JP2008272225A - Solid deodorizing composition to deodorize plurality of odor ingredients with single agent and manufacture process of this composition - Google Patents
Solid deodorizing composition to deodorize plurality of odor ingredients with single agent and manufacture process of this composition Download PDFInfo
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- JP2008272225A JP2008272225A JP2007119601A JP2007119601A JP2008272225A JP 2008272225 A JP2008272225 A JP 2008272225A JP 2007119601 A JP2007119601 A JP 2007119601A JP 2007119601 A JP2007119601 A JP 2007119601A JP 2008272225 A JP2008272225 A JP 2008272225A
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- 230000001877 deodorizing effect Effects 0.000 title claims abstract description 65
- 239000007787 solid Substances 0.000 title claims abstract description 61
- 239000000203 mixture Substances 0.000 title claims abstract description 55
- 238000000034 method Methods 0.000 title claims abstract description 14
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 12
- 239000004615 ingredient Substances 0.000 title 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 95
- BAUYGSIQEAFULO-UHFFFAOYSA-L iron(2+) sulfate (anhydrous) Chemical compound [Fe+2].[O-]S([O-])(=O)=O BAUYGSIQEAFULO-UHFFFAOYSA-L 0.000 claims abstract description 35
- 229910000358 iron sulfate Inorganic materials 0.000 claims abstract description 32
- AXCZMVOFGPJBDE-UHFFFAOYSA-L calcium dihydroxide Chemical compound [OH-].[OH-].[Ca+2] AXCZMVOFGPJBDE-UHFFFAOYSA-L 0.000 claims abstract description 25
- 239000000920 calcium hydroxide Substances 0.000 claims abstract description 25
- 229910001861 calcium hydroxide Inorganic materials 0.000 claims abstract description 25
- 235000011116 calcium hydroxide Nutrition 0.000 claims abstract description 25
- 238000001035 drying Methods 0.000 claims abstract description 6
- 239000002689 soil Substances 0.000 claims description 33
- 238000002156 mixing Methods 0.000 claims description 16
- 239000011230 binding agent Substances 0.000 claims description 12
- 239000000463 material Substances 0.000 claims description 7
- QAOWNCQODCNURD-UHFFFAOYSA-L Sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 claims description 6
- RUTXIHLAWFEWGM-UHFFFAOYSA-H iron(3+) sulfate Chemical compound [Fe+3].[Fe+3].[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O RUTXIHLAWFEWGM-UHFFFAOYSA-H 0.000 claims description 6
- 229910000360 iron(III) sulfate Inorganic materials 0.000 claims description 6
- 239000000126 substance Substances 0.000 claims description 6
- 235000013162 Cocos nucifera Nutrition 0.000 claims description 5
- 244000060011 Cocos nucifera Species 0.000 claims description 5
- 239000003245 coal Substances 0.000 claims description 5
- 150000001875 compounds Chemical class 0.000 claims description 4
- 239000010903 husk Substances 0.000 claims description 4
- 239000002994 raw material Substances 0.000 claims description 4
- 239000011790 ferrous sulphate Substances 0.000 claims description 3
- 235000003891 ferrous sulphate Nutrition 0.000 claims description 3
- 229910000359 iron(II) sulfate Inorganic materials 0.000 claims description 3
- 239000007789 gas Substances 0.000 abstract description 42
- 238000004332 deodorization Methods 0.000 abstract description 16
- 230000007935 neutral effect Effects 0.000 abstract description 10
- 239000003795 chemical substances by application Substances 0.000 abstract description 9
- 239000002253 acid Substances 0.000 abstract description 4
- 230000000694 effects Effects 0.000 abstract description 3
- 239000003864 humus Substances 0.000 abstract description 3
- 229910052799 carbon Inorganic materials 0.000 abstract 2
- 238000005453 pelletization Methods 0.000 abstract 1
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 12
- 239000007864 aqueous solution Substances 0.000 description 12
- 239000000047 product Substances 0.000 description 12
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 description 11
- 229910000037 hydrogen sulfide Inorganic materials 0.000 description 10
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 9
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 9
- 230000002378 acidificating effect Effects 0.000 description 8
- 239000002781 deodorant agent Substances 0.000 description 7
- 239000000243 solution Substances 0.000 description 7
- 239000004372 Polyvinyl alcohol Substances 0.000 description 6
- 229910021529 ammonia Inorganic materials 0.000 description 6
- 239000002245 particle Substances 0.000 description 6
- 229920002451 polyvinyl alcohol Polymers 0.000 description 6
- 229940068984 polyvinyl alcohol Drugs 0.000 description 6
- 235000019422 polyvinyl alcohol Nutrition 0.000 description 6
- QMMFVYPAHWMCMS-UHFFFAOYSA-N Dimethyl sulfide Chemical compound CSC QMMFVYPAHWMCMS-UHFFFAOYSA-N 0.000 description 5
- LSDPWZHWYPCBBB-UHFFFAOYSA-N Methanethiol Chemical compound SC LSDPWZHWYPCBBB-UHFFFAOYSA-N 0.000 description 4
- 239000000654 additive Substances 0.000 description 4
- 229960000892 attapulgite Drugs 0.000 description 4
- 230000000052 comparative effect Effects 0.000 description 4
- 238000006477 desulfuration reaction Methods 0.000 description 4
- 230000023556 desulfurization Effects 0.000 description 4
- 239000008187 granular material Substances 0.000 description 4
- 229910052625 palygorskite Inorganic materials 0.000 description 4
- 239000000843 powder Substances 0.000 description 4
- 239000003463 adsorbent Substances 0.000 description 3
- 238000009835 boiling Methods 0.000 description 3
- 238000011156 evaluation Methods 0.000 description 3
- 238000006386 neutralization reaction Methods 0.000 description 3
- 239000007800 oxidant agent Substances 0.000 description 3
- 239000008188 pellet Substances 0.000 description 3
- 229920000728 polyester Polymers 0.000 description 3
- 235000011121 sodium hydroxide Nutrition 0.000 description 3
- 238000012360 testing method Methods 0.000 description 3
- 229920002803 thermoplastic polyurethane Polymers 0.000 description 3
- 239000004113 Sepiolite Substances 0.000 description 2
- 229910000831 Steel Inorganic materials 0.000 description 2
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 2
- 229910021536 Zeolite Inorganic materials 0.000 description 2
- 229920006167 biodegradable resin Polymers 0.000 description 2
- 239000006227 byproduct Substances 0.000 description 2
- WQOXQRCZOLPYPM-UHFFFAOYSA-N dimethyl disulfide Chemical compound CSSC WQOXQRCZOLPYPM-UHFFFAOYSA-N 0.000 description 2
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 description 2
- 239000012153 distilled water Substances 0.000 description 2
- 238000005469 granulation Methods 0.000 description 2
- 230000003179 granulation Effects 0.000 description 2
- 239000010440 gypsum Substances 0.000 description 2
- 229910052602 gypsum Inorganic materials 0.000 description 2
- 229910052500 inorganic mineral Inorganic materials 0.000 description 2
