JP2010179248A - Method for treating livestock sludge - Google Patents
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- JP2010179248A JP2010179248A JP2009025456A JP2009025456A JP2010179248A JP 2010179248 A JP2010179248 A JP 2010179248A JP 2009025456 A JP2009025456 A JP 2009025456A JP 2009025456 A JP2009025456 A JP 2009025456A JP 2010179248 A JP2010179248 A JP 2010179248A
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- 239000010802 sludge Substances 0.000 title claims abstract description 69
- 244000144972 livestock Species 0.000 title claims abstract description 36
- 238000000034 method Methods 0.000 title claims abstract description 27
- 125000002091 cationic group Chemical group 0.000 claims abstract description 49
- 229920003169 water-soluble polymer Polymers 0.000 claims abstract description 40
- 239000007800 oxidant agent Substances 0.000 claims abstract description 34
- 229920002554 vinyl polymer Polymers 0.000 claims abstract description 29
- 125000000391 vinyl group Chemical group [H]C([*])=C([H])[H] 0.000 claims abstract description 24
- 230000001590 oxidative effect Effects 0.000 claims abstract description 21
- 238000006116 polymerization reaction Methods 0.000 claims abstract description 21
- WQYVRQLZKVEZGA-UHFFFAOYSA-N hypochlorite Chemical compound Cl[O-] WQYVRQLZKVEZGA-UHFFFAOYSA-N 0.000 claims abstract description 10
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 claims abstract description 8
- SXDBWCPKPHAZSM-UHFFFAOYSA-M bromate Inorganic materials [O-]Br(=O)=O SXDBWCPKPHAZSM-UHFFFAOYSA-M 0.000 claims abstract description 8
- SXDBWCPKPHAZSM-UHFFFAOYSA-N bromic acid Chemical compound OBr(=O)=O SXDBWCPKPHAZSM-UHFFFAOYSA-N 0.000 claims abstract description 8
- JGJLWPGRMCADHB-UHFFFAOYSA-N hypobromite Chemical compound Br[O-] JGJLWPGRMCADHB-UHFFFAOYSA-N 0.000 claims abstract description 8
- 230000004048 modification Effects 0.000 claims abstract description 7
- 238000012986 modification Methods 0.000 claims abstract description 7
- 238000004332 deodorization Methods 0.000 claims abstract description 5
- 229910001919 chlorite Inorganic materials 0.000 claims abstract description 4
- 229910052619 chlorite group Inorganic materials 0.000 claims abstract description 4
- QBWCMBCROVPCKQ-UHFFFAOYSA-N chlorous acid Chemical compound OCl=O QBWCMBCROVPCKQ-UHFFFAOYSA-N 0.000 claims abstract description 4
- 239000000178 monomer Substances 0.000 claims description 13
- 229910052739 hydrogen Inorganic materials 0.000 claims description 12
- 239000001257 hydrogen Substances 0.000 claims description 12
- 229920000642 polymer Polymers 0.000 claims description 12
- 229920006317 cationic polymer Polymers 0.000 claims description 10
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims description 8
- 150000001450 anions Chemical class 0.000 claims description 8
- 125000004432 carbon atom Chemical group C* 0.000 claims description 8
- 125000002496 methyl group Chemical group [H]C([H])([H])* 0.000 claims description 8
- 238000006068 polycondensation reaction Methods 0.000 claims description 8
- 125000003545 alkoxy group Chemical group 0.000 claims description 6
- 125000000217 alkyl group Chemical group 0.000 claims description 6
- 125000001797 benzyl group Chemical group [H]C1=C([H])C([H])=C(C([H])=C1[H])C([H])([H])* 0.000 claims description 6
- 150000002431 hydrogen Chemical class 0.000 claims description 4
- 238000003672 processing method Methods 0.000 claims description 4
- 125000002947 alkylene group Chemical group 0.000 claims description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical group [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 2
- 150000001768 cations Chemical class 0.000 claims description 2
- 230000001112 coagulating effect Effects 0.000 claims description 2
- 238000007334 copolymerization reaction Methods 0.000 claims description 2
- 125000004435 hydrogen atom Chemical group [H]* 0.000 claims description 2
- 229910052760 oxygen Inorganic materials 0.000 claims description 2
- 239000001301 oxygen Substances 0.000 claims description 2
- 239000000701 coagulant Substances 0.000 claims 1
- 208000005156 Dehydration Diseases 0.000 abstract description 12
- 230000018044 dehydration Effects 0.000 abstract description 12
- 238000006297 dehydration reaction Methods 0.000 abstract description 12
- 230000008569 process Effects 0.000 abstract description 10
- 230000009467 reduction Effects 0.000 abstract description 4
- DKSMCEUSSQTGBK-UHFFFAOYSA-M bromite Chemical compound [O-]Br=O DKSMCEUSSQTGBK-UHFFFAOYSA-M 0.000 abstract 2
- 230000016615 flocculation Effects 0.000 abstract 1
- 238000005189 flocculation Methods 0.000 abstract 1
- 239000000203 mixture Substances 0.000 description 12
- 238000009472 formulation Methods 0.000 description 10
- 230000000052 comparative effect Effects 0.000 description 7
- 239000000126 substance Substances 0.000 description 7
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 6
- 125000001931 aliphatic group Chemical group 0.000 description 6
- 230000015271 coagulation Effects 0.000 description 6
- 238000005345 coagulation Methods 0.000 description 6
- 230000000694 effects Effects 0.000 description 6
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- 150000001412 amines Chemical class 0.000 description 5
- 125000000129 anionic group Chemical group 0.000 description 5
- 238000006243 chemical reaction Methods 0.000 description 5
- 239000008394 flocculating agent Substances 0.000 description 5
- 238000003756 stirring Methods 0.000 description 5
- 238000012360 testing method Methods 0.000 description 5
