CN111252844B - Application of eggshell particles in bismuth-containing sewage treatment and use method thereof - Google Patents

Application of eggshell particles in bismuth-containing sewage treatment and use method thereof Download PDF

Info

Publication number
CN111252844B
CN111252844B CN202010098115.4A CN202010098115A CN111252844B CN 111252844 B CN111252844 B CN 111252844B CN 202010098115 A CN202010098115 A CN 202010098115A CN 111252844 B CN111252844 B CN 111252844B
Authority
CN
China
Prior art keywords
eggshell
bismuth
particles
adsorption
eggshells
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
CN202010098115.4A
Other languages
Chinese (zh)
Other versions
CN111252844A (en
Inventor
杨金燕
阿迪尔·阿巴斯·卡里姆
甘淳丹
廖瑜亮
于雅琪
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.)
Sichuan University
Original Assignee
Sichuan 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 Sichuan University filed Critical Sichuan University
Priority to CN202010098115.4A priority Critical patent/CN111252844B/en
Publication of CN111252844A publication Critical patent/CN111252844A/en
Application granted granted Critical
Publication of CN111252844B publication Critical patent/CN111252844B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Classifications

    • 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
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/22Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising organic material
    • B01J20/223Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising organic material containing metals, e.g. organo-metallic compounds, coordination complexes
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/28Solid 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
    • 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
    • B01J2220/4875Sorbents characterised by the starting material used for their preparation the starting material being a waste, residue or of undefined composition
    • B01J2220/4881Residues from shells, e.g. eggshells, mollusk shells
    • 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

Landscapes

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

Abstract

The invention provides an application of eggshell particles in bismuth-containing sewage treatment and a using method thereof, wherein the eggshell particles are prepared by the following method: washing the eggshell with deionized water for 2-4 times, drying, air-drying at 30-50 ℃ for 9-11 h, and crushing to 0.4-0.5 mu m to obtain the eggshell particles. According to the invention, the eggshell particles are used as an adsorbent in the treatment of bismuth-containing sewage, and the alcoholic hydroxyl, methyl and carbonyl telescopic band functional groups on the eggshell surface interact with bismuth, so that the eggshell has the capacity of adsorbing bismuth, the bismuth content in the sewage can be effectively reduced, meanwhile, the eggshell has wide sources and low cost, and the application develops the new application of the eggshell and utilizes the eggshell waste to create new economic value.