- XEEYBQQBJWHFJM-UHFFFAOYSA-N iron Substances [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- 238000012423 maintenance Methods 0.000 description 2
- 235000010755 mineral Nutrition 0.000 description 2
- 239000011707 mineral Substances 0.000 description 2
- 230000000704 physical effect Effects 0.000 description 2
- 229920002239 polyacrylonitrile Polymers 0.000 description 2
- 229910052624 sepiolite Inorganic materials 0.000 description 2
- 235000019355 sepiolite Nutrition 0.000 description 2
- 238000001179 sorption measurement Methods 0.000 description 2
- 239000010959 steel Substances 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- GETQZCLCWQTVFV-UHFFFAOYSA-N trimethylamine Chemical compound CN(C)C GETQZCLCWQTVFV-UHFFFAOYSA-N 0.000 description 2
- 239000002023 wood Substances 0.000 description 2
- 239000010457 zeolite Substances 0.000 description 2
- IXPNQXFRVYWDDI-UHFFFAOYSA-N 1-methyl-2,4-dioxo-1,3-diazinane-5-carboximidamide Chemical compound CN1CC(C(N)=N)C(=O)NC1=O IXPNQXFRVYWDDI-UHFFFAOYSA-N 0.000 description 1
- PUKLDDOGISCFCP-JSQCKWNTSA-N 21-Deoxycortisone Chemical compound C1CC2=CC(=O)CC[C@]2(C)[C@@H]2[C@@H]1[C@@H]1CC[C@@](C(=O)C)(O)[C@@]1(C)CC2=O PUKLDDOGISCFCP-JSQCKWNTSA-N 0.000 description 1
- QJZYHAIUNVAGQP-UHFFFAOYSA-N 3-nitrobicyclo[2.2.1]hept-5-ene-2,3-dicarboxylic acid Chemical compound C1C2C=CC1C(C(=O)O)C2(C(O)=O)[N+]([O-])=O QJZYHAIUNVAGQP-UHFFFAOYSA-N 0.000 description 1
- 229920000178 Acrylic resin Polymers 0.000 description 1
- 239000004925 Acrylic resin Substances 0.000 description 1
- 229920002134 Carboxymethyl cellulose Polymers 0.000 description 1
- 241000196324 Embryophyta Species 0.000 description 1
- FCYKAQOGGFGCMD-UHFFFAOYSA-N Fulvic acid Natural products O1C2=CC(O)=C(O)C(C(O)=O)=C2C(=O)C2=C1CC(C)(O)OC2 FCYKAQOGGFGCMD-UHFFFAOYSA-N 0.000 description 1
- 229920002907 Guar gum Polymers 0.000 description 1
- PMZURENOXWZQFD-UHFFFAOYSA-L Sodium Sulfate Chemical compound [Na+].[Na+].[O-]S([O-])(=O)=O PMZURENOXWZQFD-UHFFFAOYSA-L 0.000 description 1
- 229920002472 Starch Polymers 0.000 description 1
- 238000005273 aeration Methods 0.000 description 1
- 229910001583 allophane Inorganic materials 0.000 description 1
- 125000000129 anionic group Chemical group 0.000 description 1
- 150000007514 bases Chemical class 0.000 description 1
- 239000000440 bentonite Substances 0.000 description 1
- 229910000278 bentonite Inorganic materials 0.000 description 1
- SVPXDRXYRYOSEX-UHFFFAOYSA-N bentoquatam Chemical compound O.O=[Si]=O.O=[Al]O[Al]=O SVPXDRXYRYOSEX-UHFFFAOYSA-N 0.000 description 1
- 239000002802 bituminous coal Substances 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- 210000000988 bone and bone Anatomy 0.000 description 1
- 230000003139 buffering effect Effects 0.000 description 1
- 235000010418 carrageenan Nutrition 0.000 description 1
- 239000000679 carrageenan Substances 0.000 description 1
- 229920001525 carrageenan Polymers 0.000 description 1
- 229940113118 carrageenan Drugs 0.000 description 1
- 239000001913 cellulose Substances 0.000 description 1
- 229920002678 cellulose Polymers 0.000 description 1
- 239000002738 chelating agent Substances 0.000 description 1
- 239000002734 clay mineral Substances 0.000 description 1
- 239000011300 coal pitch Substances 0.000 description 1
- 238000013329 compounding Methods 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 235000013399 edible fruits Nutrition 0.000 description 1
- 239000000839 emulsion Substances 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000001125 extrusion Methods 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 239000000945 filler Substances 0.000 description 1
- 238000011049 filling Methods 0.000 description 1
- 239000010419 fine particle Substances 0.000 description 1
- 239000002509 fulvic acid Substances 0.000 description 1
- 229940095100 fulvic acid Drugs 0.000 description 1
- 239000010439 graphite Substances 0.000 description 1
- 229910002804 graphite Inorganic materials 0.000 description 1
- 239000000665 guar gum Substances 0.000 description 1
- 235000010417 guar gum Nutrition 0.000 description 1
- 229960002154 guar gum Drugs 0.000 description 1
- 239000004021 humic acid Substances 0.000 description 1
- 230000001771 impaired effect Effects 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 150000002506 iron compounds Chemical class 0.000 description 1
- 235000014413 iron hydroxide Nutrition 0.000 description 1
- -1 iron ions Chemical class 0.000 description 1
- NCNCGGDMXMBVIA-UHFFFAOYSA-L iron(ii) hydroxide Chemical compound [OH-].[OH-].[Fe+2] NCNCGGDMXMBVIA-UHFFFAOYSA-L 0.000 description 1
- 239000003077 lignite Substances 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 238000000465 moulding Methods 0.000 description 1
- 230000009965 odorless effect Effects 0.000 description 1
- 239000011301 petroleum pitch Substances 0.000 description 1
- 239000005011 phenolic resin Substances 0.000 description 1
- 229920001568 phenolic resin Polymers 0.000 description 1
- 229920000747 poly(lactic acid) Polymers 0.000 description 1
- 239000004626 polylactic acid Substances 0.000 description 1
- 239000002861 polymer material Substances 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 239000004627 regenerated cellulose Substances 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 238000007873 sieving Methods 0.000 description 1
- 235000010413 sodium alginate Nutrition 0.000 description 1
- 239000000661 sodium alginate Substances 0.000 description 1
- 229940005550 sodium alginate Drugs 0.000 description 1
- 229910052938 sodium sulfate Inorganic materials 0.000 description 1
- 235000011152 sodium sulphate Nutrition 0.000 description 1
- 239000008107 starch Substances 0.000 description 1
- 235000019698 starch Nutrition 0.000 description 1
- 229940032147 starch Drugs 0.000 description 1
- 238000004381 surface treatment Methods 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
- 239000000230 xanthan gum Substances 0.000 description 1
- 235000010493 xanthan gum Nutrition 0.000 description 1
- 229920001285 xanthan gum Polymers 0.000 description 1
- 229940082509 xanthan gum Drugs 0.000 description 1
- UHVMMEOXYDMDKI-JKYCWFKZSA-L zinc;1-(5-cyanopyridin-2-yl)-3-[(1s,2s)-2-(6-fluoro-2-hydroxy-3-propanoylphenyl)cyclopropyl]urea;diacetate Chemical compound [Zn+2].CC([O-])=O.CC([O-])=O.CCC(=O)C1=CC=C(F)C([C@H]2[C@H](C2)NC(=O)NC=2N=CC(=CC=2)C#N)=C1O UHVMMEOXYDMDKI-JKYCWFKZSA-L 0.000 description 1
Classifications
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A50/00—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
- Y02A50/20—Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters
Landscapes
- Disinfection, Sterilisation Or Deodorisation Of Air (AREA)
- Treating Waste Gases (AREA)
Abstract
Description
本発明は、複数の臭気成分を1剤で脱臭する固形脱臭組成物および該組成物の製造方法に関する。 The present invention relates to a solid deodorizing composition for deodorizing a plurality of odor components with one agent and a method for producing the composition.
