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WO2018019636A1 - Procédé de préparation de charbon actif modifié par nano-alpha-fe 2o3 et son utilisation - Google Patents

Procédé de préparation de charbon actif modifié par nano-alpha-fe 2o3 et son utilisation Download PDF

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Publication number
WO2018019636A1
WO2018019636A1 PCT/EP2017/068022 EP2017068022W WO2018019636A1 WO 2018019636 A1 WO2018019636 A1 WO 2018019636A1 EP 2017068022 W EP2017068022 W EP 2017068022W WO 2018019636 A1 WO2018019636 A1 WO 2018019636A1
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WIPO (PCT)
Prior art keywords
activated carbon
nano
modified activated
filter core
anyone
Prior art date
Application number
PCT/EP2017/068022
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English (en)
Inventor
Lei Chen
Lianjie CHEN
Miaoquan HUANG
Kaiqin PENG
Feng SU
Jinjun TU
Xiuyou YE
Zhongqi ZHANG
Original Assignee
Unilever Plc
Zhejiang Qinyuan Water Treatment S. T. Co., Ltd.
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Application filed by Unilever Plc, Zhejiang Qinyuan Water Treatment S. T. Co., Ltd. filed Critical Unilever Plc
Priority to CN201780045738.1A priority Critical patent/CN109689203A/zh
Publication of WO2018019636A1 publication Critical patent/WO2018019636A1/fr
Priority to PH12018502631A priority patent/PH12018502631A1/en

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    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/02—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
    • B01J20/20—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising free carbon; comprising carbon obtained by carbonising processes
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/02—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
    • B01J20/06—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising oxides or hydroxides of metals not provided for in group B01J20/04
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/28—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties
    • B01J20/28002—Solid 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 physical properties
    • B01J20/28004—Sorbent size or size distribution, e.g. particle size
    • B01J20/28007—Sorbent size or size distribution, e.g. particle size with size in the range 1-100 nanometers, e.g. nanosized particles, nanofibers, nanotubes, nanowires or the like
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/28—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties
    • B01J20/28014—Solid 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
    • B01J20/2805—Sorbents inside a permeable or porous casing, e.g. inside a container, bag or membrane
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/30—Processes for preparing, regenerating, or reactivating
    • B01J20/3078—Thermal treatment, e.g. calcining or pyrolizing
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/30—Processes for preparing, regenerating, or reactivating
    • B01J20/3085—Chemical treatments not covered by groups B01J20/3007 - B01J20/3078
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/30—Processes for preparing, regenerating, or reactivating
    • B01J20/32—Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating
    • B01J20/3202—Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating characterised by the carrier, support or substrate used for impregnation or coating
    • B01J20/3204—Inorganic carriers, supports or substrates
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/30—Processes for preparing, regenerating, or reactivating
    • B01J20/32—Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating
    • B01J20/3231—Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating characterised by the coating or impregnating layer
    • B01J20/3234—Inorganic material layers
    • B01J20/3236—Inorganic material layers containing metal, other than zeolites, e.g. oxides, hydroxides, sulphides or salts
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00—Treatment of water, waste water, or sewage
    • C02F1/28—Treatment of water, waste water, or sewage by sorption
    • C02F1/281—Treatment of water, waste water, or sewage by sorption using inorganic sorbents
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00—Treatment of water, waste water, or sewage
    • C02F1/28—Treatment of water, waste water, or sewage by sorption
    • C02F1/283—Treatment of water, waste water, or sewage by sorption using coal, charred products, or inorganic mixtures containing them
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00—Treatment of water, waste water, or sewage
    • C02F1/28—Treatment of water, waste water, or sewage by sorption
    • C02F1/288—Treatment of water, waste water, or sewage by sorption using composite sorbents, e.g. coated, impregnated, multi-layered
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2101/00—Nature of the contaminant
    • C02F2101/10—Inorganic compounds
    • C02F2101/103—Arsenic compounds
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2101/00—Nature of the contaminant
    • C02F2101/10—Inorganic compounds
    • C02F2101/20—Heavy metals or heavy metal compounds
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2101/00—Nature of the contaminant
    • C02F2101/10—Inorganic compounds
    • C02F2101/20—Heavy metals or heavy metal compounds
    • C02F2101/22—Chromium or chromium compounds, e.g. chromates
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2305/00—Use of specific compounds during water treatment
    • C02F2305/08—Nanoparticles or nanotubes