Description

Application of eggshell particles in bismuth-containing sewage treatment and use method thereof
Technical Field
The invention belongs to the technical field of sewage treatment, and particularly relates to application of eggshell particles in bismuth-containing sewage treatment and a using method thereof.
Background
Contamination with many heavy metals is of concern, such as arsenic, bismuth, cadmium, chromium, cobalt, lead, manganese, mercury, nickel, platinum, silver, vanadium, and zinc. Bismuth is a rare and important component which is widely used in several fields, for example in the metallurgical and cosmetic industries as an additive substance for creams and hair dyes. In addition, it has well-defined properties in drug administration and can be used as an antibacterial agent against immunodeficiency infection in humans. However, bismuth has many adverse effects on the human body, such as kidney damage, halitosis, metallic taste and gingivitis, nausea, loss of appetite, weight loss, malaise, proteinuria, diarrhea, skin reactions, stomatitis, headache, fever, insomnia, depression, rheumatalgia, and high dose lethality. According to the world health organization, the allowable limit value of the concentration of bismuth in the natural water is 0.028 mg/L. The bismuth is released into the water body, so that the water body cannot be normally used. Therefore, it is necessary to clean and prevent bismuth before it enters the natural environment.
There are several conventional physical and chemical wastewater treatment techniques for removing contaminants from contaminated water. Of all the techniques, adsorption is the most popular technique because of its convenience, ease of handling and versatility. Natural or plant waste adsorbents are widely used in water treatment to replace the current expensive method of removing heavy metals from contaminated water. The activated carbon, the activated alumina and the ion exchange resin have strong removal capability to toxic heavy metals. However, these materials have certain drawbacks, and there is a need to find and develop a low cost, widely available, and large quantity of waste materials as a substitute. The eggshells are produced by several tons every day, most of the eggshells are sent to a refuse landfill, the eggshells cannot be effectively utilized, and the management cost is high. It is economically feasible to create new value using eggshell waste.
Disclosure of Invention
Aiming at the problems in the prior art, the invention provides an application and a use method of eggshell particles in bismuth-containing sewage treatment, the eggshell particles are used as an adsorbent in the bismuth-containing sewage treatment, and alcoholic hydroxyl, methyl and carbonyl telescopic band functional groups on the surface of an eggshell interact with bismuth, so that the eggshell has the capacity of adsorbing bismuth, the bismuth content in the sewage can be effectively reduced, meanwhile, the eggshell has wide sources and low cost, and the application develops new application of the eggshell and creates new economic value by utilizing eggshell waste.
In order to achieve the purpose, the technical scheme adopted by the invention for solving the technical problems is as follows: provides an application of eggshell particles in the treatment of bismuth-containing sewage.
Furthermore, the adding proportion of the eggshell particles in the bismuth-containing sewage is 3.125-50 g/L.
Furthermore, the adding proportion of the eggshell particles in the bismuth-containing sewage is 6.25 g/L.
Further, the eggshell particles are prepared by the following method: washing the eggshell with deionized water for 2-4 times, drying, air-drying at 30-50 ℃ for 9-11 h, and crushing to 0.4-0.5 mu m to obtain the eggshell particles.
Further, the eggshell is an eggshell of poultry or birds.
Furthermore, the eggshell is a chicken eggshell.
An adsorbent for bismuth-containing sewage comprises the eggshell particles.
The application method of the eggshell particles in the bismuth-containing sewage comprises the following steps: adding the eggshell particles into bismuth-containing sewage with the temperature of 40-50 ℃ and the pH value of 8 +/-0.5, and then stirring for 30-60 min to complete the treatment of the bismuth-containing sewage.
Further, the stirring speed is 140 to 160 rpm.
In summary, the invention has the following advantages:
1. according to the invention, the eggshell particles are used as an adsorbent in the treatment of bismuth-containing sewage, and a specific using method is provided, and the alcoholic hydroxyl, methyl and carbonyl telescopic band functional groups on the eggshell surface interact with bismuth, so that the eggshell has the capacity of adsorbing bismuth, the bismuth content in the sewage can be effectively reduced, meanwhile, the eggshell has wide sources and low development cost, and the application develops a new application of the eggshell, creates a new economic value by using eggshell waste, and also reduces the management cost.
2. The adsorption effect of the eggshell on bismuth is related to the reaction time, the addition amount of the eggshell, the temperature of sewage and the pH value. The adsorption amount of the eggshell to bismuth is increased along with the prolonging of the reaction time, the balance is achieved at 45min, and the removal rate reaches 94.10%. The initial rapid removal is due to the fact that a large number of effective binding sites exist on the surface of the eggshell, bismuth ions are easily adsorbed, and therefore the bismuth ions are rapidly removed. The large surface area of the adsorbent means that the number of available adsorption sites is sufficient in the initial stage, and as the reaction proceeds, these adsorption sites are availableSaturation progresses, and thus the adsorption rate decreases. The pH of the solution affects the functional groups on the egg shell that bind to the metal ions and the competition of the metal ions for the adsorbent surface active sites. The removal rate of the eggshell to the bismuth depends on the pH value, and when the pH value is 8, OH is added-React with bismuth ions to form a precipitate of double hydroxide. At a pH of less than 6, H+Competition with bismuth ions inhibits bismuth ions from binding to active sites on the adsorbent surface. The maximum removal rate obtained at pH 8 was 93.70%.
