CN108273472A - A kind of preparation method of efficient selective absorption selenite radical adsorbent - Google Patents

A kind of preparation method of efficient selective absorption selenite radical adsorbent Download PDF

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CN108273472A
CN108273472A CN201810044075.8A CN201810044075A CN108273472A CN 108273472 A CN108273472 A CN 108273472A CN 201810044075 A CN201810044075 A CN 201810044075A CN 108273472 A CN108273472 A CN 108273472A
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adsorbent
mof
preparation
selenite radical
solution
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CN108273472B (en
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杨东江
邹译慧
欧阳欢
赵小亮
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Qingdao University
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Qingdao University
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/22Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising organic material
    • B01J20/223Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising organic material containing metals, e.g. organo-metallic compounds, coordination complexes
    • B01J20/226Coordination polymers, e.g. metal-organic frameworks [MOF], zeolitic imidazolate frameworks [ZIF]
    • 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
    • C02F2101/106Selenium compounds

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

Abstract

The invention discloses the preparation methods that a kind of efficient selective adsorbs selenite radical adsorbent, belong to sewage treatment field.The adsorbent is using five water bismuth nitrates and trimesic acid as raw material, with abundant active adsorption sites, special organic metal framework object (MOFs) micropore canals structure, there is higher adsorbance when this material is used for selenite radical adsorbent (saturated extent of adsorption can reach 255.3mg/g).Traditional selenite radical adsorbent is depositing many defects, and selectivity is relatively low, and saturated extent of adsorption is smaller, the relatively narrow pH scope of applications, and principle is low in the presence of the competing ions of larger concentration.Therefore, one kind is developed efficiently, with ph stability, the adsorbent of highly selective selenite radical ion has great importance.In the present invention, the preparation of bismuthino MOF (BI MOF) adsorbent is very simple and convenient, and its special MOF pore passage structure having can further ensure its efficient absorption property, is very promising selenite radical sorbent material.