Definitions

  • the present invention relates to an activated carbon, in particular to a method for preparing a modified activated carbon and a use thereof.
  • Activated carbon as a porous non-polar adsorbent, has a huge specific surface area on account of its special pore structure, as well as being plentiful and inexpensive, so is one of the adsorbents most widely used in water treatment at present. It has good adsorbency and stable chemical properties, can withstand strong acids and strong bases, can withstand the effects of immersion in water, high temperature and high pressure, and may also be regenerated by activation.
  • Iron-containing adsorbents has good capacity for adsorbing anions and cations.
  • the development, manufacture and application of adsorbents in which the principal adsorbing component is elemental iron has already drawn wide attention in the market.
  • nano-iron including zero valent iron, iron oxide and magnetite particles etc.
  • powdered nano-iron particles are tiny, easily deactivate and aggregate in water, and are difficult to recover and reuse. Summary of the invention
  • First aspect of the present invention provides a method for preparing a nano oFe2C>3 modified activated carbon, the method comprising steps of: a. treating activated carbon in dilute nitric acid, washing with water and anhydrous solvent, and drying at 60 to 80°C, to obtain treated activated carbon;
  • step c transferring the solution obtained from step b into a high-pressurizable vessel, adding the treated activated carbon obtained from step a, and stirring;
  • step d heating the pressurizable vessel from step c at a temperature in the range of 150 to 180°C to obtain processed activated carbon; and e. washing the processed activated carbon obtained from step d with an anhydrous solvent, and drying at 60 to 80°C to obtain nano a-Fe2C>3 modified activated carbon.
  • Second aspect of the present invention provides a nano a-Fe203 modified activated carbon (2) obtained by the method of the first aspect.
  • Third aspect of the present invention provides a filter core, comprising a filter core body, and a nano a-Fe203 modified activated carbon, wherein the nano a-Fe203 modified activated carbon is prepared by the method of the first aspect and is packed in the filter core body.
  • Fourth aspect of the present invention provides use of nano alpha iron(lll) oxide in an activated carbon-based filter to adsorb heavy metals.
  • Fifth aspect of the present invention provides use of nano alpha iron(lll) oxide in a method according to the first aspect to prepare activated carbon-based filter for adsorbing heavy metals.
  • Another aspect of the present invention provides use of nano alpha iron(lll) oxide obtained by a method according to first aspect for removal of heavy metals from water.
  • Fig. 1 is a structural schematic diagram of of the present invention.
  • Fig. 2 is a curve for the first determination method as provided in the present invention.
  • Fig. 3 is a curve for the second determination method as provided in the present invention.
  • Fig. 4 is a curve for the third determination method as provided in the present invention.
  • Fig. 5 is a curve for the fourth determination method in embodiment 4 of the present invention.
  • Fig. 6 is a curve for the fifth determination method as provided in the present invention.
  • the present invention provides a method for preparing a nano oFe2C>3 modified activated carbon and a use thereof.
  • nano a-Fe2C>3 means nano sized a-Fe2C>3, which is magnesium oxide Nanomaterials with diameters of ⁇ 100 nm, wherein a-Fe2C>3 is alpha Iron(lll) oxide or Iron(lll) oxide in the alpha phase.
  • the present invention employs the following technical solution:
  • a method for preparing a nano a-Fe2C>3 modified activated carbon comprising steps of: a. treating activated carbon in dilute nitric acid, washing with water and anhydrous solvent, and drying at 60 to 80°C, to obtain treated activated carbon;
  • step c transferring the solution obtained from step b into a high-pressurizable vessel, adding the treated activated carbon obtained from step a, and stirring;
  • step d heating the pressurizable vessel from step c at a temperature in the range of 150 to 180°C to obtain processed activated carbon; and e. washing the processed activated carbon obtained from step d with an anhydrous solvent, and drying at 60 to 80°C to obtain nano a-Fe2C>3 modified activated carbon.
  • anhydrous solvent is anhydrous ethanol.
  • the volume ratio of anhydrous solvent to water ranges from 1 :3 to 1 :1 and the washing time in each case is from 0.5 to 2 hours.
  • particle size of the activated carbon in step a ranges from 10 to 20 mesh (2mm to 0.8mm).
  • step a is immersing the activated carbon in dilute nitric acid for 0.5 to 2 hours.
  • step b the high-pressurizable vessel is provided with a polytetrafluoroethylene liner.
  • the pressurizable vessel has a volume in the range of from 70 to 200 ml_. It is preferred that in step d the heating at temperatures in the range of 150 to 180°C is for 3.5 to 6.5 hours, and the pressure inside the pressurizable vessel ranges from 1.0 to 2.0 MPa .
  • the present invention provides a nano a-Fe203 modified activated carbon obtained by the method of the present invention.
  • the present invention provides a filter core, comprising a filter core body, and a nano o Fe203 modified activated carbon, wherein the nano a-Fe203 modified activated carbon is prepared by the method of the present invention and is packed in the filter core body.