- 239000005708 Sodium hypochlorite Substances 0.000 description 4
- 239000000706 filtrate Substances 0.000 description 4
- 150000007524 organic acids Chemical class 0.000 description 4
- 239000002245 particle Substances 0.000 description 4
- 150000003839 salts Chemical class 0.000 description 4
- SUKJFIGYRHOWBL-UHFFFAOYSA-N sodium hypochlorite Chemical compound [Na+].Cl[O-] SUKJFIGYRHOWBL-UHFFFAOYSA-N 0.000 description 4
- 239000000243 solution Substances 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- HRPVXLWXLXDGHG-UHFFFAOYSA-N Acrylamide Chemical compound NC(=O)C=C HRPVXLWXLXDGHG-UHFFFAOYSA-N 0.000 description 3
- ZMANZCXQSJIPKH-UHFFFAOYSA-N Triethylamine Chemical compound CCN(CC)CC ZMANZCXQSJIPKH-UHFFFAOYSA-N 0.000 description 3
- 238000004220 aggregation Methods 0.000 description 3
- 229910021529 ammonia Inorganic materials 0.000 description 3
- 239000007864 aqueous solution Substances 0.000 description 3
- 239000006185 dispersion Substances 0.000 description 3
- 229920000768 polyamine Polymers 0.000 description 3
- 239000000843 powder Substances 0.000 description 3
- 238000012546 transfer Methods 0.000 description 3
- 239000007762 w/o emulsion Substances 0.000 description 3
- 239000002699 waste material Substances 0.000 description 3
- ROSDSFDQCJNGOL-UHFFFAOYSA-N Dimethylamine Chemical compound CNC ROSDSFDQCJNGOL-UHFFFAOYSA-N 0.000 description 2
- QUSNBJAOOMFDIB-UHFFFAOYSA-N Ethylamine Chemical compound CCN QUSNBJAOOMFDIB-UHFFFAOYSA-N 0.000 description 2
- BAVYZALUXZFZLV-UHFFFAOYSA-N Methylamine Chemical compound NC BAVYZALUXZFZLV-UHFFFAOYSA-N 0.000 description 2
- 239000004677 Nylon Substances 0.000 description 2
- 238000005054 agglomeration Methods 0.000 description 2
- AZDRQVAHHNSJOQ-UHFFFAOYSA-N alumane Chemical class [AlH3] AZDRQVAHHNSJOQ-UHFFFAOYSA-N 0.000 description 2
- NEHMKBQYUWJMIP-UHFFFAOYSA-N chloromethane Chemical compound ClC NEHMKBQYUWJMIP-UHFFFAOYSA-N 0.000 description 2
- 229920001577 copolymer Polymers 0.000 description 2
- 238000004132 cross linking Methods 0.000 description 2
- -1 dimethylaminoethyl Chemical group 0.000 description 2
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- 239000005017 polysaccharide Substances 0.000 description 2
- 239000000047 product Substances 0.000 description 2
- GETQZCLCWQTVFV-UHFFFAOYSA-N trimethylamine Chemical compound CN(C)C GETQZCLCWQTVFV-UHFFFAOYSA-N 0.000 description 2
- 239000002351 wastewater Substances 0.000 description 2
- VILCJCGEZXAXTO-UHFFFAOYSA-N 2,2,2-tetramine Chemical compound NCCNCCNCCN VILCJCGEZXAXTO-UHFFFAOYSA-N 0.000 description 1
- HZAXFHJVJLSVMW-UHFFFAOYSA-N 2-Aminoethan-1-ol Chemical compound NCCO HZAXFHJVJLSVMW-UHFFFAOYSA-N 0.000 description 1
- FVPMLCUKLBYBSV-UHFFFAOYSA-M 2-hydroxypropyl-dimethyl-(prop-2-enoyloxymethyl)azanium;chloride Chemical compound [Cl-].CC(O)C[N+](C)(C)COC(=O)C=C FVPMLCUKLBYBSV-UHFFFAOYSA-M 0.000 description 1
- RIAVQNCBHNMYFJ-UHFFFAOYSA-M 2-hydroxypropyl-dimethyl-[phenyl(prop-2-enoyloxy)methyl]azanium;chloride Chemical compound [Cl-].CC(O)C[N+](C)(C)C(OC(=O)C=C)C1=CC=CC=C1 RIAVQNCBHNMYFJ-UHFFFAOYSA-M 0.000 description 1
- NIXOWILDQLNWCW-UHFFFAOYSA-M Acrylate Chemical compound [O-]C(=O)C=C NIXOWILDQLNWCW-UHFFFAOYSA-M 0.000 description 1
- 208000024827 Alzheimer disease Diseases 0.000 description 1
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 description 1
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 1
- RPNUMPOLZDHAAY-UHFFFAOYSA-N Diethylenetriamine Chemical compound NCCNCCN RPNUMPOLZDHAAY-UHFFFAOYSA-N 0.000 description 1
- BRLQWZUYTZBJKN-UHFFFAOYSA-N Epichlorohydrin Chemical compound ClCC1CO1 BRLQWZUYTZBJKN-UHFFFAOYSA-N 0.000 description 1
- PIICEJLVQHRZGT-UHFFFAOYSA-N Ethylenediamine Chemical compound NCCN PIICEJLVQHRZGT-UHFFFAOYSA-N 0.000 description 1
- CERQOIWHTDAKMF-UHFFFAOYSA-N Methacrylic acid Chemical compound CC(=C)C(O)=O CERQOIWHTDAKMF-UHFFFAOYSA-N 0.000 description 1
- 239000004372 Polyvinyl alcohol Substances 0.000 description 1
- GSEJCLTVZPLZKY-UHFFFAOYSA-N Triethanolamine Chemical compound OCCN(CCO)CCO GSEJCLTVZPLZKY-UHFFFAOYSA-N 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 230000004931 aggregating effect Effects 0.000 description 1
- 229920006318 anionic polymer Polymers 0.000 description 1
- KCXMKQUNVWSEMD-UHFFFAOYSA-N benzyl chloride Chemical compound ClCC1=CC=CC=C1 KCXMKQUNVWSEMD-UHFFFAOYSA-N 0.000 description 1
- 229940073608 benzyl chloride Drugs 0.000 description 1
- ZGCZDEVLEULNLJ-UHFFFAOYSA-M benzyl-dimethyl-(2-prop-2-enoyloxyethyl)azanium;chloride Chemical compound [Cl-].C=CC(=O)OCC[N+](C)(C)CC1=CC=CC=C1 ZGCZDEVLEULNLJ-UHFFFAOYSA-M 0.000 description 1
- QBZPCMKUFMJWAN-UHFFFAOYSA-N benzyl-dimethyl-[3-(prop-2-enoylamino)propyl]azanium;chloride Chemical compound [Cl-].C=CC(=O)NCCC[N+](C)(C)CC1=CC=CC=C1 QBZPCMKUFMJWAN-UHFFFAOYSA-N 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 230000005591 charge neutralization Effects 0.000 description 1
- 239000000460 chlorine Substances 0.000 description 1
- 229910052801 chlorine Inorganic materials 0.000 description 1
- 230000003749 cleanliness Effects 0.000 description 1
- 238000004581 coalescence Methods 0.000 description 1
- 238000009264 composting Methods 0.000 description 1
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- ZBCBWPMODOFKDW-UHFFFAOYSA-N diethanolamine Chemical compound OCCNCCO ZBCBWPMODOFKDW-UHFFFAOYSA-N 0.000 description 1
- HPNMFZURTQLUMO-UHFFFAOYSA-N diethylamine Chemical compound CCNCC HPNMFZURTQLUMO-UHFFFAOYSA-N 0.000 description 1