Description

A kind of preparation method of efficient selective absorption selenite radical adsorbent
Technical field
The invention belongs to sewage treatment fields, and in particular to a kind of preparation of efficient selective absorption selenite radical adsorbent Method.
Background technology
Selenium in sewage mainly in the form of selenite radical ion and selenic acid radical ion existing for, but due to relatively low The toxicity of the selenite radical ion of valence state is better than selenic acid radical ion, therefore the selenite radical ion in treated sewage has Higher priority.And the mode for commonly using processing selenite radical ion at present has:Sedimentation, filtering, ion exchange, UF membrane and Absorption.However, for other several processing means, adsorption treatment mode seems more efficiently, economic and practical and suction Attached dose is more prone to synthesize.So absorption is the optimal selection of selenite radical ion in current treated sewage.It is common to inhale Attached dose has several classes:(ferrimanganic bimetallic aoxidizes for metal oxide (aluminium oxide, iron oxide, calcium oxide), bimetallic oxide Object) and double-metal hydroxide (magnalium double-metal hydroxide).However, because there is apparent lack in above several adsorbents Sunken and insufficient (low-down saturated extent of adsorption, slower adsorption equilibrium, the unstability under inclined strong acid and strong base environment, and Low-down selectivity).Therefore, it develops one kind efficiently, there is extraordinary stability, highly selective selenous acid Root adsorbent is very urgent for the selenite radical in treated sewage.Based on the bismuth oxide of business for selenous acid Root has certain absorption property, however because its specific surface area is smaller, pore passage structure is undeveloped, is unfavorable for selenite radical and its Active adsorption sites adequately contact.Therefore it is solution to develop a kind of novel bismuthino adsorbent for having more bigger serface The certainly key of this problem.And this special materials of Bi-MOF meet above all kinds of requirements, and it is real by adsorbing Demonstrate its remarkable absorption property.Therefore, one kind that this kind of material will be irreplaceable in sewage treatment field is novel Material.
Invention content
The present invention is prepared for can be used as the tool of selenite radical adsorbent using the bismuth salt of abundance and ligand as raw material There is the sorbent material Bi-MOF of special pore passage structure.
Preparation process of the present invention is simple, does not need expensive device, and products obtained therefrom quality high-performance is good, and stability is good, selection Property by force future selenite radical and the application of other Anion-adsorptions in there is bright foreground.
A kind of preparation method of efficient selective absorption selenite radical adsorbent, manufacturing process include the following steps:
1) Bi that configuration 30mL mass concentrations are 2.5mg/mL3+Methanol solution, addition 30mL mass concentrations are 12.5 mg/ The trimesic acid methanol solution of mL, Bi is obtained after stirring3+Trimesic acid mixed solution;
2) mixed solution is heated to reaction in constant temperature oven, by 100 DEG C -180 DEG C, the reaction time is at 12h-48h Reason, obtains product A;
3) by after above-mentioned product A absolute methanol diafiltrations, 60 DEG C are dried to obtain final product Bi-MOF;
4) above-mentioned adsorbent B i-MOF is used as in selenite radical adsorption experiment, and is surveyed with NITRATE BY FLAME ATOMIC spectrophotometry Try its absorption property.
The raw material that the present invention uses is mainly bismuth salt, and amount of storage is big in the earth's crust, and synthesizes and amplify economic and practical, production Amount is big.
Adsorbent with special MOF pore passage structures prepared by the method for the present invention is with highest selenite radical so far Absorption property has very fast adsorption equilibrium characteristic, and absorption property is highly stable under pH 4-11 environment, Yi Ji Also has extraordinary selectivity in the environment of counter anion under very big concentration.
Description of the drawings
Fig. 1 is the SEM figures for the Bi-MOF with special MOF pore passage structures that specific embodiment 1 obtains.
Fig. 2 is the XRD diagram for the Bi-MOF with special MOF pore passage structures that specific embodiment 1 obtains.
Fig. 3 is that specific embodiment 1 obtains the stability diagram in pH 4-11 with the Bi-MOF of special MOF pore passage structures, It is not influenced the absorption property of selenite radical by pH value variation substantially, also demonstrates its outstanding absorption stability.
Fig. 4 is that specific embodiment 1 obtains the selectivity with the Bi-MOF of special MOF pore passage structures, is in concentration ratio In the presence of 2000 competing ions, there is extraordinary selectivity.
Fig. 5 is that specific embodiment 1 obtains the isothermal adsorption concentration curve with the Bi-MOF of special MOF pore passage structures, Bi-MOF A more satisfactory maximum saturation adsorbance can be reached.
Specific implementation mode
In order to make the object, technical scheme and advantages of the embodiment of the invention clearer, below in conjunction with the embodiment of the present invention Attached drawing, the technical solution of the embodiment of the present invention is clearly and completely described.Obviously, described embodiment is this hair Bright a part of the embodiment, instead of all the embodiments.Based on described the embodiment of the present invention, the common skill in this field The every other embodiment that art personnel are obtained under the premise of without creative work, shall fall within the protection scope of the present invention.
Below in conjunction with specific embodiment, the present invention is described in detail.
Embodiment 1
1) Bi that configuration 30mL mass concentrations are 2.5mg/mL3+Methanol solution, addition 30mL mass concentrations are 12.5 mg/ The trimesic acid methanol solution of mL, Bi is obtained after stirring3+Trimesic acid mixed solution;
2) mixed solution is heated to reaction in constant temperature oven, by 120 DEG C, the reaction time is to handle for 24 hours, obtains product A;
3) by after above-mentioned product A absolute methanol diafiltrations, 60 DEG C are dried to obtain final product Bi-MOF;
4) above-mentioned adsorbent B i-MOF is used as in selenite radical adsorption experiment, and is surveyed with NITRATE BY FLAME ATOMIC spectrophotometry Try its absorption property.
Embodiment 2
1) Bi that configuration 30mL mass concentrations are 2.5mg/mL3+Methanol solution, addition 30mL mass concentrations are 12.5 mg/ The trimesic acid methanol solution of mL, Bi is obtained after stirring3+Trimesic acid mixed solution;
2) mixed solution is heated to reaction in constant temperature oven, by 150 DEG C, the reaction time is to handle for 24 hours, obtains product A;
3) by after above-mentioned product A absolute methanol diafiltrations, 60 DEG C are dried to obtain final product Bi-MOF;
4) above-mentioned adsorbent B i-MOF is used as in selenite radical adsorption experiment, and is surveyed with NITRATE BY FLAME ATOMIC spectrophotometry Try its absorption property.
Embodiment 3
1) Bi that configuration 30mL mass concentrations are 2.5mg/mL3+Methanol solution, addition 30mL mass concentrations are 12.5 mg/ The trimesic acid methanol solution of mL, Bi is obtained after stirring3+Trimesic acid mixed solution;
2) mixed solution is heated to reaction in constant temperature oven, by 100,110,130,140,160,170,180 DEG C, Reaction time be 12h, for 24 hours, 36h, 48h processing, obtain product A;
3) by after above-mentioned product A absolute methanol diafiltrations, 60 DEG C are dried to obtain final product Bi-MOF;
4) above-mentioned adsorbent B i-MOF is used as in selenite radical adsorption experiment, and is surveyed with NITRATE BY FLAME ATOMIC spectrophotometry Try its absorption property.
It should be understood that although with reference to its illustrative embodiment, particularly shown and description is carried out to the present invention, It should be understood by those skilled in the art that without departing substantially from by it is as defined in the claims the present invention spirit and Under conditions of range, the variation of various forms and details can be carried out wherein, can carry out arbitrary group of various embodiments It closes.

