JPH047018A - Desulfurization and dechlorination device - Google Patents
Desulfurization and dechlorination deviceInfo
- Publication number
- JPH047018A JPH047018A JP2106556A JP10655690A JPH047018A JP H047018 A JPH047018 A JP H047018A JP 2106556 A JP2106556 A JP 2106556A JP 10655690 A JP10655690 A JP 10655690A JP H047018 A JPH047018 A JP H047018A
- Authority
- JP
- Japan
- Prior art keywords
- filter material
- powder
- neutral
- filter medium
- parts
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
- 238000006477 desulfuration reaction Methods 0.000 title claims description 10
- 230000023556 desulfurization Effects 0.000 title claims description 10
- 238000006298 dechlorination reaction Methods 0.000 title 1
- 239000000843 powder Substances 0.000 claims abstract description 34
- 239000010813 municipal solid waste Substances 0.000 claims abstract description 29
- 241001465754 Metazoa Species 0.000 claims abstract description 26
- 210000000988 bone and bone Anatomy 0.000 claims abstract description 26
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 claims abstract description 13
- 239000000463 material Substances 0.000 claims description 49
- 239000002374 bone meal Substances 0.000 claims description 13
- 229940036811 bone meal Drugs 0.000 claims description 13
- 238000006386 neutralization reaction Methods 0.000 claims description 11
- 230000003472 neutralizing effect Effects 0.000 claims description 10
- 239000011230 binding agent Substances 0.000 claims description 9
- 238000010304 firing Methods 0.000 claims description 9
- 238000010612 desalination reaction Methods 0.000 claims description 8
- 239000004480 active ingredient Substances 0.000 claims description 5
- 238000001914 filtration Methods 0.000 claims description 5
- 238000000465 moulding Methods 0.000 claims description 4
- -1 binding aid Substances 0.000 claims description 3
- 239000007789 gas Substances 0.000 abstract description 36
- 230000007935 neutral effect Effects 0.000 abstract description 12
- 230000002378 acidificating effect Effects 0.000 abstract description 8
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 abstract description 7
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 abstract description 7
- 239000000460 chlorine Substances 0.000 abstract description 7
- 229910052801 chlorine Inorganic materials 0.000 abstract description 7
- 239000011593 sulfur Substances 0.000 abstract description 7
- 229910052717 sulfur Inorganic materials 0.000 abstract description 7
- 235000002918 Fraxinus excelsior Nutrition 0.000 abstract 2
- 239000002956 ash Substances 0.000 abstract 2
- 238000007493 shaping process Methods 0.000 abstract 2
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 10
- 239000003546 flue gas Substances 0.000 description 10
- 229910001385 heavy metal Inorganic materials 0.000 description 9
- 238000000034 method Methods 0.000 description 9
- 238000002156 mixing Methods 0.000 description 5
- 239000011148 porous material Substances 0.000 description 5
- 238000011282 treatment Methods 0.000 description 5
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 4
- 239000004927 clay Substances 0.000 description 4
- 239000000203 mixture Substances 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- 235000013339 cereals Nutrition 0.000 description 3
- 230000003750 conditioning effect Effects 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 239000010794 food waste Substances 0.000 description 3
- MWUXSHHQAYIFBG-UHFFFAOYSA-N nitrogen oxide Inorganic materials O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 description 3
- 239000005416 organic matter Substances 0.000 description 3
- 239000000243 solution Substances 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- 239000002699 waste material Substances 0.000 description 3
- 239000002023 wood Substances 0.000 description 3
- 241000283690 Bos taurus Species 0.000 description 2
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 2
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 description 2
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- 241000209094 Oryza Species 0.000 description 2
- 235000007164 Oryza sativa Nutrition 0.000 description 2
- ATUOYWHBWRKTHZ-UHFFFAOYSA-N Propane Chemical compound CCC ATUOYWHBWRKTHZ-UHFFFAOYSA-N 0.000 description 2
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 2
- RAHZWNYVWXNFOC-UHFFFAOYSA-N Sulphur dioxide Chemical compound O=S=O RAHZWNYVWXNFOC-UHFFFAOYSA-N 0.000 description 2
- 238000007792 addition Methods 0.000 description 2
- 239000000654 additive Substances 0.000 description 2
- BFNBIHQBYMNNAN-UHFFFAOYSA-N ammonium sulfate Chemical compound N.N.OS(O)(=O)=O BFNBIHQBYMNNAN-UHFFFAOYSA-N 0.000 description 2
- 229910052921 ammonium sulfate Inorganic materials 0.000 description 2
- 235000011130 ammonium sulphate Nutrition 0.000 description 2
- 229910052793 cadmium Inorganic materials 0.000 description 2
- BDOSMKKIYDKNTQ-UHFFFAOYSA-N cadmium atom Chemical compound [Cd] BDOSMKKIYDKNTQ-UHFFFAOYSA-N 0.000 description 2
- 239000011575 calcium Substances 0.000 description 2
- 229910052791 calcium Inorganic materials 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 238000011161 development Methods 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 235000009566 rice Nutrition 0.000 description 2
- CDBYLPFSWZWCQE-UHFFFAOYSA-L sodium carbonate Substances [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 2
- 238000001179 sorption measurement Methods 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- 231100000331 toxic Toxicity 0.000 description 2
- 230000002588 toxic effect Effects 0.000 description 2
- 239000002912 waste gas Substances 0.000 description 2
- 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
- 239000005995 Aluminium silicate Substances 0.000 description 1