- GQOKIYDTHHZSCJ-UHFFFAOYSA-M dimethyl-bis(prop-2-enyl)azanium;chloride Chemical compound [Cl-].C=CC[N+](C)(C)CC=C GQOKIYDTHHZSCJ-UHFFFAOYSA-M 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
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- 125000003010 ionic group Chemical group 0.000 description 1
- 150000002505 iron Chemical class 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000012263 liquid product Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 229940050176 methyl chloride Drugs 0.000 description 1
- 150000007522 mineralic acids Chemical class 0.000 description 1
- 239000003607 modifier Substances 0.000 description 1
- LSHROXHEILXKHM-UHFFFAOYSA-N n'-[2-[2-[2-(2-aminoethylamino)ethylamino]ethylamino]ethyl]ethane-1,2-diamine Chemical compound NCCNCCNCCNCCNCCN LSHROXHEILXKHM-UHFFFAOYSA-N 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 229920000058 polyacrylate Polymers 0.000 description 1
- 229920001184 polypeptide Polymers 0.000 description 1
- 229920002451 polyvinyl alcohol Polymers 0.000 description 1
- 230000002265 prevention Effects 0.000 description 1
- 102000004196 processed proteins & peptides Human genes 0.000 description 1
- 108090000765 processed proteins & peptides Proteins 0.000 description 1
- 150000003242 quaternary ammonium salts Chemical class 0.000 description 1
- 238000002407 reforming Methods 0.000 description 1
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- 230000001954 sterilising effect Effects 0.000 description 1
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- FZGFBJMPSHGTRQ-UHFFFAOYSA-M trimethyl(2-prop-2-enoyloxyethyl)azanium;chloride Chemical compound [Cl-].C[N+](C)(C)CCOC(=O)C=C FZGFBJMPSHGTRQ-UHFFFAOYSA-M 0.000 description 1
- OEIXGLMQZVLOQX-UHFFFAOYSA-N trimethyl-[3-(prop-2-enoylamino)propyl]azanium;chloride Chemical compound [Cl-].C[N+](C)(C)CCCNC(=O)C=C OEIXGLMQZVLOQX-UHFFFAOYSA-N 0.000 description 1
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Abstract
Description
本発明は畜産汚泥の処理方法に関するものであり、詳しくは畜産汚泥に対し、無機系酸化剤を添加し消臭処理及び改質処理した後、ビニル重合系カチオン性水溶性及び/またはビニル重合系両性水溶性高分子を添加、凝集処理し、その後脱水機により脱水することを特徴とする畜産汚泥の処理方法に関する。 The present invention relates to a method for treating livestock sludge, and more specifically, after adding an inorganic oxidant to a livestock sludge to deodorize and modify it, a vinyl polymerization cationic water-soluble and / or vinyl polymerization system The present invention relates to a method for treating livestock sludge, characterized in that an amphoteric water-soluble polymer is added, coagulated, and then dehydrated by a dehydrator.
汚泥を脱水する場合、従来、カチオン性凝集剤が使用されていたが、難脱水性汚泥の場合は、無機凝集剤を添加した後、カチオン性有機高分子凝集剤を併用する処方あるいは同様な処方で両性有機高分子凝集剤併用、無機凝集剤、アニオン性凝集剤およびカチオン性凝集剤の三種を併用する処方(特許文献1)、また、非イオン性ポリビニルアルコ−ルとカチオン性及び/または両性凝集剤を併用する処方などが開示されている。しかし、汚泥の変動に対して十分対応でき、安定的処理が可能で、脱水ケ−キの含水率が十分低下し、脱水後の工程を効率よく行えるかなど考慮した場合、まだまだ完全な処方というのは、提案されていないのが現状である。 In the case of dewatering sludge, a cationic flocculant has been used in the past, but in the case of difficultly dewatered sludge, after adding an inorganic flocculant, a prescription using a cationic organic polymer flocculant or a similar prescription And a combination of amphoteric organic polymer flocculants, inorganic flocculants, anionic flocculants and cationic flocculants (Patent Document 1), and nonionic polyvinyl alcohol and cationic and / or amphoteric A prescription using a flocculant in combination is disclosed. However, it is possible to handle sludge fluctuations sufficiently, stable treatment is possible, the moisture content of the dewatering cake is sufficiently reduced, and if the process after dewatering can be performed efficiently, it is still a complete recipe The current situation has not been proposed.
畜産廃水における汚泥処理方法に関しては、カチオン性あるいは両性水溶性高分子を添加した処方が主流を占めているが、作業現場における臭気の問題までは解決できていない状況である。臭気を防止するために無機系酸化剤を使用する汚泥脱水に関しては特許文献4が提案されているが、この処方は無機酸化剤を添加し攪拌、反応させた後に鉄塩やアルミニウム塩など無機凝集剤を添加した後、カチオン性および/または両性高分子凝集剤を添加し脱水する方法である。特にアルミニウム塩はアルツハイマー症との関連が懸念され、使用を控える傾向にある。従って畜産汚泥に関しては、臭気防止と汚泥処理工程の効率化に関する処方はまだ提案されていない状況である。
本発明の課題は、畜産汚泥に関し従来よりも処理コストの低減と同時に、脱水処理工程中における悪臭を低減することにより作業環境や近隣地域環境の改善を図ることが可能であり、およびより汚泥脱水性の向上した処理方法を提供することである。 The problem of the present invention is that it is possible to improve the working environment and the surrounding area environment by reducing the malodor during the dehydration process at the same time as the treatment cost of livestock sludge, and more sludge dewatering. It is to provide a processing method with improved performance.
本発明者は上記課題を解決するため、詳細な検討を行った結果、畜産汚泥の脱水処理において、従来法より効率良く、かつ脱水ケ−キ含水率も低下し、臭気も低減する処方を発見し本発明に到達した。すなわち、本発明の請求項1の発明は、畜産汚泥に対し、下記酸化剤群より選択される一種以上の無機系酸化剤により消臭処理及び改質処理を施した後、ビニル重合系カチオン性水溶性及び/またはビニル重合系両性水溶性高分子を添加し、凝集処理し、その後脱水機により脱水することを特徴とする畜産汚泥の処理方法である。
酸化剤群;亜塩素酸塩、次亜塩素酸塩、臭素酸塩、亜臭素酸塩、次亜臭素酸塩、過酸化水素。
As a result of detailed studies to solve the above-mentioned problems, the present inventor has found a prescription that is more efficient than the conventional method in dehydration treatment of livestock sludge, has a reduced dehydrated cake water content, and reduces odor. The present invention has been reached. That is, the invention of claim 1 of the present invention is a vinyl polymerized cationic substance after subjecting livestock sludge to deodorization treatment and modification treatment with one or more inorganic oxidants selected from the following oxidizer group. A livestock sludge treatment method comprising adding a water-soluble and / or vinyl polymerization-based amphoteric water-soluble polymer, aggregating and then dehydrating with a dehydrator.
Oxidizing agent group; chlorite, hypochlorite, bromate, bromate, hypobromite, hydrogen peroxide.