3. The removal rate of bismuth increases as the amount of eggshell gradually increases from 3.125g/L to 50 g/L. The removal rate is related to the amount of eggshell, since more adsorption sites are available at higher amounts; this trend is mainly due to the increase in the surface area of the eggshells and the increase in the adsorption activity. At a dose of 6.25g/L, the maximum removal rate of bismuth is 92.40%; further increasing the adsorbent amount (6.25-50 g/mL) has no significant effect on the adsorption rate of bismuth. The removal rate of bismuth ions is increased in the process that the temperature is increased between 40 and 50 ℃; the removal rate at 40 ℃ is 90.45 percent; the decrease in removal rate at 20 ℃ is due to the low temperature, since the molecules tend to move more and more from the adsorbent surface to the liquid phase, the boundary layer thickness tends to decrease, and hence the adsorption capacity decreases. One reason for the adsorption is that additional reactions initiated by the thermal cracking process form alkyne or alkene functional groups on the surface of the egg shell.
4. The eggshell has large specific surface area and high porous structure, thus having stronger adsorption capacity. Similarly, many tiny particles appear in the cavities on the surface of the eggshell, indicating that the eggshell may adsorb bismuth from the solution. In addition, the negative charge binding sites on the surface of the eggshell provide the eggshell with the ability to adsorb bismuth ions in aqueous solutions. From SEM images of the eggshells before and after adsorption, bismuth ions appear on the surfaces of the eggshells after adsorption. The image shows that there is a combination of small and large particles on the surface of the eggshell, similar to the uneven rough porous surface of the bronchiolar structure. EDS peaks show that bismuth does not exist in eggshells before adsorption, and the content of the bismuth in the eggshells after adsorption reaches 3.07%.
5. The actual interaction between the eggshell and bismuth exists, and the adsorption of the adsorbent material to the metal is realized byReactive groups and chemical bonds present on the material. From the FTIR spectrum, from 3435 to 3403cm-1The movement of (2) is stretching of-OH groups, and the difference between before and after adsorption is not large. Characteristic peaks were found between the eggshell surfaces, but at 2140.32cm-1After adsorption, a-C.ident.C bond appears. This bond refers to the alkyne or alkene bond formed by the reaction that occurs during thermal cracking. Adsorbing bismuth on the surface of eggshell, and then adsorbing bismuth on 3435, 2978, 2876, 2518, 1418, 774, 515 and 425cm-1The peaks at (A) are shifted to 3403, 2936, 2515, 1409, 791, 588 and 468cm respectively-1Here, it is illustrated that carboxyl groups, phenolic hydroxyl groups, aromatic rings, amino groups and aliphatic hydrocarbons are involved in the adsorption process.
Drawings
FIG. 1 shows the removal rate of bismuth ions by eggshells at different reaction times;
FIG. 2 shows the removal rate of bismuth by reacting eggshells at different pH values for 45 min;
FIG. 3 shows the removal rate of bismuth in eggshells at different pH values within 0-45 min;
FIG. 4 shows the bismuth removal rate of 45min reaction under different eggshell usage;
FIG. 5 shows the bismuth removal rate for different eggshell dosages within 0-45 min;
FIG. 6 shows the removal rate of bismuth ions in eggshells at different temperatures for 45 min;
FIG. 7 shows the removal rate of bismuth ions by eggshells at different reaction temperatures within 0-45 min;
fig. 8 is an SEM image of the eggshells before adsorption (1);
fig. 9 is an SEM image of the eggshells before adsorption (2);
FIG. 10 is an EDS spectrum of eggshells prior to adsorption;
fig. 11 is an SEM image of the eggshells after adsorption (1);
fig. 12 is an SEM image of the eggshells after adsorption (2);
fig. 13 is an SEM image of the eggshells after adsorption (3);
fig. 14 is an SEM image of the eggshells after adsorption (4);
figure 15 is an EDS spectrum of the eggshells after adsorption;
FIG. 16 is an FTIR spectrum of functional groups in eggshells before and after adsorption;
fig. 17 is an FTIR spectrum of functional group interactions in eggshells before and after adsorption.
Detailed Description
Example 1
The preparation method of the eggshell particles comprises the following steps: washing eggshell with deionized water for 3 times, drying, air drying at 40 deg.C for 10 hr, and pulverizing to 0.45 μm to obtain eggshell granule.
Example 2
Bismuth nitrite is adopted to prepare bismuth ion standard stock solution. A standard stock solution of bismuth ions was prepared by adding 1mL of nitric acid (65 vt%) to 1.4g of bismuth, followed by dilution to 1000mg/L with deionized water. The pH of the solution during the experiment was adjusted with 0.1M hydrochloric acid and 0.1M sodium hydroxide. The chemical reagents used in this study were purchased from Shanghai Aladdin Biotechnology Ltd.
0.25g of the eggshell particles obtained in example 1 was weighed and added to 40mL of bismuth ion standard stock solution (50mg/L) at 40 ℃ and pH 8, and then stirred at 150rpm while measuring the bismuth concentration in the solution at different reaction times, and the removal rate was calculated, the results of which are shown in FIG. 1.
As can be seen from FIG. 1, the adsorption amount of bismuth by the eggshell increases with the increase of the reaction time, and reaches equilibrium at 45min, and the removal rate reaches 94.10%. The initial rapid removal is due to the fact that a large number of effective binding sites exist on the surface of the eggshell, bismuth ions are easily adsorbed, and therefore the bismuth ions are rapidly removed. Since the surface area of the adsorbent is large, meaning that the number of available adsorption sites is sufficient in the initial stage, these adsorption sites gradually saturate as the reaction proceeds, and thus the adsorption rate decreases.
