CN111250062B - Cellulose foam capable of visually identifying and removing chromium, preparation method thereof and chromium removal method - Google Patents

Cellulose foam capable of visually identifying and removing chromium, preparation method thereof and chromium removal method Download PDF

Info

Publication number
CN111250062B
CN111250062B CN202010127485.6A CN202010127485A CN111250062B CN 111250062 B CN111250062 B CN 111250062B CN 202010127485 A CN202010127485 A CN 202010127485A CN 111250062 B CN111250062 B CN 111250062B
Authority
CN
China
Prior art keywords
cellulose
chromium
cellulose foam
solution
foam
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.)
Active
Application number
CN202010127485.6A
Other languages
Chinese (zh)
Other versions
CN111250062A (en
Inventor
张胜利
张思略
裴彥博
杨红薇
刘伯芳
周祚万
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.)
Southwest Jiaotong University
Original Assignee
Southwest Jiaotong 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 Southwest Jiaotong University filed Critical Southwest Jiaotong University
Priority to CN202010127485.6A priority Critical patent/CN111250062B/en
Publication of CN111250062A publication Critical patent/CN111250062A/en
Application granted granted Critical
Publication of CN111250062B publication Critical patent/CN111250062B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

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
    • B01J20/26Synthetic macromolecular compounds
    • B01J20/265Synthetic macromolecular compounds modified or post-treated polymers
    • B01J20/267Cross-linked polymers
    • 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
    • B01J20/24Naturally 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
    • B01J20/28042Shaped bodies; Monolithic structures
    • B01J20/28045Honeycomb or cellular structures; Solid foams or sponges
    • 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
    • B01J20/34Regenerating or reactivating
    • B01J20/345Regenerating or reactivating using a particular desorbing compound or mixture
    • B01J20/3475Regenerating or reactivating using a particular desorbing compound or mixture in the liquid phase
    • 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
    • C02F1/285Treatment of water, waste water, or sewage by sorption using synthetic organic sorbents
    • 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
    • C02F2101/22Chromium or chromium compounds, e.g. chromates

Landscapes

  • Chemical & Material Sciences (AREA)
  • Analytical Chemistry (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Hydrology & Water Resources (AREA)
  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Solid-Sorbent Or Filter-Aiding Compositions (AREA)

Abstract

The invention provides a cellulose foam capable of visually identifying and removing chromium, a preparation method thereof and a chromium removal method, wherein the preparation method comprises the following steps: adding epichlorohydrin into the cellulose solution, stirring until the color of the solution becomes light, adding PEI solution, uniformly stirring, crosslinking for 5-60min at 25-60 ℃ to form hydrogel, washing with deionized water, freezing, and freeze-drying to obtain the modified cellulose. The cellulose foam prepared by the method can quickly identify and remove Cr (VI) in a wider pH range, can regulate and control the electrostatic adsorption and the subsequent oxidation-reduction process of Cr (VI), ensures that the structure of the adsorbent cannot be damaged due to oxidation reaction while removing Cr (VI), and has high regeneration speed of the material after adsorbing Cr (VI) and cannot damage the structure of the adsorbent in the regeneration process.