- VHUUQVKOLVNVRT-UHFFFAOYSA-N Ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical class [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 1
- VYZAMTAEIAYCRO-UHFFFAOYSA-N Chromium Chemical compound [Cr] VYZAMTAEIAYCRO-UHFFFAOYSA-N 0.000 description 1
- 241000283086 Equidae Species 0.000 description 1
- 108010010803 Gelatin Proteins 0.000 description 1
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 1
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 1
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 description 1
- 241001494479 Pecora Species 0.000 description 1
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 1
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 1
- 229920002472 Starch Polymers 0.000 description 1
- 241000209140 Triticum Species 0.000 description 1
- 235000021307 Triticum Nutrition 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 238000003916 acid precipitation Methods 0.000 description 1
- 239000003463 adsorbent Substances 0.000 description 1
- 229910052784 alkaline earth metal Inorganic materials 0.000 description 1
- 150000001342 alkaline earth metals Chemical class 0.000 description 1
- 235000012211 aluminium silicate Nutrition 0.000 description 1
- 150000001412 amines Chemical class 0.000 description 1
- 239000000908 ammonium hydroxide Substances 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 229910052788 barium Inorganic materials 0.000 description 1
- DSAJWYNOEDNPEQ-UHFFFAOYSA-N barium atom Chemical compound [Ba] DSAJWYNOEDNPEQ-UHFFFAOYSA-N 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 229910000019 calcium carbonate Inorganic materials 0.000 description 1
- 229910052804 chromium Inorganic materials 0.000 description 1
- 239000011651 chromium Substances 0.000 description 1
- JOPOVCBBYLSVDA-UHFFFAOYSA-N chromium(6+) Chemical compound [Cr+6] JOPOVCBBYLSVDA-UHFFFAOYSA-N 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 230000001143 conditioned effect Effects 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 230000006378 damage Effects 0.000 description 1
- GUJOJGAPFQRJSV-UHFFFAOYSA-N dialuminum;dioxosilane;oxygen(2-);hydrate Chemical compound O.[O-2].[O-2].[O-2].[Al+3].[Al+3].O=[Si]=O.O=[Si]=O.O=[Si]=O.O=[Si]=O GUJOJGAPFQRJSV-UHFFFAOYSA-N 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 235000013312 flour Nutrition 0.000 description 1
- 239000000295 fuel oil Substances 0.000 description 1
- 239000003502 gasoline Substances 0.000 description 1
- 229920000159 gelatin Polymers 0.000 description 1
- 239000008273 gelatin Substances 0.000 description 1
- 235000019322 gelatine Nutrition 0.000 description 1
- 235000011852 gelatine desserts Nutrition 0.000 description 1
- 239000003292 glue Substances 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 238000005469 granulation Methods 0.000 description 1
- 230000003179 granulation Effects 0.000 description 1
- 239000004021 humic acid Substances 0.000 description 1
- 239000010903 husk Substances 0.000 description 1
- 239000004615 ingredient Substances 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- NLYAJNPCOHFWQQ-UHFFFAOYSA-N kaolin Chemical compound O.O.O=[Al]O[Si](=O)O[Si](=O)O[Al]=O NLYAJNPCOHFWQQ-UHFFFAOYSA-N 0.000 description 1
- 239000011133 lead Substances 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 244000144972 livestock Species 0.000 description 1
- 239000011777 magnesium Substances 0.000 description 1
- 229910052749 magnesium Inorganic materials 0.000 description 1
- 229910052748 manganese Inorganic materials 0.000 description 1
- 239000011572 manganese Substances 0.000 description 1
- QSHDDOUJBYECFT-UHFFFAOYSA-N mercury Chemical compound [Hg] QSHDDOUJBYECFT-UHFFFAOYSA-N 0.000 description 1
- 229910052753 mercury Inorganic materials 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 238000012544 monitoring process Methods 0.000 description 1
- 229910052901 montmorillonite Inorganic materials 0.000 description 1
- 229910017604 nitric acid Inorganic materials 0.000 description 1
- 239000003921 oil Substances 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 239000011574 phosphorus Substances 0.000 description 1
- 229910052698 phosphorus Inorganic materials 0.000 description 1
- 239000011591 potassium Substances 0.000 description 1
- 229910052700 potassium Inorganic materials 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 239000001294 propane Substances 0.000 description 1
- 108090000623 proteins and genes Proteins 0.000 description 1
- 102000004169 proteins and genes Human genes 0.000 description 1
- 229910052903 pyrophyllite Inorganic materials 0.000 description 1
- 235000020083 shōchū Nutrition 0.000 description 1
- 239000000377 silicon dioxide Substances 0.000 description 1
- 235000012239 silicon dioxide Nutrition 0.000 description 1
- 239000011734 sodium Substances 0.000 description 1
- 229910052708 sodium Inorganic materials 0.000 description 1
- 229910000029 sodium carbonate Inorganic materials 0.000 description 1
- 239000008107 starch Substances 0.000 description 1
- 235000019698 starch Nutrition 0.000 description 1
- XTQHKBHJIVJGKJ-UHFFFAOYSA-N sulfur monoxide Chemical class S=O XTQHKBHJIVJGKJ-UHFFFAOYSA-N 0.000 description 1
- 229910052815 sulfur oxide Inorganic materials 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
- 238000004056 waste incineration Methods 0.000 description 1
- 238000005303 weighing Methods 0.000 description 1
Landscapes
- Treating Waste Gases (AREA)
Abstract
Description
【発明の詳細な説明】
[発明の目的]
(産業上の利用分野)
本発明は、生ゴミ焼却灰を利用した脱硫脱塩機器に関す
る。DETAILED DESCRIPTION OF THE INVENTION [Object of the Invention] (Field of Industrial Application) The present invention relates to a desulfurization and desalination equipment that utilizes garbage incineration ash.
