US20070123420A1 - Anion adsorbing carbon material, as well as manufacturing method and manufacturing facilities for same - Google Patents

Anion adsorbing carbon material, as well as manufacturing method and manufacturing facilities for same Download PDF

Info

Publication number
US20070123420A1
US20070123420A1 US10/581,578 US58157804A US2007123420A1 US 20070123420 A1 US20070123420 A1 US 20070123420A1 US 58157804 A US58157804 A US 58157804A US 2007123420 A1 US2007123420 A1 US 2007123420A1
Authority
US
United States
Prior art keywords
carbon material
above described
solution
carbonized
anion adsorbing
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.)
Abandoned
Application number
US10/581,578
Other languages
English (en)
Inventor
Satoshi Hayashi
Riei Yokoyama
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.)
Nisshoku Corp
Original Assignee
Nisshoku Corp
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
Priority claimed from JP2004194432A external-priority patent/JP3718517B1/ja
Priority claimed from JP2004244656A external-priority patent/JP3822888B2/ja
Application filed by Nisshoku Corp filed Critical Nisshoku Corp
Assigned to NISSHOKU CORPORATION reassignment NISSHOKU CORPORATION ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: HAYASHI, SATOSHI, YOKOYAMA, RIEI
Publication of US20070123420A1 publication Critical patent/US20070123420A1/en
Priority to US11/923,429 priority Critical patent/US8222182B2/en
Abandoned legal-status Critical Current

Links

Images

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
    • C02F1/283—Treatment of water, waste water, or sewage by sorption using coal, charred products, or inorganic mixtures containing them
    • 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
    • B01J20/30—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
    • B01J41/00—Anion exchange; Use of material as anion exchangers; Treatment of material for improving the anion exchange properties
    • B01J41/08—Use of material as anion exchangers; Treatment of material for improving the anion exchange properties
    • B01J41/18—Carbon, coal or tar
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B32/00—Carbon; Compounds thereof
    • C01B32/05—Preparation or purification of carbon not covered by groups C01B32/15, C01B32/20, C01B32/25, C01B32/30