Example 3
0.25g of the eggshell particles obtained in example 1 was weighed, added to 40mL of bismuth ion standard stock solutions (50mg/L) having pH values of 2, 4, 6, 8, 10 and 12 at 40 ℃, and then stirred at 150rpm for 45min while measuring the bismuth concentration in the solution and calculating the removal rate, the results of which are shown in fig. 2 to 3.
As shown in FIGS. 2 to 3, the pH of the solution affects the functional groups on the eggshell that bind to the metal ions and the goldBelongs to the competition of ions on the surface active sites of the adsorbent. The removal rate of the eggshell to the bismuth depends on the pH value, and when the pH value is 8, OH is added-React with bismuth ions to form a precipitate of double hydroxide. At a pH of less than 6, H+Competition with bismuth ions inhibits bismuth ions from binding to active sites on the adsorbent surface. The maximum removal rate obtained at pH 8 was 93.70%.
Example 4
0.125g, 0.25g, 0.5g, 1g and 2g of the eggshell particles obtained in example 1 were weighed, respectively, added to 40mL of a bismuth ion standard stock solution (50mg/L) having a pH of 8 at 40 ℃, and then stirred at 150rpm for 45min, while the bismuth concentration in the solution was measured, and the removal rate was calculated, the results of which are shown in FIGS. 4 to 5.
As can be seen from FIGS. 4-5, the removal rate of bismuth increased as the amount of eggshell was gradually increased from 3.125g/L to 50 g/L. The removal rate is related to the amount of eggshell, since more adsorption sites are available at higher amounts; this trend is mainly due to the increase in the surface area of the eggshells and the increase in the adsorption activity. At a dose of 6.25g/L, the maximum removal rate of bismuth is 92.40%; further increasing the adsorbent amount (6.25-50 g/mL) has no significant effect on the adsorption rate of bismuth.
Example 5
0.25g of eggshell particles obtained in example 1 was weighed, added to 40mL of bismuth ion standard stock solution (50mg/L) having pH 8 at different temperatures of 20 ℃, 30 ℃, 40 ℃ and 50 ℃, and then stirred at 150rpm for 45min, while the bismuth concentration in the solution was measured, and the removal rate was calculated, the results of which are shown in fig. 6 to 7.
As can be seen from FIGS. 6 to 7, the removal rate of bismuth ions increases in the process of increasing the temperature between 40 ℃ and 50 ℃; the removal rate at 40 ℃ is 90.45 percent; the decrease in removal rate at 20 ℃ is due to the low temperature, since the molecules tend to move more and more from the adsorbent surface to the liquid phase, the boundary layer thickness tends to decrease, and hence the adsorption capacity decreases. One reason for the adsorption is that additional reactions initiated by the thermal cracking process form alkyne or alkene functional groups on the surface of the egg shell.
Example 6
SEM images and EDS spectra of the original eggshell before adsorption in example 1 and the eggshell after adsorption in example 2 at 45min are respectively obtained, wherein the SEM images of the original eggshell are shown in figures 8-9, the EDS spectra are shown in figure 10, the SEM images of the eggshell after adsorption are shown in figures 11-14, and the EDS spectra are shown in figure 15; and table 1 was prepared.
TABLE 1 EDS Spectrum of Eggshells
Figure BDA0002385905280000071
From the above, the eggshell has a large specific surface area and a highly porous structure, and thus has a strong adsorption capacity. Similarly, many tiny particles appear in the cavities on the surface of the eggshell, indicating that the eggshell may adsorb bismuth from the solution. In addition, the negative charge binding sites on the surface of the eggshell provide the eggshell with the ability to adsorb bismuth ions in aqueous solutions. From SEM images of the eggshells before adsorption (figures 8-9) and after adsorption (figures 11-14), bismuth ions appear on the surfaces of the eggshells after adsorption. The image shows that there is a combination of small and large particles on the surface of the eggshell, similar to the uneven rough porous surface of the bronchiolar structure. EDS peaks show that bismuth does not exist in eggshells before adsorption, and the content of the bismuth in the eggshells after adsorption reaches 3.07%. In fact, ground eggshell consists of 98.00% of calcium inorganic compounds (calcium carbonate, small amounts of magnesium carbonate, phosphoric acid) and 2% of other organic substances (proteins). These compounds interact with bismuth in the egg shell, forming the EDS spectrum peak.
From the SEM and EDS results, it can be seen that there is a real interaction between the eggshell and bismuth. The adsorption of the adsorbent material to the metal is due to active groups and chemical bonds existing on the material, and the infrared spectrum of the adsorbent material is shown in FIGS. 16-17. From 3435 to 3403cm-1The movement of (2) is stretching of-OH groups, and the difference between before and after adsorption is not large. Characteristic peaks were found between the eggshell surfaces, but at 2140.32cm-1After adsorption, a-C.ident.C bond appears. This bond refers to the alkyne or alkene bond formed by the reaction that occurs during thermal cracking. Adsorbing bismuth on the surface of eggshell, and then adsorbing bismuth on 3435, 2978, 2876, 2518, 1418, 774, 515 and 425cm-1The peak at the position is respectively shifted to 3403, 2936,2515. 1409, 791, 588 and 468cm-1Here, it is illustrated that carboxyl groups, phenolic hydroxyl groups, aromatic rings, amino groups and aliphatic hydrocarbons are involved in the adsorption process.
While the present invention has been described in detail with reference to the illustrated embodiments, it should not be construed as limited to the scope of the present patent. Various modifications and changes may be made by those skilled in the art without inventive step within the scope of the appended claims.