Description

Cellulose foam capable of visually identifying and removing chromium, preparation method thereof and chromium removal method
Technical Field
The invention belongs to the technical field of chromium adsorption materials, and particularly relates to a cellulose foam capable of visually identifying and removing chromium, a preparation method thereof and a chromium removal method thereof.
Background
China is a world large country for producing chromium salt and is also a world large country for consuming chromium and compounds thereof. For historical reasons, 670 ten thousand tons of chromium slag are completely treated in 15 provinces, but the remediation and treatment of the soil and underground water polluted by the chromium slag are heavy and far away. In addition, the discharge of three wastes in the industries of metallurgy, electroplating, tanning, paint, printing and dyeing, pigment, ceramics, catalysis, corrosion prevention and the like further aggravates the environmental chromium pollution and seriously threatens the human health. Chromium is a heavy metal with strong toxicity, is listed as one of the most toxic pollutants by the United states environmental protection agency, and is listed in the blacklist of water environment priority control pollutants in China. The chromium in the environment mainly exists in two valence states of Cr (III) and Cr (VI), and the Cr (VI) in the environment has stronger toxicity and the carcinogenic and mutagenic capacity of the Cr (III) is 1000 times that of the Cr (III); meanwhile, cr (VI) also has strong oxidation capacity and migration energy, so that the identification and removal of Cr (VI) in water and wastewater are highly regarded by people.
At present, the common treatment methods of the wastewater containing Cr (VI) mainly comprise a chemical reduction method, a barium salt precipitation method, an ion exchange method, an electrolysis method, a membrane separation method, an activated carbon adsorption method and the like. The method can realize the removal of Cr (VI) through proper combination, but the reaction process has high energy consumption or needs a large amount of chemical reagents, and secondary pollutants such as chromium sludge and the like are generated. In addition, when used for treating low-concentration Cr (VI) -containing wastewater, the method also has the problems of high cost, low treatment efficiency and the like. Compared with the traditional adsorption method, the biological adsorption method has the advantages of simple process equipment, easy operation, good treatment effect and the like, and the biological adsorbent is cheap and easy to obtain, thus becoming a hot spot of domestic and foreign research in recent years.
The prior art has the following reports: (1) The sodium carboxymethylcellulose is used as a raw material, and the Cr (VI) removing adsorbent with a three-dimensional porous network structure is prepared by a crosslinking method, but the finished product is hydrogel instead of foam. The mass transfer of pollutants is not favorable by the large amount of water filled in the hydrogel, and in the adsorption process, the adsorbed and combined Cr (VI) and the hydrogel undergo redox reaction, so that the structure of the hydrogel can be damaged due to oxidation, and the adsorption effect is finally influenced. (2) Cellulose is used as a raw material, modified cellulose fibers with a one-dimensional structure and modified cellulose membranes with a two-dimensional structure are respectively prepared by an oxidation-grafting method, the modified cellulose fibers and the modified cellulose membranes do not have rich porous structures, the exposure of active point positions and the mass transfer of pollutants are not facilitated, in addition, in the adsorption process, cr (VI) is reduced into Cr (III) by hydroxyl on the cellulose, the reaction can not be controlled to stop in the electrostatic adsorption stage, and the self structures of the adsorbent are inevitably damaged. Therefore, the prior Cr (VI) removing adsorbent mainly has the following problems: (1) the adsorbent is non-fluorescent and cannot simultaneously recognize Cr (VI). (2) The slower rate of Cr (VI) removal results in higher reactor processing costs. (3) The treated effluent can hardly reach the limit value of 0.05mg/L of Cr (VI) in sanitary Standard of Drinking Water. (4) When the PEI modified adsorbent is used for removing Cr (VI), two processes of electrostatic adsorption and oxidation-reduction reaction cannot be regulated, the Cr (VI) can be partially or completely reduced into Cr (III) by the adsorbent, and the structure of the adsorbent can be destroyed to a certain extent, so that the regeneration and use of the adsorbent are influenced. (5) The regeneration process of the used adsorbent takes a long time, and the adsorption performance is rapidly reduced in repeated use.
Disclosure of Invention
Aiming at the problems in the prior art, the invention provides a cellulose foam capable of visually identifying and removing chromium, a preparation method thereof and a chromium removal method thereof. The cellulose foam can quickly identify and remove Cr (VI) in a wider pH range, can regulate and control the electrostatic adsorption and the subsequent oxidation-reduction process of Cr (VI), ensures that the structure of the adsorbent is not damaged when the Cr (VI) is removed, has high regeneration speed after adsorbing the Cr (VI) by the adsorbent, and cannot damage the structure of the adsorbent in the regeneration process.
In order to achieve the purpose, the technical scheme adopted by the invention for solving the technical problems is as follows:
a cellulose foam capable of visually identifying and removing chromium is prepared by the following steps:
adding epichlorohydrin into the cellulose solution, adding PEI solution, stirring uniformly, crosslinking for 5-60min at 25-60 ℃ to form hydrogel, washing with deionized water, freezing, and freeze-drying to obtain the product.
Further, the concentration of the cellulose solution is 3 to 7wt%, and the concentration of the cellulose solution is preferably 4wt%.
Further, the concentration of the PEI solution is 3-20wt%, preferably the concentration of the PEI solution is 5wt%.
Further, the volume ratio of the cellulose solution, the epichlorohydrin and the PEI solution is 10.3-1.
Further, the volume ratio of the cellulose solution, epichlorohydrin and PEI solution was 10.
Further, the crosslinking temperature was 50 ℃ and the crosslinking time was 20min.
Furthermore, the freezing temperature is-18 to-20 ℃, and the freezing time is 8 to 12 hours; preferably, the freezing temperature is-18 ℃ and the freezing time is 12h.
Further, the freeze-drying time was 24 hours.
The method for removing chromium from the cellulose foam which is prepared by the preparation method and can visually identify and remove chromium comprises the following steps: and (3) putting the cellulose foam into a chromium-containing water sample, stirring, taking out before the cellulose foam turns brown, regenerating by using a sodium hydroxide solution or sodium thiosulfate, and returning to adsorb Cr (VI), and circulating the operation until the effluent meets the corresponding standard requirement.
The cellulose foam capable of visually identifying and removing chromium, the preparation method thereof and the chromium removal method provided by the invention have the following beneficial effects:
the electrostatic adsorption of Cr (VI) is far faster than the subsequent oxidation-reduction process of Cr (VI), so that the electrostatic adsorption rate is increased, the electrostatic adsorption time is shortened, and the subsequent oxidation-reduction reaction can be avoided. The cellulose foam has a three-dimensional porous structure, which is not only beneficial to the exposure of active sites, but also can improve the effective mass transfer process, so that Cr (VI) is quickly adsorbed on the cellulose foam. Meanwhile, the PEI structure contains high-density primary amine, secondary amine and tertiary amine, and the positive charge is carried out due to protonation of amino groups in a wider pH range, so that the PEI structure can be combined with CrO containing Cr (VI) anions 4 2- 、HCrO 4 When electrostatic adsorption occurs, PEI has an aggregation fluorescence effect, the prepared cellulose foam emits strong blue fluorescence under 365nm ultraviolet irradiation, and the electrostatic adsorption of Cr (VI) can quench the cellulose foam, so that Cr can be rapidly identified and removed in a wider pH range(VI). The adsorption of the cellulose foam to the Cr (VI) is electrostatic action, so that the desorption of the Cr (VI) can be realized only by regulating and controlling the surface charge of the adsorbent, and the structure of the adsorbent cannot be damaged in the regeneration process.
In conclusion, the cellulose foam prepared by the invention can quickly identify and remove Cr (VI) in a wider pH range, can regulate and control the electrostatic adsorption and subsequent oxidation-reduction process of Cr (VI), ensures that the structure of the adsorbent is not damaged while removing Cr (VI), and can quickly regenerate after adsorbing Cr (VI), and the structure of the adsorbent cannot be damaged in the regeneration process.
Drawings
Fig. 1 is an SEM image of cellulose foam.
FIG. 2 is a photograph showing the visual recognition of Cr (VI) by cellulose foam under different pH conditions.
FIG. 3 is a photograph of a cellulose foam after adsorption of 50mg/L Cr (VI) and regeneration with sodium thiosulfate solution under sunlight (top row) and ultraviolet light (bottom row)).
FIG. 4 is a photograph of a cellulose foam after adsorbing 5mg/L Cr (VI) and regenerating with a sodium thiosulfate solution under sunlight (upper row) and ultraviolet light (lower row)).
Detailed Description
Example 1
A preparation method of cellulose foam capable of visually identifying and removing chromium comprises the following steps:
and (3) taking 8.333g of dried cotton, adding 145.45ml of DMSO solution, adding 42.6ml of 40wt% TBAH aqueous solution, mechanically stirring for dissolving, standing for defoaming, and then placing in a refrigerator at 4 ℃ for cooling for 2 hours to obtain a cellulose solution with the mass fraction of 4%. And (2) putting 10mL of the solution into a 50mL beaker, adding 1mL of epoxy chloropropane, stirring until the color of the solution becomes light, adding 0.1mL of 5wt% of PEI, uniformly stirring, pouring into a mold, placing into a 50 ℃ oven for reaction for 60min, taking out to obtain hydrogel, replacing the solvent with deionized water, placing into a freezer compartment (-18 ℃) for freezing for 12h, and then placing into a freeze dryer for freeze drying at-81 ℃ for 24h to obtain cellulose foam (also called PEI modified cellulose foam).
0.02g of prepared cellulose foam is put into 20ml of Cr (VI) -containing simulated wastewater with the concentration of 100mg/L and the pH value of 2, and the sample is sampled and analyzed after being magnetically stirred and adsorbed for 30min at the temperature of 25 ℃, so that the removal rate of Cr (VI) is 6.78 percent.
Example 2
A preparation method of cellulose foam capable of visually identifying and removing chromium comprises the following steps:
taking 10mL of the cellulose solution prepared in the example 1, putting the cellulose solution into a 50mL beaker, adding 1mL of epoxy chloropropane, stirring until the color of the solution becomes light, adding 1mL of 10wt% of PEI, stirring uniformly, pouring into a mold, putting into a 50 ℃ oven for reaction for 60min, taking out to obtain hydrogel, replacing the solvent with deionized water, putting into a refrigerator freezing chamber (-18 ℃) for freezing for 12h, and putting into a freeze dryer for freeze drying at-81 ℃ for 24h to obtain cellulose foam.
0.02g of prepared cellulose foam is put into 20mL of simulated wastewater containing Cr (VI) with the concentration of 100mg/L and the pH value of 2, and the sample is sampled and analyzed after being magnetically stirred and adsorbed for 30min at the temperature of 25 ℃, and the removal rate is measured to be 65.57%.
Example 3
A preparation method of cellulose foam capable of visually identifying and removing chromium comprises the following steps:
taking 10mL of the cellulose solution prepared in the example 1, putting the cellulose solution into a 50mL beaker, adding 0.5mL of epoxy chloropropane, stirring until the color of the solution becomes light, adding 1mL of 6wt% of PEI, stirring uniformly, pouring into a mold, putting into a 50 ℃ oven for regeneration for 30min, taking out to obtain hydrogel, replacing the solvent with deionized water, putting into a freezer compartment of a refrigerator for freezing for 12h at (-18 ℃), and putting into a freeze dryer for freeze drying for 24h at-81 ℃ to obtain cellulose foam.
0.05g of prepared cellulose foam is taken and put into 25mL of simulated wastewater containing Cr (VI) with the concentration of 100mg/L and the pH value of 2, and the sample is sampled and analyzed after being magnetically stirred and adsorbed for 30min at the temperature of 25 ℃, and the removal rate is 95.53 percent.
Example 4
A preparation method of cellulose foam capable of visually identifying and removing chromium comprises the following steps:
taking 10mL of the cellulose solution prepared in the example 1, putting the cellulose solution into a 50mL beaker, adding 0.5mL of epoxy chloropropane, stirring until the color of the solution becomes light, adding 0.5mL of 10wt% of PEI, stirring uniformly, pouring into a mold, putting into a 50 ℃ oven for regeneration for 30min, taking out to obtain hydrogel, replacing the solvent with deionized water, putting into a freezer compartment of a refrigerator for freezing for 12h at (-18 ℃), and putting into a freeze dryer for freeze drying for 24h at-81 ℃ to obtain cellulose foam.
0.05g of prepared cellulose foam is put into 25mL of simulated wastewater containing Cr (VI) with the concentration of 100mg/L and the pH value of 2, and the sample is sampled and analyzed after being magnetically stirred and adsorbed for 30min at the temperature of 25 ℃, and the removal rate is measured to be 78.33%.
Example 5
0.02g of the cellulose foam obtained in example 4 was put into 20mL of Cr (VI) -containing simulated wastewater with a concentration of 50mg/L and a pH value of 2, and the sample was magnetically stirred and adsorbed at 25 ℃ for 10min, and then the removal rate was 83.4% by analysis.
Example 6
Taking 10mL of the cellulose solution prepared in the example 1, putting the cellulose solution into a 50mL beaker, adding 0.5mL of epoxy chloropropane, stirring until the color of the solution becomes light, adding 1mL of 5wt% PEI, stirring uniformly, pouring into a mold, putting into a 50 ℃ oven for regeneration for 30min, taking out to obtain hydrogel, replacing the solvent with deionized water, putting into a refrigerator freezer (-18 ℃) for freezing for 12h, and putting into a freeze dryer for freeze drying at-81 ℃ for 24h to obtain cellulose foam.
0.05g of prepared cellulose foam is put into 25mL of simulated wastewater containing Cr (VI) with the concentration of 100mg/L and the pH value of 2, and the sample is sampled and analyzed after being magnetically stirred and adsorbed for 30min at the temperature of 25 ℃, and the removal rate is measured to be 87.91 percent.
Example 7
0.02g of the cellulose foam obtained in example 6 was put into 20mL of Cr (VI) -containing simulated wastewater with a concentration of 100g/L and a pH value of 6, and the sample was magnetically stirred and adsorbed at 25 ℃ for 30min, and then the removal rate was 55.64% by analysis.
Example 8
Taking 10mL of the cellulose solution prepared in the example 1, putting the cellulose solution into a 50mL beaker, adding 0.5mL of epoxy chloropropane, stirring until the color of the solution becomes light, adding 2mL of 5wt% PEI, stirring uniformly, pouring into a mold, putting into a 50 ℃ oven for regeneration for 20min, taking out to obtain hydrogel, replacing the solvent with deionized water, putting into a refrigerator freezer (-18 ℃) for freezing for 12h, and putting into a freeze dryer for freeze drying at-81 ℃ for 24h to obtain cellulose foam.
SEM characterization of the cellulose foam produced is shown in figure 1. As can be seen from FIG. 1, the cellulose foam produced had a developed three-dimensional network structure.
0.05g of prepared cellulose foam is put into 25mL of simulated wastewater containing Cr (VI) with the concentration of 40mg/L and the pH value of 3, and the sample is sampled and analyzed after being magnetically stirred and adsorbed for 30min at the temperature of 55 ℃, and the removal rate is measured to be 95.08 percent.
Example 9
0.05g of the cellulose foam obtained in example 8 was put into 25mL of Cr (VI) -containing simulated wastewater with a concentration of 60mg/L and a pH value of 3, and the sample was magnetically stirred and adsorbed at 25 ℃ for 40min, and then was analyzed, whereby the removal rate was 96.74%.