  • the filter core body is made of meltblown polypropylene fiber.
  • the filter core body is cylindrical with an internal diameter of 25 to 35 mm and an external diameter of 60 to 65 mm.
  • the present invention provides use of nano alpha iron(lll) oxide in an activated carbon- based filter to adsorb heavy metals.
  • the present invention also provides use of nano alpha iron(lll) oxide in a method to prepare activated carbon-based filter for adsorbing heavy metals.
  • the present invention also provides use of nano alpha iron(lll) oxide obtained by a method according to the present invention for removal of heavy metals from water.
  • the present invention provides a method for preparing a nano oFe2C>3 modified activated carbon, comprising the following steps: a. immersing activated carbon in dilute nitric acid, then washing alternately with water and anhydrous ethanol, to remove substances adhering to the surface, and sun-drying, air-drying, or oven-drying at 60 - 80°C, in preparation for use; b. using FeCI3-6H20 as a precursor, making up an FeCI3 solution with a solution concentration of 167 - 835 mol/L with anhydrous ethanol as a solvent, and then adding 250 - 1250 mol/L urea, and stirring to mix evenly; c. transferring the solution processed in step b into a -pressurizable vessel, then adding the activated carbon processed in step a, and stirring thoroughly to remove gas bubbles from the solution;
  • step d putting the pressurizable vessel from step c into a blast oven and performing hydrothermal treatment
  • step d washing the activated carbon processed in step d with anhydrous ethanol, and sun-drying, air-drying, or oven-drying at 60 to 80°C, to obtain nano a-Fe2C>3 modified activated carbon.
  • the a-Fe2C>3 modified activated carbon obtained by this method can greatly improve the ability of ordinary activated carbon to adsorb heavy metals.
  • the volume ratio of ethanol to water in step a is 1 : 3 to 1 : 1 , and the washing time in each case is 0.5 to 2 h.
  • the particle size of activated carbon in step a is 10 to 20 mesh.
  • the concentration of dilute nitric acid is 0.1 M
  • the immersion time is 0.5 to 2 h
  • every 100 g of activated carbon is washed in 1 L of dilute nitric acid.
  • Impurities on the surface of the activated carbon can be effectively removed through immersion in dilute nitric acid, to prevent non-uniformity when loading nano a-Fe2C>3 modified activated carbon.
  • a polytetrafluoroethylene (PTFE) liner is provided in the pressurizable vessel in step b.
  • PTFE will not react with the solution, so will not introduce impurities.
  • the solution can be effectively prevented from not coming into contact with a stainless steel inside wall of the high-pressurizable vessel, thereby enabling the -pressurizable vessel to serve a sealing function, and maintain high temperature and high pressure inside the high-pressurizable vessel.
  • the volume of the high-pressurizable vessel is 70 to 200 ml_.
  • the hydrothermal treatment in step d consists of external heating by means of the blast oven for 3.5 to 6.5 h, such that the temperature is kept at 150 - 180°C and the pressure is kept at 1 .0 to 2.0 MPa inside the high-pressurizable vessel.
  • the internal space of the high-pressurizable vessel is kept in a high-temperature, high-pressure state by such external heating.
  • the nano material can be endowed with different morphologies in such a state; these special morphologies can increase the specific surface area of the material, and thereby increase the adsorption capacity of the material.
  • a filter core comprising a filter core body, with nano a-Fe2C>3 modified activated carbon packed in the filter core body.
  • the filter core body is made of meltblown polypropylene fibres.
  • the filter core body is cylindrical, with an internal diameter of 25 to 35 mm and an external diameter of 60 to 65 mm.
  • a-Fe2C>3 is loaded on the surface of, or in the pores of, activated carbon by a hydrothermal synthesis method, to obtain the nano oFe2C>3 modified activated carbon, which can not only retain the intrinsic characteristics of a nano material but also enhance the stability thereof, and can efficiently adsorb the heavy metals chromium and arsenic in drinking water.
  • Ordinary activated carbon has virtually no ability to adsorb the heavy metals chromium and arsenic
  • 300 g of the nano oFe2C>3 modified activated carbon of the present invention, in water with 10 times the allowed content of Cr or As, can guarantee that the water outputted meets the national safety standard for drinking water for half a month.
  • the material is suited to reactor operations, and has characteristics such as an easily controlled reaction, easy operations and convenient maintenance, so has very broad prospects for market application and development.
  • a method for preparing a nano a-Fe2C>3 modified activated carbon preferably comprising the following steps: a. 10 g of activated carbon particles with mesh number 10 are immersed in 100 mL of dilute nitric acid with a concentration of 0.1 M for 2 h, then washed alternately in water and anhydrous ethanol; the volume ratio of ethanol to water is 1 :3 - 1 :1 , and the washing time in each case is 0.5 h. Substances adhering to the surface are removed, and oven-drying at 80°C is performed, in preparation for use;
  • FeCI3-6H20 as a precursor, making up an FeCI3 solution with a solution concentration of 167 mol/L with anhydrous ethanol as a solvent, and then adding 250 mol/L urea, and stirring to mix evenly;
