JPH08205672A - Production of artificial soil - Google Patents
Production of artificial soilInfo
- Publication number
- JPH08205672A JPH08205672A JP7013948A JP1394895A JPH08205672A JP H08205672 A JPH08205672 A JP H08205672A JP 7013948 A JP7013948 A JP 7013948A JP 1394895 A JP1394895 A JP 1394895A JP H08205672 A JPH08205672 A JP H08205672A
- Authority
- JP
- Japan
- Prior art keywords
- soil
- nox
- artificial soil
- lime
- treatment
- 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.)
- Withdrawn
Links
- 239000002689 soil Substances 0.000 title claims abstract description 65
- 238000004519 manufacturing process Methods 0.000 title claims description 18
- ODINCKMPIJJUCX-UHFFFAOYSA-N Calcium oxide Chemical compound [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 claims abstract description 26
- 239000003795 chemical substances by application Substances 0.000 claims abstract description 24
- 239000000203 mixture Substances 0.000 claims abstract description 15
- 239000000292 calcium oxide Substances 0.000 claims abstract description 13
- 235000012255 calcium oxide Nutrition 0.000 claims abstract description 13
- 239000010440 gypsum Substances 0.000 claims abstract description 12
- 229910052602 gypsum Inorganic materials 0.000 claims abstract description 12
- AXCZMVOFGPJBDE-UHFFFAOYSA-L calcium dihydroxide Chemical compound [OH-].[OH-].[Ca+2] AXCZMVOFGPJBDE-UHFFFAOYSA-L 0.000 claims abstract description 11
- 235000008733 Citrus aurantifolia Nutrition 0.000 claims abstract description 10
- 235000011941 Tilia x europaea Nutrition 0.000 claims abstract description 10
- 239000000920 calcium hydroxide Substances 0.000 claims abstract description 10
- 235000011116 calcium hydroxide Nutrition 0.000 claims abstract description 10
- 229910001861 calcium hydroxide Inorganic materials 0.000 claims abstract description 10
- 239000004571 lime Substances 0.000 claims abstract description 10
- 238000002156 mixing Methods 0.000 claims abstract description 10
- 230000003009 desulfurizing effect Effects 0.000 claims abstract description 6
- 230000000887 hydrating effect Effects 0.000 claims abstract description 4
- 238000006703 hydration reaction Methods 0.000 claims description 19
- 230000036571 hydration Effects 0.000 claims description 18
- 239000010883 coal ash Substances 0.000 claims description 8
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 25
- 229910001868 water Inorganic materials 0.000 abstract description 25
- 239000003337 fertilizer Substances 0.000 abstract description 11
- 239000000463 material Substances 0.000 abstract description 4
- 230000003472 neutralizing effect Effects 0.000 abstract description 3
- 239000007789 gas Substances 0.000 abstract 3
- 239000011369 resultant mixture Substances 0.000 abstract 2
- 239000002912 waste gas Substances 0.000 abstract 2
- -1 improved in pH Substances 0.000 abstract 1
- 239000002994 raw material Substances 0.000 description 15
- 239000000047 product Substances 0.000 description 14
- 150000004683 dihydrates Chemical class 0.000 description 10
- 239000011575 calcium Substances 0.000 description 9
- 238000000034 method Methods 0.000 description 7
- 230000000052 comparative effect Effects 0.000 description 6
- 238000006477 desulfuration reaction Methods 0.000 description 6
- 230000023556 desulfurization Effects 0.000 description 6
- 239000002245 particle Substances 0.000 description 6
- 239000000126 substance Substances 0.000 description 6
- 241000196324 Embryophyta Species 0.000 description 5
- 239000002956 ash Substances 0.000 description 5
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 4
- 229910052799 carbon Inorganic materials 0.000 description 4
- 238000006243 chemical reaction Methods 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- 239000007788 liquid Substances 0.000 description 4
- 229910052717 sulfur Inorganic materials 0.000 description 4
