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WO2011119043A1 - Procédé d'élimination de contaminants de l'eau - Google Patents

Procédé d'élimination de contaminants de l'eau Download PDF

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Publication number
WO2011119043A1
WO2011119043A1 PCT/NO2011/000100 NO2011000100W WO2011119043A1 WO 2011119043 A1 WO2011119043 A1 WO 2011119043A1 NO 2011000100 W NO2011000100 W NO 2011000100W WO 2011119043 A1 WO2011119043 A1 WO 2011119043A1
Authority
WO
WIPO (PCT)
Prior art keywords
water
chitosan
absorbent
absorbents
contaminations
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.)
Ceased
Application number
PCT/NO2011/000100
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English (en)
Inventor
Dag Arntsen
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Individual
Original Assignee
Individual
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Filing date
Publication date
Application filed by Individual filed Critical Individual
Publication of WO2011119043A1 publication Critical patent/WO2011119043A1/fr
Anticipated expiration legal-status Critical
Priority to DKPA201270624A priority Critical patent/DK201270624A/da
Ceased legal-status Critical Current

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Classifications

    • 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
    • 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
    • B01J20/04—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising compounds of alkali metals, alkaline earth metals or magnesium
    • B01J20/041—Oxides or hydroxides
    • 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
    • B01J20/04—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising compounds of alkali metals, alkaline earth metals or magnesium
    • B01J20/043—Carbonates or bicarbonates, e.g. limestone, dolomite, aragonite
    • 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
    • B01J20/10—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising silica or silicate
    • B01J20/103—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising silica or silicate comprising silica
    • 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
    • B01J20/10—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising silica or silicate
    • B01J20/14—Diatomaceous earth
    • 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
    • B01J20/22—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising organic material
    • B01J20/24—Naturally occurring macromolecular compounds, e.g. humic acids or their derivatives
    • 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
    • C02F1/46—Treatment of water, waste water, or sewage by electrochemical methods
    • C02F1/469—Treatment of water, waste water, or sewage by electrochemical methods by electrochemical separation, e.g. by electro-osmosis, electrodialysis, electrophoresis
    • 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
    • B01J2220/00—Aspects relating to sorbent materials
    • B01J2220/40—Aspects relating to the composition of sorbent or filter aid materials
    • B01J2220/42—Materials comprising a mixture of inorganic materials
    • 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
    • B01J2220/00—Aspects relating to sorbent materials
    • B01J2220/40—Aspects relating to the composition of sorbent or filter aid materials
    • B01J2220/46—Materials comprising a mixture of inorganic and organic materials
    • 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
    • B01J2220/00—Aspects relating to sorbent materials
    • B01J2220/40—Aspects relating to the composition of sorbent or filter aid materials
    • B01J2220/48—Sorbents characterised by the starting material used for their preparation
    • B01J2220/4812—Sorbents characterised by the starting material used for their preparation the starting material being of organic character
    • B01J2220/4825—Polysaccharides or cellulose materials, e.g. starch, chitin, sawdust, wood, straw, cotton
    • 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
    • C02F1/286—Treatment of water, waste water, or sewage by sorption using natural organic sorbents or derivatives thereof
    • 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
    • C02F1/42—Treatment of water, waste water, or sewage by ion-exchange

Definitions

  • the present invention relates to a method for the removal of contaminations from water by using chitosan to form precipitations with the contaminations, and then remove the formed precipitations by applying an electric field generated with direct current.
  • Contaminations in water for use in the preparation of food products for human consumption represent a steadily increasing problem because of the increased use of pesticides and other chemicals that accumulate in the environment.
  • Water can contain toxic compounds such as salts of heavy metals, water soluble organic and inorganic compounds, all of which must be eliminated before making use of the water.
  • US 5480558 (“Electric enhancement of adsorbent flotation separation”) relates to removing PCB from earth by a washing process. Contaminated earth is suspended in water in a tank, gas is bubbled through the slurry and together with the
  • US 5770090 (“Method for recovery of heavy metal from waste water”) relates to a method for removing heavy metals, in particular chromium, from waste water.
  • CN 101508503 (abstract) (Nantong University, 2009.08.19) discloses purification of sewage water by contacting the water with a solid adsorbent.
  • the use of chitosan in water cleaning has been known for long.
  • the chitosan will absorb the contaminations and form precipitations which will partly sediment into a solid bottom layer, partly remain suspended in the processed water.
  • the object of the present invention is to remove the precipitated, and particularly the suspended, substances in an efficient way by the use of an electric field generated with direct current.
  • the method of the present invention can be performed by the use of a simple apparatus. The level of heavy metals and other contaminations remaining in the cleaned water will be far below the values set by health authorities.
  • the present invention relates to a method for removing contaminations from water.
  • the method is characterised in that at least one absorbent which absorb the contaminations is mixed into the water, then the water comprising the absorbent is exposed to a direct current electric field between two or optionally more electrodes having a positive and negative charge, respectively, in a period of time sufficient to obtain that the absorbent with absorbed contaminations are deposited onto the positively charged electrode, and at the end this electrode with deposited substances is lifted out of the water, and the deposited substances are removed.
  • a first absorbent and a second absorbent is used, wherein the first absorbent comprises chitosan and the second absorbent comprises activated carbon.
  • the method of the present invention can be performed both batchwise and continuously.
  • Fig 1 shows schematically a suitable vessel for use by the method of the invention; the vessel may also be provided with a heating jacket for temperature control.
  • Fig 2 shows the same vessel provided with a stirring device.
  • Fig 3 shows the vessel provided with an electrode.
  • Fig 4 shows the vessel with the anode lifted out for cleaning.
  • the present invention relates to a method for the purification of water by the use of at least one absorbent which form precipitations together with the
  • the content of foreign and potentially health hazardous substances in the purified water will be at a level well below the threshold values accepted or recommended by the health authorities.
  • any type of water of water can be purified, such as fresh water, seawater or brackish water.
  • At least one absorbent preferably a first absorbent and a second absorbent.
  • Chitosan is used as the first absorbent, optionally together with carrageenan, alginates or condroitinglycol, or mixtures thereof.
  • Chitosan may be prepared from chitin which can be found in the shell of marine shellfishes. Chitin is a natural polymer containing acyl moieties (-CH3-CO-). These can be converted to a desired extent by treating the chitin with alkaline water and thus obtain chitosan. Depending on the conditions when preparing chitosan. a desired degree of the acetylation can be obtained; that is to say that not ail acyl groups will necessarily disappear.
  • chitosan is often characterized by the viscosity of an aqueous solution of chitosan. Typically, 1 percent by weight of chitosan is dissolved in 1 percent by weight of acetic acid, and the intrinsic viscosity ([ ⁇ ]) of the solution is determined. From this follows that chitosan may have different properties depending among others on the degree of the
  • chitosan types may be used, also salts and glucose amides of chitosan, and hydrolyzed chitosan.
  • the chitosan may have a degree of acetylation from high to low, and the whole range of viscosities.
  • chitosan could be mixed directly into the water, but since chitosan has poor water solubility at pH above 7, it is more suitable to use a chitosan- containing "purification" liquid.
  • a typical purification liquid is prepared by dissolving chitosan in acidic water.
  • acidic water As an acid all types of suitable acids may be used, preferably hydrochloric acid, acetic acid or hydroxyl acetic acid, most preferred hydroxyl acetic acid (glycolic acid).
  • the purification liquid must have an acidic pH to keep the chitosan dissolved, i.e. pH must be below 6.5-7.
  • the purification liquid may be of various compositions and still provide acceptable results.
  • the purification liquid may be used an aqueous solution containing from about 0.1 percent by weight to about 10 percent by weight of chitosan and a strong acid in a sufficient amount of to keep the chitosan dissolved.
  • the amount should be at least 0.1 percent by weight.
  • the upper limit is determined by the solubility of chitosan in the purification liquid.
  • the purification liquid comprises about 1 percent by weight of chitosan and about 1 percent by weight of an acid, such as glycolic acid.
  • a particularly suitable purification liquid contains in addition to about 1 percent by weight of chitosan and about 1 percent by weight of an acid, also about 0.5 percent by weight of carrageenan and about 0.5 percent by weight of silica.
  • the second absorbent may be added.
  • the second absorbent is preferably used activated carbon as particles, and preferably as powder, optionally together with bentonite, diatomaceous earth, lime, calcium carbonate, coral sand or ion exchangers, or a mixture thereof.
  • activated carbon has as a result that chitosan with absorbed substances coalesce into greater particles which can easily be removed. This reveals a surprising synergistic effect between chitosan and activated carbon.
  • the amount of activated carbon used in the purification is not critical; but should be kept as low as possible for practical and economy reasons.
  • the above described purification liquid containing chitosan is mixed into the water followed by activated carbon. Another option is to add activated carbon to the purification liquid before this being added to the water.
  • the invention is not restricted to any certain sequence of adding the absorbents.
  • the water must be stirred vigorously or have a turbulent flow in order to obtain that the absorbents are brought into an intimate contact with the contaminations.
  • the contaminations will thereby be attached to the absorbents and form particles which can sediment and form a solid bottom layer.
  • This bottom layer may be drawn off, or removed by the use of a filter or by mechanical means, depending o the circumstances.
  • the remaining water will contain a minor amount of suspended microparticles.
  • suspended microparticles can be removed in a traditional way by filtering or centrifugation.
  • the suspended substances can be removed in a more simple way by exposing the water to an electric field generated with direct current.
  • the suspended microparticles will carry a negative charge and will thus migrate in such an electric field towards the positively charged electrode and attach thereto. With this method all contaminating substances in the water will be removed.
  • the water is heavily contaminated, it may be appropriate first to remove a possible bottom layer by mechanical means, and then remove the remaining suspended m icropartic l es by the use of an electric field .
  • the removal of precipitated particles by the use of an electric field may start at any stage of the purification process as soon as the mixing procedure is ended, that is to say as soon as the purification liquid has been completly mixed into the water.
  • the total amount of precipitated substances can be removed by the use of an electric field, omitting any mechanical removal .
  • Embodiments of the invention depend on the level of
  • the employed reactor vessel can be provided with an assembled negatively charged electrode and an positively charged electrode.
  • the negatively charged electrode will be termed cathode, and the positively charged electrode will be termed anode.
  • the jacket of the vessel may be the negative electrode, or a separate negative electrode may be used.
  • An anode is immersed into the water in the center of the vessel. Between the electrodes is applied a direct current voltage typically in the range of 0.1 to 500 volts.
  • a salt solution Prior to exposing the water to an electric field a salt solution may be added to the water in an amount of about 0.1 % by weigt of the weight of the water to make the water electrical conductive.
  • the salt used may be sodium chloride or ferric chloride.
  • the salt solution may be added at any stage of the process. Such an addition may be necessary for fresh water, while such an addition is unnecessary for seawater.
  • the water containing suspended microparticles is exposed to the electric field in a period of time from about 10 seconds to a number of hours, depending on the circumstances.
  • the electrodes are composed of an electrical conductive material, such as a metal alloy.
  • the anode may be of any suitable shape, such as one or more rods, plates, wire nets. etc.
  • the cathode may be the jacket of the vessel or a separate electrode.
  • Chitosan is negatively charged, and as a consequence chitosan with absorbed substances will have a negative surface charge and be attracted to the anode on which the chitosan-containing substances will deposit.
  • chitosan containing absorbed contaminations has deposited on the anode forming a layer of appropriate thickness, the anode is lifted out of the vessel and cleaned. Deposited substances may adhere so firmly to the anode that mechanical means must be used to remove it.
  • the collected waste material must be disposed of in an approved depot for environmentally hazardous materials. All contaminated materials separated in the process, such as a bottom layer which is drawn off or removed by filtering or by mechanical means, can be subjected to evaporation until dryness. By the evaporation all contaminatins will remain bound to the chitosan.
  • the chitosan will function in this way up to about 300 °C.
  • the evaporation method may be conducted up to a
  • a suitable vessel for use in the present method is shown in figure 1 .
  • the vessel may be of any suitable size and may be provided with an outer heating jacket to maintain a constant temperature in the water if necessary.
  • a suitable stirring device with controllable speed is used, as shown in figure 2.
  • Contaminated seawater, freshwater or brackish water which shall be purified is pumped into the vessel via a pipeline.
  • a purification liquid comprising chitosan mixed with activated carbon, carrageenan and/or bentonit is added to the water in a controlled amount. This addition may be performed in the pipeline feeding water into the vessel, or in the vessel during optionally vigorous stirring of the water in the vessel.
  • the pH in the water may be from pH 7 to pH 3, preferably in the range from pH 4 to pH 6.5.
  • the anode is then positioned in the vessel as indicated in figure 3.
  • the electrodes may be of any appropriate shape, such as plates, rods, wire nets, etc. They are preferably in the shape of a set of parallel plates, such as anode plates and cathode plates spaced in short distances from each other. Alternate plates will be an anode and a cathode, respectively.
  • a voltage is applied between the anodes and cathodes. The voltage will be in the range from about 0.1 volt to about 500 volts. Because the chitosan particles carry a negative surface charge they will be attracted to the anodes, which have a positive charge, and deposit thereon.
  • the layer on the anodes may grow to a thickness of 2 to 3 cms.
  • Operation parameters such as stirring speed, time period for each stage, flow rates, potential differences between the electrodes, etc, will depend on the equipment used and the level of contaminations in the water. A person skilled i the art will be able to decide on suitable parametres by routine experimentation.
  • the end product is purified clear water without any objectionable flavor, and free of heavy metals and contaminations. Analysis of the final water shows that the remaining content of contaminations is below the tresholds prescribed by health authorities.
  • the present method provides a simple and cost efficient industrial method for removing contaminations that are precipitated from water by the use of chitosan.
  • the present invention is applicable in all areas of industrial purification of water.

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Analytical Chemistry (AREA)
  • Inorganic Chemistry (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Environmental & Geological Engineering (AREA)
  • Hydrology & Water Resources (AREA)
  • Engineering & Computer Science (AREA)
  • Water Supply & Treatment (AREA)
  • Molecular Biology (AREA)
  • Electrochemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Geochemistry & Mineralogy (AREA)
  • Water Treatment By Sorption (AREA)
  • Water Treatment By Electricity Or Magnetism (AREA)
  • Solid-Sorbent Or Filter-Aiding Compositions (AREA)

Abstract

L'invention porte sur un procédé d'élimination des contaminants de l'eau par le mélange profond d'agents absorbants dans de l'eau, puis l'exposition de l'eau avec les agents absorbants en suspension à un champ électrique continu entre deux ou, facultativement, davantage d'électrodes, pendant une durée suffisante pour obtenir que l'agent absorbant avec les contaminants absorbés soit déposé sur l'électrode chargée positivement, qui est ensuite soulevée hors de l'eau, et les substances déposées sont éliminées. Un premier agent absorbant et un second agent absorbant sont utilisés, le premier agent absorbant comportant du chitosane et le second agent absorbant comportant du charbon actif.
PCT/NO2011/000100 2010-03-24 2011-03-24 Procédé d'élimination de contaminants de l'eau Ceased WO2011119043A1 (fr)

Priority Applications (1)

Application Number Priority Date Filing Date Title
DKPA201270624A DK201270624A (en) 2010-03-24 2012-10-11 A method for removal of contaminations from water

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
NO20100436 2010-03-24
NO20100436A NO331590B1 (no) 2010-03-24 2010-03-24 Fremgangsmate for fjerning av forurensninger fra vann

Publications (1)

Publication Number Publication Date
WO2011119043A1 true WO2011119043A1 (fr) 2011-09-29

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Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/NO2011/000100 Ceased WO2011119043A1 (fr) 2010-03-24 2011-03-24 Procédé d'élimination de contaminants de l'eau

Country Status (4)

Country Link
DK (1) DK201270624A (fr)
IS (1) IS9008A (fr)
NO (1) NO331590B1 (fr)
WO (1) WO2011119043A1 (fr)

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2014064073A1 (fr) * 2012-10-26 2014-05-01 Clariant International Ltd. Procédé et composition d'épuration d'eau et de déshydratation de boues
CN104001480A (zh) * 2014-05-30 2014-08-27 扬州天辰精细化工有限公司 一种球形水处理剂的制备方法
WO2014171812A3 (fr) * 2013-04-18 2015-05-07 ZAINAL ABIDIN, Roslan Bin Composition permettant de traiter les eaux usées
RU2645131C1 (ru) * 2017-07-18 2018-02-15 Андрей Александрович Нестеренко Способ получения сорбционного материала
CN108905982A (zh) * 2018-07-18 2018-11-30 广西南宁荣威德新能源科技有限公司 一种用于去除花生油中黄曲霉毒素的吸附剂的制备方法
CN110201649A (zh) * 2019-06-09 2019-09-06 桂林理工大学 一种硅藻土表面As（Ⅲ）离子印迹吸附材料的制备方法
CN110201648A (zh) * 2019-06-09 2019-09-06 桂林理工大学 一种硅藻土表面As（Ⅴ）离子印迹吸附材料的制备方法
CN113812469A (zh) * 2021-09-27 2021-12-21 浙江大学 一种食用油中黄曲霉素的去除方法
RU2832644C1 (ru) * 2024-02-16 2024-12-26 Федеральное государственное бюджетное образовательное учреждение высшего образования "Дагестанский государственный аграрный университет имени М.М. Джамбулатова" (ФГБОУ ВО Дагестанский ГАУ) Способ комбинированной очистки воды

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5770090A (en) * 1989-07-28 1998-06-23 Lewis, Iii; Tom Method for recovery of heavy metal from waste water
CN101508503A (zh) * 2009-03-31 2009-08-19 南通大学 降解废水中持久性有机污染物的耦合生化反应器

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5770090A (en) * 1989-07-28 1998-06-23 Lewis, Iii; Tom Method for recovery of heavy metal from waste water
CN101508503A (zh) * 2009-03-31 2009-08-19 南通大学 降解废水中持久性有机污染物的耦合生化反应器

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
MUZZARELLI ET AL.: "Chitosan as a tool for the purification of waters, CODEN: 55MHAB", CHITIN NAT. TECHNOL., [PROC. INT. CONF. CHITIN CHITOSAN], 3RD(1986), MEETING DATE 1985, 1986, pages 551 - 554 *

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2014064073A1 (fr) * 2012-10-26 2014-05-01 Clariant International Ltd. Procédé et composition d'épuration d'eau et de déshydratation de boues
WO2014171812A3 (fr) * 2013-04-18 2015-05-07 ZAINAL ABIDIN, Roslan Bin Composition permettant de traiter les eaux usées
CN104903252A (zh) * 2013-04-18 2015-09-09 北京东方协和医药生物技术有限公司 用于处理废水的组合物
CN104001480A (zh) * 2014-05-30 2014-08-27 扬州天辰精细化工有限公司 一种球形水处理剂的制备方法
RU2645131C1 (ru) * 2017-07-18 2018-02-15 Андрей Александрович Нестеренко Способ получения сорбционного материала
CN108905982A (zh) * 2018-07-18 2018-11-30 广西南宁荣威德新能源科技有限公司 一种用于去除花生油中黄曲霉毒素的吸附剂的制备方法
CN110201649A (zh) * 2019-06-09 2019-09-06 桂林理工大学 一种硅藻土表面As（Ⅲ）离子印迹吸附材料的制备方法
CN110201648A (zh) * 2019-06-09 2019-09-06 桂林理工大学 一种硅藻土表面As（Ⅴ）离子印迹吸附材料的制备方法
CN113812469A (zh) * 2021-09-27 2021-12-21 浙江大学 一种食用油中黄曲霉素的去除方法
RU2832644C1 (ru) * 2024-02-16 2024-12-26 Федеральное государственное бюджетное образовательное учреждение высшего образования "Дагестанский государственный аграрный университет имени М.М. Джамбулатова" (ФГБОУ ВО Дагестанский ГАУ) Способ комбинированной очистки воды

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