Claims (5)

1. The use method of the eggshell particles in the bismuth-containing sewage is characterized by comprising the following steps: adding the eggshell particles into bismuth-containing sewage with the temperature of 40-50 ℃ and the pH value of 8 +/-0.5, and then stirring for 30-60 min at the stirring speed of 140-160 rpm to finish the treatment of the bismuth-containing sewage;
the eggshell particles are prepared by the following method: washing the eggshell with deionized water for 2-4 times, drying, air-drying at 30-50 ℃ for 9-11 h, and crushing to 0.4-0.5 mu m to obtain the eggshell particles.
2. The method for using the eggshell particles in bismuth-containing wastewater as claimed in claim 1, wherein the proportion of the eggshell particles added in bismuth-containing wastewater is 3.125-50 g/L.
3. The method of using eggshell particles as recited in claim 1, wherein said eggshell particles are added to said bismuth-containing wastewater at a ratio of 6.25 g/L.
4. Method for using eggshell particles as in bismuth-containing wastewater according to claim 1, wherein said eggshells are avian or avian eggshells.
5. The method of using eggshell particles as recited in claim 1, wherein said eggshells are eggshells.
CN202010098115.4A 2020-02-18 2020-02-18 Application of eggshell particles in bismuth-containing sewage treatment and use method thereof Active CN111252844B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202010098115.4A CN111252844B (en) 2020-02-18 2020-02-18 Application of eggshell particles in bismuth-containing sewage treatment and use method thereof