請求項2の発明は、前記ビニル重合系水溶性カチオン性高分子が、下記一般式(1)および/または下記一般式(2)で表される単量体を20〜100モル%共重合して得られるカチオン性水溶性高分子、下記一般式(4)および/または下記一般式(5)で表される構造単位を10〜90モル%有するカチオン性水溶性高分子から選択される一種以上、前記ビニル重合系両性水溶性高分子が、下記一般式(1)および/または下記一般式(2)で表される単量体を20〜100モル%、下記一般式(3)で表される単量体を5〜50モル%共重合して得られる両性水溶性高分子であることを特徴とする請求項1に記載の畜産汚泥の処理方法である。
一般式(1)
R1は水素又はメチル基、R2、R3は炭素数1〜3のアルキル基、アルコキシ基あるいはベンジル基、R4は水素、炭素数1〜3のアルキル基、アルコキシル基あるいはベンジル基であり、同種でも異種でも良い。Aは酸素またはNH、Bは炭素数2〜4のアルキレン基またはアルコキシレン基、X1は陰イオンをそれぞれ表わす。
R5は水素又はメチル基、R6、R7は炭素数1〜3のアルキル基、アルコキシル基あるいはベンジル基、X2は陰イオンをそれぞれ表わす。
R8は水素またはCH2COOY2、QはSO3、C6H4SO3、
CONHC(CH3)2CH2SO3、C6H4COOあるいはCOO、R9は水素、メチル基またはCOOY3であり、Y1、Y2は水素または陽イオンをそれぞれ表わす。
General formula (1)
R 1 is hydrogen or a methyl group, R 2 and R 3 are an alkyl group having 1 to 3 carbon atoms, an alkoxy group or a benzyl group, and R 4 is hydrogen, an alkyl group having 1 to 3 carbon atoms, an alkoxyl group or a benzyl group. , Same or different. A represents oxygen or NH, B represents an alkylene group or alkoxylene group having 2 to 4 carbon atoms, and X 1 represents an anion.
R 5 represents hydrogen or a methyl group, R 6 and R 7 each represent an alkyl group having 1 to 3 carbon atoms, an alkoxyl group or a benzyl group, and X 2 represents an anion.
R 8 is hydrogen or CH 2 COOY 2 , Q is SO 3 , C 6 H 4 SO 3 ,
CONHC (CH 3 ) 2 CH 2 SO 3 , C 6 H 4 COO or COO, R 9 is hydrogen, a methyl group or COOY 3 , and Y 1 and Y 2 each represent hydrogen or a cation.
請求項3の発明は、前記畜産汚泥に対し、前記無機系酸化剤、重縮合系カチオン性水溶性高分子、前記ビニル重合系カチオン性水溶性及び/またはビニル重合系両性水溶性高分子をこの順に添加することを特徴とする請求項1に記載の畜産汚泥の処理方法である。 According to a third aspect of the present invention, the inorganic oxidant, the polycondensation cationic water-soluble polymer, the vinyl polymerization cationic water-soluble and / or the vinyl polymerization amphoteric water-soluble polymer are added to the livestock sludge. It is added in order, It is the processing method of the livestock sludge of Claim 1 characterized by the above-mentioned.
請求項4の発明は、前記ビニル重合系カチオン性水溶性及び/またはビニル重合系両性水溶性高分子の重量平均分子量が300万以上、2000万以下であることを特徴とする請求項1〜3のいずれかに記載の畜産汚泥の処理方法である。 The invention according to claim 4 is characterized in that the vinyl polymer cationic water-soluble and / or vinyl polymer amphoteric water-soluble polymer has a weight average molecular weight of 3 million or more and 20 million or less. It is the processing method of livestock sludge as described in any of these.
請求項5の発明は、前記脱水機がフィルタ−プレスあるいはロータリープレスであることを特徴とする請求項1〜4のいずれかに記載の畜産汚泥の処理方法である。 A fifth aspect of the present invention is the livestock sludge treatment method according to any one of the first to fourth aspects, wherein the dehydrator is a filter press or a rotary press.
本発明は、畜産汚泥に対し、無機系酸化剤により消臭処理及び改質処理を施した後、ビニル重合系カチオン性水溶性及び/またはビニル重合系両性水溶性高分子を添加し凝集処理し、その後脱水機により脱水することからなる。本発明の特徴は、無機系酸化剤を添加しない場合に較べ薬剤添加量を10%〜20%削減することが可能である。これに対して本発明では、無機系酸化剤添加後に加えるカチオン性あるいは両性水溶性高分子の凝集効果が高まることによると考えられる。すなわち無機系酸化剤添加によってある程度の凝結作用が発生し、カチオン性あるいは両性水溶性高分子のカチオン性基の電荷的に無駄がなく、ほぼ二次的な凝集反応に使用される。更に重要な効果として脱水処理工程中における悪臭を低減することにより作業環境や近隣地域環境の改善を図ることが可能である。 In the present invention, livestock sludge is subjected to deodorization treatment and modification treatment with an inorganic oxidant, and then added with a vinyl polymerization cationic water-soluble and / or vinyl polymerization amphoteric water-soluble polymer for aggregation treatment. Then, it consists of dehydrating with a dehydrator. The feature of the present invention is that it is possible to reduce the amount of drug added by 10% to 20% compared to the case where no inorganic oxidant is added. In contrast, in the present invention, it is considered that the aggregation effect of the cationic or amphoteric water-soluble polymer added after the addition of the inorganic oxidant is increased. That is, a certain degree of coagulation occurs due to the addition of the inorganic oxidant, and there is no waste in the charge of the cationic group of the cationic or amphoteric water-soluble polymer, and it is used for the secondary secondary agglomeration reaction. Furthermore, as an important effect, it is possible to improve the working environment and the surrounding area environment by reducing malodor during the dehydration process.
本発明で使用する無機系酸化剤群としては亜塩素酸塩、次亜塩素酸塩、臭素酸塩、亜臭素酸塩、次亜臭素酸塩、過酸化水素等が上げられる。中でも次亜塩素酸塩が汎用的に使用されている場合が多いので、推奨される。事前の予備試験に従った添加量を加え、適度な攪拌をする事で改質処理を実施すると同時に、脱水処理工程中における悪臭を低減することにより作業環境や近隣地域環境の改善を図ることが可能であり、更に殺菌作用による汚泥脱水工程の清潔度を提供する事が出来る。 Examples of the inorganic oxidant group used in the present invention include chlorite, hypochlorite, bromate, bromate, hypobromite, hydrogen peroxide, and the like. Of these, hypochlorite is recommended because it is often used for general purposes. It is possible to improve the working environment and the surrounding area environment by reducing the malodor during the dehydration process at the same time as the reforming process is carried out by adding the amount according to the preliminary test in advance and stirring appropriately. It is possible to provide the cleanliness of the sludge dewatering process by sterilization.