- 235000009337 Spinacia oleracea Nutrition 0.000 description 3
- OSGAYBCDTDRGGQ-UHFFFAOYSA-L calcium sulfate Chemical compound [Ca+2].[O-]S([O-])(=O)=O OSGAYBCDTDRGGQ-UHFFFAOYSA-L 0.000 description 3
- ZOMBKNNSYQHRCA-UHFFFAOYSA-J calcium sulfate hemihydrate Chemical compound O.[Ca+2].[Ca+2].[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O ZOMBKNNSYQHRCA-UHFFFAOYSA-J 0.000 description 3
- 238000002485 combustion reaction Methods 0.000 description 3
- 238000001125 extrusion Methods 0.000 description 3
- 239000010881 fly ash Substances 0.000 description 3
- 229910052742 iron Inorganic materials 0.000 description 3
- 238000003756 stirring Methods 0.000 description 3
- 229910018072 Al 2 O 3 Inorganic materials 0.000 description 2
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 description 2
- 229910004298 SiO 2 Inorganic materials 0.000 description 2
- 244000300264 Spinacia oleracea Species 0.000 description 2
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 description 2
- 230000002378 acidificating effect Effects 0.000 description 2
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 2
- 229910052681 coesite Inorganic materials 0.000 description 2
- 229910052593 corundum Inorganic materials 0.000 description 2
- 229910052906 cristobalite Inorganic materials 0.000 description 2
- 239000008187 granular material Substances 0.000 description 2
- 229910052739 hydrogen Inorganic materials 0.000 description 2
- 239000003607 modifier Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 239000011505 plaster Substances 0.000 description 2
- 229920006395 saturated elastomer Polymers 0.000 description 2
- 239000000377 silicon dioxide Substances 0.000 description 2
- 239000002002 slurry Substances 0.000 description 2
- 229910052682 stishovite Inorganic materials 0.000 description 2
- 229910052905 tridymite Inorganic materials 0.000 description 2
- 239000010455 vermiculite Substances 0.000 description 2
- 229910052902 vermiculite Inorganic materials 0.000 description 2
- 235000019354 vermiculite Nutrition 0.000 description 2
- 229910001845 yogo sapphire Inorganic materials 0.000 description 2
- 101000635799 Homo sapiens Run domain Beclin-1-interacting and cysteine-rich domain-containing protein Proteins 0.000 description 1
- 240000008415 Lactuca sativa Species 0.000 description 1
- 235000003228 Lactuca sativa Nutrition 0.000 description 1
- VCUFZILGIRCDQQ-KRWDZBQOSA-N N-[[(5S)-2-oxo-3-(2-oxo-3H-1,3-benzoxazol-6-yl)-1,3-oxazolidin-5-yl]methyl]-2-[[3-(trifluoromethoxy)phenyl]methylamino]pyrimidine-5-carboxamide Chemical group O=C1O[C@H](CN1C1=CC2=C(NC(O2)=O)C=C1)CNC(=O)C=1C=NC(=NC=1)NCC1=CC(=CC=C1)OC(F)(F)F VCUFZILGIRCDQQ-KRWDZBQOSA-N 0.000 description 1
- KKCBUQHMOMHUOY-UHFFFAOYSA-N Na2O Inorganic materials [O-2].[Na+].[Na+] KKCBUQHMOMHUOY-UHFFFAOYSA-N 0.000 description 1
- 244000088415 Raphanus sativus Species 0.000 description 1
- 102100030852 Run domain Beclin-1-interacting and cysteine-rich domain-containing protein Human genes 0.000 description 1
- 244000061456 Solanum tuberosum Species 0.000 description 1
- 235000002595 Solanum tuberosum Nutrition 0.000 description 1
- 241000219315 Spinacia Species 0.000 description 1
- 238000002441 X-ray diffraction Methods 0.000 description 1
- 229910021536 Zeolite Inorganic materials 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 150000008064 anhydrides Chemical class 0.000 description 1
- 238000007664 blowing Methods 0.000 description 1
- 229910052791 calcium Inorganic materials 0.000 description 1
- 229910000019 calcium carbonate Inorganic materials 0.000 description 1
- 239000000378 calcium silicate Substances 0.000 description 1
- 229910052918 calcium silicate Inorganic materials 0.000 description 1
- OYACROKNLOSFPA-UHFFFAOYSA-N calcium;dioxido(oxo)silane Chemical compound [Ca+2].[O-][Si]([O-])=O OYACROKNLOSFPA-UHFFFAOYSA-N 0.000 description 1