Claims (5)

1. a kind of preparation method of efficient selective absorption selenite radical adsorbent, it is characterised in that the method includes following steps Suddenly:
1) a certain amount of bismuth salt is dissolved into a certain amount of absolute methanol, Bi is obtained after stirring3+Methanol solution;
2) a certain amount of ligand is dissolved into a certain amount of absolute methanol, ligand methanol solution is obtained after stirring;
3) above two solution is mixed, obtains mixed solution, handle to obtain reaction product A by hydro-thermal reaction;
4) by above-mentioned reaction product A absolute methanol diafiltrations repeatedly, it is dried to obtain product B, product B is this novel sub- selenium Acid group adsorbent B i-MOF;
5) above-mentioned adsorbent B i-MOF is used as in selenite radical adsorption experiment, and it is tested with NITRATE BY FLAME ATOMIC spectrophotometry Absorption property.
2. preparation method according to claim 1, which is characterized in that the bismuth salt described in step 1) is five water nitric acid Bismuth, solution temperature are room temperature, and the mass concentration of addition is 2.5mg/mL.
3. preparation method according to claim 1, which is characterized in that the equal benzene three that the ligand described in step 2) uses Formic acid, solution temperature are room temperature, and the mass concentration of addition is 12.5mg/mL.Carbonization technique is calcined 1 hour for 600-1000 DEG C, Calcination atmosphere is argon gas.
4. preparation method according to claim 1, which is characterized in that the hydrothermal temperature range described in step 3) It is 100 DEG C -180 DEG C, reaction time 12h-48h.
5. preparation method according to claim 1, which is characterized in that described in step 4), in vacuum drying oven, 60 DEG C Desciccate A obtains Bi-MOF.
CN201810044075.8A 2018-01-10 2018-01-10 Preparation method of adsorbent capable of efficiently and selectively adsorbing selenious acid roots Active CN108273472B (en)

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Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109888206A (en) * 2019-01-23 2019-06-14 江苏理工学院 A kind of lithium ion battery negative material Bi/Bi2O3/ C and its preparation and application
CN111729662A (en) * 2020-06-23 2020-10-02 东莞理工学院 Preparation method and application of MXene membrane material for in-situ growth of Bi-MOF
CN113333002A (en) * 2021-06-12 2021-09-03 景德镇陶瓷大学 Preparation method of CdS quantum dot-loaded bismuth oxide composite visible light catalytic material and product prepared by same
CN113351226A (en) * 2021-06-12 2021-09-07 景德镇陶瓷大学 Petal-shaped loaded ZnIn2S4Preparation method of bismuth oxide composite visible light catalytic material and product prepared by same
CN114835233A (en) * 2022-06-01 2022-08-02 闽江学院 Method for rapidly removing chloride ions in wastewater by using bismuth-based metal organic framework material
CN114904498A (en) * 2022-05-30 2022-08-16 天津城建大学 Preparation method and application of adsorption material PEHA-CAU-17

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CN106750356A (en) * 2017-01-10 2017-05-31 北京大学 A kind of method that metal-organic framework materials of utilization UiO 66 purify selenium-containing wastewater
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CN105939774A (en) * 2013-12-19 2016-09-14 碳捕获有限公司 Methods for the capture and release of acid gases
US20170326536A1 (en) * 2016-05-13 2017-11-16 King Fahd University Of Petroleum And Minerals Metal organic frameworks as catalysts and hydrocarbon oxidation methods thereof
CN106750356A (en) * 2017-01-10 2017-05-31 北京大学 A kind of method that metal-organic framework materials of utilization UiO 66 purify selenium-containing wastewater

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Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109888206A (en) * 2019-01-23 2019-06-14 江苏理工学院 A kind of lithium ion battery negative material Bi/Bi2O3/ C and its preparation and application
CN109888206B (en) * 2019-01-23 2021-09-28 江苏理工学院 Lithium ion battery cathode material Bi/Bi2O3C, preparation and application thereof
CN111729662A (en) * 2020-06-23 2020-10-02 东莞理工学院 Preparation method and application of MXene membrane material for in-situ growth of Bi-MOF
CN113333002A (en) * 2021-06-12 2021-09-03 景德镇陶瓷大学 Preparation method of CdS quantum dot-loaded bismuth oxide composite visible light catalytic material and product prepared by same
CN113351226A (en) * 2021-06-12 2021-09-07 景德镇陶瓷大学 Petal-shaped loaded ZnIn2S4Preparation method of bismuth oxide composite visible light catalytic material and product prepared by same
CN113333002B (en) * 2021-06-12 2023-03-03 景德镇陶瓷大学 Preparation method of CdS quantum dot-loaded bismuth oxide composite visible light catalytic material and product prepared by same
CN113351226B (en) * 2021-06-12 2023-04-18 景德镇陶瓷大学 Petal-shaped loaded ZnIn 2 S 4 Preparation method of bismuth oxide composite visible light catalytic material and product prepared by same
CN114904498A (en) * 2022-05-30 2022-08-16 天津城建大学 Preparation method and application of adsorption material PEHA-CAU-17
CN114835233A (en) * 2022-06-01 2022-08-02 闽江学院 Method for rapidly removing chloride ions in wastewater by using bismuth-based metal organic framework material
CN114835233B (en) * 2022-06-01 2023-09-12 闽江学院 Method for rapidly removing chloride ions in wastewater by bismuth-based metal organic framework material

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