  • step b transferring the solution processed in step b into a -pressurizable vessel (in this embodiment, the pressurizable vessel has a volume of 70 ml and a PTFE liner is provided therein), then adding the activated carbon processed in step a, and stirring thoroughly to remove gas bubbles from the solution; d. putting the pressurizable vessel from step c into a blast oven and performing hydrothermal treatment; externally heating by means of the blast oven for 3.5 - 6.5 h, such that the temperature is kept at 150 - 180°C and the pressure is kept at 1 .0 MPa inside the pressurizable vessel.
  • the internal space of the - pressurizable vessel is kept in a high-temperature, high-pressure state by such external heating.
  • the nano material can be endowed with different morphologies in such a state.
  • step d washing the activated carbon processed in step d with anhydrous ethanol, and oven-drying at 60°C, to obtain nano a-Fe2C>3 modified activated carbon.
  • the present invention also provides a method for preparing a nano oFe2C>3 modified activated carbon, the method preferably comprising the following steps: a. 10 g of activated carbon particles with mesh number 10 are immersed in 100 mL of dilute nitric acid with a concentration of 0.1 M for 0.5 h, then washed alternately in water and anhydrous ethanol; the volume ratio of ethanol to water is 1 : 3 to 1 : 1 , and the washing time in each case is 2 h. Substances adhering to the surface are then removed, and sun-drying is performed, in preparation for use; b. using FeCI3-6H20 as a precursor, making up an FeCI3 solution with a solution concentration of 500 mol/L with anhydrous ethanol as a solvent, and then adding 800 mol/L urea, and stirring to mix evenly;
  • step b transferring the solution processed in step b into a pressurizable vessel (in this embodiment, the pressurizable vessel has a volume of 135 mL and a PTFE liner is provided therein), then adding the activated carbon processed in step a, and stirring thoroughly to remove gas bubbles from the solution; d. putting the high-pressurizable vessel from step c into a blast oven and performing hydrothermal treatment; externally heating by means of the blast oven for 3.5 - 6.5 h, such that the temperature is kept at 150 - 180°C and the pressure is kept at 2.0 MPa inside the pressurizable vessel.
  • the internal space of the pressurizable vessel is kept in a high-temperature, high-pressure state by such external heating.
  • the nano material can be endowed with different morphologies in such a state.
  • step d washing the activated carbon processed in step d with anhydrous ethanol, and oven-drying at 80°C, to obtain nano a-Fe203 modified activated carbon.
  • the present invention also provides a method wherein, preferably in step b, instead of using FeC ⁇ -ei-bO as a precursor, an FeC solution with a solution concentration of 835 mol/L is made up with anhydrous ethanol as a solvent, and then 1250 mol/L urea is added, and the mixture is stirred to mix evenly; and in step c, the high-pressurizable vessel has a volume of 200 mL.
  • the present invention also provides a method wherein, preferably a filter core, as shown in Fig. 1 , comprises a filter core body 1 , with the nano a-Fe2C>3 modified activated carbon 2 that was made in embodiment 1 or embodiment 2 or embodiment 3 packed in the filter core body 1 ; the filter core body 1 is cylindrical, and is made of meltblown polypropylene fibres.
  • nano oFe2C>3 modified activated carbon 2 is used to treat heavy metal in drinking water by adsorption; water containing heavy metal is passed into the filter core packed with nano oFe2C>3 modified activated carbon 2, then the original water and the water coming out are respectively sampled to measure the change in heavy metal concentration, wherein the specific determination methods are divided into the following types:
  • First type Original waters containing the heavy metals chromium and arsenic and both having a concentration of 10 mg/L are respectively made up, the initial pH is adjusted to 7, and the flow speed is adjusted by means of an electromagnetic flow meter, such that the incoming water has a flow speed of 100 mL/min, being pressed in from the outside of the filter core body 1 , and after passing through the nano a-Fe203 modified activated carbon, comes out; the original water and the water coming out are respectively sampled to measure the change in heavy metal concentration. See Fig. 2 for the results.
  • Second type Original water containing the heavy metal chromium at a concentration of 10 mg/L is made up, the pH is adjusted to 4 and 10 respectively, and the flow speed is adjusted by means of an electromagnetic flow meter, such that the incoming water has a flow speed of 100 mL/min, being pressed in from the outside of the filter core body 1 , and after passing through the nano a-Fe203 modified activated carbon, comes out; the original water and the water coming out are respectively sampled to measure the change in heavy metal concentration. See Fig. 3 for the results.
  • Second type Original water containing the heavy metal arsenic at a concentration of 10 mg/L is made up, the pH is adjusted to 4 and 10 respectively, and the flow speed is adjusted by means of an electromagnetic flow meter, such that the incoming water has a flow speed of 100 mL/min, being pressed in from the outside of the filter core body 1 , and after passing through the nano a-Fe203 modified activated carbon, comes out; the original water and the water coming out are respectively sampled to measure the change in heavy metal concentration. See Fig. 4 for the results.

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Analytical Chemistry (AREA)
  • Inorganic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Water Supply & Treatment (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Environmental & Geological Engineering (AREA)
  • Hydrology & Water Resources (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Crystallography & Structural Chemistry (AREA)
  • Materials Engineering (AREA)
  • Nanotechnology (AREA)
  • Solid-Sorbent Or Filter-Aiding Compositions (AREA)
  • Water Treatment By Sorption (AREA)

Abstract

La présente invention concerne un charbon actif, et dévoile une méthode pour préparer un charbon actif modifié par nano-alpha-Fe2O3 et son utilisation, le procédé consistant : (a). à traiter du charbon actif dans de l'acide nitrique dilué, laver avec de l'eau et un solvant anhydre, et sécher à 60 jusqu'à 80°C, pour obtenir du charbon actif traité; (b). à fournir une solution FeCl3 à une concentration de 167 à 835 mol/L dans un solvant anhydre, et à ajouter de l'urée à une concentration de 250 à 1250 mol/L, et à agiter pour mélanger uniformément; (c). à transférer la solution obtenue à l'étape (b) dans un réservoir à haute pression, à ajouter du charbon actif traité obtenu dans l'étape (a) et à agiter; (d). à chauffer le réservoir à haute pression de l'étape (c) à une température dans la plage de 150 à 180°C pour obtenir du charbon actif traité; et (e). à laver le charbon actif préparé obtenu à l'étape (d). avec un solvant anhydre, et à sécher à 60 jusqu'à 80°C pour obtenir du charbon actif modifié par nano-alpha-Fe2O3. Le charbon actif modifié par nano-alpha-Fe 2O3 obtenu dans la présente invention peut non seulement conserver les caractéristiques intrinsèques d'un nanomatériau mais également améliorer sa stabilité, peut adsorber efficacement les métaux lourds, le chrome et l'arsenic dans de l'eau potable, convient aux opérations de réacteur, et présente des caractéristiques telles qu'une réaction facilement contrôlée, des opérations faciles et une maintenance pratique, ce qui offre des perspectives très étendues pour une application et un développement sur le marché.
PCT/EP2017/068022 2016-07-25 2017-07-17 Procédé de préparation de charbon actif modifié par nano-alpha-fe 2o3 et son utilisation WO2018019636A1 (fr)

Priority Applications (2)

Application Number Priority Date Filing Date Title
CN201780045738.1A CN109689203A (zh) 2016-07-25 2017-07-17 制备纳米α-Fe2O3改性活性炭的方法及其用途
PH12018502631A PH12018502631A1 (en) 2016-07-25 2018-12-13 Method for preparing nano alpha-fe203 modified activated carbon and use thereof

Applications Claiming Priority (2)

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