(従来の技術)
人類か開発した近代産業、工業によって新しい文化が生
み出されているが、その反面、それに伴って自然環境に
大きな影響を与え、自然の浄化作用分趣見て自然の破壊
や汚染か発生している。(Conventional technology) A new culture has been created by modern industries and industries developed by humans, but on the other hand, this has had a great impact on the natural environment, causing the destruction and pollution of nature due to its purifying function. or is occurring.
人類か常に健康で文化的な生活を確保するには産業の発
達と共にその悪影響を取り除いて生活の発展に適した新
しい環境を作り出していく必要かある。In order to ensure that humankind always lives a healthy and cultured life, it is necessary to eliminate the negative effects of industrial development and create a new environment suitable for the development of life.
その一番身近な生活公害の生ゴミ焼却灰処理問題が各国
の悩みになっている。この生ゴミ焼却灰処理問題につい
ては各国の各関係機関等で色々と研究しているが、抜本
的な解決策は見いだされていないのが現状である。The issue of how to dispose of incinerated ash from food waste, which is the most familiar daily pollution, is a concern in many countries. Various related organizations in various countries are conducting various studies on this issue of garbage incineration ash disposal, but at present no fundamental solution has been found.
また、化学工業の進展や自動車の増加に伴って、酸性雨
等の原因となる硫黄や塩素あるいは鉛を含んだ排ガス問
題も上記と同様に各国の悩みとなっており、これも画期
的な解決策は見いだされていない。In addition, with the progress of the chemical industry and the increase in the number of automobiles, the problem of exhaust gas containing sulfur, chlorine, or lead, which causes acid rain, has become a problem in many countries, similar to the above, and this is also an epoch-making project. No solution has been found.
従来の排ガス処理法、例えば排煙脱硫には乾式法と湿式
法の二つがあり、乾式法では活性炭、活性マンガンなど
に吸着または反応後、硫酸、硫酸アンモニウムなどとし
て回収する。湿式法では二酸化硫黄を水酸化ナトリウム
、炭酸ナトリウムなとの水溶液で洗浄し、吸収液に炭酸
カルシウムを加えてセラコラとして回収する方法、水酸
化アンモニウム液に吸収後、硫酸アンモニウムとして回
収する方法などがある。Conventional exhaust gas treatment methods, such as flue gas desulfurization, include a dry method and a wet method. In the dry method, the gas is adsorbed or reacted with activated carbon, activated manganese, etc., and then recovered as sulfuric acid, ammonium sulfate, etc. Wet methods include washing sulfur dioxide with an aqueous solution of sodium hydroxide and sodium carbonate, adding calcium carbonate to the absorption liquid and recovering it as Ceracola, and recovering it as ammonium sulfate after absorbing it in an ammonium hydroxide solution. .
(発明が解決しようとする課題)
しかしなから、これらの方法では処理された排ガスが酸
性であったり、特別の大掛がすな装置を要する等の欠点
があった。(Problems to be Solved by the Invention) However, these methods have drawbacks such as the treated exhaust gas being acidic and the need for special large-scale equipment.
本発明は生ゴミ焼却灰処理問題を解決する一つの有力な
方法を提供するとともに、硫黄や塩素を含んだ酸性の排
カスに対する従来力処理方法め難点を克服し、排ガスを
中性て放出し得る脱硫脱塩機器を提供するものである。The present invention not only provides an effective method for solving the problem of garbage incineration ash disposal, but also overcomes the drawbacks of conventional methods for treating acidic waste gases containing sulfur and chlorine, and releases the waste gases in a neutral state. The purpose of the present invention is to provide desulfurization and desalination equipment.
[発明の構成]
(課題を解決するための手段)
本発明の脱硫脱塩機器は、ガス入口、中和濾過材を充填
してなる中和層、調整濾過材を充填してなる調整層、及
びガス出口と、調整層とガス出口との間に設けられたP
H6乃至7を検出し得るPHセンサとを有してなり、中
和濾過材が動物骨粉、つなぎ助材、生ゴミ焼却灰の有効
成分、アルミナ及び有機物粉体を成形し焼成してなる動
物骨粉が40重量%以上のアルカリ度の高い粒状の濾過
材で、調整濾過材が動物骨粉、つなぎ助材、生ゴミ焼却
灰の有効成分、アルミナ及び有機物粉体を成形し焼成し
てなり中和濾過材よりも動物骨粉の含有量が少なくアル
カリ度の低い粒状の濾過材であることを特徴とする。[Structure of the Invention] (Means for Solving the Problems) The desulfurization and desalination equipment of the present invention includes a gas inlet, a neutralization layer filled with a neutralization filter material, an adjustment layer filled with a conditioning filter material, and P provided between the gas outlet, the adjustment layer and the gas outlet.
Animal bone meal, which has a PH sensor capable of detecting H6 to H7, and whose neutralizing filter material is made by molding and firing animal bone meal, binding aid, active ingredients of garbage incineration ash, alumina, and organic powder. is a granular filter material with a high alkalinity of 40% by weight or more, and the adjusted filter material is made by molding and firing animal bone meal, binder additives, active ingredients of garbage incineration ash, alumina, and organic powder. It is characterized by being a granular filter material with a lower alkalinity and a lower content of animal bone meal than wood.