Definitions

  • This invention relates to an anion adsorption carbon material for adsorbing anions such as nitrate ions and fluoride ions, as well as a manufacturing method and a manufacturing facilities for the same.
  • Contamination of a water quality and soil by heavy metals, agricultural chemicals and an organochlorine compounds has become a problem in that it destroys the environment. Though these harmful substances can be adsorbed and removed with adsorbents such as activated carbon and a zeolite, it is presently difficult to treat nitrate nitrogen, nitrite nitrogen, fluorine, arsenic and cyan which exist in the form of anions with adsorbents.
  • nitrate nitrogen and nitrite nitrogen are included in fertilizers used in tea fields, turfs for golfing and the like, and have become a factor in ground water contamination, which is presently a large problem.
  • nitrate ions and nitrite ions have negative charge and do not become insoluble salt by combining with other chemical substances, and therefore, very easily washes out from negatively charged soil.
  • measures against the above described problem are r there are limitations, such that anaerobic conditions are required in biological treatment where, for example, denitrifying bacteria are used to remove nitrate ions and nitrite ions, and in addition, there are similar limitations with other methods, and no effective measures have been found.
  • nitrate nitrogen and nitrite nitrogen are environmental hormones.
  • fluorine is included in wastewater from semiconductor factories, glass factories, plating factories and the like, and though a method for adding calcium compounds to fluorine in industrial wastewater so that the fluorine can be removed in the form of calcium fluorine is used, further installation of adsorption towers having an anion exchange resin for active alumina and fluorine is required, raising the cost.
  • expensive dedicated anion exchange resins are required in order to meet the Japanese environmental standard of 0.8 mg/L.
  • expensive anion exchange resins are separately required for treating arsenic, cyan and the like, which are included in industrial wastewater and ground water.
  • charcoal which is a representative porous material, together with activated carbon, is widely used as a humidity controller, liver purifier and soil conditioner, and is used for removing chlorine based gases and sulfur oxides in waste gas, for example, it simply uses the adsorptive properties of micro pores inside porous carbon materials, in the same manner as activated carbon, and nitrate nitrogen, nitrite nitrogen, fluorine, arsenic, cyan and the like which exist in the form of anions are barely absorbed.
  • This invention is provided taking the above described situation into consideration, and an object thereof is to provide an anion adsorbing carbon material which is inexpensive, environmentally friendly and excellent in the anion adsorption, as well as a manufacturing method and a manufacturing facilities for the same.
  • a solution including calcium ions for example, a solution (lime water) or suspension (milk of lime) of a calcium hydroxide with a raw material which comprises plant(s), in advance, that is, before carbonizing this material, so that Ca (calcium) is introduced into this material, after that, carbonizing this material into which Ca has been introduced and contacting the gained charcoal into which Ca has been introduced with an acid such as HCl, H 2 SO 4 or the like, and as a result, found that the material had excellent anion adsorption ability.
  • wastewater is treated simply by neutralizing the acid, which is environmentally friendly.
  • a calcium acetate solution, a calcium chloride solution and the like can be cited, in addition to lime water and milk of lime, and a solution including 0.03 weight % to 30 weight % of calcium, preferably 0.1 weight % to 7.0 weight %, is appropriate.
  • a manufacturing method for an anion adsorbing carbon material according to claim 1 is characterized in that a raw material which comprises plant(s) is contacted with a solution including calcium ions, and after that, carbonized, and subsequently, contacted with an acid solution.
  • a manufacturing method for an anion adsorbing carbon material according to claim 2 is characterized in that a raw material which comprises plant(s) with which a solution including calcium ions have contacted is carbonized and the carbonized material is contacted with an acid solution.
  • a manufacturing method for an anion adsorbing carbon material according to claim 3 is characterized in that a carbonized material gained by carbonizing a raw material which comprises plant(s) with which a solution including calcium ions have contacted is contacted with an acid solution.
  • any plant can be applied, a material of one or more from among natural fibers and biomass materials, which makes the carbonized material of the above described material porous, is desirable, and any type of wood material, such as thinning, lumber and waste wood, as well as natural fibers such as hemp, can be cited as examples.
  • the above described material in the case where a solution (for example, lime water or milk of lime) barely including anions (for example, chloride ions) that can be ion exchanged with anions that are the object of adsorption and including calcium ions is used as the solution with which the above described material is contacted, it is desirable for the above described material to be a material where innumerable particles of a calcium compound having a diameter of no greater than 100 nm are formed in the micro pores of a carbonized material when the material is carbonized after calcium has been introduced, and concretely, it is preferable to use ligneous chips of a size of no greater than 10 mm gained by processing a conifer, such as Japanese cypress or cedar having high water absorbency.
  • a conifer such as Japanese cypress or cedar having high water absorbency.
  • a solution for example, a calcium chloride solution
  • anions for example, chloride ions
  • anions for example, chloride ions
  • bamboo, sawdust, chaff, coconut palm, betel-nut palm, jute and straw can be used as the material originating from plant(s).
  • agricultural waste such as peels and pulp from mandarin oranges and apples
  • mandarin oranges and apples can be cited as the above described material originating from plant(s).
  • portion of plants having conductive tissue are particularly preferable as the material originating from plant(s).
  • a solution including calcium ions for example, lime water or milk of lime
  • a raw material which comprises plant(s) contacts with a raw material which comprises plant(s).
  • the solution soaks into the material, and thereby, chips into which Ca has been introduced can be gained.
  • an alkali solution for ample, lime water
  • FIG. 7 (A) the solution including calcium ions
  • organic matter in capitaous chips 2 is dissolved in alkali, and calcium ions react with a certain component of ligneous chips 2 .
  • the solution including calcium ions it is preferable for the solution including calcium ions to contain 0.03 weight % to 30 weight % of calcium, and it is more preferable for it to contain 0.1 weight % to 7.0 weight %.
  • a raw material which comprises plant(s) which has been contacted with a solution including calcium ions is carbonized, and after that, an acid solution contacts with this carbonized material, and thereby, functional groups which have been drawn out form the walls of micro pores in the carbonized material are combined with anions which can be ion exchanged with anions that are the object of adsorption.
  • the present inventors found that more functional groups of the carbonized material can be generated during the process of carbonization by controlling the temperature and the time.
  • the present inventors confirmed that in the case where calcium has contacted with a material as that described above in advance, as in the invention according to claim 1 , and the material is cooled naturally after the temperature for carbonization of 650° C. to 750° C. has been maintained for, for example, one hour, more functional groups can be formed, in comparison with the case where the material is cooled naturally after the temperature for carbonization of approximately 600° C. or approximately 800° C. has been maintained for one hour.
  • a material was contacted with a calcium and carbonized at a temperature for carbonization of 650° C. to 750° C. as described above, and observed through an electron microscope, a state where microscopic particles of the calcium compound half deposited on the surface of walls of the micro pores as described above and were uniformly dispersed was observed.
  • a raw material which comprises plant(s) is contacted with a solution including calcium ions, and after that, carbonized, and an acid solution contacts with this carbonized material.
  • a solution including calcium ions for example
  • calcium ions which have combined with functional groups on the surface of the walls of the micro pores in Ca charcoal 31 and the above described functional groups [see FIG. 9 (B)] combine with chloride ions [see FIG. 9 (C)], so that acid treated Ca charcoal 32 [see FIG. 9 (D)] where chloride ions combine with these functional groups directly or via calcium ions is gained.
  • the concentration of the acid solution is no lower than 0.01 mol/L that is to say, in a range from 0.01 mol/L to 20 mol/L, and a range from 0.1 mol/L to 10 mol/L is preferable.
  • a concentration of lower, than 0.01 mol/L has a disadvantage, such that sufficient effects cannot be gained.
  • the acid solution to include anions which can be ion exchanged with anions that are the object of adsorption
  • anions which can be ion exchanged with anions that are the object of adsorption are included in the solution with which the material originating from plant(s) is contacted before carbonization.
  • the present inventors found, as a result of diligent research, that in the case where a raw material which comprises plant(s) has been contacted with a solution including a metal chloride, for example, a solution including CaCl 2 , in advance, so that CaCl 2 is introduced into the material before this material is carbonized, and after that, this material into which CaCl 2 has been introduced is carbonized, the carbonized material gained as a result of this has excellent anion absorbing performance.
  • a solution including a metal chloride for example, a solution including CaCl 2
  • a manufacturing method for an anion adsorbing carbon material according to claim 4 is characterized in that a raw material which comprises plant(s) is contacted with a solution including a metal chloride, and after that, carbonized, and the above described metal chloride is contained within this carbonized material. Chloride ions of the metal chloride that is contained within the carbonized material exhibit anion exchanging ability, and therefore, the carbonized material functions as an anion adsorbing carbon material.
  • the method for contacting the solution that includes a metal chloride with the above described material originating from plant(s) though dripping, application, spraying, atomization and the like of the above described solution are possible, immersion of the above described material in the above described solution is most efficient.
  • the concentration of the above described CaCl 2 solution M that is used for pre-processing (contact processing) on the material 0.1 weight % to 50 weight % of CaCl 2 is preferable, and 1 weight % to 20 weight % is more preferable, in terms of cost.
  • the concentration is lower than 0.1 weight %, high anion adsorbing ability is not gained, while in the case where the concentration exceeds 50 weight %, the anion adsorbing ability does not increase.
  • FIG. 15 (A) a carton material 37 is gained, as shown in FIG. 15 (C) During this process of carbonization, organic matter in chips 35 into which CaCl 2 has been introduced decomposes due to heat, and at the same time, chloride ions and calcium ions deposit on the surface of the walls of the micro pores in chips 35 into which CaCl 2 has been introduced.
  • FIG. 15 (B) chloride ions and calcium ions deposit on the surface of the walls of the micro pores in chips 35 , into which CaCl 2 has been introduced, in a fine and highly dispersed state, and draw out many functional groups from every corner in the walls of the micro pores.
  • a manufacturing method for an anion adsorbing carbon material according to claim 5 is characterized in that a raw material which comprises plant(s) with which a solution including a metal chloride have contacted is carbonized and the above described metal chloride is contained within this carbonized material. That is to say, in the case a raw material which comprises plant(s) with which a solution including a metal chloride has contacted is prepared in advance, the same anion adsorbing carbon material as that in the invention according to claim 4 can be gained, simply by carbonizing this material.
  • the metal compound which combines within the carbonized material is a metal chloride excluding metal chlorides which simply adhere to the inside of the carbonized material, that is to say, a metal chloride which combines within the carbonized material, and therefore, remains undissolved after being washed with water or an acid.
  • the anion adsorbing ability becomes inferior, while, in the case where the content exceeds 25%, the anion absorbing ability tends not to increase.
  • the above described carbonized material is contacted with water and/or an acid in the invention according to any of claims 4 to 6 (claim 7 ).
  • the method for contacting water and/or an acid with the above described carbonized material though dripping, application, spraying, atomization or the like of water and/or acid is possible, immersion of the above described carbonized material in water and/or an acid is most efficient.
  • the reason why it is preferable to contact water add/or an acid with the above described carbonized material can be considered to be as follows. That is to say, when carbon material (CaCl 2 charcoal) 37 which has been gained as shown in FIGS. 14 and 15 is immersed in (contacted with) an acid, for example, hydrochloric acid H or sulfuric acid, as shown in FIG. 16 (A), extra crystal of a metal chloride which adheres to carbon material 37 is removed.
  • hydrochloric acid H is used as the acid, new chloride ions which combine with the functional groups of the above described, carbon material 37 are added, so that the state changes from that shown in FIG. 16 (B) to that shown in FIG.
  • the anion adsorbing ability of the manufactured anion adsorbing carbon material increases, which is preferable.
  • an acid such as hydrochloric acid H
  • extra crystal of a metal chloride adhering to carbon material 37 is removed, and the anionic adsorbing ability increases.
  • any plant can be used, materials of one or more types from natural fibers and ligneous materials of which the carbonized material has micro pores are preferable, and any type of ligneous material, such as thing, lumber, and waste wood, and natural fibers such as hemp can be cited as examples.
  • any type of ligneous material such as thing, lumber, and waste wood, and natural fibers such as hemp can be cited as examples.
  • bamboo, sawdust, chaff, coconut palm, betel-nut palm, jute, straw, agricultural waste, such as peels from mandarin oranges and apples and pulp from mandarin oranges and apples may be used.
  • the portion of plants having conductive tissue are particularly preferable.
  • CaCl 2 and BaCl 2 can be cited as the above described metal chloride (claim 8 ).
  • the temperature for carbonization of the above described material it is preferable for the temperature for carbonization of the above described material to be 400° C. to 1000° C. This is because in the case where the temperature for the carbonization process is lower than 400° C., micro pores are not created, and the performance as a an adsorbing material becomes inferior, while in the case where the above described temperature exceeds 1000° C., adsorbing properties are not gained, due to excessive carbonization.
  • the temperature for the carbonization process is more preferably 500° C. to 900° C., and most preferably approximately 600° C. to 800° C.
  • the anion adsorbing carbon material according to claim 9 is characterized by being manufactured by the manufacturing method for an anion adsorbing carbon material according to any of claim 1 to 8 .
  • anion adsorbing carbon material of this invention may be gained by removing the adsorbed anions from the anion adsorbing carbon material according to claim 9 which has adsorbed anions and combining anions which can be ion exchanged with anions which are the next object of adsorption with the carbon material in place of the above described removed anions (claim 10 ).
  • anions which can be adsorbed by the anion adsorbing carbon material of this invention are anions which can be an ion exchanged with anions that have combined in advance with the surface of the walls of the micro pores in the carbon material, and are naturally anions excluding the anions which have combined with functional groups on the surface of the walls of the micro pores in the above described carbon material directly or via metal ions.