- HHSPVTKDOHQBKF-UHFFFAOYSA-J calcium;magnesium;dicarbonate Chemical compound [Mg+2].[Ca+2].[O-]C([O-])=O.[O-]C([O-])=O HHSPVTKDOHQBKF-UHFFFAOYSA-J 0.000 description 1
- 239000007795 chemical reaction product Substances 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 239000002361 compost Substances 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 229910001653 ettringite Inorganic materials 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 230000004720 fertilization Effects 0.000 description 1
- 150000004677 hydrates Chemical class 0.000 description 1
- 239000004615 ingredient Substances 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- XEEYBQQBJWHFJM-UHFFFAOYSA-N iron Substances [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 1
- 238000004898 kneading Methods 0.000 description 1
- 229910052749 magnesium Inorganic materials 0.000 description 1
- 239000011777 magnesium Substances 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- QJGQUHMNIGDVPM-UHFFFAOYSA-N nitrogen group Chemical group [N] QJGQUHMNIGDVPM-UHFFFAOYSA-N 0.000 description 1
- 235000015097 nutrients Nutrition 0.000 description 1
- 239000010451 perlite Substances 0.000 description 1
- 235000019362 perlite Nutrition 0.000 description 1
- 229910052698 phosphorus Inorganic materials 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 229910052700 potassium Inorganic materials 0.000 description 1
- 235000012015 potatoes Nutrition 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 230000009257 reactivity Effects 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
- 239000010457 zeolite Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C05—FERTILISERS; MANUFACTURE THEREOF
- C05D—INORGANIC FERTILISERS NOT COVERED BY SUBCLASSES C05B, C05C; FERTILISERS PRODUCING CARBON DIOXIDE
- C05D9/00—Other inorganic fertilisers
-
- C—CHEMISTRY; METALLURGY
- C05—FERTILISERS; MANUFACTURE THEREOF
- C05D—INORGANIC FERTILISERS NOT COVERED BY SUBCLASSES C05B, C05C; FERTILISERS PRODUCING CARBON DIOXIDE
- C05D3/00—Calcareous fertilisers
- C05D3/02—Calcareous fertilisers from limestone, calcium carbonate, calcium hydrate, slaked lime, calcium oxide, waste calcium products
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Inorganic Chemistry (AREA)
- Organic Chemistry (AREA)
- Treating Waste Gases (AREA)
- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
- Fertilizers (AREA)
- Cultivation Of Plants (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は人工土壌の製造方法に関
する。FIELD OF THE INVENTION The present invention relates to a method for producing artificial soil.
【0002】[0002]
【従来の技術】日本の土壌は酸性土壌が多いため土壌p
Hを調整することが必要であり、一般の植物でpH:6
〜6.5に、ほうれんそう、レタスなど酸性に極めて敏
感な植物を栽培する場合でpH7程度になるように土壌
に炭酸カルシウムまたは苦土炭酸カルシウムを混合し中
和していた。また土壌の保水性、保肥力を改善するため
に土壌に腐食酸質資材、ゼオライト、パーライト、バー
ミュキュライト等の土壌改質材を混合していた。しかし
ながら中和剤、土壌改質材自体には栄養分が含まれてい
ないので更に肥料を与える必要があった。[Prior Art] Japanese soil is often acidic, so soil p
It is necessary to adjust H, and pH is 6 in general plants.
In the case of cultivating plants extremely sensitive to acidity such as spinach and lettuce, the soil was mixed with calcium carbonate or calcium magnesium carbonate to neutralize the pH to about 7. Further, in order to improve the water retention and fertilizing power of the soil, soil-modifying materials such as corrosive acid materials, zeolite, perlite and vermiculite have been mixed with the soil. However, since the neutralizer and the soil modifier itself do not contain nutrients, it was necessary to add fertilizer.
【0003】[0003]
【発明が解決しようとする課題】本発明は前記従来技術
の実状に鑑み、植物を栽培する場合、中和剤、土壌改質
材としてのみならず、元肥としての働きをも有する人工
土壌の製造方法を提供しようとするものである。In view of the above-mentioned conventional state of the art, the present invention is for producing an artificial soil which not only functions as a neutralizing agent and a soil modifier, but also as a fertilizer when cultivating a plant. It is intended to provide a method.