本発明で処理する被処理ガスは、主に硫黄又は塩素を含
む酸性めガスである。例えば石炭、重油、軽油、プロパ
ン及びガソリン等を燃焼させた排ガスである。The gas to be treated in the present invention is acidic gas mainly containing sulfur or chlorine. For example, it is exhaust gas from burning coal, heavy oil, light oil, propane, gasoline, etc.
上記生ゴミは日常生活により排出されるゴミであり、生
ゴミ焼却灰には通常、有機物、強熱減量成分、フミン酸
、残さく二酸化ケイ素)、金属類及び有害重金属、等が
含まれる。The above-mentioned garbage is garbage discharged from daily life, and the garbage incineration ash usually contains organic matter, ignition loss components, humic acid, residual silicon dioxide), metals, toxic heavy metals, etc.
本発明の中和濾過材及び調整濾過材に用いる生ゴミ焼却
灰としては、有害重金属を実質的に含まない生ゴミ焼却
灰が好ましい。生ゴミ焼却灰の有効成分とは、この有害
重金属を実質的に含まない生ゴミ焼却灰をいう。As the garbage incineration ash used in the neutralized filter medium and the adjusted filter medium of the present invention, garbage incineration ash that substantially does not contain harmful heavy metals is preferable. The active ingredient of garbage incineration ash refers to garbage incineration ash that is substantially free of these harmful heavy metals.
この有害重金属を実質的に含まない生ゴミ焼却圧粉は、
生ゴミ焼却圧粉から有害重金属を除いたもの、又は生ゴ
ミを焼却する際に重金属を除去しつつ焼却して得られた
焼却戻粉、例えば重金属の吸着剤の存在下に水銀、カド
ミウム、鉛、クロム等を吸着させつつ焼却して得られた
焼却戻粉である。This garbage incineration powder, which does not substantially contain harmful heavy metals,
Food waste incineration powder from which toxic heavy metals have been removed, or incineration return powder obtained by incinerating food waste while removing heavy metals, such as mercury, cadmium, and lead in the presence of a heavy metal adsorbent. This is incineration return powder obtained by incineration while adsorbing chromium, etc.
本発明で有害重金属を実質的に含まない生ゴミ焼却灰は
、通常、生ゴミ焼却灰1kg当たり、アルキル水銀0.
05mg以下、カドミウム1mg以下、鉛10mg以下
、六価クロム5mg以下てあり、好ましくはこれら重金
属が検出されない焼却戻粉である。この焼却戻粉はアル
カリ性である。In the present invention, the garbage incineration ash that is substantially free of harmful heavy metals usually has 0.00% alkylmercury per 1 kg of garbage incineration ash.
05 mg or less, cadmium 1 mg or less, lead 10 mg or less, and hexavalent chromium 5 mg or less, preferably incineration return powder in which these heavy metals are not detected. This incineration return powder is alkaline.
また、動物骨粉は、従来畜産場等でほとんど廃棄されて
いた骨、特に牛、馬、羊等の硬骨が主体の動物の骨が採
用される。In addition, the animal bone meal uses bones that have conventionally been mostly discarded at livestock farms, especially bones of animals such as cows, horses, sheep, etc., which are mainly hard bones.
これらの動物の生骨は焼成しやすい大きさに切断し、そ
の上て圧力釜に投入し、200〜400°C前後で、約
90分前後煮沸する。次いて、この骨を焼成炉に入れ、
900〜1100°C前後で、60〜180分前後焼成
し、そのまま炉内で60分前後自然冷却させて室温乃至
これに近い状態に戻す。The raw bones of these animals are cut into sizes that are easy to burn, and then put into a pressure cooker and boiled at about 200 to 400°C for about 90 minutes. Next, the bones are placed in a kiln,
It is fired at about 900 to 1100°C for about 60 to 180 minutes, and then allowed to naturally cool in the furnace for about 60 minutes to return to room temperature or a state close to this temperature.
骨に青成分以外のゼラチン、脂肪、蛋白質、にかわ等の
有機物が残存すると酸化腐敗の原因となるのて、これを
確実に除去しておくことが重要である。上記煮沸工程に
よって、外側のみならず気孔内に付着している有機物を
骨から大力分離除去することができる。If organic substances other than the blue component, such as gelatin, fat, protein, and glue, remain in the bones, they will cause oxidative decay, so it is important to ensure that they are removed. By the above boiling process, organic matter adhering not only to the outside but also to the inside of the pores can be strongly separated and removed from the bone.
その上で上記焼成工程を通すことによって、残存する有
機物を完全に除去することができ、同時に骨中の湿度(
水分)を数%以下、好ましくはほぼ0%にまで低下させ
ることができる。また、上記焼成条件によれば、骨は白
骨化して無数の気孔を有した原形組織を維持する。By then passing through the above baking process, remaining organic matter can be completely removed, and at the same time the humidity in the bone can be reduced.
The water content can be reduced to several percent or less, preferably to almost 0%. Further, according to the above firing conditions, the bone becomes skeletal and maintains its original structure having countless pores.
上記焼成、冷却後、この骨を破砕し、パウダー機にかけ
て20〜200メツシユ前後、特に好ましくは50〜1
00メツシユの粉状の骨粉とする。After the above-mentioned baking and cooling, the bone is crushed and powdered into powder powder to produce approximately 20 to 200 meshes, particularly preferably 50 to 1 mesh.
00 mesh powdered bone meal.