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202010098115.4A CN111252844B (en) 2020-02-18 2020-02-18 Application of eggshell particles in bismuth-containing sewage treatment and use method thereof

Publications (2)

Publication Number Publication Date
CN111252844A CN111252844A (en) 2020-06-09
CN111252844B true CN111252844B (en) 2022-01-04

Family

ID=70941604

Family Applications (1)

Application Number Title Priority Date Filing Date
CN202010098115.4A Active CN111252844B (en) 2020-02-18 2020-02-18 Application of eggshell particles in bismuth-containing sewage treatment and use method thereof

Country Status (1)

Country Link
CN (1) CN111252844B (en)

Citations (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1478594A (en) * 2003-07-04 2004-03-03 睿 王 Preparation method of heavy metal ion adsorbing agent
CN101269858A (en) * 2008-05-05 2008-09-24 同济大学 Application of longan shell in adsorbing heavy metal ion and method for adsorbing heavy metal ion with longan shell
CN101538075A (en) * 2008-03-19 2009-09-23 广西大学 Method for removing heavy metallic salts from industrial waste water by using egg shells
CN102190343A (en) * 2010-03-03 2011-09-21 南京信息工程大学 Method for adsorbing phosphate in sewage by using eggshells
CN102658090A (en) * 2012-04-20 2012-09-12 大连交通大学 Eggshell heavy metal ion adsorbent and preparation method thereof
CN103539283A (en) * 2013-10-11 2014-01-29 金川集团股份有限公司 Comprehensive treatment method for removing Sb and Bi impurities in Cu electrolyte
CN103608104A (en) * 2011-02-03 2014-02-26 萨里大学 Composite adsorbent material containing a porous carbon matrix
CN104874366A (en) * 2015-05-29 2015-09-02 西北师范大学 Preparation of chitosan magnetic adsorption materials and application in adsorbing Pb2+ and As3+ in sewage
CN105344324A (en) * 2015-09-30 2016-02-24 太仓碧奇新材料研发有限公司 Preparation method of soybean straw diatomite composite material for adsorbing bismuth ions in electroplating water
CN106186166A (en) * 2016-08-24 2016-12-07 华南理工大学 A kind of method utilizing eggshell fixed bed same for treating acidic mine wastewater
CN106925205A (en) * 2017-03-14 2017-07-07 东华理工大学 A kind of lime-preserved egg shell adsorbent of uranium and its preparation method and application

Patent Citations (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1478594A (en) * 2003-07-04 2004-03-03 睿 王 Preparation method of heavy metal ion adsorbing agent
CN101538075A (en) * 2008-03-19 2009-09-23 广西大学 Method for removing heavy metallic salts from industrial waste water by using egg shells
CN101269858A (en) * 2008-05-05 2008-09-24 同济大学 Application of longan shell in adsorbing heavy metal ion and method for adsorbing heavy metal ion with longan shell
CN102190343A (en) * 2010-03-03 2011-09-21 南京信息工程大学 Method for adsorbing phosphate in sewage by using eggshells
CN103608104A (en) * 2011-02-03 2014-02-26 萨里大学 Composite adsorbent material containing a porous carbon matrix
CN102658090A (en) * 2012-04-20 2012-09-12 大连交通大学 Eggshell heavy metal ion adsorbent and preparation method thereof
CN103539283A (en) * 2013-10-11 2014-01-29 金川集团股份有限公司 Comprehensive treatment method for removing Sb and Bi impurities in Cu electrolyte
CN104874366A (en) * 2015-05-29 2015-09-02 西北师范大学 Preparation of chitosan magnetic adsorption materials and application in adsorbing Pb2+ and As3+ in sewage
CN105344324A (en) * 2015-09-30 2016-02-24 太仓碧奇新材料研发有限公司 Preparation method of soybean straw diatomite composite material for adsorbing bismuth ions in electroplating water
CN106186166A (en) * 2016-08-24 2016-12-07 华南理工大学 A kind of method utilizing eggshell fixed bed same for treating acidic mine wastewater
CN106925205A (en) * 2017-03-14 2017-07-07 东华理工大学 A kind of lime-preserved egg shell adsorbent of uranium and its preparation method and application