これら無機系酸化剤群とカチオン性高分子あるいは両性高分子の単量体に対する添加量としては、50:1〜2:1であり、好ましくは10:1〜5:1である。50:1以下では、酸化剤としての効果がなく、5:1以上では、コスト的に不利になる。 The addition amount of these inorganic oxidant group and cationic polymer or amphoteric polymer monomer is 50: 1 to 2: 1, preferably 10: 1 to 5: 1. If it is 50: 1 or less, there is no effect as an oxidizing agent, and if it is 5: 1 or more, it is disadvantageous in terms of cost.
添加する無機系酸化剤群と組み合わせて使用するカチオン性及び/または両性水溶性高分子は、アクリル系カチオン性単量体、たとえば、(メタ)アクリル酸ジメチルアミノエチルやジメチルアミノプロピル(メタ)アクリルアミドなどの無機酸や有機酸の塩、あるいは塩化メチルや塩化ベンジルによる四級アンモニウム塩の単独重合体、あるいはアクリルアミドとの共重合体である。例えば単量体として、(メタ)アクリロイルオキシエチルトリメチルアンモニウム塩化物、(メタ)アクリロイルオキシ2−ヒドロキシプロピルトリメチルアンモニウム塩化物、(メタ)アクリロイルアミノプロピルトリメチルアンモニウム塩化物、(メタ)アクリロイルオキシエチルジメチルベンジルアンモニウム塩化物、(メタ)アクリロイルオキシ2−ヒドロキシプロピルジメチルベンジルアンモニウム塩化物、(メタ)アクリロイルアミノプロピルジメチルベンジルアンモニウム塩化物などがあげられ、これら単量体と非イオン性単量体との共重合体である。共重合する単量体としてはアクリルアミドが好ましい。また(メタ)アクリル酸などアニオン性単量体を共重合することにより両性高分子を合成し使用することもできる。また、これら(メタ)アクリル系高分子に限らず、ジメチルジアリルアンモニウム塩化物(共)重合体、ポリビニルアミン系高分子、ポリアミジン系高分子も使用可能である。 Cationic and / or amphoteric water-soluble polymers used in combination with the inorganic oxidant group to be added are acrylic cationic monomers such as dimethylaminoethyl (meth) acrylate and dimethylaminopropyl (meth) acrylamide. A salt of an inorganic acid or an organic acid such as a homopolymer of a quaternary ammonium salt with methyl chloride or benzyl chloride, or a copolymer with acrylamide. For example, as a monomer, (meth) acryloyloxyethyl trimethylammonium chloride, (meth) acryloyloxy 2-hydroxypropyltrimethylammonium chloride, (meth) acryloylaminopropyltrimethylammonium chloride, (meth) acryloyloxyethyldimethylbenzyl Ammonium chloride, (meth) acryloyloxy 2-hydroxypropyldimethylbenzylammonium chloride, (meth) acryloylaminopropyldimethylbenzylammonium chloride, and the like. Copolymerization of these monomers with nonionic monomers It is a coalescence. Acrylamide is preferred as the monomer to be copolymerized. Also, amphoteric polymers can be synthesized and used by copolymerizing anionic monomers such as (meth) acrylic acid. In addition to these (meth) acrylic polymers, dimethyldiallylammonium chloride (co) polymers, polyvinylamine polymers, and polyamidine polymers can also be used.
これらカチオン性水溶性高分子中のイオン性基のモル%は、以下のようになる。すなわちカチオン性水溶性高分子中のカチオン性基は20〜100モル%、非イオン性基は0〜80モル%であり、好ましくはカチオン性基50〜100モル%、非イオン性基は0〜50モル%である。また両性水溶性高分子中のカチオン性基は20〜100モル%、アニオン性基5〜50モル%、非イオン性基0〜75モル%であり、好ましくはカチオン性基50〜90モル%、アニオン性基10〜30モル%、非イオン性基0〜40モル%である。カチオン性基が20モル%未満では、カチオン性が低く脱水効率が低下する。またアニオン性基が50以上では、アニオン性が強すぎ、カチオン性基の効果が発現せず好ましくない。 The mol% of the ionic group in these cationic water-soluble polymers is as follows. That is, the cationic group in the cationic water-soluble polymer is 20 to 100 mol%, the nonionic group is 0 to 80 mol%, preferably the cationic group is 50 to 100 mol%, and the nonionic group is 0 to 0 mol%. 50 mol%. The cationic groups in the amphoteric water-soluble polymer are 20 to 100 mol%, anionic groups 5 to 50 mol%, nonionic groups 0 to 75 mol%, preferably cationic groups 50 to 90 mol%, It is 10-30 mol% of anionic groups and 0-40 mol% of nonionic groups. When the cationic group is less than 20 mol%, the cationic property is low and the dehydration efficiency is lowered. On the other hand, when the anionic group is 50 or more, the anionicity is too strong, and the effect of the cationic group is not manifested.
これらカチオン性水溶高分子性あるいは両性水溶性高分子の分子量は、300万〜2000万であるが、好ましくは500万〜1500万である。300万以下では凝集力が不足し、2000万以上では、凝集力が高すぎ、フロックが巨大化してかえって脱水性が低下する。また、溶液粘度も高くなり過ぎ分散性も悪くなるほか、水溶液の取り扱いも悪くなる。また本発明で使用するビニル重合系カチオン性水溶性またはビニル重合系両性水溶性高分子の製品形態は、粉末型、水溶液型、油中水型エマルジョン及び塩水溶液分散型等が考えられるが、溶解の素早さ、あるいは高分子構造改質剤による架橋あるいは分岐処理などの変性の容易さなどを考慮すると、油中水型エマルジョンが好ましい。 The molecular weight of the cationic water-soluble polymer or amphoteric water-soluble polymer is 3 million to 20 million, preferably 5 million to 15 million. If it is 3 million or less, the cohesive force is insufficient, and if it is 20 million or more, the cohesive force is too high, and the flocs become enormous and the dewaterability is lowered. In addition, the solution viscosity becomes too high, dispersibility is deteriorated, and handling of the aqueous solution is also deteriorated. The product form of the vinyl polymerization cationic water-soluble or vinyl polymerization amphoteric water-soluble polymer used in the present invention may be powder type, aqueous solution type, water-in-oil emulsion, salt aqueous solution dispersion type, etc. In view of the quickness of the polymer, the ease of modification such as crosslinking or branching with a polymer structure modifier, a water-in-oil emulsion is preferred.