上記骨粉は、牛骨の場合、原料の生骨に比して重量比的
40%の収量か得られる。粒子は、カルシウム(約33
重量%)を主成分とし、リン(約167%)、バリウム
(約1.03%〉、ナトリウム(約076%)、イオウ
(約0.64%)、他にマグネシウム、カリウム、塩素
、アミン、鉄等からなっており、粒子の内外に渡って無
数の微小気孔が連通存在している。この骨粉はカルシウ
ム等によりアルカリ性である。In the case of bovine bones, the above-mentioned bone powder can be obtained at a yield of 40% by weight compared to raw raw bones. The particles contain calcium (approximately 33
The main components are phosphorus (approximately 167%), barium (approximately 1.03%), sodium (approximately 0.076%), sulfur (approximately 0.64%), and magnesium, potassium, chlorine, amine, It is made of iron, etc., and has countless microscopic pores that communicate with each other both inside and outside the particle.This bone powder is alkaline due to calcium, etc.
つなぎ助材としては粘土質のものか好適で、例えばヘン
トナイト、酸性白土、活性白土、カオリン粘土、セリサ
イト、パイロフィライト、耐火粘土、モンモリロナイト
、クロライド、等があげられる。Suitable binding aids include clay materials, such as hentonite, acid clay, activated clay, kaolin clay, sericite, pyrophyllite, fireclay, montmorillonite, chloride, and the like.
アルミナもつなぎ材の役目をし、添加によって、濾過材
の強度が増大するが、多すぎると濾過材中の細孔が少な
くなる傾向かある。Alumina also acts as a binder, and its addition increases the strength of the filter medium, but if it is added too much, the pores in the filter medium tend to decrease.
有1物粉体は他の成分と混合し形成し焼成することによ
って焼成時に成形体中に微細孔を生ザしぬるものであり
、その作用を成すものであればよいが、濾過材を安価に
得るには安価な材料、例えば木粉、米ぬか、麦カス、も
みがら、廃材の粉末、澱粉カス、焼酎カス、等が好まし
い。By mixing the powder with other ingredients, forming it, and firing it, it creates micropores in the molded body during firing, and it is fine as long as it can perform this function, but the filter material is not cheap. It is preferable to use inexpensive materials such as wood flour, rice bran, wheat dregs, rice husks, waste wood powder, starch dregs, and shochu dregs.
本発明で用いる中和濾過材及び調整濾過材の各成分の量
割きは本発明の目的か達成される範囲内であればよい。The amounts of each component of the neutralized filter medium and the adjusted filter medium used in the present invention may be within a range that achieves the object of the present invention.
すなわち、中和濾過材の割合は通常、生ゴミ焼却圧粉と
つなぎ助材の合計量100重量部に対して、動物骨粉6
0〜190重量部、好ましくは95〜125重量部:ア
ルミナ9〜27重量部、好ましくは14〜23重量部:
有1lIi物粉体4〜12重量部、好ましくは6〜10
重量部である。In other words, the ratio of neutralized filter media is usually 6 parts by weight of animal bone meal to 100 parts by weight of the total amount of garbage incineration powder and binder.
0 to 190 parts by weight, preferably 95 to 125 parts by weight: 9 to 27 parts by weight, preferably 14 to 23 parts by weight of alumina:
4 to 12 parts by weight, preferably 6 to 10 parts by weight of powder containing
Parts by weight.
また、調整濾過材の割合は通常、生ゴミ焼却圧粉とつな
ぎ助材の合計量100重量部に対して、動物骨粉10〜
30重量部、好ましくは16〜26重量部:アルミナ8
〜26重量部、好ましくは13〜21重量部、有m物粉
体2〜6重量部、好ましくは3〜5重量部である。In addition, the ratio of the adjusted filter material is usually 10 to 10 parts by weight of animal bone powder to 100 parts by weight of the total amount of garbage incineration powder and binder.
30 parts by weight, preferably 16-26 parts by weight: alumina 8
~26 parts by weight, preferably 13 to 21 parts by weight, and 2 to 6 parts by weight, preferably 3 to 5 parts by weight.
生ゴミ焼却圧粉は濾過材の強度を大にし、かつ排煙処理
能力を増大させる。また、動物骨粉は吸着性を有し、か
つ排煙中の酸性ガスと反応する性質を有し、さらに濾過
材の細孔の量を増大させる効果がある。Garbage incineration compacted powder increases the strength of the filter medium and increases the flue gas treatment capacity. In addition, animal bone powder has adsorption properties and has the property of reacting with acidic gas in flue gas, and has the effect of increasing the amount of pores in the filter medium.
上記中和濾過材及び調整濾過材の製造に際しては、上述
した各成分含所望の組成になるように計量し、撹拌し、
水を加えて混合した後、造粒する。When producing the above-mentioned neutralized filter medium and adjusted filter medium, each of the above-mentioned components is weighed and stirred to obtain the desired composition,
After adding water and mixing, granulate.
得られた粒を乾燥し、焼成し、冷却し、製品とする。The obtained grains are dried, fired, and cooled to form a product.
通常、乾燥温度は200℃前後、焼成温度は800〜1
000°CM11後である。Normally, the drying temperature is around 200℃, and the firing temperature is 800~1
000°CM11 later.
これら中和濾過材及び調整濾過材はいずれも粒状であり
、そのサイズは通常、それぞれ3〜8φ、10〜15φ
である。Both of these neutralizing filter media and adjustment filter media are granular, and their sizes are usually 3 to 8 φ and 10 to 15 φ, respectively.
It is.