Example 10
0.05g of the cellulose foam obtained in example 8 was put into 25mL of Cr (VI) -containing simulated wastewater with a concentration of 40mg/L and a pH value of 2, and the sample was magnetically stirred and adsorbed at 25 ℃ for 30min, and then the removal rate was 97.35% by analysis.
Example 11
The cellulose foam 9 pieces prepared in example 8 were cut out, put into Cr (VI) -containing simulated wastewater with a concentration of 0.5mg/L and a pH of 2, 3, 4, 5, 6, 7, 8, 9, 10, respectively, reacted for 30min under magnetic stirring at 25 ℃, the cellulose foam was taken out, washed with deionized water, after surface moisture was blotted, fluorescence quenching was observed under 365nm ultraviolet irradiation, and the results are shown in fig. 2.
As can be seen from FIG. 2, the cellulose foam emits bright blue fluorescence under 365nm ultraviolet light, and the presence of Cr (VI) quenches the fluorescence when the pH is between 3 and 8, so that the cellulose foam can identify Cr (VI) in a wide pH range (3-8).
Example 12
2 pieces of the cellulose foam prepared in example 8 were cut, put into Cr (VI) -containing simulated wastewater with a concentration of 50 and 5mg/L and a pH of 7, and reacted for 2min under magnetic stirring at 25 ℃, the cellulose foam was taken out, washed with deionized water, and after absorbing surface water, fluorescence quenching was observed under 365nm ultraviolet irradiation. Then the solution is put into 5g/L sodium thiosulfate solution for regeneration, and the fluorescence recovery is observed under the irradiation of 365nm ultraviolet light, and the results are shown in figure 3 and figure 4.
As can be seen from FIGS. 3 and 4, the color of the cellulose foam changed to yellow and the blue fluorescence was quenched after exposure to 50 and 5mg/L Cr (VI) -containing solutions; after the cellulose foam absorbing Cr (VI) is regenerated by a sodium thiosulfate solution, the yellow color is faded and the fluorescence energy is recovered, so that the structure of the absorbent is not damaged in the regeneration process.
Example 13
A plurality of cellulose foam pieces prepared in example 8 were cut out, put into simulated wastewater containing Cr (VI) with a concentration of 5mg/L and a pH of 6, magnetically stirred at 25 ℃ for reaction for 10min, and taken out, and the cellulose foam was observed to turn yellow and to be quenched by fluorescence. Then, the mixture was put into sodium thiosulfate solution or sodium hydroxide solution at concentrations of 0.5, 2.5, 5, and 10g/L, and reacted for 10, 30, 60, and 120min, and the fluorescence recovery of the cellulose foam was observed. The experimental result shows that the cellulose foam after adsorbing the Cr (VI) can be regenerated by using 0.5-10g/L sodium thiosulfate solution or sodium hydroxide solution, and the regeneration time is 10-120min.
Example 14
100mL of laboratory tap water was added to 0.5mL of 100mg/L Cr (VI) standard solution, and then a piece of the cellulose foam obtained in example 8 was cut out and placed therein, and reacted at 25 ℃ for 10min with magnetic stirring. Taking out the cellulose foam, observing the cellulose to turn yellow on the surface of the foam by naked eyes, washing the foam by deionized water, sucking dry the surface water, and then quenching the fluorescence of the cellulose foam under the irradiation of an ultraviolet lamp with the wavelength of 365 nm. The fluorescence recovered after elution with 1g/L sodium hydroxide solution.
Example 15
Taking 100mL of campus lake water, adding 0.5mL of 10, 20, 30, 50, 60, 80 and 100mg/L Cr (VI) standard solution, cutting a piece of cellulose foam prepared in example 8, placing the piece of cellulose foam in the piece of cellulose foam, and reacting for 10min at 25 ℃ by magnetic stirring. Taking out the cellulose foam, observing the surface of the cellulose foam to turn yellow by naked eyes, washing with deionized water, sucking dry the surface water, and quenching the fluorescence of the cellulose foam under the irradiation of an ultraviolet lamp with the wavelength of 365 nm. The fluorescence recovered after elution with 1g/L sodium hydroxide solution.
Example 16
Cutting several parts of the cellulose foam obtained in example 8, wherein each part is 0.05g, respectively putting the parts into Cr (VI) -containing water samples with the concentrations of 10, 60 and 100mg/L, controlling the adsorption time, and taking out the parts before the cellulose foam is browned; meanwhile, according to the concentration of Cr (VI) in the water sample and the type of the receiving water body, multistage adsorption is set.
The Cr (VI) concentrations in the effluent after the multi-stage treatment of the cellulose foam with different initial concentrations of Cr (VI) are shown in Table 1.
TABLE 1 results of multistage treatment of PEI modified cellulose foam with different initial concentrations of Cr (VI)
Cr (VI) concentration (mg/L) First-stage treatment of effluent Secondary treatment of effluent Three-stage treatment of effluent Four-stage treatment of effluent
100 24.77 2.77 0.21 0.03
60 5.69 0.95 0.06 0.01
10 2.99 0.13 0.01
Note: 25mL of Cr (VI) solution, 0.05g of adsorbent was used for each treatment.
As can be seen from Table 1, the simulated wastewater containing Cr (VI) with different concentrations can reach the specified value of 0.5mg/L in Integrated wastewater discharge Standard (GB 8978-1996) or 0.05mg/L in sanitary Standard for Drinking Water after the multi-stage treatment of cellulose foam.