本発明の無機系酸化剤群とビニル重合系カチオン性水溶性及び/またはビニル重合系両性水溶性高分子を併用する畜産汚泥の処理方法は、従来汎用されているカチオンポリマー単独処方に較べ薬剤添加量を10%〜20%削減することが可能である。この理由は、無機系酸化剤を添加することによって、その後添加するカチオン性あるいは両性水溶性高分子のロスが少ないことによると考えられる。すなわち無機系酸化剤添加による事によりある程度の凝結作用が発生し、カチオン性あるいは両性水溶性高分子のカチオン性基の電荷的な無駄がなく、ほぼ二次的な凝集反応に使用される。更に重要な効果として脱水処理工程中における悪臭を低減することにより作業環境や近隣地域環境の改善を図ることが可能である。 The method for treating livestock sludge using the inorganic oxidant group of the present invention in combination with a vinyl polymerized cationic water-soluble and / or vinyl polymerized amphoteric water-soluble polymer is compared with a conventional cationic polymer single formulation. The amount can be reduced by 10% to 20%. The reason for this is considered to be that the loss of the cationic or amphoteric water-soluble polymer added thereafter is small by adding the inorganic oxidant. That is, a certain degree of coagulation occurs due to the addition of the inorganic oxidant, there is no charge waste of the cationic group of the cationic or amphoteric water-soluble polymer, and it is used for the secondary secondary agglomeration reaction. Furthermore, as an important effect, it is possible to improve the working environment and the surrounding area environment by reducing malodor during the dehydration process.
畜産業における汚泥の特徴として以下のことがあげられる。畜産汚泥の場合、汚泥中の繊維分が高めであり(敷き藁の裁断等が混合されるケースが多い)、SS分(懸濁粒子浮遊分)は10質量%が大半であること。揮発性懸濁粒子浮遊分(VSS分、燃焼させた時に減少する量)が高めであり、有機分が一般汚泥より多いこと。アニオン当量値が高めであり、5.0meq/L以上が大半であること(一般汚泥は2〜6meq/L)。M−アルカリ度が高めであり、3000mg/L以上が大半であり、平均5000mg/Lである(一般汚泥は1000〜6000mg/L)。また、家畜の尿が多い為か電気伝導度が高く、溶解性塩分が多いと言える。このうち最も特徴的なのは電気伝導度とM−アルカリ度が高いことであると考えられる。そのためカチオン系ポリマー単独処方の外にポリ鉄等無機凝集剤を併用して汚泥改質を図った後にカチオン系又は両性ポリマーによる脱水処方のケースが多く、本発明のように無機系酸化剤により最初弱い凝結処理を施し、その後カチオン性あるいは両性水溶性高分子により更に強固な凝集処理を施す処方は、まさに畜産汚泥に適した処方と考えられる。 The characteristics of sludge in the livestock industry are as follows. In the case of livestock sludge, the fiber content in the sludge is high (in many cases, cutting of the litter is mixed), and the SS content (suspended particle suspension) is 10% by mass. Volatile suspended particle suspended matter (VSS component, amount reduced when burned) is high and organic content is higher than general sludge. The anion equivalent value is high, and 5.0 meq / L or more is the majority (general sludge is 2 to 6 meq / L). M-alkalinity is high, 3000 mg / L or more is the majority, and the average is 5000 mg / L (general sludge is 1000 to 6000 mg / L). In addition, it can be said that the electrical conductivity is high due to the large amount of livestock urine, and there is a high amount of soluble salt. Among these, the most characteristic is considered to be high electrical conductivity and M-alkaliness. Therefore, there are many cases of dehydration prescription with cationic or amphoteric polymers after sludge modification by using an inorganic flocculant such as polyiron in addition to the cationic polymer single prescription, and first with an inorganic oxidizing agent as in the present invention. A formulation in which a weak coagulation treatment is performed and then a stronger coagulation treatment is performed with a cationic or amphoteric water-soluble polymer is considered to be a formulation suitable for livestock sludge.
本発明では次亜塩素酸ナトリウムなど無機系酸化剤を併用する。この無機系酸化剤を使用することにより脱水処理工程中における悪臭を低減することができるだけでなく、汚泥の凝集効果が向上することがわかっている。後に記載する実施例をみても明らかである。この理由として考えられることは、畜産汚泥中の溶解性有機物質を酸化作用により分解しているのではないかと推定される。汚泥中には排水中有機物の分解物である有機酸、多糖類、ポリペプチド、硫黄系化合物など悪臭を発するもの、あるいは凝集剤の性能を阻害する有機酸やポリアニオン性の多糖類など存在するが、これら物質を一定以下に分解することにより、結果として凝集性能を向上させ、また悪臭を低減させていると思われる。上記次亜塩素酸ナトリウム(有効塩素8質量%)など液体品の場合は、汚泥分散液量に対し0.05〜0.3質量%であり、好ましくは0.1〜0.3質量%である。また臭素酸塩など粉末の場合は、汚泥分散液量に対し0.005〜0.05質量%であり、好ましくは0.01〜0.03質量%である。 In the present invention, an inorganic oxidizing agent such as sodium hypochlorite is used in combination. It has been found that the use of this inorganic oxidant can not only reduce malodor during the dehydration process, but also improve the sludge aggregation effect. It will be clear from the examples described later. A possible reason for this is presumed that the soluble organic substances in livestock sludge are decomposed by oxidation. The sludge contains organic acids, polysaccharides, polypeptides, sulfur compounds such as organic acid decomposition products in wastewater, or organic acids and polyanionic polysaccharides that inhibit the performance of flocculants. By decomposing these substances below a certain level, it seems that as a result, the coagulation performance is improved and the malodor is reduced. In the case of liquid products such as sodium hypochlorite (effective chlorine 8% by mass), it is 0.05 to 0.3% by mass, preferably 0.1 to 0.3% by mass, based on the amount of sludge dispersion. is there. Moreover, in the case of powders, such as bromate, it is 0.005-0.05 mass% with respect to the amount of sludge dispersion liquid, Preferably it is 0.01-0.03 mass%.
前述の物性からも分かるように電気伝導度とM−アルカリ度が高いということはそれだけ無機塩類の含有量は多く有機物の含有量が低く、無機系酸化剤のみで消臭と汚泥改質が達成できる。下水汚泥、製紙汚泥などでは無機系酸化剤と無機系凝集剤を併用した例が先願としてあるが、畜産汚泥にはまだなく畜産汚泥に適した処方と言える。 As can be seen from the above-mentioned physical properties, the high electrical conductivity and M-alkalinity means that the content of inorganic salts is large and the content of organic substances is low. Deodorization and sludge modification can be achieved with only inorganic oxidants. it can. In the case of sewage sludge, papermaking sludge, etc., an example of using an inorganic oxidant and an inorganic flocculant in combination is a prior application.
