above-mentioned mixed solution, reaction 24 h is shaken under 20 ~ 40 DEG C, water bath with thermostatic control oscillator, 100 ~ 120 r/min conditions, product deionized water is washed till neutrality, and namely vacuum drying obtains integrated fenton catalyst Fe 3+c 2o 4/ R product.
2. a kind of bamboo pulp fiber element basis set according to claim 1 becomes fenton catalyst Fe 3+c 2o 4the preparation method of/R, it is characterized in that: described alkaline solution is NaOH and urea mixed solution, wherein the mass percent of NaOH, urea and deionized water is respectively 4 ~ 6 wt%, 9 ~ 11 wt% and 83 ~ 87 wt%, and bamboo pulp powder carries out mixing and reacting with 2 g: 50 ~ 70 mL with this mixed solution.
3. a kind of bamboo pulp fiber element basis set according to claim 1 becomes fenton catalyst Fe 3+c 2o 4the preparation method of/R, is characterized in that: described bamboo pulpboard is the one in black bamboo pulpboard, square bamboo pulp plate, mao bamboon pulpboard and henon bamboo pulpboard.
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CN106006903A (en) * 2016-05-27 2016-10-12 浙江理工大学 Preparation method of bamboo-pulp cellulose and poly(N-vinylformamide) composite flocculating and decolorizing material
CN106219821A (en) * 2016-08-30 2016-12-14 嘉兴赛维环保科技有限公司 One utilizes cellulose base integrated Fenton catalyst Fe3+c2o4the method of/R advanced treatment of dyeing wastewater
CN106587296A (en) * 2016-11-28 2017-04-26 浙江理工大学 Bamboo pulp cellulose based flocculation decolorization composite functional material and preparation method thereof
CN106824996A (en) * 2017-02-16 2017-06-13 广东工业大学 A kind of method of smooth thermal coupling degradation biological matter discarded object
CN107213916A (en) * 2017-06-27 2017-09-29 广西大学 The preparation method and applications of modified wood fibre element ester group class fenton catalyst
CN107233916A (en) * 2017-06-27 2017-10-10 广西大学 Carry the preparation method and applications of the cellulose ester-based spheric catalyst of hophornbeam matter
CN107321384A (en) * 2017-06-27 2017-11-07 广西大学 The preparation method and applications of lignocellulosic ester/sodium alginate complex spherical class fenton catalyst
CN110745982A (en) * 2019-09-12 2020-02-04 生态环境部华南环境科学研究所 Method for deep oxidation treatment of organic wastewater based on visible light assisted complexing iron ion activated monoperoxybisulfate
CN113663737A (en) * 2021-08-19 2021-11-19 南京医科大学康达学院 CMC-Fe-based microsphere and preparation method and application thereof

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Cited By (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105170183A (en) * 2015-09-16 2015-12-23 天津工业大学 Wool fiber metal complex photocatalyst and preparation method thereof
CN106006903A (en) * 2016-05-27 2016-10-12 浙江理工大学 Preparation method of bamboo-pulp cellulose and poly(N-vinylformamide) composite flocculating and decolorizing material
CN106006903B (en) * 2016-05-27 2018-12-18 浙江理工大学 A kind of preparation method of bamboo pulp fiber element & polyvinylformamide composite flocculation decoloring material
CN106219821A (en) * 2016-08-30 2016-12-14 嘉兴赛维环保科技有限公司 One utilizes cellulose base integrated Fenton catalyst Fe3+c2o4the method of/R advanced treatment of dyeing wastewater
CN106587296A (en) * 2016-11-28 2017-04-26 浙江理工大学 Bamboo pulp cellulose based flocculation decolorization composite functional material and preparation method thereof
CN106824996A (en) * 2017-02-16 2017-06-13 广东工业大学 A kind of method of smooth thermal coupling degradation biological matter discarded object
CN107233916A (en) * 2017-06-27 2017-10-10 广西大学 Carry the preparation method and applications of the cellulose ester-based spheric catalyst of hophornbeam matter
CN107321384A (en) * 2017-06-27 2017-11-07 广西大学 The preparation method and applications of lignocellulosic ester/sodium alginate complex spherical class fenton catalyst
CN107213916A (en) * 2017-06-27 2017-09-29 广西大学 The preparation method and applications of modified wood fibre element ester group class fenton catalyst
CN107233916B (en) * 2017-06-27 2019-10-01 广西大学 Carry the preparation method and applications of the cellulose ester-based spheric catalyst of hophornbeam matter
CN110745982A (en) * 2019-09-12 2020-02-04 生态环境部华南环境科学研究所 Method for deep oxidation treatment of organic wastewater based on visible light assisted complexing iron ion activated monoperoxybisulfate
CN113663737A (en) * 2021-08-19 2021-11-19 南京医科大学康达学院 CMC-Fe-based microsphere and preparation method and application thereof
CN113663737B (en) * 2021-08-19 2023-08-15 南京医科大学康达学院 CMC-Fe-based microsphere, and preparation method and application thereof

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