  • a manufacturing facilities for an anion adsorbing carbon material according to claim 11 is characterized by comprising a carbonization apparatus for carbonizing a raw material which comprises plant(s) and an apparatus for contacting a carbonized material which is produced by this carbonization apparatus with an acid solution.
  • a carbonization furnace which allows for setting of the temperature for carbonization is used as the carbonization apparatus.
  • any type of well-known container for an acid solution such as an acid-resistant tank, can be used as the apparatus for contacting the carbonized material which is produced by this carbonization apparatus with an acid solution.
  • a manufacturing facilities for an anion adsorbing carbon material according to claim 12 is characterized by comprising an apparatus for contacting a raw material which comprises plant(s) with a solution including calcium ions, a carbonization apparatus for carbonizing the above described material after it has been contacted with the solution, and an apparatus for contacting the carbonized material which has been produced by this carbonization apparatus with an acid solution.
  • any type of well-known container such as a tank
  • a carbonization furnace which allows for setting of the temperature for carbonization is used as the carbonization apparatus.
  • any type of well-known container for an acid solution such as an acid-resistant tank, can be used as the apparatus for contacting the carbonized material which is produced by this carbonization apparatus with an acid solution.
  • a raw material which comprises plant(s) is carbonized, and after that, this carbonized material is contacted with an acid solution, and thereby, anions which can be ion ex with anions that are the object of absorption can combine with functional groups which have formed on the walls of micro pores in the carbonized material originating from plant(s) directly or via calcium ions
  • a raw material which comprises plant(s) which has contacted with a solution including calcium ions is carbonated, and after that, this carbonated material is contacted with an acid solution, and thereby, anions which can be ion exchanged with anions that are the object of absorption can combine with functional groups which have been formed by being drawn out from the walls of the micro pores in the carbonized material directly or via calcium ions.
  • the carbonization apparatus may allow for the formation of micro pores inside the carbonized material originating from plant(s), as well as the formation of a great number of functional groups on these walls of the micro pores, and the apparatus for contacting the carbonized material with an acid solution may allow for the combination of the above described functional groups with anions which can be ion exchange with anions that are the object of absorption directly or via calcium ions (claim 13 ).
  • the present inventors found, as a result of diligent research, that more functional groups of the material can be created by controlling the temperature and the time during the process of carbonation. That is to say, in the case where no calcium is introduced into the above described material, as in the invention according to claim 11 , the difference in the amount of created functional groups of the carbonized material is small, irrespectively of the temperature for heating at the time of carbonization. Meanwhile, the present inventors confirmed that in the case where calcium is introduced into the above described material in advance, as in the invention according to claim 12 , more functional groups can be formed in the case where the material is naturally cooled after the temperature for carbonization of approximately 650° C. to 750° C. has been maintained for, for example, one hour, in comparison with a case where the material is naturally cooled after the temperature for carbonization of approximately 600° C. or approximately 800° C. has been maintained for one hour.
  • the temperature for carbonization was approximately 800° C.
  • the state was such that there were many missing portions.
  • approximately 650° C. to 750° C. can be cited as the temperature for carbonization which is required for calcium to draw out as many functional groups as possible from the surface of the walls of the micro pores in the carbonized material, as described above.
  • the concentration of the acid solution is no lower than 0.01 mol/L, that is to say, in a range from 0.01 mol/L to 20 mol/L, and a range from 0.1 mol/L to 10 mol/L is preferable.
  • a concentration of lower than 0.01 mol/L has a disadvantage, such that sufficient effects cannot be gained.
  • the acid solution to include anions which can be ion exchanged with anions that are the object of adsorption
  • anions which can be ion exchanged with anions that are the object of adsorption are included in the solution with which the material originating from plant(s) is contacted before carbonization.
  • an acid solution for example, an HCl solution
  • anions for example, chloride ions, which can be ion exchanged with anions, for example, nitrate nitrogen or nitrite nitrogen, which is the object of absorption, can combine with the functional groups which formed on the surface of the walls of the micro pores in the carbonized material originating from plant(s).
  • an acid solution for example, an HCl solution
  • anions for example, chloride ions, which can be ion exchanged with anions, for example, nitrate nitrogen or nitrite nitrogen, which is the object of adsorption
  • the manufacturing facilities for an anion adsorbing carbon material according to claim 14 is characterized by comprising a carbonization apparatus for carbonizing a raw material which comprises plant(s) which has contacted with a solution including a metal chloride.
  • a carbonization furnace for allowing for the setting of the temperature for carbonization is used as the carbonization apparatus.
  • the manufacturing facilities for an anion adsorbing carbon material according to claim 15 is characterized by comprising an apparatus for contacting a raw material which comprises plant(s) with a solution including a metal chloride and a carbonization apparatus for carbonizing the above described material after it has contacted with the solution.
  • a carbonization furnace for allowing for the setting of the temperature for carbonization is used as the carbonization apparatus.
  • an apparatus for contacting a solution including a metal chloride with the above described material originating from plant(s) though an apparatus for dripping the above described solution, an apparatus for applying the above described solution, an apparatus for spraying the above described solution, an apparatus for atomizing the above described solution and the like are possible, an immersion apparatus for immersing the above described material in the above described solution is most efficient.
  • the metal chloride which combines within the above described carbonized material is a metal chloride excluding metal chlorides which simply adhere to the inside of the carbonized material, that is to say, a metal chloride which combines within the carbonized material, and therefore, remains undissolved after being washed with water or an acid.
  • the anion adsorbing ability becomes inferior, while, in the case where the content exceeds 25%, the anion absorbing ability tends not to increase. Accordingly, it is desirable for 2% to 25% of the metal chloride which combines within the carbonized material to be contained as an ash component.
  • a carbonization apparatus may carbonize a raw material which comprises plant(s), form micro pores inside, and draw out a great number of functional groups to the surface of the walls of these micro pores, and combine anions which can be ion exchanged with anions that are the object of adsorption directly or via metal ions (claim 16 ).
  • anions which can be adsorbed by the anion adsorbing carbon material are anions which can be ion exchanged with anions that have combined in advance with the surface of the walls of the micro pores in the carbon material, and are naturally anions excluding the anions included in the metal chloride which has combined with functional groups on the surface of the walls of the micro pores in the above described carbon material directly or via metal ions.
  • An apparatus for contacting a carbonized material which has been created by the above described carbonization apparatus with water and/or an acid solution, to remove extra crystal of the metal chloride which adheres to the carbonized material, and to increase anion adsorbing ability may be provided (claim 17 ).
  • the method for contacting the above described carbonized material with water and/or an acid though dripping, application, spraying, atomization or the like of water and/or acid is possible, immersion of the above described carbonized material in water and/or an acid is most efficient.
  • the configuration may be provided with a drying area for an intermediate body for gaining an anion adsorbing carbon material so that the above described intermediate body is dried in this drying area using heat discharged from the carbonization apparatus (claim 18 ).
  • the temperature for carbonization in the above described carbonization apparatus may be 400° C. to 1000° C.
  • this temperature for carbonization is preferably 500° C. to 900° C., and is more preferably 650° C. to 750° C.
  • a raw material which comprises plant(s) is contacted with a solution including calcium ions, and after, that, carbonized, and subsequently, was contacted with an acid solution, a raw material which comprises plant(s) which has contacted with a solution including calcium ions is carbonized, and this carbonized material is contacted with an acid solution, or a carbonized material gained by carbonizing a raw material which comprises plant(s) which has contacted with a solution including calcium ions is contacted with an acid solution, and therefore, an anion adsorbing carbon material having anion adsorbing properties equal or superior to those of an anion exchange resin can be gained by setting an appropriate temperature for carbonization.
  • an anion adsorbing carbon material manufactured in accordance with the above described manufacturing method for an anion adsorbing carbon material has a material originating from plant(s) as a main body and is environmentally friendly.
  • an anion adsorbing carbon material having anion adsorbing properties which are equal or superior to those of an anion exchange resin can be gained. Furthermore, this anion adsorbing carbon material has a raw material which comprises plant(s) as a main body and is environmentally friendly.
  • the adsorbed anions are removed from the above described anion adsorbing carbon material, and anions which can be ion exchanged with anions that are the next object of adsorption are combined with the above described anion adsorbing carbon material in place of the above described removed anions, and thereby, the above described anion adsorbing carbon material can be repeatedly restored for use.
  • a carbonization apparatus for carbonizing a raw material which comprises plant(s) and an apparatus for contacting a carbonized material which has been created in this carbonization apparatus with an acid solution are provided, and therefore, an acid solution can contact with the walls of the micro pores in the carbonized material, and thus, anions which can be ion exchanged with anions that are the object of adsorption can be combined with the functional groups which have formed on the walls of the above described micro pores.
  • an apparatus for contacting a raw material which comprises plant(s) with a solution including calcium ions, a carbonization apparatus for carbonizing the above described material after it has been contacted with the solution, and an apparatus for contacting a carbonized material which has been created by this carbonization apparatus with an acid solution are provided, and therefore, an acid solution can contact with the walls of the micro pores of a carbonized material, and anions which can be ion exchanged with anions that are the object of adsorption can be combined with the functional groups which have been drawn out from and formed on the walls of the above described micro pores directly or via calcium ions.
  • an anion adsorbing carbon material having anion adsorbing ability can be gained without any problems in the treatment of wastewater with Fe, unlike in the case where a raw material which comprises plant(s) is immersed in a solution of iron chloride after being carbonized.
  • an anion adsorbing carbon material having anion adsorbing properties which are equal or superior to those of an anion exchange resin can be gained by setting an appropriate temperature for carbonization when a raw material which comprises plant(s) is contacted with a solution including calcium ions, and after that, carbonized.
  • a raw material which comprises plant(s) is carbonized, and thereby, micro pores are formed inside, and a great number of functional groups are formed on the walls of these micro pores, and therefore, these functional groups can combine with anions which can be ion exchanged with anions that are the object of adsorption directly or via calcium ions, so that the anion adsorption ability of the carbonized material can be efficiently increased.
  • chloride ions of the metal chloride which is contained within the carbonized material exhibit anion exchanging ability, and therefore, the carbonized material functions as an anion adsorbing carbon material.
  • the above described carbonization apparatus carbonizes a raw material which comprises plant(s) so that micro pores are formed inside and a great number of functional groups are drawn out to the surface of the walls of these micro pores, and at the same time, anions (for example, Cl—) which can be ion exchanged with anions (for example, NO 3 —) that are the object of adsorption are combined with these functional groups directly or via metal ions (claim 16 ), the anion adsorption ability can be efficiently increased by carbonizing a raw material which comprises plant(s) which has contacted with a metal chloride.
  • anions for example, Cl—
  • anions for example, NO 3 —
  • the anion adsorption ability of the anion adsorbing carbon material can further be increased, which is preferable.
  • the configuration is provided with a drying area for drying an intermediate body for gaining an anion adsorbing carbon material, so that the above described intermediate body is dried by using the heat that is discharged from the carbonization apparatus in this drying area (claim 18 ), the time for heating which is required for carbonizing this intermediate body can be shortened.
  • this intermediate body is dried, and thereby, a lightweight anion adsorbing carbon material which is easy to handle can be gained.
  • an intermediate body is dried using discharged heat in the drying area, and therefore, energy can be used efficiently.
  • FIG. 1 is a diagram showing the configuration of the entirety of the first embodiment.
  • FIG. 2 is a diagram illustrating the entirety of the manufacturing process according to the above described embodiment.
  • FIG. 3 is a diagram showing the configuration of the entirety of the second embodiment.
  • FIG. 4 is a diagram illustrating the entirety of the manufacturing process according to the second embodiment.
  • FIG. 5 is a graph respectively showing the amount of nitrate nitrogen and nitrite nitrogen adsorbed by anion adsorbing carbon materials which are gained in the first and second embodiments during adsorption testing.
  • FIG. 6 is a graph respectively showing the amount of fluoride ions adsorbed by anion adsorbing carbon materials which are gained in the first and second embodiments during adsorption testing.
  • FIG. 7 is a diagram showing the steps in contacting a raw material which comprises plant(s) with a solution including calcium ions in the second embodiment.
  • FIG. 8 is a diagram showing the steps in carbonizing the above described material after it has been contacted with the solution in the second embodiment.
  • FIG. 9 is a diagram showing the steps in contacting a carbonized material which has been created by the carbonization apparatus with an acid solution in the second embodiment.
  • FIG. 10 is a diagram showing the mechanism for nitrate ion adsorption in an anion adsorbing carbon material gained in the second embodiment.
  • FIG. 11 is a diagram schematically showing the configuration of a facilities for manufacturing an anion adsorbing carton material according to the third embodiment of this invention.
  • FIG. 12 (A) is a diagram showing an example of an anion adsorbing carbon material
  • FIG. 12 (B) is a diagram showing an example of the above described anion adsorbing carbon material after processing.
  • FIG. 13 is a diagram showing an example of a process for manufacturing a carbon material as that described above using the above described manufacturing facilities.