【0004】[0004]
【課題を解決するための手段】本発明は脱硫・脱硝剤と
して用いた後の使用済み石灰系排ガス処理剤に消石灰・
生石灰及び石膏から選ばれた少なくとも一つを混合し、
水和処理することを特徴とする人工土壌の製造方法及び
石炭灰及び使用済み石灰系排ガス処理剤から選ばれた少
なくとも一つに消石灰・生石灰及び石膏から選ばれた少
なくとも一つを混合し、水和処理した後SO2 、NOx
及びO2 を含有するガスで処理することを特徴とする人
工土壌の製造方法であり、得られる人工土壌は土壌と混
合することにより植物を栽培する場合、土壌を適正状態
に調整することが可能となる。[Means for Solving the Problems] The present invention uses slaked lime as a used lime-based exhaust gas treatment agent after being used as a desulfurization / denitration agent.
Mix at least one selected from quicklime and gypsum,
A method for producing an artificial soil characterized by hydration treatment and at least one selected from coal ash and a used lime-based exhaust gas treatment agent are mixed with at least one selected from slaked lime, quick lime and gypsum, and water is added. After the sum treatment, SO 2 , NOx
And a method for producing an artificial soil characterized by treating with a gas containing O 2 , wherein the artificial soil can be adjusted to an appropriate state when the plant is cultivated by mixing with the soil. Becomes
【0005】ここで原料としての石炭灰には微粉炭燃焼
ボイラから排出される平均粒径が20〜30ミクロンの
いわゆるフライアッシュと呼ばれるものと火炉底に落下
するクリンカーアッシュと呼ばれるものがあり、両者共
使用が可能であるが、水和反応性の面からは粒径が細か
いフライアッシュの方が好ましい。また、石膏としては
無水石膏、半水石膏、二水石膏などがあげられる。石膏
を含む物質として、流動層燃焼灰などの炉内脱硫剤及び
使用済み石灰系排ガス処理剤などがあげられる。ここで
使用済み石灰系排ガス処理剤とは、CaO、Ca(O
H)2 、CaCO 3 などを原料として製造されるカルシ
ウム系脱硫剤の使用済みのもの及び特開昭61−209
038号、特開昭63−283745号各公報などに示
されるCaO・Al2 O3 ・SiO2 ・CaSO4 系組
成物からなる脱硫剤の使用済みのものなどを言う。Here, the coal ash as a raw material is pulverized coal combustion
The average particle size discharged from the boiler is 20-30 microns
What is called fly ash and falls to the bottom of the furnace
There is something called clinker ash that both
It can be used, but the particle size is fine from the viewpoint of hydration reactivity.
I prefer fly ash. Also, as plaster
Examples include anhydrous gypsum, hemihydrate gypsum, and dihydrate gypsum. plaster
As a substance containing, the in-furnace desulfurization agent such as fluidized bed combustion ash and
Examples include used lime-based exhaust gas treatment agents. here
Used lime-based exhaust gas treatment agents are CaO, Ca (O
H)2, CaCO 3Calci produced from such ingredients
Used um-based desulfurizing agent and JP-A-61-209
No. 038, JP-A-63-283745, etc.
CaO ・ Al2O3・ SiO2・ CaSOFourSystem
It refers to a used desulfurizing agent composed of a product.
【0006】[0006]
【作用】本発明において、これらの原料を混合し、水和
して得られる水和物をSO2 、NOx及びO2 を含有す
るガスで処理した後の物質は複雑な組成のもので、分析
上の成分割合は無水物の重量%として、下記表1に示す
ようなものである。In the present invention, the hydrate obtained by mixing these raw materials and hydrating them and treating the hydrate with a gas containing SO 2 , NOx and O 2 has a complex composition and is analyzed. The above component ratios are as shown in Table 1 below as weight% of the anhydride.
【表1】 ここでCa(NO3 )2 はガス処理した時にNOxを吸
収して生成したものである。[Table 1] Here, Ca (NO 3 ) 2 is generated by absorbing NOx during gas treatment.
【0007】本発明で水和処理とは、原料混合物に水を
加えて水和反応物を形成させるために必要な処理のこと
を言い、例えば熱水養生、蒸気養生などが含まれ、硬化
性水和処理と非固結性水和処理とに分類される。In the present invention, the hydration treatment means a treatment necessary for adding water to a raw material mixture to form a hydration reaction product, and includes, for example, hot water curing, steam curing, etc. It is classified into hydration treatment and non-caking hydration treatment.