Claims (6)

1. The preparation method of the cellulose foam capable of visually identifying and removing chromium is characterized by comprising the following steps of:
adding epichlorohydrin into the cellulose solution, stirring until the color of the solution becomes light, adding a PEI solution, uniformly stirring, crosslinking for 5-60min at 25-60 ℃ to form hydrogel, washing with deionized water, freezing, and freeze-drying to obtain the modified cellulose hydrogel;
wherein the concentration of the cellulose solution is 4wt%; the concentration of the PEI solution is 5wt%; the volume ratio of the cellulose solution to the epichlorohydrin to the PEI solution is 10.5.
2. The method for preparing cellulose foam capable of visually identifying and removing chromium according to claim 1, wherein the crosslinking temperature is 50 ℃ and the crosslinking time is 20min.
3. The method for preparing the cellulose foam capable of visually identifying and removing chromium according to claim 1, wherein the freezing temperature is-18 to-20 ℃, and the freezing time is 8 to 12 hours.
4. The preparation method of the cellulose foam capable of visually identifying and removing chromium according to claim 1, wherein the freeze-drying temperature is-80 to-85 ℃, and the freeze-drying time is 22 to 26 hours.
5. Cellulose foam which is visually identifiable and has been freed of chromium and which is obtainable by a process according to any one of claims 1 to 4.
6. The method for removing chromium using the cellulose foam capable of visually recognizing and removing chromium according to claim 5, comprising the steps of: the visual identification of the cellulose foam to chromium is realized by observing the fluorescence quenching condition of the cellulose foam before and after absorbing the sample under the irradiation of 365nm ultraviolet light; and mixing the cellulose foam and the chromium-containing sample, stirring until the cellulose foam turns brown, taking out, regenerating the taken-out cellulose foam, continuously adsorbing the chromium-containing sample, and repeating the steps to finish the chromium removal process.
CN202010127485.6A 2020-02-28 2020-02-28 Cellulose foam capable of visually identifying and removing chromium, preparation method thereof and chromium removal method Active CN111250062B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202010127485.6A CN111250062B (en) 2020-02-28 2020-02-28 Cellulose foam capable of visually identifying and removing chromium, preparation method thereof and chromium removal method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202010127485.6A CN111250062B (en) 2020-02-28 2020-02-28 Cellulose foam capable of visually identifying and removing chromium, preparation method thereof and chromium removal method