各濾過材の各成分の配合割合の一態様を示すと、中和濾
過材は、好ましくは動物骨粉50部(重量部、以下同じ
)、つなぎ助材及び生ゴミ焼却灰の合計量が40部、ア
ルミナ7部てあり、有機物粉体は中和濾過材を、多孔質
体とするためのもので3部であり、中和濾過材は動物骨
粉含有量が多くアルカリ度か高い。One aspect of the blending ratio of each component of each filter medium is that the neutralized filter medium preferably contains 50 parts of animal bone meal (parts by weight, the same applies hereinafter), and the total amount of binder and garbage incineration ash is 40 parts. , 7 parts of alumina, 3 parts of organic powder to make the neutralized filter material porous, and the neutralized filter material contains a large amount of animal bone powder and has a high alkalinity.
また調整濾過材は好まし【は動物骨粉15部、つなぎ助
材及び生ゴミ焼却灰の合計量が70部、アルミナか12
部てあり、有FR物粉体は3部である。In addition, the adjusted filter material is preferably [15 parts of animal bone meal, a total of 70 parts of binder material and garbage incineration ash, and 12 parts of alumina or
1 part, and the FR-containing powder is 3 parts.
このような中和濾過材及び調整濾過材は排煙の流路に配
置し排煙と接触させて用いられる。Such neutralizing filter media and adjustment filter media are placed in the flue gas flow path and used in contact with the flue gas.
(作用及び効果)
本発明は、動物骨粉が高いアルカリ土類金属という性質
を利用したもので、例えばブロワ−で吸い上げられた被
処理ガスとしての硫黄又は塩素を含む酸性の排ガスは、
ガス入口から吸入され、中和層を通過することにより中
和され、さらに調整層通過することによりPHが6乃至
7の中性に調整されて、ガス出口から排出される。(Functions and Effects) The present invention takes advantage of the property that animal bone meal is high in alkaline earth metals.
The gas is inhaled from the gas inlet, neutralized by passing through the neutralization layer, and further adjusted to a neutral pH of 6 to 7 by passing through the adjustment layer, and then discharged from the gas outlet.
また、調整層とガス出口との間にPHセンサが設けられ
ており、排出カスのPHが中性を越えれば、上述した中
和濾過材及び調¥M′a過材を交換する。Further, a PH sensor is provided between the adjustment layer and the gas outlet, and if the PH of the discharged waste exceeds neutrality, the above-mentioned neutralization filter material and adjustment M'a filter material are replaced.
本発明の脱硫脱塩機器に用いる中和濾過材及び調整濾過
材は生ゴミ焼却灰を利用するものであり、生ゴミ焼却灰
処理問題を解決する一つの有力な手段となり得る。The neutralization filter material and the adjustment filter material used in the desulfurization and desalination equipment of the present invention utilize garbage incineration ash, and can be an effective means for solving the problem of garbage incineration ash treatment.
本発明によれば、硫黄又は塩素を含む酸性の排煙の脱硫
または脱塩を行って中性の排ガスとして放出できるので
排煙公害を除去することができる。According to the present invention, acidic flue gas containing sulfur or chlorine can be desulfurized or desalted and released as neutral flue gas, thereby making it possible to eliminate flue gas pollution.
例えば、工場、ゴミ焼却場等の煙突から出る硫黄酸化物
を本発明の中和濾過材及び調整濾過材と反応させて硫酸
にしたり、車から出る窒素酸化物を反応させて硝酸にし
、これらの有害物質を反応させ、かつ吸着除去すること
かてきる。また、排煙は酸性(PH3〜4)であるが、
本発明の中和濾過材及び調整濾過材を用いれば処理後の
排煙は中性(PH6〜7)となる。For example, sulfur oxides emitted from chimneys of factories, garbage incinerators, etc. can be reacted with the neutralized filter material and adjusted filter material of the present invention to produce sulfuric acid, or nitrogen oxides emitted from cars can be reacted to produce nitric acid. It can react with harmful substances and remove them by adsorption. In addition, flue gas is acidic (PH3-4),
If the neutralized filter material and adjusted filter material of the present invention are used, the flue gas after treatment will be neutral (PH6 to 7).
本発明に用いる中和濾過材及び調整濾過材は極めて多孔
質であるため処理速度か大きいという利点がある。Since the neutralized filter material and the adjusted filter material used in the present invention are extremely porous, they have the advantage of high processing speed.
また、上記中和濾過材及び調整濾過材を用いれば特別の
装置を要せず、簡易にこれらの処理を行うことができる
。Further, by using the neutralized filter material and the adjusted filter material, these treatments can be easily performed without requiring any special equipment.
(実施例)
中和濾過材は、動物骨粉50部、つなぎ助材及び生ゴミ
焼却灰の合計量が40部、アルミナ7部、及び有機物粉
体3部を、上記割きの組成になるように計量し、撹拌し
、水?加えて混合した後、3〜8φに造粒する。得られ
た粒を200℃前後で乾燥し、800〜1000℃前後
で焼成し、冷却して製造する。(Example) The neutralized filter material was composed of 50 parts of animal bone powder, a total of 40 parts of binder and garbage incineration ash, 7 parts of alumina, and 3 parts of organic powder, so that the composition was as follows. Measure, stir, water? After addition and mixing, granulation is performed to a size of 3 to 8 φ. The obtained grains are dried at around 200°C, fired at around 800 to 1000°C, and cooled to produce it.