  • FIGS. 14 (A) to 14 (C) are diagrams showing a detail in Step S 2 in FIG. 13 .
  • FIGS. 15 (A) to 15 (C) are diagrams showing a detail in Step S 4 in FIG. 13 .
  • FIGS. 16 (A) to 16 (C) are diagrams showing a detail in Step S 5 in FIG. 13 .
  • FIGS. 17 (A) to 17 (D) are diagrams showing a detail during adsorption of nitrate ions in the above described embodiment
  • FIG. 17 (E) is a diagram showing the carbon material after restoration.
  • FIG. 18 is a graph showing the results of comparison of the adsorbed amount of nitrate nitrogen/nitrite nitrogen between the above described carbon material and a material for comparison.
  • FIG. 19 is a graph respectively showing the amount of nitrate nitrogen adsorbed by a carbon material which has been prepared by changing the concentration of a CaCl 2 solution in Step S 2 and by a carbon material gained through HCl treatment.
  • FIG. 20 is a graph show the results of comparison of the adsorbed amount of fluoride ions between the above described carbon material and material for comparison.
  • FIGS. 1 and 2 show the first embodiment of this invention.
  • 1 indicates a carbonization furnace (an example of a carbonization apparatus for carbonizing a raw material which comprises plant(s)) for carbonizing a biomass material (an example of a raw material which comprises plant(s)) 2 of plant(s), for example, natural fibers, including hemp, or lumber, without activating the material.
  • Ligneous chips for example, are used as the above described material 2 . These bambooous chips are gained by processing a conifer, such as Japanese cypress or cedar having high water absorbency and have a size of no greater than, for example, 10 mm.
  • Apparatus for acid treatment 3 treats charcoal A in chip form that has been gained in carbonization furnace 1 with acid.
  • acid treated charcoal an example of an intermediate body S which can be used immediately after acid treatment is used as it is.
  • the above described charcoal S may be neutralized with alkali after acid treatment if necessary, and in this case, (3) the neutralized acid treated charcoal S may be washed with water if necessary.
  • 6 indicates a drier for drying acid treated charcoal S after acid treatment or acid treated charcoal S after acid treatment, neutralization and washing with water using the heat discharged from the carbonization furnace. Here, drying may be omitted if the charcoal is used in a moist state.
  • 6 a indicates a processing portion for processing the dried acid treated charcoal S.
  • 7 indicates a product in pellet form which has been processed from the above described dried acid treated charcoal S
  • 8 indicates a product which has been formed by crushing dried acid treated charcoal S.
  • the products are processed in different ways, depending on the application.
  • another product, where dried acid treated charcoal S is stuck to an unwoven cloth, for example can be cited, in addition to products 7 and 8 .
  • FIGS. 3 and 4 show the seed embodiment of this invention.
  • acid treated Ca charcoal 32 which is an example of an anion adsorbing carbon material is gained by drying ligneous material (an example of a raw material which comprises plant(s)) 2 of plant(s), for example, natural fibers, including hemp or lumber, using dryer 12 after immersion in a solution including calcium ions (for example, lime water C) which is prepared in a Ca introducing apparatus (an example of an apparatus for contacting a raw material which comprises plant(s) with a solution including calcium ions) 9 , and subsequently, carbonizing the material in carbonization furnace (an example of a carbonization apparatus) 1 without activating the material, and after that, immersing the material in acid solution H, for example, HCl or H 2 SO 4 , using apparatus for acid treatment 3 for contacting the carbonized material which has been created by carbonization apparatus 1 with an acid solution, and furthermore, drying the material using dryer 6 and processing the material in processing portion 6 a.
  • a solution including calcium ions for example, lime water C
  • the above described Ca introducing apparatus 9 is an apparatus for introducing Ca into ligneous chips 2 , and is provided with a container 10 which contains a solution including calcium ions in which ligneous chips 2 are immersed.
  • the gained chips 30 into which Ca has been induced are dried using the above described dryer 12 .
  • dryer 12 dries chips 30 into which Ca has been introduced using heat discharged from the carbonization furnace.
  • the efficiency in processing improves when milk of lime is used.
  • a calcium chloride solution or a calcium acetate solution can be used instead of lime water C or milk of lime.
  • the dried chips 30 into which Ca has been introduced are carbonized in carbonization furnace 1 , so that Ca charcoal (an example of an intermediate body made of a carbonized material) 31 in chip form is gained.
  • the temperature for carbonization is 650° C. to 750° C.
  • the above described apparatus for acid treatment 3 is provided with a container 4 which contains acid solution H, for example, HCl or H 2 SO 4 , and mixing blades 5 are provided inside this container 4 .
  • the concentration of this acid solution H is, for example, 5 mol/L.
  • Ca charcoal 31 in chip form that has been gained in carbonization furnace 1 is treated with acid, so that acid treated Ca charcoal 32 is gained.
  • the gained acid treated Ca charcoal (an example of an intermediate body made of a carbonized material) 32 is dried using the above described drier 6 .
  • dryer 6 dries acid treated Ca charcoal 32 using heat discharged from the carbonization furnace.
  • acid treated Ca charcoal 32 which can be used immediately after acid treatment and drying is processed directly into a product as an anion adsorbing material.
  • acid treated Ca charcoal 32 may be neutralized with alkali after treatment with acid if necessary, and in this case, (3) the neutralized acid treated Ca charcoal may be washed with water if necessary.
  • drying may be omitted in the case where the product is used in a moist state.
  • 7 ′ indicates a product in pellet form which is gained by processing acid treated Ca charcoal 32
  • 8 ′ is a product which is formed by crushing acid treated Ca charcoal 32 .
  • the products are processed differently, as shown below, depending on the application.
  • another product where acid treated Ca charcoal 32 is stuck to an unwoven cloth, for example can be cited, in addition to products 7 ′ and 8 ′.
  • chips 30 into which Ca has been introduced and Ca charcoal 31 are prepared in separate factories, and in such cases, manufacturing of acid treated Ca charcoal 32 may start in the middle of the process in each of the above described embodiments.
  • acid treated Ca charcoal 32 can be used as it is, without processing.
  • FIG. 5 shows the comparison in the adsorbing abilities of nitrate nitrogen and nitride nitrogen among the above described respective samples.
  • the charcoal of (1) which was carbonized at 700° C. barely adsorbed nitrate nitrogen or nitrite nitrogen, while the iron chloride charcoal of (2) adsorbed 2.75 mg/g and 2.35 mg/g of nitrate nitrogen and nitrite nitrogen, respectively.
  • acid treated charcoal S of (3) adsorbed 2.50 mg/g and 2.20 mg/g of nitrate nitrogen and nitrite nitrogen, respectively.
  • the anion exchange resin of (5) adsorbed 10.80 mg/g and 10.00 mg/g of nitrate nitrogen and nitrite nitrogen, respectively.
  • FIG. 10 (A) when acid treated Ca charcoal 32 (anion adsorbing carbon material) is immersed in a nitrate solution L, for example, nitrate ions in nitrate solution L are exchanged with chloride ions [see FIG. 10 (B)] which have combined with functional groups on the surface of the walls of the micro pores in acid treated Ca charcoal 32 directly or via calcium ions [see FIG. 10 (C)], and thus, the nitrate ions adsorbed by acid treated Ca charcoal 32 [see FIG. 10 (D)].
  • FIG. 10 (E) shows a change in acid treated Ca charcoal 32 shown in FIG.
  • the above described samples were put into a nitrate solution and the containers were shaken for ten hours under the conditions of, for example, 200 rpm at 20° C., and after that, the concentration of nitrate nitrogen the above described nitrate solution was measured and the amount of adsorption was calculated, and in this manner, the first restoration test was carried out on the above described samples.
  • the above described samples were put into 50 ml (milliliter) of a nitrate solution and the containers were shaken for ten hours under the conditions of, for example, 200 rpm at 20° C., and after that, the concentration of nitrate nitrogen in the above described nitrate solution was measured and the amount of adsorption was calculated, and in this manner, the second restoration test was carried out on the above described samples. This process was repeated two additional times.
  • FIG. 6 shows the comparison in the fluoride ion adsorbing ability among the above described respective samples.
  • the charcoal of (1) carbonized at 700° C. barely adsorbed chloride ions, while the ion chloride charcoal of (2) adsorbed 7.50 mg/g of fluoride ions.
  • acid treated charcoal S of (3) adsorbed 5.00 mg/g of fluoride ions.
  • the anion exchange resin of (5) adsorbed 8.50 mg/g of fluoride ions.
  • the above described samples were put into the above described solution and the containers were shaken for ten hours under the conditions of 200 rpm at 20° C., and after that, the concentration of fluoride ions in the above described solution was measured and the amount of adsorption was calculated, and in this manner, the first restoration test was carried out on the above described samples.
  • the above described samples which had been used in the first restoration test were washed with 1 mol/L of a hydrochloric acid (or sulfuric acid), and furthermore, it was washed with water.
  • the standard solution was exchanged and 50 ml (milliliter) of a solution of which the concentration of fluoride ions was 50 mg/L was prepared as described above, and a restoration test was carried out on 200 mg of the above described samples which had been washed with water as described above. That is to say, the above described samples were put into the containers of 50 ml (milliliter) of the above described solution, and the containers were shaken for ten hours under the conditions of, for example, 200 rpm at 20° C., and after that, the concentration of fluoride ions in the above described solution was measured and the amount of adsorption was calculated, and in this manner, the second restoration test was carried out on the above described samples. This process was repeated two additional times.
  • acid treated charcoal S and acid treated Ca charcoal 32 (anion adsorbing carton material) which are once used can be washed with a hydrochloric acid (or sulfuric acid), and furthermore, it was washed with water, after each use, and thereby, can be used a number of times.
  • FIGS. 11 to 20 show the third embodiment of this invention.
  • FIG. 11 schematically shows an example of a facilities for manufacturing an anion adsorbing carbon material (hereinafter referred to as carbon material) 37 according to the third embodiment of this invention, and in this figure, 2 indicates a plant material which is capitaous chips in this embodiment.
  • These ligneous chips 2 are gained by processing a conifer, such as Japanese cypress or cedar having high water absorbency and have an appropriate size of no greater than, for example, 50 mm.
  • the above described ligneous chips 2 are fed to a process tank 20 (apparatus for contacting a material with a solution including a metal chloride) which contain a metal chloride solution (CaCl 2 solution in this embodiment) M having an appropriate concentration, and within this process tank 20 , a process for introducing a metal chloride (CaCl 2 in this embodiment) is carried out on biomass chips 2 so that chips into which a metal chloride has been introduced (an example of an intermediate body) 35 are formed.
  • 20 a indicates mixing blades which are provided within process tank 20 and are driven by a motor (not shown) so as to rotate, and thus, are used when stirring a liquid or the like within process tank 20 .
  • Chips 35 into which a metal chloride has been introduced and which have been gained as described above are dried using a drier 12 , and after that, fed to a carbonization process furnace 1 (carbonization apparatus) where a carbonization process is carried out on the chips without activation.
  • the above described drier 12 is an example of a drying area for drying chips 35 into which a metal chloride has been introduced and which are an intermediate body for gaining a carbon material 37 , and is formed such that the heat discharged from carbonization process face 1 is used for the above described drying.
  • the main body 1 a of the carbonization furnace which is heated by an appropriate heat source 21 is contained inside the above described carbonization process face 1 .
  • chips 35 into which a metal chloride has been introduced are supplied to the inside of the above described main body 1 a of the carbonization furnace through an introduction portion 1 b, and are heated at an appropriate temperature (described below) and for an appropriate period of time (described below) so as to be carbonized and converted to a carbonized material, and this carbonized material is discharged to the outside of the main body 1 a of the carbonization furnace through a discharging portion 1 c as carbon material 36 , which is an example of an intermediate body.
  • a process tank 22 (apparatus for enhancing the anion adsorbing ability) which contains water or an HCl solution (hydrochloric acid) H, and a process for contacting (immersing) carbon material 36 with (in) water or HCl solution H is carried out within this process tank 22 .
  • 23 indicates mixing blades which are provided within process tank 22 , and are driven by a motor (not shown) so as to rotate, and thus, are used when stirring a liquid or the like within process tank 22 .
  • a process for contacting a material with water is carried out after a process for contacting the material with an acid, or they may be carried out in the opposite order.
  • carbon material (an example of an intermediate body) 37 which has been immersed in water or HCl solution H is fed to a drier 24 so as to be dried, and after that, are formed into grains (pellets) 7 ′′ having an appropriate diameter or further crushed into powder 8 ′ which is finer than gains.
  • the above described drier 24 is an example of a drying area for drying carbon material 37 which is an intermediate body before being processed to pellets 7 ′′ or powder 8 ′′, and is formed so that the heat that is discharged from carbonization process furnace 1 is used for the above described drying.
  • FIG. 12 (A) shows the carbon material 37 which has been formed into chips having a length of approximately 10 mm and
  • FIG. 12 (B) shows an example of grains (pellets) 7 ′′ having an appropriate diameter which have been formed from the above described carbon material 37 in chip form.
  • Step S 2 the above described biomass chips 2 are immersed in CaCl 2 solution M which has been prepared so as to have 1 weight % to 20 weight % within process tank 20 for no less than, for example, three hours. It is preferable to rotate mixing blades 20 a while these ligneous chips 2 are immersed. As a result, CaCl 2 solution M soaks into bambooous chips 2 , and thus, chips 35 into which a metal chloride has been introduced, that is, plantous chips 2 into which calcium ions and chloride ions have been introduced are gained (Step S 2 ).
  • the above described ligneous chips 2 are supplied to main body 1 a of the carbonization furnace in carbonation process furnace 1 , and is heated for approximately one hour in a temperature range (700° C. in this embodiment) from 400° C. to 1000° C. so that a carbonization process is carried out (Step S 4 ). As a result, the carbon material 37 is gained.
  • the above described carbon material 37 is supplied to process tank 22 and is immersed and processed in HCl solution H that has been prepared so as to have 0.01 mol/L to 11 mol/L (for example, 5 mol/L) within process tank 22 (Step S 5 ).
  • HCl solution H that has been prepared so as to have 0.01 mol/L to 11 mol/L (for example, 5 mol/L) within process tank 22 (Step S 5 ).
  • it is preferable to rotate mixing blades 23 and thereby, extra crystal of the metal chloride (CaCl 2 ) which remains within carbon material 37 can be removed and at the same time chloride ions can further be added, and thus, desired carbon material 37 is gained.
  • carbon material 37 after the above described immersion process is dried in general using drier 24 (Step S 6 ).
  • carbon material 37 may be directly fed to drier 24 , or a neutralization process such as ion in an appropriate alkaline solution may be carried out, and additionally, the carbon material may be washed with water after the neutralization process.
  • a neutralization process such as ion in an appropriate alkaline solution
  • the carbon material may be washed with water after the neutralization process.
  • it may not be dried.
  • the above described carbon material 37 is not necessarily manufactured by carrying out all the above described Steps S 1 to S 7 within the same factory. In the case where several steps from among the above described Steps S 1 to S 7 have been carried out during the manufacture in another factory, or the like, carbon material 37 may be manufactured by starting from a step in the middle.
  • this invention is not limited to any of the above described embodiments, and can be implemented by modifying in various manners.
  • BaCl 2 , MnCl 2 , and the like, for example, can be cited as the metal chloride, though CaCl 2 , which allows the anio n adsorbing carbon material having the highest performance to be gained, is used in the above described embodiments.
  • hugh carbon material 37 is fed to process tank 22 after it has been gained by carrying out a carbonization process on chips 35 into which a metal chloride has been introduced in carbonization process furnace 1 , it is not necessary to feed the carbon material to process tank 22 . In this case, it becomes unnecessary to feed the above described carbon material 37 to drier 24 , and therefore, the above described Steps S 5 and S 6 are omitted from the manufacturing method for carbon material 37 . In addition, in this case the manufacturing method for carbon material 37 may be completed with Steps S 1 to S 4 , or Step S 7 may be carried out afterwards.
  • samples in one set were individually put into 50 mL of nitrate nitrogen solution (first standard liquid) of which the concentration of nitrate nitrogen was 50 mg/L (50 ppm) and samples in the other set were individually put into 50 mL of nitrite nitrogen solution (second standard liquid) of which the concentration of nitrite nitrogen was 50 mg/L (50 ppm).
  • first standard liquid the concentration of nitrate nitrogen
  • second standard liquid the concentration of nitrite nitrogen solution
  • the containers of the solutions were shaken for ten hours under the conditions of 200 rpm at 20° C., and then, the concentration of nitrate nitrogen in the first standard liquid and the concentration of nitrite nitrogen in the second standard liquid were respectively measured, and the amount of nitrate nitrogen and nitrite nitrogen which were adsorbed by each sample was calculated.
  • FIG. 18 shows the comparison results in the nitrate nitrogen adsorbing ability and nitrite nitrogen adsorbing ability among the respective samples which were gained in the above described test.
  • this figure shows the amount of nitrate nitrogen and nitrite nitrogen adsorbed by each sample is shown in pairs of bars in a graph, where the bars on the left show the amount of adsorbed nitrate nitrogen and the bars on the right show the amount of adsorbed nitrite nitrogen. It can be seen from the results shown in this graph that all the samples of the present invention have high nitrate nitrogen adsorbing ability and nitrite nitrogen adsorbing ability.
  • the amount of adsorbed nitrate nitrogen and nitrite nitrogen is compared between BaCl 2 charcoal of (4) and HCl processed BaCl 2 charcoal of (5) and the amount of adsorbed nitrate nitrogen and nitrite nitrogen is compared between CaCl 2 charcoal of (6) and HCl processed CaCl 2 charcoal of (7), and they, it can be seen that it is better to carry out a process (HCl process) for immersing carbon material 37 in an HCl solution in order to enhance the nitrate nitrogen/nitrite nitrogen adsorbing ability of carbon material 37 .
  • HCl process for immersing carbon material 37 in an HCl solution in order to enhance the nitrate nitrogen/nitrite nitrogen adsorbing ability of carbon material 37 .
  • carbon material 37 having a sufficiently high nitrate nitrogen/nitrite nitrogen adsorbing ability can be gained without carrying out an HCl process, and in this case, carbon material 37 can be manufactured at a cost which is lower by the portion for carrying out a process for contacting the material with an HCl solution.
  • the above described carbon material 37 adsorbs, for example, nitrate ions, and this is considered to be because, as shown in FIG. 17 (A), when carbon material (CaCl 2 charcoal) 37 is immersed in a nitrate solution L, chloride ions which has been combined with functional groups on the surface of carbon material 37 directly or via calcium ions (see FIG. 17 (B)) and nitrate ions in nitrate solution L are exchanged (see FIG. 17 (C)) so that nitrate ions are adsorbed by carbon material 37 (see FIG. 17 (D)).
  • FIG. 17 (A) when carbon material (CaCl 2 charcoal) 37 is immersed in a nitrate solution L, chloride ions which has been combined with functional groups on the surface of carbon material 37 directly or via calcium ions (see FIG. 17 (B)) and nitrate ions in nitrate solution L are exchanged (see FIG. 17 (C)) so that nitrate ions are adsorbed by carbon
  • FIG. 17 (E) shows a state of carbon material 37 , which was in a state shown in FIG. 17 (D) adsorbing nitrate ions, after being immersed in a chloride solution having a high concentration (for example, a metal chloride solution of KCl or NaCl, or HCl solution H). That is to say, the nitrate ions which have been adsorbed by carbon material 37 are exchanged with chloride ions in chloride solution, and thereby, carbon material 37 is restored and becomes a state where it can adsorb anions such as nitrate ions.
  • a chloride solution having a high concentration for example, a metal chloride solution of KCl or NaCl, or HCl solution H.
  • carbon material 37 of this invention is not always limited to those which are newly gained in accordance with the above described manufacturing method, but may be those which are gained (that is to say, restored) by removing the adsorbed anions (for example, nitrate ions) from carbon material 37 which has been gained in accordance with the above described manufacturing method and has adsorbed anions (nitrate ions) and combining anions (chloride ions in this embodiment) which can be ion exchanged with anions (for example, nitrate ions) of the next object of adsorption with the carbon material instead of the above described removed anion (nitrate ions).
  • anions for example, nitrate ions
  • sulfuric acid is used instead of the above described chloride solution
  • nitrate ions are ion exchanged with sulfate ions instead of the above described chloride ions.
  • the amount of carbon material 37 which was added to each solution was 200 mg.
  • 200 mg of carbon material 37 which was gained by immersing ligneous chips 2 in 10 weight % of CaCl 2 solution M, and after that, heating and carbonizing the chips for one hour at 700° C., and then carrying out an HCl process, was used so that the nitrate nitrogen adsorbing ability thereof was checked.
  • the results of the above described test are shown in FIG. 19 .
  • the anion adsorbing ability of carbon material 37 does not increase in proportion to the concentration of the CaCl 2 solution, and it can be said that it is most preferable for the concentration to be approximately 10 weight % when takin cost and the like into consideration.
  • the above described CaCl 2 charcoal was washed with a KCl (or NaCl) solution of 1 mol/L, and furthermore, it was washed with water and then restored.
  • the restored CaCl 2 charcoal was put in a newly prepared standard liquid (that is to say, 50 mL of a nitrate nitrogen solution of which the concentration of nitrate nitrogen was 50 mg/L), and the container was shaken for ten hours under the conditions of 200 rpm at 20° C., and after that, the concentration of nitrate nitrogen in the above described standard liquid was measured and the amount of nitrate nitrogen adsorbed by the above described CaCl 2 charcoal was calculated.
  • the process starting from the restoration of this CaCl 2 charcoal up to the calculation of the amount of nitrate nitrogen adsorbed by the CaCl 2 charcoal, was carried out three times in total (first restoration time to third time).
  • carbon material 37 (CaCl 2 charcoal) could be used a number of times to adsorb nitrate nitrogen in the case where the carbon material was restored by washing it with a KCl (or NaCl) solution, and then washing it with water.
  • the restoring principle is the same in the case where the above described carbon material 37 (CaCl 2 charcoal) is used to adsorb nitrite nitrogen.
  • FIG. 20 shows the results of comparison in the fluoride ion adsorbing ability among the respective samples which were gained in the above described test. It can be seen from the results shown in this figure that the samples of the present invention all had a high fluoride ion adsorbing ability.
  • the amount of fluoride ions assorted by the BaCl 2 charcoal of (4) and the amount of fluoride ions adsorbed by the HCl processed BaCl 2 charcoal of (5) are compared, and in addition, the amount of fluoride ions adsorbed by the CaCl 2 charcoal of (6) and the amount of fluoride ions adsorbed by the HCl processed CaCl 2 charcoal of (7) are compared, and thereby, it can be seen that it is better to carry out a process (HCl process) of immersing carbon material 37 in an HCl solution in order to enhance the fluoride ion adsorbing ability of carbon material 37 .
  • carbon material 37 having a sufficiently high fluoride ion adsorbing ability, can be gained without carrying out an HCl process, and in this case, carbon material 37 can be manufactured at a cost that is lower by the portion for carrying out a process for contacting the carton material with an HCl solution.
  • the above described CaCl 2 charcoal was washed with a hydrochloric acid (or sulfuric acid) of 1 mol/L, and furthermore, it was washed with water and then restored.
  • the restored CaCl 2 charcoal was put in a newly prepared standard liquid (that is to say, 50 mL of a solution of which the concentration of fluoride ions was 50 mg/L), and the container was shaken for ten hours under the conditions of 200 rpm at 20° C., and after that, the concentration of fluoride ions in the above described standard liquid was measured and the amount of fluoride ions adsorbed by the above described CaCl 2 charcoal was calculated.
  • the process starting from the restoration of this CaCl 2 charcoal up to the calculation of the amount of fluoride ions adsorbed by the CaCl 2 charcoal, was carried out three times in total (first restoration time to third time).
  • carbon material 37 (CaCl 2 charcoal) could be used a number of times to adsorb fluoride ions in the case where the carbon material was restored by washing it with a hydrochloric acid (or sulfuric acid), and then washing it with water.
  • carton material 37 (HCl processed CaCl 2 charcoal), which was gained by processing the chips after carbonization through immersion in an HCl solution, was also restored by washing it with a dense hydrochloric acid (or sulfuric acid) solution, and furthermore, washing it with water after it was used to adsorb fluoride ions.
  • the fluoride ion adsorbing ability of the HCl processed CaCl 2 charcoal which increased by processing the charcoal through immersion in an HCl solution, was maintained (kept increasing) even when the HCl processed CaCl 2 charcoal was repeatedly restored by washing it with a hydrochloric acid (or sulfuric acid), and then washing it with water.
  • An anion adsorbing carbon material according to this invention adsorbs anions such as nitrate nitrogen, nitrite nitrogen and fluorine, and therefore, can be mainly used in the applications, for example, as follows:
  • nitrate nitrogen components such as nitrite ions and nitrate ions as well as fluoride ions which exist in processed sewage water and groundwater are discharged without being treated.
  • An anion adsorbing carbon material of this invention can be used as an inexpensive and effective purifier for processing sewage and groundwater.
  • a purifier for processing sewage having an appropriate size for example, is floated in the sewage or is contained in a cage having an appropriate mesh size or a mesh bag so as to be installed in a state of making sufficient contact with the water to be treated, and thereby, anions such as nitrite ions, nitrate ions and fluoride ions that are included in the water to be treated are adsorbed without fail.
  • anions such as nitrite ions, nitrate ions and fluoride ions that are included in the water to be treated are adsorbed without fail.
  • the purifier in powder form, this may be stuck to an unwoven cloth.
  • An anion adsorbing carbon material of this invention can be used as an inexpensive and effective purifier for processing discharged wastewater.
  • a purifier for processing sewage having an appropriate size for example, is floated in the discharged wastewater or is contained in a cage having an appropriate mesh size or a mesh bag so as to be installed in a state of making sufficient contact with the water to be treated, and thereby, anions such as nitrite ions, nitrate ions and fluoride ions that are included in the water to be treated are adsorbed without fail.
  • the purifier in powder form, this may be stuck to an unwoven cloth.
  • An anion adsorbing carbon material of this invention can be used as an inexpensive and effective purifier for tap water.
  • a purifier for processing tap water having an appropriate size for example, is floated in the tap water or is contained in a cage having an appropriate mesh size or a mesh bag so as to be installed in a state of making sufficient contact with the water to be treated, and thereby, anions such as nitrite ions, nitrate ions and fluoride ions that are included in the water to be treated are adsorbed without fail.
  • anions such as nitrite ions, nitrate ions and fluoride ions that are included in the water to be treated are adsorbed without fail.
  • the purifier in powder form, this may be stuck to an unwoven cloth.
  • An anion adsorbing carbon material of this invention can be used as an inexpensive and effective purifier for farmlands.
  • a purifier for farmlands having an appropriate size for example is mixed with the soil of farmlands or buried deep into the soil of farmlands, and thereby, nitrite ions and nitrate ions which originate from excessive fertilizers or excrements from livestock can be adsorbed, and thus, the amount of nitrite ions and nitrate ions which flow into underground water can be reduced. Furthermore, this purifier for farmlands is effective as a material for physically improving the soil, and in addition, the adsorbed nitrite ions and nitrate ions can be used by plants, and therefore, this purifier for farmlands functions as a fertilizer having gradual effects. Accordingly, the anion adsorbing carbon material of this invention, which has adsorbed nitrite ions and nitrate ions, can be used as a soil improving fertilizer.
  • a tank for breeding creatures for example, a tank in an aquarium and a tank for a business or a home
  • aquatic creatures and amphibians are bred as well as in a culture pond for fish or shrimps
  • ammonia which is then oxidized so as to be converted to nitrite ions or nitrate ions, and when the concentration of these is high, poisoning symptoms may appear in the creatures that are being bred, though the toxicity thereof is gradually reduced.
  • An anion adsorbing carbon material of this invention can be used as an inexpensive and effective purifier for tank water.
  • a purifier for tank water and culture ponds having an appropriate size for example, is floated in the water to be treated or is contained in a cage having an appropriate mesh size or a mesh bag so as to be installed in a state of making sufficient contact with the water to be treated, and thereby, anions such as nitrite ions, nitrate ions and fluoride ions that are included in the water to be treated are adsorbed without fail.
  • anions such as nitrite ions, nitrate ions and fluoride ions that are included in the water to be treated are adsorbed without fail.
  • the purifier in powder form, this may be stuck to an unwoven cloth.
  • An anion adsorbing carbon material according to the present invention adsorbs nitrate nitrogen and nitrite nitrogen, and therefore, can be applied to purification of water, prevention of contamination caused by the livestock industry, and prevention of contamination caused by excessive fertilizing in agriculture.
  • an anion adsorbing carbon material according to the present invention adsorbs fluorine, and therefore, can be applied in final treatment installations in semiconductor factories, glass factories, plating factories and the like, where cleaning is carried out using hydrofluoric acid.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Analytical Chemistry (AREA)
  • Inorganic Chemistry (AREA)
  • Hydrology & Water Resources (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Solid-Sorbent Or Filter-Aiding Compositions (AREA)
  • Carbon And Carbon Compounds (AREA)
US10/581,578 2003-12-05 2004-12-03 Anion adsorbing carbon material, as well as manufacturing method and manufacturing facilities for same Abandoned US20070123420A1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US11/923,429 US8222182B2 (en) 2003-12-05 2007-10-24 Anion adsorbing carbon material, as well as manufacturing method and manufacturing facilities for same

Applications Claiming Priority (11)

Application Number Priority Date Filing Date Title
JP2003407705 2003-12-05
JP2003-407705 2003-12-05
JP2004072362 2004-03-15
JP2004-072362 2004-03-15
JP2004-074074 2004-03-16
JP2004074074 2004-03-16
JP2004-194432 2004-06-30
JP2004194432A JP3718517B1 (ja) 2004-06-30 2004-06-30 陰イオン吸着炭素材料およびその製造方法
JP2004-244656 2004-08-25
JP2004244656A JP3822888B2 (ja) 2004-08-25 2004-08-25 陰イオン吸着炭素材料の製造装置
PCT/JP2004/018058 WO2005053846A1 (ja) 2003-12-05 2004-12-03 陰イオン吸着炭素材料とその製造方法および製造装置

Publications (1)

Publication Number Publication Date
US20070123420A1 true US20070123420A1 (en) 2007-05-31

Family

ID=34658219

Family Applications (2)

Application Number Title Priority Date Filing Date
US10/581,578 Abandoned US20070123420A1 (en) 2003-12-05 2004-12-03 Anion adsorbing carbon material, as well as manufacturing method and manufacturing facilities for same
US11/923,429 Expired - Fee Related US8222182B2 (en) 2003-12-05 2007-10-24 Anion adsorbing carbon material, as well as manufacturing method and manufacturing facilities for same

Family Applications After (1)

Application Number Title Priority Date Filing Date
US11/923,429 Expired - Fee Related US8222182B2 (en) 2003-12-05 2007-10-24 Anion adsorbing carbon material, as well as manufacturing method and manufacturing facilities for same

Country Status (6)

Country Link
US (2) US20070123420A1 (pt)
EP (3) EP1878490A3 (pt)
KR (2) KR100795118B1 (pt)
BR (2) BRPI0419283B1 (pt)
CA (1) CA2546477C (pt)
WO (1) WO2005053846A1 (pt)

Cited By (35)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20100291167A1 (en) * 2008-09-29 2010-11-18 Sony Corporation Porous carbon material composites and their production process, adsorbents, cosmetics, purification agents, and composite photocatalyst materials
US20110135561A1 (en) * 2008-07-31 2011-06-09 Sony Corporation Adsorbent, cleansing agent, renal disease drug, and functional food
US20140361501A1 (en) * 2013-06-05 2014-12-11 Cal-Comp Electronics & Communications Company Limited Carrier
US9114358B2 (en) 2006-08-23 2015-08-25 Sulvaris Inc. Acid-impregnated activated carbon and methods of forming and using the same
US20160023959A1 (en) * 2011-06-06 2016-01-28 Cool Planet Energy Systems, Inc. Biochars and biochar treatment processes
US20170204017A1 (en) * 2011-06-06 2017-07-20 Cool Planet Energy Systems, Inc. Biochars and biochar treatment processes
US9809502B2 (en) 2011-06-06 2017-11-07 Cool Planet Energy Systems, Inc. Enhanced Biochar
US9944538B2 (en) 2013-10-25 2018-04-17 Cool Planet Energy Systems, Inc. System and method for purifying process water
US9963650B2 (en) 2011-07-25 2018-05-08 Cool Planet Energy Systems, Inc. Method for making sequesterable biochar
US9980912B2 (en) 2014-10-01 2018-05-29 Cool Planet Energy Systems, Inc. Biochars for use with animals
US10059634B2 (en) 2011-06-06 2018-08-28 Cool Planet Energy Systems, Inc. Biochar suspended solution
US10065163B2 (en) * 2014-10-01 2018-09-04 Cool Planet Energy Systems, Inc Biochar extracts and method for capturing material extracted from biochar
US10066167B2 (en) 2011-05-09 2018-09-04 Cool Planet Energy Systems, Inc. Method for biomass fractioning by enhancing biomass thermal conductivity
US10118870B2 (en) 2011-06-06 2018-11-06 Cool Planet Energy Systems, Inc. Additive infused biochar
US10173937B2 (en) 2011-06-06 2019-01-08 Cool Planet Energy Systems, Inc. Biochar as a microbial carrier
US10233129B2 (en) 2011-06-06 2019-03-19 Cool Planet Energy Systems, Inc. Methods for application of biochar
US10265670B2 (en) * 2012-01-20 2019-04-23 Cool Planet Energy Systems, Inc. Biochar extracts and method for capturing material extracted from biochar
US10273195B2 (en) 2011-06-06 2019-04-30 Cool Planet Energy Systems, Inc. Method for the bioactivation of biochar for use as a soil amendment
US10301228B2 (en) 2011-06-06 2019-05-28 Cool Planet Energy Systems, Inc. Enhanced biochar
US10322389B2 (en) 2014-10-01 2019-06-18 Cool Planet Energy Systems, Inc. Biochar aggregate particles
US10392313B2 (en) 2011-06-06 2019-08-27 Cool Planet Energy Systems, Inc. Method for application of biochar in turf grass and landscaping environments
US10472297B2 (en) 2014-10-01 2019-11-12 Cool Planet Energy System, Inc. Biochars for use in composting
US10550044B2 (en) 2011-06-06 2020-02-04 Cool Planet Energy Systems, Inc. Biochar coated seeds
US10696603B2 (en) * 2011-06-06 2020-06-30 Carbon Technology Holdings, LLC Mineral solubilizing microorganism infused biochars
US10714750B2 (en) 2007-04-04 2020-07-14 Sony Corporation Porous carbon materials and production process thereof, and adsorbents, masks, adsorbing sheets and carriers
US10870608B1 (en) 2014-10-01 2020-12-22 Carbon Technology Holdings, LLC Biochar encased in a biodegradable material
US11053171B2 (en) 2014-10-01 2021-07-06 Carbon Technology Holdings, LLC Biochars for use with animals
US11097241B2 (en) 2014-10-01 2021-08-24 Talipot Cool Extract (Ip), Llc Biochars, biochar extracts and biochar extracts having soluble signaling compounds and method for capturing material extracted from biochar
US11214528B2 (en) 2011-06-06 2022-01-04 Carbon Technology Holdings, LLC Treated biochar for use in water treatment systems
US11279662B2 (en) 2011-06-06 2022-03-22 Carbon Technology Holdings, LLC Method for application of biochar in turf grass and landscaping environments
US11390569B2 (en) 2011-06-06 2022-07-19 Carbon Technology Holdings, LLC Methods for application of biochar
US11426350B1 (en) 2014-10-01 2022-08-30 Carbon Technology Holdings, LLC Reducing the environmental impact of farming using biochar
US11866329B2 (en) 2017-12-15 2024-01-09 Talipot Cool Extract (Ip), Llc Biochars, biochar extracts and biochar extracts having soluble signaling compounds and method for capturing material extracted from biochar
US12054440B2 (en) 2011-06-06 2024-08-06 Carbon Technology Holdings, LLC Method for application of biochar in turf grass and landscaping environments
US12084392B2 (en) 2011-06-06 2024-09-10 Carbon Technology Holdings, LLC Treated biochar for use in water treatment systems

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101898125B (zh) * 2010-08-02 2012-05-09 清华大学 用于去除水中嗅味物质或重金属离子的竹炭及其制备方法
CN104069808A (zh) * 2014-06-20 2014-10-01 江苏浦士达环保科技有限公司 一种载银椰壳活性炭的制造方法
CN110947362B (zh) * 2019-11-27 2022-05-17 南通大学 一种用于除水中氟的三元改性生物炭及其制备方法

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2003278A (en) * 1933-08-28 1935-05-28 Cleveland Cliffs Iron Preparation of activated carbon
US3168485A (en) * 1960-06-27 1965-02-02 Standard Oil Co Removal of metal contaminants from activated carbon
US3835064A (en) * 1971-09-23 1974-09-10 T Shinomiya Process for manufacturing an activated carbon
US4937223A (en) * 1988-02-10 1990-06-26 Mitsubishi Kasei Corporation Process for preparing activated carbon
US5614459A (en) * 1995-06-07 1997-03-25 Universidad De Antioquia Process for making activated charcoal
US6495730B1 (en) * 1999-09-21 2002-12-17 Asahi Kasei Kabushiki Kaisha Catalysts for hydrogenation of carboxylic acid
US20030179537A1 (en) * 2001-09-11 2003-09-25 Masako Tanaka Activated carbon, method for production thereof and use thereof

Family Cites Families (32)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5427316B2 (pt) 1972-03-10 1979-09-08
JPS4930141A (pt) 1972-07-25 1974-03-18
JPS4954151A (pt) 1972-10-06 1974-05-25
JPS513975A (pt) 1974-06-28 1976-01-13 Takahiko Kondo
JPS5827995B2 (ja) 1975-07-14 1983-06-13 丸善石油株式会社 スイチユウノ ムキセイオヨビ ユウキセイオセンブツオ ドウジニ キユウチヤクシヨリスルホウホウ
JPS5216363A (en) 1975-07-29 1977-02-07 Yawata Kagaku Kougiyou Kk Mixed chmical fertilizer containing activated matter
JPS5234260A (en) 1975-09-09 1977-03-16 Hokuriku Seiren Kk Method of soil improvement using active carbon and elementary ash
JPS6050724B2 (ja) 1977-08-18 1985-11-09 武田薬品工業株式会社 活性炭の製造法
JPS56160312A (en) * 1980-05-15 1981-12-10 Sumitomo Bakelite Co Ltd Manufacture of granular activated carbon
JPS63129007A (ja) 1986-11-15 1988-06-01 Masaru Tanaka 新活性炭の製法と農林業への有効利用
JPH01308818A (ja) * 1988-02-10 1989-12-13 Tatsuaki Yamaguchi 活性炭の製造方法
JP2790328B2 (ja) * 1988-09-07 1998-08-27 武田薬品工業株式会社 薬品賦活成型活性炭並びにその製造法及び用途
CN1040185A (zh) 1989-04-01 1990-03-07 张志强 一种工业生产活性炭的方法
GB8923662D0 (en) 1989-10-20 1989-12-06 Norit Uk Ltd A method of producing granular activated carbon
JPH04122490A (ja) 1990-09-14 1992-04-22 Akio Onda 環境汚染物質の総合的処理利用方法
JP3066145B2 (ja) 1991-03-15 2000-07-17 社会福祉法人北海道リハビリー 活性炭及びその製法
JP2549481B2 (ja) 1992-03-09 1996-10-30 炭平ファイナンス株式会社 連続炭化装置及び連続炭化方法
JP3282238B2 (ja) * 1992-10-15 2002-05-13 三菱化学株式会社 薬品賦活活性炭の製造方法
JP3245485B2 (ja) * 1993-08-05 2002-01-15 ハウス食品株式会社 食品製造用の水の事前処理方法
JPH09225454A (ja) 1996-02-28 1997-09-02 Takeda Chem Ind Ltd 湿潤活性炭及びその保存方法
JP3695845B2 (ja) 1996-06-03 2005-09-14 日本エンバイロケミカルズ株式会社 浄水用材
JPH1017390A (ja) 1996-06-28 1998-01-20 Chie Igami 木質細片炭、その製造方法、木質細片炭を含有する肥料、きのこ廃培地の処理方法およびきのこ廃培地炭化物およびそれを含有した肥料
JPH11106751A (ja) 1997-10-06 1999-04-20 Mokushitsu Fukugou Zairyo Gijutsu Kenkyu Kumiai 土壌改良材及びＳＯｘ吸着材
JP3138749B2 (ja) 1999-01-26 2001-02-26 北海道 植物資材による脱臭能、イオン交換能、触媒能を有する炭化物製造方法
JP2002104816A (ja) * 1999-11-16 2002-04-10 Kuraray Co Ltd 活性炭及びその製造方法
KR100744984B1 (ko) 1999-11-16 2007-08-02 혼다 기켄 고교 가부시키가이샤 전기 이중층 캐패시터용 전극 및 그것의 제조 방법
JP2001232894A (ja) 2000-02-25 2001-08-28 Canon Inc 操作パネル
FR2806072B1 (fr) 2000-03-07 2002-06-07 Air Liquide Charbon actif ameliore par traitement a l'acide et son utilisation pour separer des gaz
JP2002088373A (ja) 2000-09-14 2002-03-27 Shimabara Sangyo Kk チップ状木炭の製造方法及びその装置
CN2469321Y (zh) 2001-01-02 2002-01-02 秦才东 一种连续干馏和炭化装置
US20020177520A1 (en) * 2001-03-30 2002-11-28 Nichias Co., Ltd. Chemical filter
JP4804659B2 (ja) 2001-07-11 2011-11-02 日本植生株式会社 タンパク質吸着用多孔質炭素材料の製造方法

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2003278A (en) * 1933-08-28 1935-05-28 Cleveland Cliffs Iron Preparation of activated carbon
US3168485A (en) * 1960-06-27 1965-02-02 Standard Oil Co Removal of metal contaminants from activated carbon
US3835064A (en) * 1971-09-23 1974-09-10 T Shinomiya Process for manufacturing an activated carbon
US4937223A (en) * 1988-02-10 1990-06-26 Mitsubishi Kasei Corporation Process for preparing activated carbon
US5614459A (en) * 1995-06-07 1997-03-25 Universidad De Antioquia Process for making activated charcoal
US6495730B1 (en) * 1999-09-21 2002-12-17 Asahi Kasei Kabushiki Kaisha Catalysts for hydrogenation of carboxylic acid
US20030179537A1 (en) * 2001-09-11 2003-09-25 Masako Tanaka Activated carbon, method for production thereof and use thereof

Cited By (52)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US9114358B2 (en) 2006-08-23 2015-08-25 Sulvaris Inc. Acid-impregnated activated carbon and methods of forming and using the same
US11955638B2 (en) 2007-04-04 2024-04-09 Sony Corporation Sheet-shaped member
US11545665B2 (en) 2007-04-04 2023-01-03 Sony Corporation Carbon-polymer complex
US10756346B2 (en) 2007-04-04 2020-08-25 Sony Corporation Porous Carbon Material
US10714750B2 (en) 2007-04-04 2020-07-14 Sony Corporation Porous carbon materials and production process thereof, and adsorbents, masks, adsorbing sheets and carriers
US20110135561A1 (en) * 2008-07-31 2011-06-09 Sony Corporation Adsorbent, cleansing agent, renal disease drug, and functional food
US11697106B2 (en) 2008-09-29 2023-07-11 Sony Corporation Porous carbon material composites and their production process, adsorbents, cosmetics, purification agents, and composite photocatalyst materials
US20100291167A1 (en) * 2008-09-29 2010-11-18 Sony Corporation Porous carbon material composites and their production process, adsorbents, cosmetics, purification agents, and composite photocatalyst materials
US10066167B2 (en) 2011-05-09 2018-09-04 Cool Planet Energy Systems, Inc. Method for biomass fractioning by enhancing biomass thermal conductivity
US10550044B2 (en) 2011-06-06 2020-02-04 Cool Planet Energy Systems, Inc. Biochar coated seeds
US10301228B2 (en) 2011-06-06 2019-05-28 Cool Planet Energy Systems, Inc. Enhanced biochar
US10059634B2 (en) 2011-06-06 2018-08-28 Cool Planet Energy Systems, Inc. Biochar suspended solution
US12084392B2 (en) 2011-06-06 2024-09-10 Carbon Technology Holdings, LLC Treated biochar for use in water treatment systems
US12054440B2 (en) 2011-06-06 2024-08-06 Carbon Technology Holdings, LLC Method for application of biochar in turf grass and landscaping environments
US10093588B2 (en) 2011-06-06 2018-10-09 Cool Planet Energy Systems, Inc. Method for enhancing soil growth using bio-char
US10106471B2 (en) * 2011-06-06 2018-10-23 Cool Planet Energy Systems, Inc. Biochars and biochar treatment processes
US10118870B2 (en) 2011-06-06 2018-11-06 Cool Planet Energy Systems, Inc. Additive infused biochar
US10173937B2 (en) 2011-06-06 2019-01-08 Cool Planet Energy Systems, Inc. Biochar as a microbial carrier
US10233129B2 (en) 2011-06-06 2019-03-19 Cool Planet Energy Systems, Inc. Methods for application of biochar
US10252951B2 (en) * 2011-06-06 2019-04-09 Cool Planet Energy Systems, Inc. Biochars and biochar treatment processes
US10023503B2 (en) 2011-06-06 2018-07-17 Cool Planet Energy Systems, Inc. Biochars and biochar treatment processes
US10273195B2 (en) 2011-06-06 2019-04-30 Cool Planet Energy Systems, Inc. Method for the bioactivation of biochar for use as a soil amendment
US11130715B2 (en) 2011-06-06 2021-09-28 Talipot Cool Extract (Ip), Llc Biochar coated seeds
US20160023959A1 (en) * 2011-06-06 2016-01-28 Cool Planet Energy Systems, Inc. Biochars and biochar treatment processes
US10392313B2 (en) 2011-06-06 2019-08-27 Cool Planet Energy Systems, Inc. Method for application of biochar in turf grass and landscaping environments
US20170204017A1 (en) * 2011-06-06 2017-07-20 Cool Planet Energy Systems, Inc. Biochars and biochar treatment processes
US10472298B2 (en) 2011-06-06 2019-11-12 Cool Planet Energy System, Inc. Biochar suspended solution
US11180428B2 (en) 2011-06-06 2021-11-23 Talipot Cool Extract (Ip), Llc Biochar suspended solution
US10556838B2 (en) 2011-06-06 2020-02-11 Cool Planet Energy Systems, Inc. Biochars and biochar treatment processes
US10696603B2 (en) * 2011-06-06 2020-06-30 Carbon Technology Holdings, LLC Mineral solubilizing microorganism infused biochars
US11390569B2 (en) 2011-06-06 2022-07-19 Carbon Technology Holdings, LLC Methods for application of biochar
US9809502B2 (en) 2011-06-06 2017-11-07 Cool Planet Energy Systems, Inc. Enhanced Biochar
US11384031B2 (en) 2011-06-06 2022-07-12 Carbon Technology Holdings, LLC Biochar as a microbial carrier
US11312666B2 (en) 2011-06-06 2022-04-26 Carbon Technology Holdings, LLC Mineral solubilizing microorganism infused biochars
US11279662B2 (en) 2011-06-06 2022-03-22 Carbon Technology Holdings, LLC Method for application of biochar in turf grass and landscaping environments
US11214528B2 (en) 2011-06-06 2022-01-04 Carbon Technology Holdings, LLC Treated biochar for use in water treatment systems
US9963650B2 (en) 2011-07-25 2018-05-08 Cool Planet Energy Systems, Inc. Method for making sequesterable biochar
US10265670B2 (en) * 2012-01-20 2019-04-23 Cool Planet Energy Systems, Inc. Biochar extracts and method for capturing material extracted from biochar
US20140361501A1 (en) * 2013-06-05 2014-12-11 Cal-Comp Electronics & Communications Company Limited Carrier
US9944538B2 (en) 2013-10-25 2018-04-17 Cool Planet Energy Systems, Inc. System and method for purifying process water
US11426350B1 (en) 2014-10-01 2022-08-30 Carbon Technology Holdings, LLC Reducing the environmental impact of farming using biochar
US10870608B1 (en) 2014-10-01 2020-12-22 Carbon Technology Holdings, LLC Biochar encased in a biodegradable material
US10864492B2 (en) 2014-10-01 2020-12-15 Carbon Technology Holdings, LLC Method for producing biochar aggregate particles
US11053171B2 (en) 2014-10-01 2021-07-06 Carbon Technology Holdings, LLC Biochars for use with animals
US11111185B2 (en) 2014-10-01 2021-09-07 Carbon Technology Holdings, LLC Enhanced biochar
US10472297B2 (en) 2014-10-01 2019-11-12 Cool Planet Energy System, Inc. Biochars for use in composting
US10322389B2 (en) 2014-10-01 2019-06-18 Cool Planet Energy Systems, Inc. Biochar aggregate particles
US11739031B2 (en) 2014-10-01 2023-08-29 Carbon Technology Holdings, LLC Biochar encased in a biodegradable material
US11097241B2 (en) 2014-10-01 2021-08-24 Talipot Cool Extract (Ip), Llc Biochars, biochar extracts and biochar extracts having soluble signaling compounds and method for capturing material extracted from biochar
US9980912B2 (en) 2014-10-01 2018-05-29 Cool Planet Energy Systems, Inc. Biochars for use with animals
US10065163B2 (en) * 2014-10-01 2018-09-04 Cool Planet Energy Systems, Inc Biochar extracts and method for capturing material extracted from biochar
US11866329B2 (en) 2017-12-15 2024-01-09 Talipot Cool Extract (Ip), Llc Biochars, biochar extracts and biochar extracts having soluble signaling compounds and method for capturing material extracted from biochar

Also Published As

Publication number Publication date
KR100834410B1 (ko) 2008-06-09
EP1707266A1 (en) 2006-10-04
CA2546477A1 (en) 2005-06-16
KR20070091695A (ko) 2007-09-11
KR100795118B1 (ko) 2008-01-17
BRPI0419283B1 (pt) 2014-10-14
BRPI0417351A (pt) 2007-03-27
EP1878490A3 (en) 2008-03-05
WO2005053846A1 (ja) 2005-06-16
EP2805764A3 (en) 2015-01-07
EP2805764A2 (en) 2014-11-26
US8222182B2 (en) 2012-07-17
CA2546477C (en) 2012-03-27
EP1878490A2 (en) 2008-01-16
EP1707266A4 (en) 2008-03-05
US20080139384A1 (en) 2008-06-12
KR20060121214A (ko) 2006-11-28

Similar Documents

Publication Publication Date Title
US8222182B2 (en) Anion adsorbing carbon material, as well as manufacturing method and manufacturing facilities for same
JP2007099619A (ja) 土壌改良肥料およびこれを用いた植物栽培方法
CN1890027B (zh) 阴离子吸附用炭材料及其制造方法和制造装置
JP3790540B2 (ja) 中毒防止材
JP3822888B2 (ja) 陰イオン吸着炭素材料の製造装置
JP4001886B2 (ja) 土壌改良肥料およびこれを用いた植物栽培方法
JP3790538B2 (ja) 陰イオン吸着炭素材料ならびにその製造方法
JP3828130B2 (ja) 下水処理場用浄化材およびこれを用いた下水浄化方法並びに下水処理設備
JP3828131B2 (ja) 下水処理場用を除く排廃水処理用浄化材およびこれを用いた排廃水浄化方法並びに排廃水処理装置
JP3718520B2 (ja) 陰イオン吸着炭素材料とその製造方法
JP3822894B2 (ja) 陰イオン吸着炭素材料の製造装置
JP2005296933A (ja) 養殖場用浄化材およびこれを用いた養殖場浄化方法並びに養殖場浄化装置
JP2005296930A (ja) 浄水器用浄化材およびこれを用いた上水浄化方法並びに浄水器
JP3828132B2 (ja) 浄水器用を除く上水用浄化材およびこれを用いた上水浄化方法並びに上水浄化装置
JP2005296933A5 (pt)
JP2006015216A (ja) 陰イオン吸着炭素材料およびその製造方法
JP2005296930A5 (pt)
JP2005295999A5 (pt)
JP2005296932A (ja) 水槽水浄化材並びにこれを用いた水槽水浄化方法および装置
JP2007091591A (ja) 土壌改良肥料およびこれを用いた植物栽培方法
JP2005296926A5 (pt)
JP2006061770A5 (pt)
JP2006061769A (ja) 陰イオン吸着炭素材料ならびにその製造方法
JP2005296932A5 (pt)
JP2005306716A5 (pt)

Legal Events

Date Code Title Description
AS Assignment

Owner name: NISSHOKU CORPORATION, JAPAN

Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNORS:HAYASHI, SATOSHI;YOKOYAMA, RIEI;REEL/FRAME:018662/0065

Effective date: 20060728

STCB Information on status: application discontinuation

Free format text: ABANDONED -- FAILURE TO RESPOND TO AN OFFICE ACTION