各種有害ガスや悪臭ガスの脱臭剤としては、それらガス成分の物理吸着を利用した脱臭剤が広く実用化されており、このような脱臭剤として、固形脱臭剤に代表される活性炭やゼオライトなどの鉱物質多孔性物質が知られている。また、より高い脱臭効果を得るために、悪臭の種類に応じて固形脱臭剤の表面処理が施され、性能改質がなされている。 As deodorizers for various harmful gases and odorous gases, deodorizers using physical adsorption of these gas components have been widely put into practical use, and as such deodorizers, activated carbon and zeolite such as solid deodorizers are used. Mineral porous materials are known. Further, in order to obtain a higher deodorizing effect, the surface treatment of the solid deodorizer is performed according to the type of malodor, and the performance is improved.
一般に、酸性ガス、塩基性ガスおよび中性ガス等の複数の臭気成分を脱臭する場合は、活性炭脱臭塔に酸性ガス用活性炭、塩基性ガス用活性炭および中性ガス用活性炭を投入したものが知られている。しかし、このような方法では、複数の臭気成分を脱臭するために、3種類の活性炭を、酸性ガス用活性炭、塩基性ガス用活性炭および中性ガス用活性炭の順番にガスに接触するように脱臭塔に投入しなければならず、投入順序の間違い防止に作業が繁雑であった。 Generally, when deodorizing multiple odor components such as acid gas, basic gas and neutral gas, activated carbon for acidic gas, activated carbon for basic gas and activated carbon for neutral gas are known in activated carbon deodorization tower. It has been. However, in such a method, in order to deodorize a plurality of odor components, three types of activated carbon are deodorized so as to contact the gas in the order of activated carbon for acidic gas, activated carbon for basic gas, and activated carbon for neutral gas. It had to be thrown into the tower, and the work was complicated to prevent mistakes in the order.
また、このような中、活性炭脱臭塔の維持管理の利便性の面から、2種類の活性炭をあらかじめ混合して1剤とする方法も提案されている(例えば、特許文献1参照)。しかし、たとえば苛性ソーダを添着したアルカリ添着活性炭と硫酸を添着した酸添着活性炭を混合すると、両者の接触面で中和反応が起こり、脱臭効果が低下するといった問題があった。特に高湿度のガスを通気した場合や、冬季に結露が発生した状態でガスを通気した場合などには、2種類の活性炭の接触面に中和塩が析出し、活性炭同士の固化(ブロッキング)が起こり、脱臭能が低下するといった問題があった。 In such circumstances, a method of mixing two types of activated carbon in advance to make one agent has been proposed from the viewpoint of the convenience of maintenance and management of the activated carbon deodorization tower (for example, see Patent Document 1). However, for example, when alkali-added activated carbon impregnated with caustic soda and acid-added activated carbon impregnated with sulfuric acid are mixed, there is a problem that a neutralization reaction occurs at the contact surface between the two and the deodorizing effect is reduced. Especially when high-humidity gas is ventilated or when gas is ventilated while condensation occurs in winter, neutralized salt is deposited on the contact surface of the two types of activated carbon, and the activated carbon is solidified (blocking). Occurred, and the deodorizing ability was reduced.
さらに、多孔質焼結体に酸化剤を添加することで、酸性ガス、塩基性ガス、中性ガスを同時に脱臭できる吸着材も知られている(例えば、特許文献2参照)。しかし、該吸着材では、酸化剤を内部に保持または浸透させているため、高湿度の悪臭ガスが通過すると、酸化剤が脱離し、装置が腐食するという問題があった。また、該吸着材は、鉄化合物を含むものではない。 Furthermore, an adsorbent that can simultaneously deodorize acidic gas, basic gas, and neutral gas by adding an oxidizing agent to the porous sintered body is also known (see, for example, Patent Document 2). However, in the adsorbent, since the oxidizing agent is held or infiltrated inside, there is a problem that when the high-odor malodorous gas passes, the oxidizing agent is detached and the apparatus is corroded. The adsorbent does not contain an iron compound.
また同様に、臭気成分のうち硫化水素、メチルメルカプタンなどの酸性ガスを脱臭する場合は、固形脱臭剤の表面を苛性ソーダなどの塩基性物質で表面処理し、酸性ガスと化学中和・脱臭する方法が知られている。しかし、このような方法では、高湿度の悪臭ガスが通過すると、固形脱臭剤の表面に吸着している塩基性物質が脱離し、装置が腐食するという問題があった。 Similarly, in the case of deodorizing acidic gases such as hydrogen sulfide and methyl mercaptan among odor components, the surface of the solid deodorizer is surface treated with a basic substance such as caustic soda and chemically neutralized and deodorized with acidic gas. It has been known. However, in such a method, there is a problem that, when a high-humidity malodorous gas passes, the basic substance adsorbed on the surface of the solid deodorant is desorbed and the apparatus is corroded.
また、鉄イオンを配合した消石灰の微粒子を脱硫成分とする脱硫剤が提案されている(例えば、特許文献3参照)。しかし、該脱硫剤は、消石灰を主成分とするアルカリ性脱硫剤であり、装置の腐食等の問題を解決できるものではない。 In addition, a desulfurization agent that uses fine particles of slaked lime containing iron ions as a desulfurization component has been proposed (see, for example, Patent Document 3). However, the desulfurization agent is an alkaline desulfurization agent mainly composed of slaked lime, and cannot solve problems such as corrosion of the apparatus.
一方、腐植質土壌は、種々の物質を吸収、吸着したり、また交換作用や緩衝作用を有することが知られ、脱臭剤や水浄化剤、さらにはキレート剤として利用されている。ところが、腐植質土壌のみをバインダーを用いて成型した脱臭剤は、充分な脱臭効果が得られないといった問題があった。 On the other hand, humic soils are known to absorb and adsorb various substances and have exchange and buffering effects, and are used as deodorants, water purifiers, and chelating agents. However, a deodorizer obtained by molding only humic soil using a binder has a problem that a sufficient deodorizing effect cannot be obtained.
したがって、装置を腐食することなく、維持管理に有利な、1剤(1種類)で酸性ガス、塩基性ガス、中性ガスを同時に脱臭できる脱臭剤の開発が望まれている。 Therefore, it is desired to develop a deodorant that can deodorize acid gas, basic gas, and neutral gas simultaneously with one agent (one kind), which is advantageous for maintenance management, without corroding the apparatus.
本発明は、装置を腐食することなく、維持管理の容易な利便性の高い活性炭脱臭塔を可能とする、複数の臭気成分を1剤で脱臭する固形脱臭組成物および該組成物の製造方法を提供することを目的とする。 The present invention provides a solid deodorizing composition for deodorizing a plurality of odor components with one agent, which enables a highly convenient activated carbon deodorizing tower that is easy to maintain and maintain without corroding the apparatus, and a method for producing the composition. The purpose is to provide.
すなわち、本発明は、硫酸鉄、消石灰、活性炭および腐植質土壌を含み、該硫酸鉄の含有量が固形脱臭組成物の全量中、固形分として10〜50重量%であり、pHが6〜8である固形脱臭組成物に関する。 That is, the present invention includes iron sulfate, slaked lime, activated carbon, and humic soil, the content of the iron sulfate is 10 to 50% by weight as the solid content in the total amount of the solid deodorizing composition, and the pH is 6 to 8 It is related with the solid deodorizing composition which is.
硫酸鉄が、硫酸第一鉄、硫酸第二鉄およびポリ硫酸第二鉄からなる群から選択される1種以上の化合物であることが好ましい。 The iron sulfate is preferably one or more compounds selected from the group consisting of ferrous sulfate, ferric sulfate and polyferric sulfate.
活性炭が、木質材料、ヤシガラおよび石炭からなる群から選択される1種以上の原料からなる活性炭であることが好ましい。 The activated carbon is preferably activated carbon made of one or more raw materials selected from the group consisting of woody material, coconut husk and coal.
腐植質土壌が腐植物質を10重量%以上含有する土壌であることが好ましい。 It is preferable that the humic soil is a soil containing 10% by weight or more of humic substances.
腐植質土壌の含有量が、固形脱臭組成物の全量中10〜30重量%であることが好ましい。 It is preferable that content of humic soil is 10 to 30 weight% in the whole quantity of a solid deodorizing composition.
さらにバインダーを含むことが好ましい。 Furthermore, it is preferable that a binder is included.
また、本発明は、消石灰、活性炭および腐植質土壌を予め配合し、硫酸鉄溶液を添加混合した後、造粒、乾燥する工程を含む前記固形脱臭組成物の製造方法に関する。 Moreover, this invention relates to the manufacturing method of the said solid deodorizing composition including the process of granulating and drying after previously mix | blending slaked lime, activated carbon, and humic soil, adding and mixing an iron sulfate solution.
硫酸鉄溶液を添加混合した後に、さらに、バインダーを添加混合する工程を含むことが好ましい。 It is preferable to further include a step of adding and mixing a binder after adding and mixing the iron sulfate solution.
本発明は、硫酸鉄、消石灰、活性炭および腐植質土壌を含み、該硫酸鉄の含有量が固形脱臭組成物の全量中、固形分として10〜50重量%であり、pHを6〜8とすることで、装置を腐食することなく、酸性ガス、塩基性ガスおよび中性ガスを1剤で同時に脱臭することができる固形脱臭組成物を提供することができる。 The present invention includes iron sulfate, slaked lime, activated carbon, and humic soil, and the content of the iron sulfate is 10 to 50% by weight as the solid content in the total amount of the solid deodorizing composition, and the pH is 6 to 8. Thus, a solid deodorizing composition capable of simultaneously deodorizing acidic gas, basic gas and neutral gas with one agent without corroding the apparatus can be provided.
本発明は、硫酸鉄、消石灰、活性炭および腐植質土壌を含み、該硫酸鉄の含有量が固形脱臭組成物の全量中、固形分として10〜50重量%であり、pHが6〜8である固形脱臭組成物に関する。 The present invention includes iron sulfate, slaked lime, activated carbon, and humic soil, and the content of the iron sulfate is 10 to 50% by weight as a solid content in the total amount of the solid deodorizing composition, and the pH is 6 to 8. The present invention relates to a solid deodorizing composition.
本発明で用いる硫酸鉄としては、硫酸第一鉄、硫酸第二鉄およびポリ硫酸第二鉄からなる群から選択される1種以上の化合物であることが好ましく、ポリ硫酸第二鉄がより好ましい。 The iron sulfate used in the present invention is preferably one or more compounds selected from the group consisting of ferrous sulfate, ferric sulfate and polyferric sulfate, and polyferric sulfate is more preferable. .
ポリ硫酸第二鉄は、[Fe2(OH)n(SO4)3-n/2]m(0<n≦2、m=f(n)である)で示される化合物であり、市販されているものを用いることができる。市販品としては、たとえば、ポリテツ(登録商標)(商品名、日鉄鉱業(株)製)などをあげることができる。 Polyferric sulfate is a compound represented by [Fe 2 (OH) n (SO 4 ) 3 -n / 2 ] m (0 <n ≦ 2, m = f (n)), and is commercially available. Can be used. Examples of commercially available products include Polytetsu (registered trademark) (trade name, manufactured by Nittetsu Mining Co., Ltd.).
硫酸鉄の含有量は、固形脱臭組成物の全量中、固形分として10〜50重量%であり、20〜40重量%であることが好ましい。硫酸鉄の含有量が10重量%未満であると充分な脱臭効果が得られない傾向があり、50重量%をこえると充分な脱臭効果が得られない傾向があり、さらに、固形脱臭組成物の乾燥に長時間を要するため、経済的にも好ましくない。 Content of iron sulfate is 10-50 weight% as solid content in the whole quantity of a solid deodorizing composition, and it is preferable that it is 20-40 weight%. If the content of iron sulfate is less than 10% by weight, a sufficient deodorizing effect tends not to be obtained, and if it exceeds 50% by weight, a sufficient deodorizing effect tends not to be obtained. Since drying requires a long time, it is not preferable economically.
本発明においては、消石灰は硫酸鉄を中和するために添加する。消石灰を用いて中和すると石膏が副生する。副生した石膏は、水に難溶性であるため、高湿度のガスが通気してもペレットから溶出することがないため好ましい。一方、例えば、水酸化ナトリウムで中和すると硫酸ナトリウムが副生する。該副生物は水に溶解し易いため、高湿度のガスを通気するとペレットから溶出し、造粒物が崩れて粉化してしまうおそれがあるため、好ましくない。したがって、消石灰以外の塩基性化合物では充分な脱臭効果が得られない。 In the present invention, slaked lime is added to neutralize iron sulfate. When neutralized with slaked lime, gypsum is by-produced. The by-product gypsum is preferable because it is hardly soluble in water and thus does not elute from the pellets even when high-humidity gas is passed. On the other hand, for example, sodium sulfate is by-produced when neutralized with sodium hydroxide. Since the by-product is easily dissolved in water, it is not preferable since it may be eluted from the pellets when a high-humidity gas is passed through, and the granulated material may collapse and be pulverized. Therefore, a basic compound other than slaked lime cannot provide a sufficient deodorizing effect.
消石灰の含有量は、硫酸鉄を中和するために必要な量を添加すればよく、特に限定されるものではないが、固形脱臭組成物の全量中5〜25重量%であることが好ましく、10〜20重量%であることがより好ましい。消石灰の含有量がこの範囲を外れると、硫酸鉄を充分に中和することができないため、装置が腐食する傾向がある。 The slaked lime content is not particularly limited as long as the amount necessary to neutralize iron sulfate is added, but is preferably 5 to 25% by weight in the total amount of the solid deodorizing composition, More preferably, it is 10 to 20% by weight. If the content of slaked lime is out of this range, iron sulfate cannot be sufficiently neutralized, and the device tends to corrode.
また、硫酸鉄と消石灰の配合比は、特に限定されるものではないが、消石灰/硫酸鉄=0.4〜0.6(重量比)であることが好ましく、0.5〜0.6(重量比)であることがより好ましい。消石灰の配合比が0.4未満であると固形脱臭組成物のpHが6未満となり、装置が腐食する傾向があり、0.6をこえると固形脱臭組成物のpHが8をこえ、装置が腐食する傾向がある。 Moreover, the compounding ratio of iron sulfate and slaked lime is not particularly limited, but is preferably slaked lime / iron sulfate = 0.4 to 0.6 (weight ratio), 0.5 to 0.6 ( (Weight ratio) is more preferable. If the blending ratio of slaked lime is less than 0.4, the pH of the solid deodorizing composition tends to be less than 6, and the device tends to corrode. If it exceeds 0.6, the pH of the solid deodorizing composition exceeds 8, and the device There is a tendency to corrode.
本発明で用いる活性炭としては、特に限定されず、種々の活性炭を用いることができる。活性炭としては、黒鉛;褐炭、れき青炭などの石炭、石油または石炭ピッチなどの鉱物系材料;オガクズや間伐材、解体廃材などの木質材料;果実殻(ヤシガラなど)などの植物系材料;動物の骨、皮などの動物系材料;ポリアクリロニトリル(PAN)、フェノール系樹脂、セルロース、再生セルロースなどの高分子材料を原料とする活性炭などがあげられ、これらは、単独でまたは二種以上組み合わせて使用することができる。これらの中でも、木質材料、ヤシガラおよび石炭からなる群から選択される1種以上の原料からなる活性炭が安価に入手できる点から好ましい。 The activated carbon used in the present invention is not particularly limited, and various activated carbons can be used. As activated carbon, graphite; coal such as lignite and bituminous coal; mineral materials such as petroleum or coal pitch; woody materials such as sawdust, thinned wood, and demolition waste; plant materials such as fruit shells (coconut husks); Animal materials such as bones and skins; activated carbons made from polymer materials such as polyacrylonitrile (PAN), phenolic resins, cellulose, and regenerated cellulose. These may be used alone or in combination of two or more. Can be used. Among these, the activated carbon which consists of 1 or more types of raw materials selected from the group which consists of a woody material, coconut husk, and coal is preferable from the point that it can obtain cheaply.
活性炭の形状は、特に限定されるものではないが、粒状(粉粒状)、繊維状などであってもよい。 The shape of the activated carbon is not particularly limited, but may be granular (powdered) or fibrous.
粉粒状活性炭の平均粒子径は、1〜1000μmであることが好ましく、繊維状活性炭の平均繊維径は、10〜50μmであることが好ましい。 The average particle diameter of the granular activated carbon is preferably 1-1000 μm, and the average fiber diameter of the fibrous activated carbon is preferably 10-50 μm.
また、活性炭の比表面積は、100〜1500m2/gであることが好ましく、200〜1000m2/gであることがより好ましい。比表面積が100m2/g未満であると脱臭効果が低下する傾向があり、1500m2/gをこえると活性炭価格が高くなるため、経済的に好ましくないものである。 The specific surface area of the activated carbon is preferably 100~1500m 2 / g, more preferably 200~1000m 2 / g. If the specific surface area is less than 100 m 2 / g, the deodorizing effect tends to decrease, and if it exceeds 1500 m 2 / g, the activated carbon price increases, which is economically undesirable.
活性炭の含有量は、固形脱臭組成物の全量中5〜80重量%であることが好ましく、5〜60重量%であることがより好ましい。活性炭の含有量が5重量%未満であると固形脱臭組成物の乾燥に長時間を要するため経済的に好ましくない。また、80重量%をこえると充分な脱臭効果が得られない傾向がある。 The content of activated carbon is preferably 5 to 80% by weight, and more preferably 5 to 60% by weight, based on the total amount of the solid deodorizing composition. If the content of the activated carbon is less than 5% by weight, it takes a long time to dry the solid deodorizing composition, which is not economically preferable. Moreover, when it exceeds 80 weight%, there exists a tendency for sufficient deodorizing effect not to be acquired.
本発明に用いる腐植質土壌とは、非晶質粘土鉱物であるアロフェン土を主成分とし、フミン酸、ニトロフミン酸、フルボ酸などの有機成分を含む火山灰土壌であり、黒ボク土や黒土、黒暗土と呼称される土壌である。 The humic soil used in the present invention is a volcanic ash soil that is mainly composed of allophane soil, which is an amorphous clay mineral, and contains organic components such as humic acid, nitrohumic acid, and fulvic acid. This soil is called dark soil.
本発明に用いる腐植質土壌は、有機成分が10重量%以上含有されているものであることが好ましく、15重量%以上含有されているものがさらに好ましい。有機成分の含有量が10重量%未満であると、塩基性ガスに対する脱臭効果が低下する傾向がある。 The humic soil used in the present invention preferably contains 10% by weight or more of organic components, and more preferably contains 15% by weight or more. There exists a tendency for the deodorizing effect with respect to basic gas to fall that content of an organic component is less than 10 weight%.
腐植質土壌の配合量は、固形脱臭組成物の全量中5〜60重量%であることが好ましく、10〜30重量%であることがより好ましい。腐植質土壌の含有量が5重量%未満であると、塩基性ガスに対する充分な脱臭効果が得られない傾向があり、60重量%以上であると中性ガスに対する充分な脱臭効果が得られない傾向がある。 The blending amount of the humic soil is preferably 5 to 60% by weight, and more preferably 10 to 30% by weight, based on the total amount of the solid deodorizing composition. When the content of humic soil is less than 5% by weight, there is a tendency that a sufficient deodorizing effect for basic gas cannot be obtained, and when it is 60% by weight or more, a sufficient deodorizing effect for neutral gas cannot be obtained. Tend.
また、本発明の固形脱臭組成物には、適当な形状(例えば、粒状、シート状、ハニカム状など)に成形するために、バインダー成分をさらに含有してもよい。 In addition, the solid deodorizing composition of the present invention may further contain a binder component in order to form into an appropriate shape (for example, granular shape, sheet shape, honeycomb shape, etc.).
バインダー成分としては、ウレタン樹脂、アクリル樹脂、ポリエステル系生分解性樹脂、カルボキシメチルセルロース(CMC)、デンプン、アルギン酸ソーダ、キサンタンガム、グアーガム、カラギーナン、ポリビニルアルコールなどをあげることができ、これらを、単独でまたは二種以上組み合わせて使用することができる。これらの中でも、脱臭性能と生産コストの点から、ポリビニルアルコールが好ましい。 Examples of the binder component include urethane resin, acrylic resin, polyester-based biodegradable resin, carboxymethyl cellulose (CMC), starch, sodium alginate, xanthan gum, guar gum, carrageenan, polyvinyl alcohol, and the like. Two or more types can be used in combination. Among these, polyvinyl alcohol is preferable from the viewpoint of deodorization performance and production cost.
バインダー成分の添加量としては、固形脱臭組成物の全固形分を100とし、これに対し、固形分として0.1〜15重量%となるように添加することが好ましく、1〜5重量%となるように添加することがより好ましい。 As the addition amount of the binder component, the total solid content of the solid deodorizing composition is 100, and it is preferable to add 0.1 to 15% by weight as the solid content, and 1 to 5% by weight. More preferably, it is added.
本発明の固形脱臭組成物には、発明の効果を損なわない程度で種々の添加物を配合することができる。そのような添加物の具体例としては、例えば、ベントナイト、アタパルジャイト、セピオライト、ゼオライトなどがあげられる。 Various additives can be blended with the solid deodorizing composition of the present invention to the extent that the effects of the invention are not impaired. Specific examples of such additives include bentonite, attapulgite, sepiolite, zeolite and the like.
また、本発明の固形脱臭組成物のpHは、6〜8であり、6.5〜7.5であることが好ましい。pHがこの範囲を外れると、装置が腐食する傾向があるため好ましくない。 Moreover, pH of the solid deodorizing composition of this invention is 6-8, and it is preferable that it is 6.5-7.5. If the pH is out of this range, the device tends to corrode, which is not preferable.
ここで、固形脱臭組成物のpHは、以下の方法で測定した値で示される。 Here, the pH of the solid deodorizing composition is indicated by a value measured by the following method.
100ccの三角フラスコに固形脱臭組成物(造粒物)を3g秤取り、水100ccを追加して総重量を測定し、ホットプレートに乗せ穏やかに煮沸を5分間継続後、室温で放冷する。室温になった後、総重量を計り、煮沸前より不足分の蒸留水を追加する。得られた固形脱臭剤の水溶液のpHをpHメータにて測定し、該値を本発明の固形脱臭組成物のpHとする。 3 g of a solid deodorizing composition (granulated product) is weighed in a 100 cc Erlenmeyer flask, 100 cc of water is added and the total weight is measured. After it reaches room temperature, weigh the total weight and add a short amount of distilled water before boiling. The pH of the aqueous solution of the obtained solid deodorant is measured with a pH meter, and this value is defined as the pH of the solid deodorant composition of the present invention.
また、本発明の固形脱臭組成物の製造方法としては、消石灰、活性炭および腐植質土壌を予め配合し、硫酸鉄溶液を添加混合した後、造粒、乾燥して製造することが好ましい。 Moreover, as a manufacturing method of the solid deodorizing composition of this invention, it is preferable to mix | blend slaked lime, activated carbon, and humic soil previously, and after adding and mixing an iron sulfate solution, granulating and drying and manufacturing are preferable.
硫酸鉄溶液は、硫酸鉄水溶液であることが好ましい。また、硫酸鉄溶液の濃度は特に限定されるものではなく、適宜決定することができる。 The iron sulfate solution is preferably an iron sulfate aqueous solution. Moreover, the density | concentration of an iron sulfate solution is not specifically limited, It can determine suitably.
消石灰、活性炭および腐植質土壌を予め配合することで急激な中和熱の発生を防止し、中和で生成する水酸化鉄を均一に分散させることができるため好ましい。 Preliminary blending of slaked lime, activated carbon and humic soil is preferable because it can prevent sudden generation of heat of neutralization and uniformly disperse iron hydroxide produced by neutralization.
造粒方法、乾燥方法としては、通常の方法を用いることができるが、たとえば、圧縮造粒機や押出造粒機により造粒し、振動乾燥機や流動層乾燥機等により乾燥することができる。 As the granulation method and the drying method, usual methods can be used. For example, the granulation method can be granulated by a compression granulator or an extrusion granulator, and dried by a vibration dryer, a fluidized bed dryer or the like. .
また、前記製造方法において、硫酸鉄溶液を添加混合した後に、さらに、バインダーを添加混合する工程を含むことが好ましい。 Moreover, in the said manufacturing method, after adding and mixing an iron sulfate solution, it is preferable to further include the process of adding and mixing a binder.
本発明の固形脱臭組成物が脱臭できる気体としては、硫化水素、メチルメルカプタンなどの酸性ガス、アンモニア、トリメチルアミンなどの塩基性ガスならびに硫化メチル、二硫化メチルなどの中性ガスなどがあげられる。 Examples of gases that can be deodorized by the solid deodorizing composition of the present invention include acidic gases such as hydrogen sulfide and methyl mercaptan, basic gases such as ammonia and trimethylamine, and neutral gases such as methyl sulfide and methyl disulfide.
また、本発明の固形脱臭組成物は、乾式吸着脱臭塔の充填剤として好適に用いることができる。 Moreover, the solid deodorizing composition of this invention can be used suitably as a filler of a dry adsorption deodorizing tower.
つぎに本発明を実施例をあげて説明するが、本発明はかかる実施例のみに限定されるものではない。 Next, the present invention will be described with reference to examples, but the present invention is not limited to such examples.
<造粒物の物性測定>
(pH)
(1)100ccの三角フラスコに造粒物を3g秤取り、水100ccを追加して総重量を測定する。
(2)ホットプレートに載せ穏やかに煮沸を5分間継続後、室温で放冷する。室温になった後、総重量を計り、煮沸前より不足分の蒸留水を追加する。
(3)pHメーターでpHを測定する。測定値をその造粒物のpHとする。
<Measurement of physical properties of granulated product>
(PH)
(1) Weigh 3 g of the granulated material in a 100 cc Erlenmeyer flask, add 100 cc of water, and measure the total weight.
(2) Place on a hot plate and continue boiling gently for 5 minutes, then allow to cool at room temperature. After it reaches room temperature, weigh the total weight and add a short amount of distilled water before boiling.
(3) Measure the pH with a pH meter. The measured value is taken as the pH of the granulated product.
(硬度)
(1)メスシリンダーの空重量を予め計り、次にペレットサンプルを100ccの標線まで充填し、全重量を測定後、サンプル重量を求める。
(2)篩受器に鋼球(直径11mm)30個と上記サンプル100ccを投入し、篩蓋をして篩振とう機に30分かける。
(3)受器の鋼球を取り除いたサンプルを予め計量した別の10メッシュの篩に移し、篩振とう機に3分かける。
(4)篩の全重量を測定し、次式により硬度を算出する。
硬度(%)=(10メッシュ篩上のサンプル重量)/(サンプルの全重量)×100
(hardness)
(1) Weigh the graduated cylinder in advance, then fill the pellet sample up to the 100 cc mark, measure the total weight, and then determine the sample weight.
(2) Thirty steel balls (diameter 11 mm) and 100 cc of the above sample are put into a sieve receiver, and a sieve cover is put on a sieve shaker for 30 minutes.
(3) Transfer the sample from which the steel balls of the receiver have been removed to another 10-mesh sieve weighed in advance, and put it on a sieve shaker for 3 minutes.
(4) The total weight of the sieve is measured, and the hardness is calculated by the following formula.
Hardness (%) = (sample weight on 10 mesh sieve) / (total weight of sample) × 100
(粒度)
(1)7.5メッシュの篩の空重量を予め測定する。
(2)篩受器に7.5メッシュ、3.5メッシュの順にセットし、精秤したサンプル100gを投入し、篩蓋をして篩振とう機にセットし10分間振とうする。
(3)7.5メッシュの篩を取り出し総重量を測定する。
(4)粒度(%)=(7.5メッシュの篩総重量−篩空重量)/サンプル重量×100
(Granularity)
(1) The empty weight of a 7.5 mesh sieve is measured in advance.
(2) Set the sieve receiver in the order of 7.5 mesh and 3.5 mesh, put 100 g of the accurately weighed sample, cover the sieve lid, set on a sieve shaker, and shake for 10 minutes.
(3) Take out a 7.5 mesh screen and measure the total weight.
(4) Particle size (%) = (7.5 mesh total sieve weight−sieving weight) / sample weight × 100
<脱臭性能評価方法>
(硫化水素)
(1)5Lのテドラバックに造粒サンプルを5g投入し、無臭空気を3L充填した。
(2)そこへ初期硫化水素濃度が100ppmとなるようにマイクロシリンジで注入し、注入時点から30、60、120分後の硫化水素濃度を検知管で測定した。なお、造粒物を投入しない空試験も実施し、硫化水素濃度が100ppmであることを確認した。
(3)脱臭率は次式にて算出した。
脱臭率(%)=(100−(測定値))/100×100
<Deodorization performance evaluation method>
(Hydrogen sulfide)
(1) 5 g of the granulated sample was put into a 5 L tedra bag and filled with 3 L of odorless air.
(2) The initial hydrogen sulfide concentration was injected with a microsyringe so that the concentration was 100 ppm, and the hydrogen sulfide concentration after 30, 60, and 120 minutes from the injection point was measured with a detector tube. In addition, the blank test which does not throw in the granulated material was also implemented, and it confirmed that the hydrogen sulfide concentration was 100 ppm.
(3) The deodorization rate was calculated by the following formula.
Deodorization rate (%) = (100− (measured value)) / 100 × 100
(アンモニア)
硫化水素と同様に初期アンモニア濃度を800ppmとして、脱臭率を求めた。
(ammonia)
The deodorization rate was determined by setting the initial ammonia concentration to 800 ppm as in the case of hydrogen sulfide.
(硫化メチル)
硫化水素と同様にして初期硫化メチル濃度を10ppmとして、脱臭率を求めた。
(Methyl sulfide)
The deodorization rate was determined in the same manner as hydrogen sulfide, with an initial methyl sulfide concentration of 10 ppm.
実施例1〜5および比較例1〜4
小型ミキサー(MARUI(株)製)の受け皿に表1に示す量の活性炭、消石灰、腐植質土壌および添加物を投入し、攪拌しながら、表1に示す量の硫酸鉄の水溶液とバインダー水溶液を投入した。投入後5分間攪拌し、造粒用粉体を得た。バインダー水溶液は脱臭剤組成物の固形分全量を100とし、これに対し固形分2重量%を、外数で添加した。
Examples 1-5 and Comparative Examples 1-4
The amount of activated carbon, slaked lime, humic soil and additives shown in Table 1 are put into a saucer of a small mixer (made by MARUI), and the aqueous solution of iron sulfate and binder solution shown in Table 1 are added while stirring. I put it in. After the addition, the mixture was stirred for 5 minutes to obtain a granulating powder. The total amount of the solid content of the deodorant composition was 100, and 2% by weight of the solid content was added in an external number.
得られた造粒用粉体をディスクペレッター(不二パウダル(株)製F−5/11型)に全量投入し、5mm径の円柱状造粒物を得た。その後、得られた造粒物を105℃の恒温乾燥機にて2時間乾燥させ、評価用の造粒物を得た。得られた造粒物の物性(pH、硬度および粒度)を、表1に示す。また、得られた造粒物の硫化水素、アンモニアおよび硫化メチルの脱臭率を評価した。結果をそれぞれ表2、3および4に示す。 The whole amount of the obtained granulating powder was put into a disk pelleter (F-5 / 11 type manufactured by Fuji Powder Co., Ltd.) to obtain a cylindrical granulated product having a diameter of 5 mm. Thereafter, the obtained granulated product was dried for 2 hours with a constant temperature dryer at 105 ° C. to obtain a granulated product for evaluation. Table 1 shows the physical properties (pH, hardness and particle size) of the obtained granulated product. Moreover, the deodorization rate of hydrogen sulfide, ammonia, and methyl sulfide of the obtained granulated product was evaluated. The results are shown in Tables 2, 3 and 4, respectively.
実施例1〜6および比較例1〜4で使用した各原料の詳細を以下に示す。 The detail of each raw material used in Examples 1-6 and Comparative Examples 1-4 is shown below.
<硫酸鉄>
a)ポリ硫酸第二鉄水溶液(商品名:ポリテツ(登録商標)、日鉄鉱業(株)製、固形分濃度:40重量%)
b)硫酸第二鉄水溶液(濃度:40重量%)
c)硫酸第二鉄水溶液(濃度:30重量%)
<Iron sulfate>
a) Aqueous polyferric sulfate aqueous solution (trade name: Polytetsu (registered trademark), manufactured by Nittetsu Mining Co., Ltd., solid content concentration: 40% by weight)
b) Ferric sulfate aqueous solution (concentration: 40% by weight)
c) Ferric sulfate aqueous solution (concentration: 30% by weight)
<消石灰>
消石灰(特号消石灰(弓橋工業(株)製))
<Slaked lime>
Slaked lime (special slaked lime (manufactured by Yumihashi Kogyo Co., Ltd.))
<活性炭>
a)ヤシガラ活性炭:比表面積800m2/g、平均粒子径120μm、水分8%
b)石炭系活性炭:比表面積600m2/g、平均粒子径100μm、水分10%
c)木質系活性炭:比表面積500m2/g、平均粒子径130μm、水分6%
<Activated carbon>
a) Coconut shell activated carbon: specific surface area 800 m 2 / g, average particle size 120 μm, moisture 8%
b) Coal-based activated carbon: specific surface area 600 m 2 / g, average particle size 100 μm, moisture 10%
c) Wood-based activated carbon: specific surface area 500 m 2 / g, average particle size 130 μm, moisture 6%
<腐植質土壌>
a)有機成分17重量%の腐植質土壌:鹿児島県産
b)有機成分10重量%の腐植質土壌:三重県産
c)有機成分5重量%の腐植質土壌:山形県産
<Humus soil>
a) Humic soil with 17% organic content: Kagoshima Prefecture b) Humic soil with 10% organic component: Mie Prefecture c) Humic soil with 5% organic component: Yamagata Prefecture
<添加物>
a)アタパルジャイト(商品名:SGB(Zemex Attapulgite LLC製))
b)セピオライト(商品名:ミルエンSP(昭和鉱業(株)製))
<Additives>
a) Attapulgite (trade name: SGB (manufactured by Zemex Attapulgite LLC))
b) Sepiolite (trade name: Milen SP (manufactured by Showa Mining Co., Ltd.))
<バインダー>
a)ポリビニルアルコール(PVA)(商品名:ゴーゼノールKH−17(日本合成化学工業(株)製))の7.7重量%水溶液
b)水系ウレタン樹脂(商品名:スーパーフレックス860(第一工業製薬(株)製)、ポリエステル系アニオン性水系ウレタン樹脂)の40重量%水溶液
c)ポリエステル系生分解性樹脂(商品名:プラセマL110(第一工業製薬(株)製)、ポリ乳酸エマルジョン)の13重量%水溶液
<Binder>
a) 7.7 wt% aqueous solution of polyvinyl alcohol (PVA) (trade name: Gozenol KH-17 (manufactured by Nippon Synthetic Chemical Industry Co., Ltd.)) b) water-based urethane resin (trade name: Superflex 860 (Daiichi Kogyo Seiyaku) 13) of polyester-based anionic water-based urethane resin) 40% by weight aqueous solution c) polyester-based biodegradable resin (trade name: Prasema L110 (Daiichi Kogyo Seiyaku Co., Ltd.), polylactic acid emulsion) % By weight aqueous solution
表2から明らかなように、腐植質土壌の配合量に関係なく、硫化水素を充分に脱臭する効果があることがわかる。 As is apparent from Table 2, it can be seen that there is an effect of sufficiently deodorizing hydrogen sulfide regardless of the blending amount of humic soil.
表3から明らかなように、腐植質土壌を添加していない場合(比較例1〜3)では、アンモニアの脱臭率は低く、充分な脱臭効果が得られないことがわかる。また、アンモニアは腐植質土壌が増加すると脱臭率が向上することがわかる。 As can be seen from Table 3, when no humic soil is added (Comparative Examples 1 to 3), the deodorization rate of ammonia is low, and it is understood that a sufficient deodorizing effect cannot be obtained. In addition, it can be seen that ammonia increases the deodorization rate when the humic soil increases.
表4から明らかなように、活性炭を配合していない場合(比較例3)は、硫化メチルの脱臭率が低く、脱臭効果が充分でないことがわかる。 As can be seen from Table 4, when activated carbon is not blended (Comparative Example 3), the deodorization rate of methyl sulfide is low and the deodorizing effect is not sufficient.
実施例6
小型ミキサー(MARUI(株)製)の受け皿に木質活性炭30重量部、消石灰12重量部、腐植質土壌(有機成分17重量%)30重量部およびアタパルジャイト4重量部を投入し、攪拌しながら、ポリ硫酸第二鉄水溶液60重量部とバインダーとしてポリビニルアルコール水溶液を投入した。投入後5分間攪拌し、造粒用粉体を得た。ポリビニルアルコール水溶液は脱臭剤組成物の固形分全量を100とし、これに対し固形分2重量%を、外数で添加した。
Example 6
In a small mixer (made by MARUI), 30 parts by weight of activated carbon, 12 parts by weight of slaked lime, 30 parts by weight of humic soil (17% by weight of organic components) and 4 parts by weight of attapulgite are added, and while stirring, 60 parts by weight of a ferric sulfate aqueous solution and a polyvinyl alcohol aqueous solution as a binder were added. After the addition, the mixture was stirred for 5 minutes to obtain a granulating powder. The total amount of the solid content of the deodorant composition in the polyvinyl alcohol aqueous solution was 100, and 2% by weight of the solid content was added in an external number.
得られた造粒用粉体をディスクペレッター(不二パウダル(株)製F−5/11型)に全量投入し、5mm径の円柱状造粒物を得た。その後、得られた造粒物を105℃の恒温乾燥機にて2時間乾燥させ、評価用の造粒物を得た。得られた造粒物を以下の試験に使用した。 The whole amount of the obtained granulating powder was put into a disk pelleter (F-5 / 11 type manufactured by Fuji Powder Co., Ltd.) to obtain a cylindrical granulated product having a diameter of 5 mm. Thereafter, the obtained granulated product was dried for 2 hours with a constant temperature dryer at 105 ° C. to obtain a granulated product for evaluation. The obtained granulated material was used for the following tests.
試験例1
下水処理場における活性炭脱臭塔の入口臭気(表4の臭気成分を含有する)を、小型脱臭装置(直径20cm、固形脱臭組成物の充填高さ1.5m)にガス通過速度0.116m/s、接触時間約13秒の条件で1年間通気し、入口と出口の悪臭濃度を測定した。各臭気成分の測定は、環境庁告示第9号に準じて行なった。
Test example 1
The entrance odor of the activated carbon deodorization tower in the sewage treatment plant (containing the odor components shown in Table 4) was passed through a small deodorization device (diameter 20 cm, filling height of solid deodorization composition 1.5 m) at a gas passage speed of 0.116 m / s. Then, aeration was conducted for 1 year under the condition of a contact time of about 13 seconds, and the malodor concentration at the inlet and outlet was measured. Each odor component was measured according to Environmental Agency Notification No. 9.
結果を表5に示す。 The results are shown in Table 5.
表5より、本発明の固形脱臭組成物は、酸性ガス、塩基性ガスおよび中性ガスの複数の臭気を同時に脱臭できることがわかる。 From Table 5, it turns out that the solid deodorizing composition of this invention can deodorize several odor of acidic gas, basic gas, and neutral gas simultaneously.
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JP2010051840A (en) * | 2008-08-26 | 2010-03-11 | Jikco Ltd | Agent for treating flue gas, and method for treating flue gas |
JP2010222163A (en) * | 2009-03-23 | 2010-10-07 | Kuraray Chem Corp | High functional granulated carbon and method for manufacturing the same |
JP2011045827A (en) * | 2009-08-26 | 2011-03-10 | Dai Ichi Kogyo Seiyaku Co Ltd | Desulfurizing agent and method of manufacturing the same |
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JPS63203161A (en) * | 1987-02-19 | 1988-08-23 | エンザイム株式会社 | Malodor deodorant composed of humus in solid phase, liquid phase and mixed phase, and its production and use |
JPH02131137A (en) * | 1988-11-10 | 1990-05-18 | Fujisawa Pharmaceut Co Ltd | Deodorant |
JPH05293162A (en) * | 1992-04-15 | 1993-11-09 | Nippon Steel Corp | Air cleaner and its production |
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JPH02131137A (en) * | 1988-11-10 | 1990-05-18 | Fujisawa Pharmaceut Co Ltd | Deodorant |
JPH05293162A (en) * | 1992-04-15 | 1993-11-09 | Nippon Steel Corp | Air cleaner and its production |
JP2002253960A (en) * | 2001-02-27 | 2002-09-10 | Tanimoto Daiki | Deodorant and production method therefor |
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Cited By (3)
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JP2010051840A (en) * | 2008-08-26 | 2010-03-11 | Jikco Ltd | Agent for treating flue gas, and method for treating flue gas |
JP2010222163A (en) * | 2009-03-23 | 2010-10-07 | Kuraray Chem Corp | High functional granulated carbon and method for manufacturing the same |
JP2011045827A (en) * | 2009-08-26 | 2011-03-10 | Dai Ichi Kogyo Seiyaku Co Ltd | Desulfurizing agent and method of manufacturing the same |
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