一方、調整濾過材は動物骨粉15部、つなぎ助材及び生
ゴミ焼却灰のき計量が70部、アルミナ12部及び有機
物粉体3部を、上記割合の組成になるように計量し、撹
拌し、水を加えて混きした後、10〜15φに造粒する
。得られた粒を200℃前後で乾燥し、800〜100
0″C前後て焼成し、冷却して製造する。On the other hand, the adjusted filter material was prepared by weighing 15 parts of animal bone meal, 70 parts of binder additives and garbage incineration ash, 12 parts of alumina, and 3 parts of organic powder so that the composition was in the above proportions, and stirring. After adding water and mixing, the mixture is granulated to a size of 10 to 15 φ. The obtained grains are dried at around 200℃, and
It is manufactured by firing at around 0''C and cooling.
このようにして製造された中和濾過材及び調整濾過材は
、それぞれ第2図に示す容器に充填される。The neutralized filtration medium and the adjusted filtration medium thus manufactured are each filled into containers shown in FIG. 2.
第2図に示す容器は、例えば側板1で形成された簡に2
つの穴2a、3aが形成された底板4を溶着し、さらに
、この筒内部に小さい2つの円筒2.3を配置して構成
される。小円筒2及び3は底面2a、3aが開口され、
上面2b、3bは封止されるとともに、その側面には多
数の小穴が形成されている。The container shown in FIG.
A bottom plate 4 in which two holes 2a and 3a are formed is welded together, and two small cylinders 2.3 are placed inside this cylinder. The small cylinders 2 and 3 have open bottom surfaces 2a and 3a,
The upper surfaces 2b and 3b are sealed, and a large number of small holes are formed in the side surfaces thereof.
中和濾過材又は調整濾過材は容器内部く小円筒2.3の
周囲〉に充填される。The neutralized filter material or the conditioned filter material is filled inside the container and around the small cylinder 2.3.
この容器は、上方から例えばブロワ−等て吸弓されるこ
とにより、図中二点鎖線で示すように、g 3下方部か
ら供給された排ガスが小円筒2.3内に導かれ、更にそ
の側面に設けられた小穴を通して容器内に導かれ、容器
に充填された中和濾過材又は調整濾過材に接触した後に
上方に吸引されるようになっている。By suctioning the container from above with a blower or the like, the exhaust gas supplied from the lower part of g3 is guided into the small cylinder 2.3, as shown by the chain double-dashed line in the figure, and further into the small cylinder 2.3. It is guided into the container through a small hole provided on the side, and is sucked upward after coming into contact with the neutralizing filter material or adjusting filter material filled in the container.
第1図は一実施例としての脱硫脱塩機器の一部切り欠い
た側面図である。FIG. 1 is a partially cutaway side view of a desulfurization and desalination equipment as an example.
図中、カス入口10は、排ガスを取り入れる口である。In the figure, a waste inlet 10 is an opening that takes in exhaust gas.
円筒形に形成された本体11は、密閉構造となっており
、その内部下方には、中和濾過材を充填したS′器12
が配置され、所定の空間部13を挟んで内部上方には調
整濾過材を充填した容器14が配置されるようになって
いる。これら容器12.14は本体1,1の側面部に設
けられた扉(図示しない)により挿脱可能になっており
、調整濾過材又は中和濾過材の交換ができるようになっ
ている。The main body 11 formed in a cylindrical shape has a closed structure, and an S' container 12 filled with a neutralizing filter material is disposed at the lower part of the inside thereof.
is arranged, and a container 14 filled with a conditioning filter material is arranged above the interior with a predetermined space 13 in between. These containers 12, 14 can be inserted and removed through doors (not shown) provided on the sides of the main bodies 1, 1, so that the adjustment filter material or the neutralization filter material can be replaced.
本体11の上方部は排ガスを導く煙道となっており、こ
の煙道の中途部にはブロワ−15が設けられている。さ
らに、ブロワ−15の先方には煙突16が取り付けられ
ており、その先端がガス出口17となっている。また、
ガス出口′近傍の煙突ゴロ内部には、PHセンサ18が
設けられており、脱硫脱塩された排ガスの濃度を検知す
るようになっている。The upper part of the main body 11 is a flue for guiding exhaust gas, and a blower 15 is provided in the middle of this flue. Furthermore, a chimney 16 is attached to the front of the blower 15, and the tip thereof serves as a gas outlet 17. Also,
A PH sensor 18 is provided inside the chimney near the gas outlet' to detect the concentration of the desulfurized and desalinated exhaust gas.
このような構成の脱硫脱塩機器においては、ブロワ−1
5が駆動されることにより、ガス入口10から供給され
た排ガスが、図中二点鎖線てしめすように導かれる。ま
ず、排ガスは、中和濾過材が充填された容器12の小円
筒内に導かれ、その側面に設けられた多数の小穴から周
囲に流出し、動物骨粉を多く含んてアルカリ度が高くな
っている中和濾過材に接触されて中和される。この容器
12で中和された排ガスは、空間部13を介して調整濾
過材が充填され、小円筒位置が容器12と例えば直交す
るように配置された容器14の小円筒内に導かれ、その
側面に設けられた多数の小穴から周囲に流出し、適量の
動物骨粉を含んだ調整濾過材に接触されて、PHが6〜
7に調整される。In desulfurization desalination equipment with such a configuration, the blower 1
5 is driven, the exhaust gas supplied from the gas inlet 10 is guided as shown by the two-dot chain line in the figure. First, the exhaust gas is guided into a small cylinder of the container 12 filled with neutralizing filter material, and flows out into the surrounding area through a number of small holes provided on the side of the container, and contains a large amount of animal bone powder, resulting in high alkalinity. It is neutralized when it comes into contact with a neutralizing filter medium. The exhaust gas neutralized in this container 12 is guided through a space 13 into a small cylinder of a container 14 filled with an adjustment filter material and arranged such that the small cylinder position is perpendicular to the container 12, for example. It flows out into the surrounding area from the many small holes provided on the side, and comes into contact with the adjusting filter material containing an appropriate amount of animal bone powder, and the pH reaches 6~6.