【0008】硬化性水和処理とは処理時の前記諸原料と
水の重量混合割合(固液比)を小に、例えば1:0.2
〜1:0.99とすることによって材料粒子間の結合を
促進させ硬化物を得る水和処理を言い、この処理法には
蒸気養生があげられる。前記諸原料と水を混合、混練り
し蒸気養生は温度60〜180℃、相対湿度100%の
飽和水分下で数分〜数日間が好ましい。The curable hydration treatment means that the weight mixing ratio (solid-liquid ratio) of the raw materials and water at the time of treatment is made small, for example, 1: 0.2.
It is a hydration treatment in which the bond between the material particles is promoted to obtain a cured product by setting the ratio to ˜1: 0.99, and this treatment method includes steam curing. It is preferable that steam curing be carried out by mixing and kneading the above-mentioned raw materials with water at a temperature of 60 to 180 ° C. and a saturated moisture of 100% relative humidity for several minutes to several days.
【0009】非固結性水和処理とは処理開始時の固液比
を大に、例えば1:1〜1:20ととし熱水で処理を行
う熱水養生のことを言い、この場合においては、60〜
180℃で水中に原料を分散し原料が下部に沈降、硬化
しないように攪拌しながら数分〜十数時間処理する方法
である。The non-consolidating hydration treatment refers to hot water curing in which the solid-liquid ratio at the start of treatment is set to a large value, for example, 1: 1 to 1:20, and the treatment is carried out with hot water. Is 60 ~
This is a method in which the raw material is dispersed in water at 180 ° C., and the raw material is treated for a few minutes to a dozen hours while stirring so that the raw material does not settle down and harden.
【0010】上記処理により得られる水和物は比表面積
が40〜80m2 /gと大きく、またX線回析から非晶
質のケイ酸カルシウム及びエトリンガイトを含む物質で
あることが確認された。この水和物はアルカリ性のため
そのままでも中和力があり、また比表面積が大きいため
保水性を有し保肥力もあるが、更にSO2 、NOx及び
O2 を含有するガスで処理することによって肥料として
働きを付加させることができる。この場合CaOとCa
SO4 、Ca(NO3 )2 の比率は当然変化するが、こ
のうちNOxの吸収により生成するCa(NO3 )2 は
水に溶けやすい物質であり、これから溶出するNO3 イ
オンは十分に窒素(N)肥料となりうるものであり施肥
効果を一層向上させることができる。The hydrate obtained by the above treatment had a large specific surface area of 40 to 80 m 2 / g, and it was confirmed by X-ray diffraction that it was a substance containing amorphous calcium silicate and ettringite. This hydrate has an alkaline neutralizing power as it is, and has a large specific surface area, so that it has water retention and fertilizing power. However, it can be treated with a gas containing SO 2 , NOx and O 2 . It can be added as a fertilizer. In this case CaO and Ca
The ratio of SO 4 and Ca (NO 3 ) 2 naturally changes, but of these, Ca (NO 3 ) 2 generated by absorption of NOx is a substance that is easily dissolved in water, and NO 3 ions eluted from this are sufficiently nitrogenous. (N) It can be a fertilizer and can further improve the fertilization effect.
【0011】SO2 、NOx及びO2 を含むガス処理の
方法は得られる水和物の形態によって異なるが、S
O2 、NOxをそれぞれ100ppm〜1vol%含
み、O2 を5〜21vol%含む温度80〜200℃の
ガスでSVが5〜50000h-1で水和物の乾燥重量1
kg当たりSO2 及びNOxが少なくとも1モル接触す
るのに十分な時間処理すればよい。ここでガス処理を行
うに当たり、SO2 、NOx及びO2 は水和物がNOx
を吸収しCa(NO3 )2 として固定するために必要な
成分である。SO2 と水和物との反応において、温度が
80℃以下の場合はNOx、O2 はあまり関与しない
が、SO2 及びNOxを吸収して肥料成分となるN分を
Ca(NO3 )2 として固定するためにはSO2 及びO
2 の共存がないと起こりにくい。従って水和物中に固定
されるN分の含有量も少なく人工土壌としての利用効果
が薄れることとなる。The method of gas treatment containing SO 2 , NOx and O 2 depends on the form of the hydrate obtained.