また本発明の畜産汚泥の処理方法では、重縮合系カチオン性高分子を併用すると更に脱水効率を向上させることができる。すなわち畜産汚泥に対し、前記無機系酸化剤、重縮合系カチオン性水溶性高分子、ビニル重合系カチオン性水溶性及び/またはビニル重合系両性水溶性高分子をこの順に添加する処方である。重縮合系カチオン性水溶性高分子は、具体的には以下のようなものが使用できる。アンモニア、脂肪族一価アミン及び脂肪族ポリアミンから選択された少なくとも一種以上の化合物とエピハロヒドリンとの重縮合物である。脂肪族一価アミンや脂肪族ポリアミンの例としては、モノメチルアミン、モノエチルアミン、ジメチルアミン、ジエチルアミン、トリメチルアミン、トリエチルアミン、モノ、ジ、トリの各エタノ−ルアミンなどであり、エチレンジアミン、ジエチレントリアミン、トリエチレンテトラミン、ペンタエチレンヘキサミンなどである。これらアンモニアとアミン類のうち一種以上の化合物とエピクロロヒドリンのようなエピハロヒドリンと反応させ、重縮合物を得ることができる。またこれら重縮合物は、アミン類とエピハロヒドリンを一段階で反応させる必要はなく、一段目は脂肪族一価アミンと反応させ、その後アンモニアや脂肪族ポリアミンと架橋反応をさせ分子量を増大した重縮合物を製造しても良い。これら重縮合物の分子量としては、500〜200万であり、好ましくは1000〜200万である。これら重縮合系カチオン性高分子の汚泥に対する添加量は、揮発性懸濁粒子浮遊分(VSS分、燃焼させた時に減少する量)に対し、0.02〜0.3質量%であり、好ましくは0.03〜0.1質量%である。これらは主にアニオン当量値が検出される物質の電荷中和に消費され、凝結作用によって生成する小さなフロックの形成に寄与する。 In the livestock sludge treatment method of the present invention, when a polycondensation cationic polymer is used in combination, the dehydration efficiency can be further improved. That is, it is a prescription in which the inorganic oxidant, the polycondensation cationic water-soluble polymer, the vinyl polymerization cationic water-soluble and / or the vinyl polymerization amphoteric water-soluble polymer are added to the livestock sludge in this order. Specific examples of the polycondensation cationic water-soluble polymer include the following. It is a polycondensate of at least one compound selected from ammonia, an aliphatic monovalent amine and an aliphatic polyamine with an epihalohydrin. Examples of aliphatic monovalent amines and aliphatic polyamines include monomethylamine, monoethylamine, dimethylamine, diethylamine, trimethylamine, triethylamine, mono, di, and triethanolamine, and ethylenediamine, diethylenetriamine, and triethylenetetramine. And pentaethylenehexamine. A polycondensate can be obtained by reacting one or more of these ammonia and amines with an epihalohydrin such as epichlorohydrin. These polycondensates do not require the reaction of amines and epihalohydrin in one step, the first step is a reaction with an aliphatic monovalent amine followed by a crosslinking reaction with ammonia or an aliphatic polyamine to increase the molecular weight. You may manufacture things. The molecular weight of these polycondensates is 500 to 2 million, preferably 1000 to 2 million. The amount of these polycondensation-based cationic polymers added to the sludge is 0.02 to 0.3% by mass, preferably 0.02 to 0.3% by mass, based on the volatile suspended particle suspended matter (VSS component, the amount that decreases when burned). Is 0.03-0.1 mass%. These are mainly consumed for charge neutralization of substances whose anion equivalent value is detected, and contribute to the formation of small flocs produced by the coagulation action.
脱水機は、デカンタ−、フィルタ−プレス、ベルトプレス、スクリュ−プレス、多重円盤型あるいはロータリープレスなど従来からの機種を用いて脱水処理が行えるが、スクリュ−プレスあるいは多重円盤型脱水機使用時が好ましい。また、汚泥としては、畜産業における生汚泥、消化汚泥、余剰汚泥などがあげられる。したがって、上記理由により、本発明の畜産汚泥の処理方法は従来のカチオンポリマー単独処方又はアニオン性高分子凝集剤/カチオン性高分子凝集剤処方に較べ汚泥処理時の臭気低減による環境の改善、汚泥の処理量のアップ、ケ−キ含水率の低下、それに伴う焼却時の燃料費の低減、廃棄物投棄量の削減、コンポスト等への好影響など利点がある。また本発明で使用するビニル重合系カチオン性水溶性またはビニル重合系両性水溶性高分子の汚泥に対する添加量は、揮発性懸濁粒子浮遊分(VSS分、燃焼させた時に減少する量)に対し、0.1〜1.0質量%であり、好ましくは0.2〜0.7質量%である。 The dehydrator can be dehydrated using conventional models such as decanters, filter presses, belt presses, screw presses, multiple disk molds or rotary presses, but when using a screw press or multiple disk dehydrator. preferable. Examples of sludge include raw sludge, digested sludge and surplus sludge in the livestock industry. Therefore, for the above reasons, the livestock sludge treatment method of the present invention improves the environment by reducing odor during sludge treatment compared to conventional cationic polymer single formulation or anionic polymer flocculant / cationic polymer flocculant formulation, sludge There are advantages such as an increase in the amount of water treatment, a reduction in the moisture content of the cake, a reduction in fuel costs during incineration, a reduction in the amount of waste dumped, and a positive impact on composting. In addition, the addition amount of the vinyl polymerization cationic water-soluble or vinyl polymerization amphoteric water-soluble polymer used in the present invention to sludge is based on the volatile suspended particle suspended matter (VSS component, amount reduced when burned). 0.1 to 1.0 mass%, preferably 0.2 to 0.7 mass%.
(実施例) 以下、実施例および比較例によって本発明をさらに詳しく説明するが、本発明はその要旨を超えない限り、以下の実施例に制約されるものではない。 (Examples) Hereinafter, the present invention will be described in more detail with reference to Examples and Comparative Examples. However, the present invention is not limited to the following Examples unless it exceeds the gist.
試験用試料として表1の組成の水溶性高分子を用意し、試験を行った。養豚場現場より排出される養豚汚泥(pH7.02、全ss分11,250mg/L)200mlをポリビ−カ−に採取し、次亜塩素酸ナトリウムを対汚泥量1500ppm添加し、ビ−カ−移し変え攪拌10回行った後、カチオン性あるいは両性水溶性高分子(表1の試料−1から試料−5)をそれぞれ対液150ppm添加し、ビ−カ−移し変え攪拌20回を行い、T−1179Lの濾布(ナイロン製)により濾過し、45秒後の濾液量を測定した。また濾過した汚泥をプレス圧4Kg/m2で1分間脱水する。その後ケ−キ含水率(105℃で20hr乾燥)を測定した。結果を表2に示す。 A water-soluble polymer having the composition shown in Table 1 was prepared as a test sample and tested. Collect 200 ml of pig sludge discharged from the pig farm site (pH 7.02, total ss 11,250 mg / L) in a poly beaker, add sodium hypochlorite to the sludge amount 1500 ppm, and beaker After 10 times of transfer and stirring, 150 ppm of a cationic or amphoteric water-soluble polymer (sample 1 to sample 5 in Table 1) was added to each solution, and the beaker was transferred and stirred 20 times. The solution was filtered through a −1179 L filter cloth (made of nylon), and the filtrate amount after 45 seconds was measured. The filtered sludge is dehydrated at a press pressure of 4 kg / m 2 for 1 minute. Thereafter, the moisture content of the cake (dried at 105 ° C. for 20 hours) was measured. The results are shown in Table 2.