Publications (2)

Publication Number Publication Date
CN111250062A CN111250062A (en) 2020-06-09
CN111250062B true CN111250062B (en) 2022-12-27

Family

ID=70949438

Family Applications (1)

Application Number Title Priority Date Filing Date
CN202010127485.6A Active CN111250062B (en) 2020-02-28 2020-02-28 Cellulose foam capable of visually identifying and removing chromium, preparation method thereof and chromium removal method

Country Status (1)

Country Link
CN (1) CN111250062B (en)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112341832B (en) * 2020-11-25 2022-05-27 河南省第一公路工程有限公司 Freeze-thaw abrasion resistant pavement repair material and production process and application thereof
CN112958047A (en) * 2021-03-11 2021-06-15 武汉纺织大学 Modified magnetic cellulose microsphere heavy metal adsorbent based on waste cotton fabric and preparation method thereof
CN115845810B (en) * 2022-11-23 2024-05-03 浙江农林大学 Preparation method and application of cellulose-based porous material for carbon capture
CN115709055A (en) * 2022-11-28 2023-02-24 东北林业大学 Wood cellulose-based carbon dioxide adsorption and desorption foam and preparation method thereof

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5948829A (en) * 1997-11-25 1999-09-07 Kimberly-Clark Worldwide, Inc. Process for preparing an absorbent foam
CN107837791A (en) * 2017-12-06 2018-03-27 西南交通大学 A kind of PEI modified celluloses membrane adsorbent and preparation method thereof
CN109289805A (en) * 2018-10-12 2019-02-01 南京林业大学 A kind of method nano-cellulose composite aerogel adsorbent preparation and its adsorb heavy metal ion