Non-Patent Citations (2)

* Cited by examiner, † Cited by third party
Title
Removal of Cr(Ⅲ) from chrome tanning wastewater by adsorption using two natural carbonaceous materials:Eggshell and powderde marbe;Saliha Elabbas etal;《Journal of Environmental Management》;20161231;第166卷;第589-595页 *
鸡蛋壳废料对水体中Cr(Ⅵ)的吸附特征与机理;谢越等;《环境工程学报》;20150430;第9卷(第4期);第1585-1592页,参见第1.2实验方法、2研究结果 3讨论部分 *

Also Published As

Publication number Publication date
CN111252844A (en) 2020-06-09

Similar Documents

Publication Publication Date Title
Krishnani et al. Biosorption mechanism of nine different heavy metals onto biomatrix from rice husk
Karthikeyan et al. Adsorption dynamics and equilibrium studies of Zn (II) onto chitosan
Abdel-Ghani et al. Individual and competitive adsorption of phenol and nickel onto multiwalled carbon nanotubes
Shukla et al. The role of sawdust in the removal of unwanted materials from water
Pehlivan et al. Utilization of barley straws as biosorbents for Cu2+ and Pb2+ ions
Chiban et al. Characterization and application of dried plants to remove heavy metals, nitrate, and phosphate ions from industrial wastewaters
Bhattacharyya et al. Adsorption of Pb (II) from aqueous solution by Azadirachta indica (Neem) leaf powder
Jalali-Rad et al. Biosorption of cesium by native and chemically modified biomass of marine algae: introduce the new biosorbents for biotechnology applications
Bayo Kinetic studies for Cd (II) biosorption from treated urban effluents by native grapefruit biomass (Citrus paradisi L.): The competitive effect of Pb (II), Cu (II) and Ni (II)
Doshi et al. Bioaccumulation of heavy metals by green algae
Rajamohan et al. Equilibrium, kinetic and thermodynamic studies on the removal of Aluminum by modified Eucalyptus camaldulensis barks
Joshi et al. Utilization of polypyrrole/ZnO nanocomposite in the adsorptive removal of Cu 2+, Pb 2+ and Cd 2+ ions from wastewater
Liu et al. Adsorption dynamics and mechanism of aqueous sulfachloropyridazine and analogues using the root powder of recyclable long-root Eichhornia crassipes
CN108311117B (en) Magnetic biochar material for heavy metal wastewater treatment and preparation method thereof
JPS55159835A (en) High selective heavy metal ion adsorbing agent, and method of preparation and adsorption thereof
Malik et al. Removal of heavy metal from wastewater by the use of modified aloe vera leaf powder
Dupont et al. Biosorption of Cu (II) and Zn (II) onto a lignocellulosic substrate extracted from wheat bran
Mahajan et al. Kinetics and equilibrium studies of Cr (VI) metal ion remediation by Arachis hypogea shells: a green approach
Kalkan et al. Experimental study to remediate Acid Fuchsin dye using laccase-modified zeolite from aqueous solutions.
Tanhaei et al. Magnetic EDTA functionalized Preyssler cross linked chitosan nanocomposite for adsorptive removal of Pb (II) ions
Amin et al. Biosorption of mercury (II) from aqueous solution by fungal biomass Pleurotus eryngii: isotherm, kinetic, and thermodynamic studies
De Martino et al. Adsorption of phenols from olive oil waste waters on layered double hydroxide, hydroxyaluminium–iron-co-precipitate and hydroxyaluminium–iron–montmorillonite complex
CN111252844B (en) Application of eggshell particles in bismuth-containing sewage treatment and use method thereof
Ali et al. Nypa fruticans as a potential low cost adsorbent to uptake heavy metals from industrial wastewater
Li et al. Characterization of metal removal by os sepiae of Sepiella maindroni Rochebrune from aqueous solutions

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