(表1)
組成はモル%、EM;油中水型エマルジョン、PW;粉末、PL;ペースト、分子量;重量平均分子量
(Table 1)
Composition: mol%, EM; water-in-oil emulsion, PW; powder, PL; paste, molecular weight; weight average molecular weight
(比較例1)
実施例1と同様な試験操作により無機酸化剤を添加しない処方(比較1−1)、
に関して試験を行った。結果を表2に示す。
(Comparative Example 1)
Formulation (Comparative 1-1) in which an inorganic oxidizing agent is not added by the same test operation as in Example 1,
Were tested. The results are shown in Table 2.
(表2)
無機酸化剤;対汚泥量ppm、薬剤添加量;対汚泥量ppm、濾液量;mL、
ケーキ含水量;質量%
(Table 2)
Inorganic oxidizer; ppm of sludge, amount of chemical added; ppm of sludge, amount of filtrate; mL,
Cake water content; mass%
実施例1とは異なる畜産汚泥の汚泥(pH8.00、全ss分11,000mg/L)200mlをポリビ−カ−に採取し、次亜塩素酸ナトリウムを対汚泥量6,000ppm添加し、ビ−カ−移し変え攪拌10回行い、重縮合系高分子(試料−6)を加えビ−カ−移し変え攪拌10回行い、その後カチオン性あるいは両性水溶性高分子(表1の試料−1から試料−5)をそれぞれ対液500ppm添加し、ビ−カ−移し変え攪拌10回を行い、T−1179Lの濾布(ナイロン製)により濾過し、45秒後の濾液量を測定した。また重縮合系高分子(試料―6)を加えない処方を試料−1、試料−3、試料−5に関して行った。次に濾過した汚泥はプレス圧4Kg/m2で1分間脱水する。その後ケ−キ含水率(105℃で20hr乾燥)を測定した。結果を表3に示す。 200 ml of livestock sludge different from Example 1 (pH 8.00, total ss 11,000 mg / L) was collected in a polyvinyl carbonate, sodium hypochlorite was added to the sludge amount of 6,000 ppm, -Carry transfer and stir 10 times, add polycondensation polymer (sample-6) and beaker transfer and stir 10 times, then cationic or amphoteric water-soluble polymer (from sample-1 in Table 1) Sample 5) was added to each solution at 500 ppm, the beaker was transferred, stirred 10 times, filtered through a T-1179L filter cloth (made of nylon), and the amount of filtrate after 45 seconds was measured. Moreover, the prescription which does not add a polycondensation type | system | group polymer (sample-6) was performed regarding sample-1, sample-3, and sample-5. Next, the filtered sludge is dehydrated at a press pressure of 4 kg / m 2 for 1 minute. Thereafter, the moisture content of the cake (dried at 105 ° C. for 20 hours) was measured. The results are shown in Table 3.
(比較例2)
実施例2と同様な試験操作により、無機系酸化剤を添加しない処方(比較2−1)、酸化剤と縮合系カチオン水溶性高分子を併用した処方(比較2−2)およびカチオン水溶性高分子単独処方(比較2−3)に関して試験を行った。結果を表3に示す。
(Comparative Example 2)
According to the same test operation as in Example 2, a formulation without adding an inorganic oxidant (Comparative 2-1), a formulation with a combination of an oxidant and a condensed cationic water-soluble polymer (Comparative 2-2), and a cationic water-soluble high The test was performed on the molecular alone formulation (Comparative 2-3). The results are shown in Table 3.
(表3)
無機酸化剤;対汚泥量ppm、薬剤添加量;対汚泥量ppm、濾液量;mL、
ケーキ含水量;質量%
(Table 3)
Inorganic oxidizer; ppm of sludge, amount of chemical added; ppm of sludge, amount of filtrate; mL,
Cake water content; mass%
Claims (5)
酸化剤群;亜塩素酸塩、次亜塩素酸塩、臭素酸塩、亜臭素酸塩、次亜臭素酸塩、過酸化水素。 After adding one or more inorganic oxidizers selected from the following oxidizer group to livestock sludge and applying deodorization treatment and modification treatment, vinyl polymerization cationic water-soluble and / or vinyl polymerization amphoteric water-solubility A method for treating livestock sludge, characterized by adding a coagulant polymer, coagulating, and then dehydrating with a dehydrator.
Oxidizing agent group; chlorite, hypochlorite, bromate, bromate, hypobromite, hydrogen peroxide.
R1は水素又はメチル基、R2、R3は炭素数1〜3のアルキル基、アルコキシ基あるいはベンジル基、R4は水素、炭素数1〜3のアルキル基、アルコキシル基あるいはベンジル基であり、同種でも異種でも良い。Aは酸素またはNH、Bは炭素数2〜4のアルキレン基またはアルコキシレン基、X1は陰イオンをそれぞれ表わす。
R5は水素又はメチル基、R6、R7は炭素数1〜3のアルキル基、アルコキシル基あるいはベンジル基、X2は陰イオンをそれぞれ表わす。
R8は水素またはCH2COOY2、QはSO3、C6H4SO3、
CONHC(CH3)2CH2SO3、C6H4COOあるいはCOO、R9は水素、メチル基またはCOOY3であり、Y1、Y2は水素または陽イオンをそれぞれ表わす。
R 1 is hydrogen or a methyl group, R 2 and R 3 are an alkyl group having 1 to 3 carbon atoms, an alkoxy group or a benzyl group, and R 4 is hydrogen, an alkyl group having 1 to 3 carbon atoms, an alkoxyl group or a benzyl group. , Same or different. A represents oxygen or NH, B represents an alkylene group or alkoxylene group having 2 to 4 carbon atoms, and X 1 represents an anion.
R 5 represents hydrogen or a methyl group, R 6 and R 7 each represent an alkyl group having 1 to 3 carbon atoms, an alkoxyl group or a benzyl group, and X 2 represents an anion.
R 8 is hydrogen or CH 2 COOY 2 , Q is SO 3 , C 6 H 4 SO 3 ,
CONHC (CH 3 ) 2 CH 2 SO 3 , C 6 H 4 COO or COO, R 9 is hydrogen, a methyl group or COOY 3 , and Y 1 and Y 2 each represent hydrogen or a cation.
前記ビニル重合系カチオン性水溶性及び/またはビニル重合系両性水溶性高分子をこの順に添加することを特徴とする請求項1に記載の畜産汚泥の処理方法。 For the livestock sludge, the inorganic oxidant, polycondensation cationic water-soluble polymer,
The method for treating livestock sludge according to claim 1, wherein the vinyl polymerization-based cationic water-soluble and / or the vinyl polymerization-based amphoteric water-soluble polymer is added in this order.
The livestock sludge treatment method according to any one of claims 1 to 4, wherein the dehydrator is a filter press or a rotary press.
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