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5948829A (en) * 1997-11-25 1999-09-07 Kimberly-Clark Worldwide, Inc. Process for preparing an absorbent foam
CN107837791A (en) * 2017-12-06 2018-03-27 西南交通大学 A kind of PEI modified celluloses membrane adsorbent and preparation method thereof
CN109289805A (en) * 2018-10-12 2019-02-01 南京林业大学 A kind of method nano-cellulose composite aerogel adsorbent preparation and its adsorb heavy metal ion

Non-Patent Citations (3)

* Cited by examiner, † Cited by third party
Title
A cellulose-based adsorbent with pendant groups of quaternary ammonium and amino for enhanced capture of aqueous Cr(VI);Xingtang Liang et al.;《International Journal of Biological Macromolecules》;20200121;第148卷;第802–810页 *
Xingtang Liang et al..A cellulose-based adsorbent with pendant groups of quaternary ammonium and amino for enhanced capture of aqueous Cr(VI).《International Journal of Biological Macromolecules》.2020,第148卷第802–810页. *
甲醛功能化聚乙烯亚胺-罗丹明B酰肼比率及可视化荧光测定Cr(Ⅵ);杨传孝等;《高等学校化学学报》;20160510(第05期);第852-859页 *

Also Published As

Publication number Publication date
CN111250062A (en) 2020-06-09

Similar Documents

Publication Publication Date Title
CN111250062B (en) Cellulose foam capable of visually identifying and removing chromium, preparation method thereof and chromium removal method
CN104289185A (en) Granular filtering material for adsorbing and removing heavy metals in water and preparation method thereof
CN110898802B (en) Sludge-based biochar and preparation method and application thereof, acetic acid modified sludge-based biochar and preparation method and application thereof
CN104525129A (en) Preparation method of modified activated carbon used for heavy metal wastewater treatment
CN104190360A (en) Oxidation-load iron modified active carbon water treatment adsorbent and preparation method thereof
CN105771889A (en) Preparation method and application of modified activated carbon
CN104785202A (en) Preparation method for modified attapulgite adsorbing agent
Magoling et al. Optimization and response surface modelling of activated carbon production from Mahogany fruit husk for removal of chromium (VI) from aqueous solution
CN108772038B (en) Adsorbent for removing lead ions in water and preparation method and application thereof
CN105170107B (en) A kind of preparation method of green heavy metal chelating agent
CN113600133A (en) Phosphorus removal adsorbent and preparation method and application thereof
CN111977873B (en) Method for using photoactivated sepiolite Si-OH for adsorption and photodegradation of water-soluble organic pollutants
CN109759024A (en) A kind of preparation method of the light sorbent based on plant cellulose
CN113351173A (en) Humic acid-containing magnetic adsorption material and preparation method and application thereof
CN113042018A (en) Preparation method and application of calcium-rich biochar
CN114990046B (en) Biochar-based three-dimensional composite material and method for repairing high-concentration chromium-polluted soil by using same
CN112777817B (en) Method for treating high-salinity wastewater containing aniline compounds
CN107282023A (en) A kind of chemical waste fluid processing nano adsorber and preparation method thereof
CN103212376A (en) Preparation method of nanometer CuS grafting modified bamboo powder capable of adsorbing heavy metal ions
CN114146681A (en) Composite material for treating nitrogen-containing sewage and preparation method and application thereof
CN113213579A (en) Application of photocatalytic biochar composite material in catalytic degradation of printing and dyeing wastewater
CN112316972A (en) Preparation method and application of mesoporous-microporous ZSM-5-based ozone catalyst
Bishnoi et al. Adsorption of Cr (VI) from aqueous and electroplating wastewater
CN104925890A (en) Method for treating highly concentrated ammonia nitrogen in petroleum refining wastewater
CN115532232B (en) Asphaltene-based adsorbent and preparation method and application thereof

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant