Classifications

• • A—HUMAN NECESSITIES
  • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
  • A61L—METHODS OR APPARATUS FOR STERILISING MATERIALS OR OBJECTS IN GENERAL; DISINFECTION, STERILISATION OR DEODORISATION OF AIR; CHEMICAL ASPECTS OF BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES; MATERIALS FOR BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES
  • A61L9/00—Disinfection, sterilisation or deodorisation of air
  • A61L9/01—Deodorant compositions
  • A61L9/014—Deodorant compositions containing sorbent material, e.g. activated carbon
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01D—SEPARATION
  • B01D39/00—Filtering material for liquid or gaseous fluids
  • B01D39/14—Other self-supporting filtering material ; Other filtering material
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01D—SEPARATION
  • B01D39/00—Filtering material for liquid or gaseous fluids
  • B01D39/14—Other self-supporting filtering material ; Other filtering material
  • B01D39/16—Other self-supporting filtering material ; Other filtering material of organic material, e.g. synthetic fibres
  • B01D39/1607—Other self-supporting filtering material ; Other filtering material of organic material, e.g. synthetic fibres the material being fibrous
  • B01D39/1623—Other self-supporting filtering material ; Other filtering material of organic material, e.g. synthetic fibres the material being fibrous of synthetic origin
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01D—SEPARATION
  • B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
  • B01D46/0027—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours with additional separating or treating functions
  • B01D46/0036—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours with additional separating or treating functions by adsorption or absorption
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01D—SEPARATION
  • B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
  • B01D46/0027—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours with additional separating or treating functions
  • B01D46/0038—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours with additional separating or treating functions with means for influencing the odor, e.g. deodorizing substances
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01D—SEPARATION
  • B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
  • B01D53/02—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
  • B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
  • B01J20/02—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
  • B01J20/04—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising compounds of alkali metals, alkaline earth metals or magnesium
  • B01J20/043—Carbonates or bicarbonates, e.g. limestone, dolomite, aragonite
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
  • B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
  • B01J20/02—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
  • B01J20/10—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising silica or silicate
  • B01J20/103—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising silica or silicate comprising silica
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
  • B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
  • B01J20/02—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
  • B01J20/20—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising free carbon; comprising carbon obtained by carbonising processes
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
  • B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
  • B01J20/22—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising organic material
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
  • B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
  • B01J20/28—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties
  • B01J20/28002—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties characterised by their physical properties
  • B01J20/28004—Sorbent size or size distribution, e.g. particle size
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
  • B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
  • B01J20/28—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties
  • B01J20/28014—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties characterised by their form
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
  • B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
  • B01J20/28—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties
  • B01J20/28014—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties characterised by their form
  • B01J20/28033—Membrane, sheet, cloth, pad, lamellar or mat
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
  • B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
  • B01J20/28—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties
  • B01J20/28014—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties characterised by their form
  • B01J20/28033—Membrane, sheet, cloth, pad, lamellar or mat
  • B01J20/28038—Membranes or mats made from fibers or filaments
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
  • B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
  • B01J20/28—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties
  • B01J20/28054—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties characterised by their surface properties or porosity
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
  • B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
  • B01J20/28—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties
  • B01J20/28054—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties characterised by their surface properties or porosity
  • B01J20/28057—Surface area, e.g. B.E.T specific surface area
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
  • B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
  • B01J20/28—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties
  • B01J20/28054—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties characterised by their surface properties or porosity
  • B01J20/28057—Surface area, e.g. B.E.T specific surface area
  • B01J20/28061—Surface area, e.g. B.E.T specific surface area being in the range 100-500 m2/g
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
  • B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
  • B01J20/28—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties
  • B01J20/28054—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties characterised by their surface properties or porosity
  • B01J20/28057—Surface area, e.g. B.E.T specific surface area
  • B01J20/28064—Surface area, e.g. B.E.T specific surface area being in the range 500-1000 m2/g
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
  • B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
  • B01J20/28—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties
  • B01J20/28054—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties characterised by their surface properties or porosity
  • B01J20/28057—Surface area, e.g. B.E.T specific surface area
  • B01J20/28066—Surface area, e.g. B.E.T specific surface area being more than 1000 m2/g
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
  • B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
  • B01J20/28—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties
  • B01J20/28054—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties characterised by their surface properties or porosity
  • B01J20/28069—Pore volume, e.g. total pore volume, mesopore volume, micropore volume
  • B01J20/28073—Pore volume, e.g. total pore volume, mesopore volume, micropore volume being in the range 0.5-1.0 ml/g
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
  • B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
  • B01J20/28—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties
  • B01J20/28054—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties characterised by their surface properties or porosity
  • B01J20/28088—Pore-size distribution
  • B01J20/28092—Bimodal, polymodal, different types of pores or different pore size distributions in different parts of the sorbent
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
  • B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
  • B01J20/30—Processes for preparing, regenerating, or reactivating
  • B01J20/32—Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating
  • B01J20/3202—Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating characterised by the carrier, support or substrate used for impregnation or coating
  • B01J20/3204—Inorganic carriers, supports or substrates
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
  • B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
  • B01J20/30—Processes for preparing, regenerating, or reactivating
  • B01J20/32—Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating
  • B01J20/3231—Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating characterised by the coating or impregnating layer
  • B01J20/3234—Inorganic material layers
  • B01J20/3236—Inorganic material layers containing metal, other than zeolites, e.g. oxides, hydroxides, sulphides or salts
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
  • B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
  • B01J20/30—Processes for preparing, regenerating, or reactivating
  • B01J20/32—Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating
  • B01J20/3231—Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating characterised by the coating or impregnating layer
  • B01J20/3242—Layers with a functional group, e.g. an affinity material, a ligand, a reactant or a complexing group
  • B01J20/3244—Non-macromolecular compounds
  • B01J20/3246—Non-macromolecular compounds having a well defined chemical structure
  • B01J20/3248—Non-macromolecular compounds having a well defined chemical structure the functional group or the linking, spacer or anchoring group as a whole comprising at least one type of heteroatom selected from a nitrogen, oxygen or sulfur, these atoms not being part of the carrier as such
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
  • B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
  • B01J20/30—Processes for preparing, regenerating, or reactivating
  • B01J20/32—Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating
  • B01J20/3231—Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating characterised by the coating or impregnating layer
  • B01J20/3242—Layers with a functional group, e.g. an affinity material, a ligand, a reactant or a complexing group
  • B01J20/3244—Non-macromolecular compounds
  • B01J20/3246—Non-macromolecular compounds having a well defined chemical structure
  • B01J20/3248—Non-macromolecular compounds having a well defined chemical structure the functional group or the linking, spacer or anchoring group as a whole comprising at least one type of heteroatom selected from a nitrogen, oxygen or sulfur, these atoms not being part of the carrier as such
  • B01J20/3251—Non-macromolecular compounds having a well defined chemical structure the functional group or the linking, spacer or anchoring group as a whole comprising at least one type of heteroatom selected from a nitrogen, oxygen or sulfur, these atoms not being part of the carrier as such comprising at least two different types of heteroatoms selected from nitrogen, oxygen or sulphur
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
  • B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
  • B01J20/30—Processes for preparing, regenerating, or reactivating
  • B01J20/32—Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating
  • B01J20/3291—Characterised by the shape of the carrier, the coating or the obtained coated product
  • B01J20/3293—Coatings on a core, the core being particle or fiber shaped, e.g. encapsulated particles, coated fibers
• • 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
  • C01B32/30—Active carbon
  • C01B32/354—After-treatment
  • C01B32/372—Coating; Grafting; Microencapsulation
• • C—CHEMISTRY; METALLURGY
  • C01—INORGANIC CHEMISTRY
  • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
  • C01B33/00—Silicon; Compounds thereof
  • C01B33/113—Silicon oxides; Hydrates thereof
  • C01B33/12—Silica; Hydrates thereof, e.g. lepidoic silicic acid
• • C—CHEMISTRY; METALLURGY
  • C01—INORGANIC CHEMISTRY
  • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
  • C01B33/00—Silicon; Compounds thereof
  • C01B33/113—Silicon oxides; Hydrates thereof
  • C01B33/12—Silica; Hydrates thereof, e.g. lepidoic silicic acid
  • C01B33/18—Preparation of finely divided silica neither in sol nor in gel form; After-treatment thereof
• • A—HUMAN NECESSITIES
  • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
  • A61L—METHODS OR APPARATUS FOR STERILISING MATERIALS OR OBJECTS IN GENERAL; DISINFECTION, STERILISATION OR DEODORISATION OF AIR; CHEMICAL ASPECTS OF BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES; MATERIALS FOR BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES
  • A61L2209/00—Aspects relating to disinfection, sterilisation or deodorisation of air
  • A61L2209/10—Apparatus features
  • A61L2209/14—Filtering means
• • A—HUMAN NECESSITIES
  • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
  • A61L—METHODS OR APPARATUS FOR STERILISING MATERIALS OR OBJECTS IN GENERAL; DISINFECTION, STERILISATION OR DEODORISATION OF AIR; CHEMICAL ASPECTS OF BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES; MATERIALS FOR BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES
  • A61L2209/00—Aspects relating to disinfection, sterilisation or deodorisation of air
  • A61L2209/20—Method-related aspects
  • A61L2209/22—Treatment by sorption, e.g. absorption, adsorption, chemisorption, scrubbing, wet cleaning
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01D—SEPARATION
  • B01D2239/00—Aspects relating to filtering material for liquid or gaseous fluids
  • B01D2239/04—Additives and treatments of the filtering material
  • B01D2239/0407—Additives and treatments of the filtering material comprising particulate additives, e.g. adsorbents
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01D—SEPARATION
  • B01D2239/00—Aspects relating to filtering material for liquid or gaseous fluids
  • B01D2239/04—Additives and treatments of the filtering material
  • B01D2239/0435—Electret
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01D—SEPARATION
  • B01D2239/00—Aspects relating to filtering material for liquid or gaseous fluids
  • B01D2239/04—Additives and treatments of the filtering material
  • B01D2239/045—Deodorising additives
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01D—SEPARATION
  • B01D2239/00—Aspects relating to filtering material for liquid or gaseous fluids
  • B01D2239/04—Additives and treatments of the filtering material
  • B01D2239/0464—Impregnants
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01D—SEPARATION
  • B01D2239/00—Aspects relating to filtering material for liquid or gaseous fluids
  • B01D2239/04—Additives and treatments of the filtering material
  • B01D2239/0471—Surface coating material
  • B01D2239/0485—Surface coating material on particles
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01D—SEPARATION
  • B01D2239/00—Aspects relating to filtering material for liquid or gaseous fluids
  • B01D2239/04—Additives and treatments of the filtering material
  • B01D2239/0471—Surface coating material
  • B01D2239/0492—Surface coating material on fibres
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01D—SEPARATION
  • B01D2239/00—Aspects relating to filtering material for liquid or gaseous fluids
  • B01D2239/06—Filter cloth, e.g. knitted, woven non-woven; self-supported material
  • B01D2239/0604—Arrangement of the fibres in the filtering material
  • B01D2239/0618—Non-woven
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01D—SEPARATION
  • B01D2239/00—Aspects relating to filtering material for liquid or gaseous fluids
  • B01D2239/06—Filter cloth, e.g. knitted, woven non-woven; self-supported material
  • B01D2239/0604—Arrangement of the fibres in the filtering material
  • B01D2239/0627—Spun-bonded
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01D—SEPARATION
  • B01D2239/00—Aspects relating to filtering material for liquid or gaseous fluids
  • B01D2239/06—Filter cloth, e.g. knitted, woven non-woven; self-supported material
  • B01D2239/065—More than one layer present in the filtering material
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01D—SEPARATION
  • B01D2251/00—Reactants
  • B01D2251/30—Alkali metal compounds
  • B01D2251/304—Alkali metal compounds of sodium
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01D—SEPARATION
  • B01D2251/00—Reactants
  • B01D2251/30—Alkali metal compounds
  • B01D2251/306—Alkali metal compounds of potassium
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01D—SEPARATION
  • B01D2251/00—Reactants
  • B01D2251/50—Inorganic acids
  • B01D2251/512—Phosphoric acid
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01D—SEPARATION
  • B01D2251/00—Reactants
  • B01D2251/60—Inorganic bases or salts
  • B01D2251/606—Carbonates
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01D—SEPARATION
  • B01D2251/00—Reactants
  • B01D2251/70—Organic acids
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01D—SEPARATION
  • B01D2253/00—Adsorbents used in seperation treatment of gases and vapours
  • B01D2253/10—Inorganic adsorbents
  • B01D2253/102—Carbon
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01D—SEPARATION
  • B01D2253/00—Adsorbents used in seperation treatment of gases and vapours
  • B01D2253/10—Inorganic adsorbents
  • B01D2253/106—Silica or silicates
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01D—SEPARATION
  • B01D2253/00—Adsorbents used in seperation treatment of gases and vapours
  • B01D2253/25—Coated, impregnated or composite adsorbents
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01D—SEPARATION
  • B01D2253/00—Adsorbents used in seperation treatment of gases and vapours
  • B01D2253/30—Physical properties of adsorbents
  • B01D2253/302—Dimensions
  • B01D2253/304—Linear dimensions, e.g. particle shape, diameter
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01D—SEPARATION
  • B01D2253/00—Adsorbents used in seperation treatment of gases and vapours
  • B01D2253/30—Physical properties of adsorbents
  • B01D2253/302—Dimensions
  • B01D2253/306—Surface area, e.g. BET-specific surface
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01D—SEPARATION
  • B01D2253/00—Adsorbents used in seperation treatment of gases and vapours
  • B01D2253/30—Physical properties of adsorbents
  • B01D2253/302—Dimensions
  • B01D2253/311—Porosity, e.g. pore volume
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01D—SEPARATION
  • B01D2253/00—Adsorbents used in seperation treatment of gases and vapours
  • B01D2253/30—Physical properties of adsorbents
  • B01D2253/34—Specific shapes
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01D—SEPARATION
  • B01D2257/00—Components to be removed
  • B01D2257/40—Nitrogen compounds
  • B01D2257/406—Ammonia
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01D—SEPARATION
  • B01D2257/00—Components to be removed
  • B01D2257/70—Organic compounds not provided for in groups B01D2257/00 - B01D2257/602
  • B01D2257/708—Volatile organic compounds V.O.C.'s
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01D—SEPARATION
  • B01D2257/00—Components to be removed
  • B01D2257/90—Odorous compounds not provided for in groups B01D2257/00 - B01D2257/708
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01D—SEPARATION
  • B01D2258/00—Sources of waste gases
  • B01D2258/06—Polluted air
• • C—CHEMISTRY; METALLURGY
  • C01—INORGANIC CHEMISTRY
  • C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
  • C01P2004/00—Particle morphology
  • C01P2004/60—Particles characterised by their size
• • C—CHEMISTRY; METALLURGY
  • C01—INORGANIC CHEMISTRY
  • C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
  • C01P2006/00—Physical properties of inorganic compounds
  • C01P2006/12—Surface area
• • C—CHEMISTRY; METALLURGY
  • C01—INORGANIC CHEMISTRY
  • C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
  • C01P2006/00—Physical properties of inorganic compounds
  • C01P2006/14—Pore volume

Definitions

• the present invention relates to gas adsorbents and gas adsorption sheets, filter media and air filters using the same.
• Air purifiers are used to remove dust and odorous gas components in the home.
• deodorizing performance against volatile organic compounds (VOC) generated in the living environment where the air purifier is used is required as a performance requirement for the deodorizing function of the air purifier for home use.
• VOCs such as formaldehyde have been shown to have an undesirable effect on the human body, and laws and ordinances of each country stipulate that indoor environmental concentrations should be controlled below a certain level.
• Air purifiers are expected to have performance as removal equipment for this VOC.
• there is a demand for high efficiency in removing formaldehyde which is at risk of being released from building materials such as wallpaper, which is thought to cause sick house syndrome, and for a long service life.
• a high deodorizing efficiency means that the operation time of the air purifier required to lower the gas concentration in a predetermined space is short. Longer life means that the above deodorizing efficiency is maintained even after a predetermined amount of gas is adsorbed.
• the deodorizing efficiency is shown as the space purification capacity (CADR: Clean Air Delivery Rate), and the lifetime is shown as the cumulative clean mass (CCM: Cumulate Clean Mass) with evaluation criteria such as GB/T 18801 2015 (Chinese national standard).
• the present invention is capable of maintaining the ability to remove odorous components such as formaldehyde for a long period of time and suppressing the desorption of gas components adsorbed during use from the air filter. To provide an adsorbent effective in suppressing secondary odor generation.
• the gas adsorbent of the present invention that solves the above problems includes (A1) acid-impregnated activated carbon, (A2) base-impregnated activated carbon and (B) aldehyde adsorbent.
• the gas adsorbent of the present invention preferably satisfies the following (1) to (4).
• the ratio of the pore volume of pores with a pore diameter of 0.4 to 2.0 nm calculated by the MP method of (A1) acid-impregnated activated carbon is 75 to 100% of the pore volume of pores with a calculated pore diameter of 0.4 nm or more, and/or (A2) the pore diameter of the base-impregnated activated carbon calculated by the MP method is 0.4 to 2.0 nm is 75 to 100% of the pore volume of pores having a pore diameter of 0.4 nm or more calculated by the MP method and BJH method of (A2) base-impregnated activated carbon.
• the specific surface area of (A1) acid-impregnated activated carbon and/or (A2) base-impregnated activated carbon is 400 to 1300 m 2 /g.
• the gas adsorption sheet of the present invention contains the gas adsorbent of the present invention.
• the filter medium of the present invention holds the gas adsorbent of the present invention in at least one of one or more layers formed by two or more layers of nonwoven fabric.
• the air filter of the present invention includes the filter medium of the present invention.
• the present invention it is possible to suppress desorption from the air filter of gas components such as aldehyde, ammonia, and acetic acid adsorbed on the air filter. It is possible to provide a gas adsorbent that is effective in suppressing and prolonging the life of formaldehyde gas removal performance.
• the present invention solves the above problem, that is, it is possible to suppress detachment from the air filter of odorous components such as aldehyde, ammonia, and acetic acid once adsorbed on the air filter.
• odorous components such as aldehyde, ammonia, and acetic acid
• the gas adsorbent of the present invention includes (A1) acid-impregnated activated carbon, (A2) base-impregnated activated carbon and (B) aldehyde adsorbent.
• activated carbon to which no acid or base is impregnated has only a so-called physical adsorption action, in which the pore structure allows gas to be adsorbed on the pore surfaces by intermolecular force generated by contact with gas in the air. Therefore, when a gas exceeding the physical adsorption capacity of activated carbon is adsorbed, the same component as the adsorbed gas is released again.
• Acid-impregnated activated carbon is an unimpregnated activated carbon impregnated with an acid agent to make the acid exist on the pore surface of the activated carbon. It is an activated carbon imparted with a so-called chemisorption effect, which is a neutralization reaction that converts to a non-volatile component different from that before adsorption.
• the acid of the acid-impregnated activated carbon (A1) used in the gas adsorbent of the present invention is not particularly limited, and inorganic acids such as phosphoric acid, hydrochloric acid, sulfuric acid, nitric acid and boric acid, citric acid, oxalic acid and apple acid. acid, and other organic acids.
• inorganic acids such as phosphoric acid, hydrochloric acid, sulfuric acid, nitric acid and boric acid, citric acid, oxalic acid and apple acid. acid, and other organic acids.
• an inorganic acid selected from phosphoric acid, hydrochloric acid, sulfuric acid and nitric acid is more preferable in terms of deodorizing effect.
• Base-impregnated activated carbon impregnates unimpregnated activated carbon with a chemical consisting of a base, and by making the base exist on the pore surface of the activated carbon, in addition to the physical adsorption action inherent to activated carbon, acid gases such as acetic acid can be removed. It is an activated carbon imparted with a so-called chemisorption effect, which is a neutralization reaction that changes the components into non-volatile components different from those before adsorption.
• the base of the base-impregnated activated carbon (A2) used in the gas adsorbent of the present invention is not particularly limited, and hydroxides or salts of alkali metal and alkaline earth metal ions such as potassium, calcium, sodium and magnesium are used.
• alkali metal and alkaline earth metal ions such as potassium, calcium, sodium and magnesium are used.
• Examples include potassium hydroxide, sodium hydroxide, potassium carbonate, sodium carbonate, potassium hydrogen carbonate, sodium hydrogen carbonate, and the like.
• hydrogencarbonates such as potassium hydrogencarbonate and sodium hydrogencarbonate are preferable because they hardly clog pores of activated carbon due to deliquescence.
• the method for impregnating the acid or base drug is not particularly limited, but an aqueous solution or dispersion of the acid or base is sprayed onto the activated carbon and dried to remove moisture, thereby allowing the drug component to adhere to the pores of the activated carbon. A method is preferred.
• (A1) acid-impregnated activated carbon and/or (A2) base-impregnated activated carbon in the present invention preferably have the following pore structure. That is, (A1) the ratio of the pore volume of pores with a pore diameter of 0.4 to 2.0 nm calculated by the MP method of acid-impregnated activated carbon is calculated by (A1) the MP method and BJH method of acid-impregnated activated carbon. and (A2) the pore diameter calculated by the MP method of the base-impregnated activated carbon is 0.4 to 2.0 nm.
• the ratio of the pore volume of the pores of (A2) is 75 to 100% of the pore volume of pores having a pore diameter of 0.4 nm or more calculated by the MP method and the BJH method of the base-impregnated activated carbon. It is preferable to satisfy at least one of
• the ratio of the pore volume of pores with a pore diameter of 0.4 to 2 nm is 0.4 to 2 nm.
• the adsorbent with activated carbon exhibits physical adsorption of organic gas components such as toluene and chemisorption performance of acidic or basic gases. Furthermore, re-release of gas components once adsorbed from the adsorbent is further suppressed.
• the mechanism by which this effect is obtained is as follows. That is, among the pores provided in (A1) the acid-impregnated activated carbon and (A2) the base-impregnated activated carbon, the pores having a pore diameter of 0.4 to 2 nm impregnated with an acid or a base contain an acid gas such as acetic acid. Alternatively, since the molecular size is close to that of a basic gas such as ammonia, it has excellent physical adsorption performance, and furthermore, it is said that odorous components once adsorbed in the pores are difficult to desorb from the pores. It has characteristics.
• Methods for analyzing the pore diameter and pore volume of activated carbon include the MP (MICROPORE) method and the BJH (Barrett-Joyner-Halenda) method.
• the MP method was adopted for the analysis of micropores with a pore diameter of 0.4 to 2 nm, in which capillary condensation does not occur, among the pores of activated carbon.
• the BJH method was adopted for the analysis of macropores having a pore diameter of 2 nm or more among the pores of activated carbon.
• the pore volume of pores having a pore diameter of 0.4 nm or more calculated by the MP method and the BJH method of activated carbon in the present invention means the value of the pore volume obtained by the MP method and the pore volume obtained by the BJH method. It refers to the total value of the pore volume values obtained.
• the specific surface area of (A1) acid-impregnated activated carbon and/or (A2) base-impregnated activated carbon is preferably in the range of 400 to 1300 m 2 /g, more preferably in the range of 600 to 1000 m 2 /g.
• the specific surface area referred to here is determined by the BET multipoint method specified in JIS R 1626-1996. measurement.).
• the amount of acid or base impregnated to obtain the above specific surface area is preferably 2 to 40% by mass, more preferably 5 to 25% by mass, based on the entire impregnated activated carbon.
• Activated carbon having a pore structure as described above can be arbitrarily selected as a raw material from known materials such as coconut shells, charcoal, coal pitch, and phenolic resin. It is obtained by adjusting the activation conditions that form pores by Among them, it is more preferable to use coconut shells as a raw material and select the activation method with steam, because it is easy to obtain activated carbon with a smaller pore size.
• Aldehyde adsorbent is a chemical adsorbent in which inorganic particles are used as a carrier and agents having chemical reactivity with aldehyde components such as acetaldehyde and formaldehyde are added thereto.
• inorganic particles inorganic particles that react less with the attached drug are preferable.
• the specific surface area of the inorganic particles employed in the present invention is preferably 50-1200 m 2 /g, more preferably 100-1000 m 2 /g.
• the specific surface area of the inorganic particles is measured according to the BET multi-point method specified in JIS R 1626-1996 (constant volume method described in 6.1 Volume method, preheating, N 2 as adsorbate, and measurement by the constant volume method). can.
• the inorganic particles preferably have a pore volume of 0.3 to 2.5 cc/g, more preferably 1.0 to 2.0 cc/g.
• a pore volume of the inorganic particles By setting the pore volume of the inorganic particles to 0.3 to 2.5 cc/g, it is possible to increase the amount of the chemical to be impregnated while retaining pores that are excellent in reacting with aldehyde gas in the air. It is preferable because it can increase the adsorption efficiency and adsorption capacity as an adsorbent.
• the pore volume referred to here can be measured by the BJH method described above.
• the inorganic particles preferably have pores with an average diameter of 0.5 to 100 nm, more preferably 2 to 50 nm.
• the average diameter of the pores of the inorganic particles is 0.5 to 100 nm, it is possible to secure a large specific surface area for supporting the drug while ensuring mechanical strength even in a porous body, and This is preferable because it facilitates penetration of the drug into the pores.
• pores with a diameter of 2 to 50 nm are called mesopores, and particles having mesopores are excellent in efficiently advancing the reaction between the attached drug and acetaldehyde.
• Inorganic particles employed in the present invention include porous silicon dioxide (silica), zeolite, sepiolite, activated alumina, aluminum silicate, silica gel, alumina gel, activated clay, layered compounds such as zirconium phosphate and ammonium polytriphosphate, porous
• porous silicon dioxide (silica) has the above-mentioned preferred average pore diameter, specific surface area, and pore size. It is possible to procure a large volume at a low cost, which is preferable.
• tertiary amine compounds can be used as agents having chemical reactivity with aldehyde components employed in the present invention, and hydrazide compounds such as adipic acid dihydrazide, dodecanedioic acid dihydrazide, and succinic acid dihydrazide are preferred. , p-aminobenzenesulfonic acid, ethylene urea condensates, tris(hydroxymethyl)aminomethane and the like. Among them, adipic acid dihydrazide is preferable in terms of adsorption performance of aldehydes.
• the amount of adipic acid dihydrazide used in the present invention is preferably 7 mg to 120 mg, more preferably 35 to 90 mg, per 1 g of inorganic particles.
• the gas adsorbent of the present invention is composed of the above two types of drug-impregnated activated carbon and aldehyde adsorbent.
• the first point is that when a gas adsorbent is used as an air filter, the gas in the air is composed of an extremely large number of components, among which are basic gases typified by ammonia, acidic gases typified by acetic acid, acetaldehyde, Aldehyde gases, such as formaldehyde, have a low concentration threshold at which humans perceive them as odors, and chemisorption by acids, bases, and aldehyde adsorbents are all used as a means of suppressing the re-emission of these gases from adsorbents.
• the second point is that many of the chemicals that react with the aldehyde component impregnated on the inorganic particles are highly reactive with the aldehyde gas in the air when the pH is weakly acidic to near neutral.
• activated carbon or base-impregnated activated carbon alone, by using both together with an aldehyde adsorbent, it is possible to maintain an appropriate pH. can be exhibited, and its performance can be maintained even after long-term storage.
• the gas adsorbent By blending the gas adsorbent within this range, the re-release amount of the adsorbed gas when used as a filter is reduced, and (A1) the acid-impregnated activated carbon and (A2) the base-impregnated activated carbon come into contact with each other, resulting in a decrease in the performance of each other. can be suppressed.
• the ratio of (M A ) By setting the ratio of (M A ) to 95 or less, it is possible to reduce the neutralization reaction due to contact between (A1) the acid-impregnated activated carbon and (A2) the base-impregnated activated carbon in the gas adsorbent, and the mutual chemisorption performance It is preferable because it is possible to suppress the decrease in On the contrary, by setting the ratio of (M A ) to 25 or more, the adsorption performance of acidic and basic gases in the air becomes more sufficient, and (B) these gas components adhering to the surface of the aldehyde adsorbent are chemisorbed. It is preferable because it can suppress the generation of unpleasant odors.
• the pH of the gas adsorbent of the present invention is preferably 3-7, more preferably 5-7.
• a pH of 3 to 7 is preferable because the absorption-desorption characteristics of acid gases, basic gases, and non-polar gases such as formaldehyde are not biased.
• the pH of the gas adsorbent 0.3 g of the gas adsorbent is put into 5 g of ultrapure water at a temperature of 20° C., and the pH in the water can be measured with a glass electrode type pH meter.
• the average particle size of (A1) acid-impregnated activated carbon used in the gas adsorbent of the present invention is preferably 40 to 500 ⁇ m, and the average particle size of (A2) base-impregnated activated carbon is preferably 40 to 500 ⁇ m.
• (B) the average particle diameter of the aldehyde adsorbent is preferably 100, and (A1) the average particle diameter of the acid-impregnated activated carbon is preferably 95 to 600.
• the average particle size of the base-impregnated activated carbon is preferably 95-600.
• the average particle size of the acid-impregnated activated carbon is 40 ⁇ m or more, preferably 50 ⁇ m or more. Since the frequency of contact between (A1) the acid-impregnated activated carbon and (A2) the base-impregnated activated carbon is reduced, deterioration in performance can be suppressed.
• (A1) the average particle size of the acid-impregnated activated carbon is 500 ⁇ m or less, preferably 400 ⁇ m or less
• (A2) the average particle size of the base-impregnated activated carbon is 500 ⁇ m or less, preferably 400 ⁇ m or less. Since the degree of contact with the activated carbon particles can be reduced, deterioration in performance can be suppressed.
• the ratio of the average particle size of (A1) acid-impregnated activated carbon to the average particle size of (A2) base-impregnated activated carbon is preferably close.
• the average particle size of the base-impregnated activated carbon is preferably 80-120.
• the average particle size of the aldehyde adsorbent is 100, and (A1) the average particle size of the acid-impregnated activated carbon is 95 or more, preferably 100 or more, (B) the average particle size of the aldehyde adsorbent is 100, and (A2) a base
• the average particle size of the impregnated activated carbon is 95 or more, preferably 100 or more, the air permeability after forming into a sheet can be made more sufficient.
• (A1) the average particle size of the acid-impregnated activated carbon is 600 or less, preferably 500 or less;
• (B) the average particle size of the aldehyde adsorbent is 100;
• the average particle size referred to here means the particle size distribution measured according to JIS-Z-8815 (1994), and the granular (A1) acid-impregnated activated carbon, (A2) base-impregnated activated carbon and (B) aldehyde adsorbent. For each of the particles, the particle size is determined to correspond to the size of the sieve through which 50% by mass of the total mass passes.
• the shape of (A1) acid-impregnated activated carbon, (A2) base-impregnated activated carbon, and (B) aldehyde adsorbent can be arbitrarily selected from known shapes such as spherical, crushed, and columnar shapes.
• the gas adsorbent of the present invention is preferably used in the form of a sheet. That is, the gas adsorbent of the present invention is suitable for use in gas adsorption sheets.
• the gas adsorbent is formed in the form of a sheet, which means a method of forming a sheet by dispersing the gas adsorbent particles between the fibers of the fabric, or a method of connecting the surface of the composite gas adsorbent with an adhesive or the like. and forming it into a sheet.
• the form of the fabric is not particularly limited, and can be arbitrarily selected from woven fabrics, knitted fabrics, molded nets, non-woven fabrics, and the like.
• nonwoven fabrics are preferable because the desired physical properties can be easily obtained by arbitrarily selecting the fiber diameter, fiber length, etc. of the fibers to be used and combining them.
• nonwoven fabrics include chemical bond nonwoven fabrics, wet stamp nonwoven fabrics, spunbond nonwoven fabrics, meltblown nonwoven fabrics, spunlace nonwoven fabrics and air-laid nonwoven fabrics.
• the basis weight of the gas adsorbent is preferably in the range of 15 to 400 g/m 2 . Furthermore, the range of 30 to 300 g/m 2 is more preferable because the gas adsorption capacity is high and the obtained sheet-like filter material is excellent in pleating (bending) workability when processed into an air filter.
• the gas adsorbent is preferably particulate, and the shape can be arbitrarily selected from known ones such as spherical, crushed, and columnar.
• the gas adsorbent of the present invention is suitable for use as a filter medium.
• the filter medium comprises two or more layers of nonwoven fabric and the gas adsorbent of the present invention. At least one of the layers formed by two or more layers of nonwoven fabric holds the gas adsorbent of the present invention.
• the amount of the gas adsorbent used in the filter medium of the present invention is preferably in the range of 40 to 400 g/ m2 , more preferably 100 to 200 g/m2, from the viewpoint of obtaining gas removal efficiency and adsorption capacity when used as the filter medium. 2 .
• the nonwoven fabric included in the filter material is preferably an electret nonwoven fabric.
• the electret nonwoven fabric is preferable because the filter medium can collect dust in the air with higher efficiency.
• gas adsorbent particles and powdery heat-bonding resin particles are uniformly dispersed on one non-woven fabric, and after heating and melting the heat-bonding resin particles with a heater, the other non-woven fabric is produced.
• a method of integrating by laminating and pressure bonding, and a method of integrating by laminating and pressure bonding the other nonwoven fabric after spraying gas adsorbent particles on one nonwoven fabric while spraying a heated molten resin is not limited to these.
• the thickness of the nonwoven fabric is preferably 0.08 to 0.60 mm from the viewpoint of having a certain strength and increasing the area that can be accommodated in a certain volume when pleated, and the lower limit is 0.15 mm or more. More preferably, the upper limit is 0.50 mm or less.
• the filter medium has two or more layers of nonwoven fabric, the thickness of these nonwoven fabrics may be the same or different.
• fibers used in the above nonwoven fabric natural fibers, synthetic fibers, or inorganic fibers such as glass fibers or metal fibers can be used.
• thermoplastic resin synthetic fibers that can be melt-spun are preferable.
• the air filter of the present invention comprises the gas adsorption sheet of the present invention or the filter material and outer frame of the present invention. It is preferable that the four sides of the filter medium are fixed to the outer frame.
• the gas adsorption sheet or filter medium may be used as a sheet, or may be pleated to form a three-dimensional shape having ridges and valleys.
• a gas adsorbent and a polyethylene adhesive powder (Abifor 1200 manufactured by Abifor AG) (hereinafter referred to as an adhesive powder) are blended at a mass ratio of 2 gas adsorbents: 1 adhesive powder, and a spunbond nonwoven fabric made of polyester fibers (Toray Axter (registered trademark) H2070-1S manufactured by Co., Ltd., thickness 0.27 mm) is uniformly dispersed in a predetermined amount, and the adhesive powder is melted by heating to 110 ° C. to 130 ° C.
• melt-blown nonwoven fabric (basis weight: 30 g/m 2 , thickness: 0.25 mm)
• pressure is applied by nip rolls to obtain a sheet-like filter medium with a predetermined thickness.
• the mass (g) of the filter material taken out from the desiccator was measured with an electronic balance. The obtained measured value was defined as m2 (g).
• the toluene concentration (ppm) of the air on the downstream side of the filter medium sample was measured using an infrared absorption gas concentration meter (Nippon Thermo Co., Ltd. The passage of the gas was stopped after 25 minutes of measurement at 10-second intervals using the MIRAN Apphl Re). was calculated .
• the ammonia concentration (ppm) in the air on the downstream side of the filter medium sample was measured using an infrared absorption gas concentration meter (manufactured by Nippon Thermo Co., Ltd. MIRAN ApphlRe) was used to measure for 60 minutes at 10 second intervals until the ammonia gas concentration on the downstream side of the sample reached 9 ppm, that is, the ammonia adsorption efficiency of the filter material reached 10%.
• the cumulative adsorption amount (g/m 2 ) of ammonia per (1 m 2 ) was calculated and taken as the saturated adsorption amount.
• a relative humidity of 50% was passed from one side of the filter medium sample to the other side at a wind speed of 20 cm/sec. . 120 seconds after passing acetic acid gas through the filter medium sample, the acetic acid concentration (ppm) of the air on the downstream side of the filter medium sample (the other side of the filter medium sample) was measured using an infrared absorption gas concentration meter (Nippon Thermo Co., Ltd. The passage of the gas was stopped after 25 minutes of measurement at 10-second intervals using a MIRAN Apphl Re), and the concentration of acetic acid in the air detected from the downstream side until then was determined to be acetic acid per unit area (1 m 2 ) of the filter medium. was calculated .
• Acetic acid _ _ The desorption rate (%) was calculated.
• Acetic acid desorption rate (%) [accumulated desorption amount of acetic acid per unit area (1 m 2 ) (g/m 2 )/accumulated adsorption amount of acetic acid per unit area (1 m 2 ) (g/m 2 ) ] ⁇ 100.
• Polyolefin adhesive (Hitachi Kasei Polymer Hibon YH450-1 manufactured by Co., Ltd.) was attached to the four sides of the pleated filter medium to obtain an air filter with a frontage size of 372 mm long, 291 mm wide, and 60 mm high.
• the air purifier after collecting the tobacco combustion smoke is left in a test room with a volume of 30 m 3 for 24 hours without being operated, and then the air purifier is operated, and the odor intensity and comfort level of the discharged air were scored by five panelists according to the criteria shown in Tables 1 and 2, and the average value was obtained.
• Pore volume of activated carbon pores Put 0.10 g of activated carbon in a glass cell, degassed at 150 ° C. for 5 hours, and then, using a device BELSORP-18PLUS manufactured by Bell Japan Co., Ltd., liquid nitrogen temperature 77 K, Activated carbon was put into the apparatus under the condition that the temperature inside the apparatus was set to 35° C. and the saturated vapor pressure was set to 101.3 kPa, and the isothermal adsorption and desorption processes of nitrogen were measured. From the measurement results, the pore volume of pores with a pore diameter of 0.4 to 2 nm was calculated by the MP method, and the pore volume of pores with a pore diameter of 0.4 nm or more was calculated by the BJH method.
• Example 1 As the acid-impregnated activated carbon, granular activated carbon (MNC30/60-O manufactured by Manei Kogyo Co., Ltd., average particle size 300 ⁇ m according to JIS Z8815 method, specific surface area 1200 m 2 /g measured by BET multipoint method) was added with 40 mass of citric acid. and an impregnated activated carbon having a specific surface area of 450 m 2 /g impregnated so as to have a specific surface area of 450 m 2 /g.
• MNC30/60-O manufactured by Manei Kogyo Co., Ltd., average particle size 300 ⁇ m according to JIS Z8815 method, specific surface area 1200 m 2 /g measured by BET multipoint method was added with 40 mass of citric acid.
• an impregnated activated carbon having a specific surface area of 450 m 2 /g impregnated so as to have a specific surface area of 450 m 2 /g.
• the acid-impregnated activated carbon was 30 g/m 2
• the base-impregnated activated carbon was 30 g/m 2
• the aldehyde adsorbent was 90 g/m 2
• total impregnated activated carbon: aldehyde adsorbent A mass ratio of 40:60 was obtained.
• the thickness of this filter medium was 1.1 mm.
• the gas adsorbent was 80 g/m 2
• the acid-impregnated activated carbon was 36 g/m 2
• the base-impregnated activated carbon was 36 g/m 2
• the aldehyde adsorbent was 8 g/m 2
• total impregnated activated carbon: aldehyde adsorbent A mass ratio of 90:10 was obtained.
• the thickness of this filter medium was 0.7 mm.
• Example 4 As the acid-impregnated activated carbon, granular activated carbon (MNC30/60-O manufactured by Manei Kogyo Co., Ltd., average particle size 300 ⁇ m according to JIS Z8815 method, specific surface area 1200 m 2 /g measured by BET multipoint method) was added with 20 mass of orthophosphoric acid. and an impregnated activated carbon having a specific surface area of 700 m 2 /g impregnated so as to have a specific surface area of 700 m 2 /g.
• MNC30/60-O manufactured by Manei Kogyo Co., Ltd., average particle size 300 ⁇ m according to JIS Z8815 method, specific surface area 1200 m 2 /g measured by BET multipoint method was added with 20 mass of orthophosphoric acid.
• an impregnated activated carbon having a specific surface area of 700 m 2 /g impregnated so as to have a specific surface area of 700 m 2 /g.
• the acid-impregnated activated carbon was 30 g/m 2
• the base-impregnated activated carbon was 30 g/m 2
• the aldehyde adsorbent was 90 g/m 2
• total impregnated activated carbon: aldehyde adsorbent A mass ratio of 40:60 was obtained.
• the thickness of this filter medium was 1.2 mm.
• Example 5 The same acid-impregnated activated carbon and base-impregnated activated carbon as in Example 4, and as an aldehyde adsorbent, porous silica particles (pore volume 1.0 cc/g measured by BJH method, specific surface area 500 m measured by BET multipoint method 2 / g, average particle size 280 ⁇ m according to JISZ8815 method), and an adsorbent in which adipic acid dihydrazide (manufactured by Nippon Kasei Co., Ltd.) is impregnated so that it becomes 7% by mass of the total.
• porous silica particles pore volume 1.0 cc/g measured by BJH method, specific surface area 500 m measured by BET multipoint method 2 / g, average particle size 280 ⁇ m according to JISZ8815 method
• adipic acid dihydrazide manufactured by Nippon Kasei Co., Ltd.
• Acid-impregnated activated carbon base-impregnated activated carbon: aldehyde adsorption
• a gas adsorbent blended at a mass ratio of agent 30:30:90 was used.
• a filter medium having a gas adsorbent was produced by the method described in the above [Method for producing filter medium using gas adsorbent].
• the acid-impregnated activated carbon was 30 g/m 2
• the base-impregnated activated carbon was 30 g/m 2
• the aldehyde adsorbent was 90 g/m 2
• total impregnated activated carbon: aldehyde adsorbent A mass ratio of 40:60 was obtained.
• the thickness of this filter medium was 1.1 mm.
• Example 6 As the acid-impregnated activated carbon, granular activated carbon (Kuraray Co., Ltd., Kuraray Coal (registered trademark) GW30/60D, average particle size 300 ⁇ m according to JIS Z8815 method, specific surface area 950 m 2 /g measured by BET multipoint method) was added with orthorin in the same manner as in Example 4. Impregnated activated carbon having a specific surface area of 600 m 2 /g impregnated with an acid of 20% by mass of the whole, and sodium hydrogen carbonate similar to that of Example 4 as the base-impregnated activated carbon and the same granular activated carbon as the above-mentioned impregnated activated carbon.
• Kuraray Co., Ltd., Kuraray Coal (registered trademark) GW30/60D average particle size 300 ⁇ m according to JIS Z8815 method, specific surface area 950 m 2 /g measured by BET multipoint method
• Impregnated activated carbon with a specific surface area of 850 m 2 /g impregnated so as to be 5% by mass, and the same adsorbent as in Example 5 as an aldehyde adsorbent, acid-impregnated activated carbon: base-impregnated activated carbon: aldehyde adsorbent 20 : A gas adsorbent blended at a mass ratio of 40:90 was used. Using this gas adsorbent, a filter medium having a gas adsorbent was produced by the method described in the above [Method for producing filter medium using gas adsorbent].
• the gas adsorbent was 150 g/m 2
• the acid-impregnated activated carbon was 20 g/m 2
• the base-impregnated activated carbon was 40 g/m 2
• the aldehyde adsorbent was 90 g/m 2
• total impregnated activated carbon: aldehyde adsorbent A mass ratio of 40:60 was obtained.
• the thickness of this filter medium was 1.2 mm.
• Example 1 Without using the base-impregnated activated carbon, the same citric acid-impregnated granular activated carbon as in Example 1 was used as the acid-impregnated activated carbon, and the same adsorbent as in Example 5 was used as the aldehyde adsorbent. A gas adsorbent blended at a mass ratio was used. Using 150 g/m 2 of this gas adsorbent, a filter medium having a gas adsorbent was produced by the method described in the above [Method for producing filter medium using gas adsorbent].
• the acid-impregnated activated carbon was 60 g/m 2 and the aldehyde adsorbent was 90 g/m 2 , so the mass ratio of the total impregnated activated carbon: aldehyde adsorbent was 40:60. .
• the thickness of this filter medium was 1.0 mm.
• Example 2 Without using acid-impregnated activated carbon, the same potassium carbonate-impregnated granular activated carbon as in Example 1 was used as the base-impregnated activated carbon, and the same adsorbent as in Example 5 was used as the aldehyde adsorbent. A gas adsorbent blended at a mass ratio was used. Using 150 g/m 2 of this gas adsorbent, a filter medium having a gas adsorbent was produced by the method described in the above [Method for producing filter medium using gas adsorbent].
• the base-impregnated activated carbon was 60 g/m 2 and the aldehyde adsorbent was 90 g/m 2 , so the mass ratio of the total impregnated activated carbon: aldehyde adsorbent was 40:60. .
• the thickness of this filter medium was 1.0 mm.
• the thickness of this filter medium was 1.0 mm.
• Tables 3 and 4 show the gas adsorbents of Examples 1 to 6 and the filter media and air filters using the gas adsorbents of Examples 1 to 6.
• Tables 5 and 6 summarize the filter media and air filters using adsorbents.
• Example 1 a gas adsorbent that combines acid-impregnated activated carbon, base-impregnated activated carbon, and an aldehyde adsorbent is used, so the desorption rate after adsorption is low.
• citric acid used as an acid adsorbs ammonia gas in the air through an acid-base reaction, so it has excellent adsorption capacity for ammonia
• potassium carbonate used as a base adsorbs acetic acid gas in the air through an acid-base reaction. Therefore, the desorption rate after adsorption of acetic acid is low.
• the neutralization reaction due to the contact of citric acid and potassium carbonate, which are the impregnated components of the activated carbon is suppressed by the inclusion of inorganic particles, so that the adsorption performance of ammonia gas and acetic acid gas was maintained even after long-term storage.
• the formaldehyde cleanability (F-CADR) performance is also good, and the odor intensity of the secondary odor after adsorption of tobacco odor is small. It was a long-life air filter that made it difficult to perceive unpleasant odors.
• Example 4 the activated carbon impregnated with orthophosphoric acid, which has better reactivity with ammonia gas in the air than in Example 1, was used, so the saturated adsorption amount of ammonia was improved.
• the obtained filter material is processed into a filter and installed in an air purifier, the odor intensity of the secondary odor after adsorbing the tobacco odor is small, and the user does not feel uncomfortable, that is, it is a long-life air filter. there were.
• Example 5 the average particle size of the aldehyde adsorbent composed of inorganic particles was approximately the same as the average particle size of the acid-impregnated activated carbon and the base-impregnated activated carbon. Since the neutralization reaction due to contact between acid and sodium bicarbonate is suppressed, the adsorption performance of ammonia gas and acetic acid gas was maintained even after long-term storage. In addition, when the obtained filter material is processed into a filter and mounted in an air purifier, the formaldehyde cleanability (F-CADR) performance is also good, and the odor intensity of the secondary odor after adsorption of tobacco odor is small. It was a long-life air filter that made it difficult to perceive unpleasant odors.
• F-CADR formaldehyde cleanability
• Example 6 compared with Examples 1 to 5, the ratio of the pore volume due to pores having a pore diameter of 0.4 to 2 nm to the pore volume of all pores of acid-impregnated activated carbon and base-impregnated activated carbon was Since the higher one is used, the desorption rate after adsorption of toluene and acetic acid was decreased as compared with Examples 1-5.
• the formaldehyde cleanability (F-CADR) performance is also good, and the odor intensity of the secondary odor after adsorption of tobacco odor is small. It was a long-life air filter that made it difficult to perceive unpleasant odors.
• Comparative Example 1 does not contain base-impregnated activated carbon, all acetic acid gas in the air is adsorbed by the physical adsorption properties of activated carbon, and the desorption rate after adsorption is remarkably high. Therefore, after processing it into a filter and installing it in an air purifier, the odor intensity of the secondary odor emitted after adsorption of tobacco odor was high, and the odor was felt to be highly unpleasant.
• Comparative Example 2 did not contain acid-impregnated activated carbon, so the saturated adsorption capacity for ammonia was remarkably low. Therefore, it was processed into a filter and installed in an air purifier, and the odor intensity of the secondary odor after adsorption of the cigarette odor containing a high concentration of ammonia component was high, and the odor was felt to be highly unpleasant. In addition, it is thought that the pH of the entire gas adsorbent changed to the alkaline side due to the influence of the base-impregnated activated carbon, causing a decrease in the formaldehyde adsorption performance, and a decrease in the formaldehyde detergency (F-CADR) was observed.
• F-CADR formaldehyde detergency
• Comparative Example 3 does not use an aldehyde chemical adsorbent, so when processed into a filter and installed in an air purifier, the formaldehyde cleanability (F-CADR) performance is low.
• F-CADR formaldehyde cleanability
• acid-impregnated activated carbon and base-impregnated activated carbon adhere to each other, and the neutralization reaction of the impregnating agent reduces the adsorption performance of ammonia and acetic acid. The amount of re-released was increased, the intensity of the secondary odor was strong, and the odor was felt to be highly unpleasant.
• the gas adsorbent according to the present invention is mainly installed in household air purifiers and used in air filters and filtering materials for cleaning indoor air.

Landscapes

• Chemical & Material Sciences (AREA)
• Chemical Kinetics & Catalysis (AREA)
• Organic Chemistry (AREA)
• Analytical Chemistry (AREA)
• Inorganic Chemistry (AREA)
• Health & Medical Sciences (AREA)
• Engineering & Computer Science (AREA)
• Materials Engineering (AREA)
• Epidemiology (AREA)
• Life Sciences & Earth Sciences (AREA)
• Animal Behavior & Ethology (AREA)
• General Health & Medical Sciences (AREA)
• Public Health (AREA)
• Veterinary Medicine (AREA)
• Oil, Petroleum & Natural Gas (AREA)
• General Chemical & Material Sciences (AREA)
• Disinfection, Sterilisation Or Deodorisation Of Air (AREA)
• Solid-Sorbent Or Filter-Aiding Compositions (AREA)

Priority Applications (5)

Applications Claiming Priority (2)

Publications (1)

Family

ID=85782510

Family Applications (1)

Country Status (6)

Cited By (1)

Citations (5)

Family Cites Families (13)

• 2022
  • 2022-09-16 US US18/692,383 patent/US20240382929A1/en active Pending
  • 2022-09-16 CN CN202280063677.2A patent/CN117980064A/zh active Pending
  • 2022-09-16 EP EP22875883.5A patent/EP4410418A4/en active Pending
  • 2022-09-16 WO PCT/JP2022/034719 patent/WO2023054012A1/ja not_active Ceased
  • 2022-09-16 JP JP2022558067A patent/JPWO2023054012A1/ja active Pending
  • 2022-09-16 KR KR1020247002562A patent/KR20240066244A/ko active Pending

Patent Citations (5)

Non-Patent Citations (1)

Also Published As

Similar Documents

Legal Events