Adjusted to 7.
このようにしてPHが調整された排ガスは煙道を通って
ブロワ−15を通過し、煙突16のガス出口かち排出さ
れる。この際、排出されるガスの4度は、PHセンサ1
8で監視されており、この濃度が中性値(例えばPH7
>を越えれば、別場所に設けられている監視盤てアラー
ムを発するようになっている。これにより、操作員は中
和濾過材又は調整濾過材を交換することになる。The exhaust gas whose pH has been adjusted in this manner passes through the flue, passes through the blower 15, and is discharged from the gas outlet of the chimney 16. At this time, the 4 degree of gas discharged is PH sensor 1
8, and this concentration is monitored at a neutral value (e.g. pH 7).
> is exceeded, an alarm is set off on a monitoring board located elsewhere. This causes the operator to replace the neutralizing filter media or conditioning filter media.
このように、中和濾過材及び調整濾過材を通過させるこ
とにより排カスを中性に調整して排出するようにしたの
て、排煙公害を防止できるものとなっている。In this way, exhaust gas pollution can be prevented by adjusting the exhaust residue to neutrality and discharging it by passing it through the neutralizing filter medium and the adjusting filter medium.
なお、上記容器には小円筒を2つ設けた場合について説
明したが、小円筒の数はこれに限定されるものでなく、
任意の数てあっても良い。In addition, although the case where two small cylinders were provided in the above-mentioned container was explained, the number of small cylinders is not limited to this,
There may be any number.
第1図は本発明の脱硫脱塩機器の一部を切り欠いた側面
図、第2図は中和濾過材又は調整濾過材を収容する容器
の構成を示す斜視図である。
10・・・ガス入口、12・・・中和濾過材を充填した
容器(中和層)、14・調整濾過材を充填した容器(調
整層)、17・・−ガス出口、18・PHセンサ。FIG. 1 is a partially cutaway side view of the desulfurization and desalination equipment of the present invention, and FIG. 2 is a perspective view showing the configuration of a container that accommodates the neutralization filter material or the adjustment filter material. 10...Gas inlet, 12...Container filled with neutralization filter material (neutralization layer), 14.Container filled with adjustment filter material (adjustment layer), 17...-Gas outlet, 18.PH sensor .
Claims (1)
材を充填してなる調整層、及び調整層とガス出口との間
に設けられたPH6乃至7を検出し得るPHセンサを有
してなり、中和濾過材が動物骨粉、つなぎ助材、生ゴミ
焼却灰の有効成分、アルミナ及び有機物粉体を成形し焼
成してなる動物骨粉が40重量%以上のアルカリ度の高
い粒状の濾過材で、調整濾過材が動物骨粉、つなぎ助材
、生ゴミ焼却灰の有効成分、アルミナ及び有機物粉体を
成形し焼成してなり中和濾過材よりも動物骨粉の含有量
が少なくアルカリ度の低い粒状の濾過材であることを特
徴とする脱硫脱塩機器。A gas inlet, a neutralization layer filled with a neutralization filtration material, an adjustment layer filled with an adjustment filtration material, and a PH sensor capable of detecting pH 6 to 7 provided between the adjustment layer and the gas outlet. The neutralizing filter material is formed by molding and firing animal bone powder, binding aid, active ingredients of garbage incineration ash, alumina, and organic powder.The animal bone powder is granular with a high alkalinity of 40% by weight or more. This filter material is made by molding and firing animal bone meal, binding agent, active ingredients of garbage incineration ash, alumina, and organic powder, and has a lower content of animal bone meal than neutralized filter material, making it more alkaline. Desulfurization and desalination equipment characterized by a granular filter material with a low degree of filtration.
Priority Applications (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2106556A JPH0775654B2 (en) | 1990-04-24 | 1990-04-24 | Desulfurization desalination equipment |
| KR1019900008075A KR970004694B1 (en) | 1990-04-24 | 1990-05-31 | Porous active material for removing harmful ingredients mainly from raw incineration ash, method for removing harmful ingredients and apparatus therefor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2106556A JPH0775654B2 (en) | 1990-04-24 | 1990-04-24 | Desulfurization desalination equipment |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH047018A true JPH047018A (en) | 1992-01-10 |
| JPH0775654B2 JPH0775654B2 (en) | 1995-08-16 |
Family
ID=14436604
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2106556A Expired - Lifetime JPH0775654B2 (en) | 1990-04-24 | 1990-04-24 | Desulfurization desalination equipment |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0775654B2 (en) |
Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS63287469A (en) * | 1987-05-21 | 1988-11-24 | Sanai Fujita | Alkalinizing material and production thereof |
-
1990
- 1990-04-24 JP JP2106556A patent/JPH0775654B2/en not_active Expired - Lifetime
Patent Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS63287469A (en) * | 1987-05-21 | 1988-11-24 | Sanai Fujita | Alkalinizing material and production thereof |
Also Published As
| Publication number | Publication date |
|---|---|
| JPH0775654B2 (en) | 1995-08-16 |
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