O 2, NOx and includes each 100ppm~1vol%, dry weight of the hydrate at a temperature 80 to 200 ° C. of the gas in the SV 5~50000H -1 containing O 2 5~21vol% 1
The treatment may be performed for a sufficient time so that at least 1 mol of SO 2 and NOx per kg are contacted. In the gas treatment, SO 2 , NOx and O 2 are hydrates of NOx.
Is a component necessary for absorbing and fixing as Ca (NO 3 ) 2 . In the reaction between SO 2 and hydrate, when the temperature is 80 ° C. or lower, NOx and O 2 do not participate so much, but the N content that absorbs SO 2 and NOx and becomes a fertilizer component is Ca (NO 3 ) 2 To fix as SO 2 and O
It is unlikely to occur without the coexistence of 2 . Therefore, the content of N content fixed in the hydrate is small and the utilization effect as artificial soil is weakened.
【0012】この反応についてのメカニズムは次のよう
に考えられる。すなわち、上記水和物をSO2 、NOx
及びO2 を含む排ガスで処理すると、その際排ガスが脱
硫・脱硝されるので、先ずこれを脱硫・脱硝剤として用
い、その後で処理後の水和物は人工土壌として利用する
ことができる。このように本発明の方法で、ガス処理を
SO2 、NOx、O2 等を含む排ガスを用いて行う場合
は、排ガスの脱硫・脱硝が同時に行われるので、人工土
壌の製造を極めて経済的に行うことができる。ここでは
下記の化学反応が起るものと考えられる。The mechanism of this reaction is considered as follows. That is, the above hydrate is converted into SO 2 , NOx
Since the exhaust gas is desulfurized and denitrified when it is treated with the exhaust gas containing O 2 and O 2 , it can be used as a desulfurization / denitration agent first, and then the hydrate after the treatment can be used as artificial soil. Thus, in the method of the present invention, when the gas treatment is carried out using the exhaust gas containing SO 2 , NOx, O 2, etc., the desulfurization and denitration of the exhaust gas are carried out at the same time, which makes the production of artificial soil extremely economical. It can be carried out. The following chemical reactions are considered to occur here.
【化1】NO+1/2O2 →NO2 NO2 +SO2 →SO3 +NO Ca(OH)2 +SO3 +H2 O→CaSO4 +2H2
O Ca(OH)2 +NO2 +1/2O2 →Ca(NO3 )
2 +2H2 O 但しこれらの反応では水和物の構成物質を便宜的にCa
(OH)2 とした。また、脱硫・脱硝剤として用いた後
の使用済み剤を水和物の製造原料例えば石膏源として使
用する場合は、それ自体に肥料成分となるN分を含有す
るため敢えてSO2 及びNOx処理しなくても人工土壌
として十分適用可能である。[Chemical Formula 1] NO + 1 / 2O 2 → NO 2 NO 2 + SO 2 → SO 3 + NO Ca (OH) 2 + SO 3 + H 2 O → CaSO 4 + 2H 2
O Ca (OH) 2 + NO 2 + 1 / 2O 2 → Ca (NO 3 )
2 + 2H 2 O However, in these reactions, the hydrate constituents are expediently Ca
(OH) 2 . Further, when the used agent after being used as a desulfurizing / denitrifying agent is used as a raw material for producing a hydrate, for example, a gypsum source, it is intentionally treated with SO 2 and NOx because it contains N as a fertilizer component. Even if it is not used, it can be sufficiently applied as artificial soil.
【0013】ここで、人工土壌としての使用形態は、得
られる水和物が硬化物かあるいはスラリ状のものかによ
って粒状または粉状で使われる。硬化性水和処理の場合
は、原料と水を混合・混練りした後、ペレタイザ等で押
し出し成形し蒸気養生することにより任意のサイズに整
粒された粒状物が得られる。一方非固結性水和処理の場
合は、水和物スラリを乾燥することにより粉状の水和物
が得られる。ここで得られた各水和物をSO2 、NOx
及びO2 を含有する排ガスで処理する方法としては、粒
状物については固定床または流動床タイプの反応器に充
填してこれに排ガスを流すことにより達成でき、また粉
状物については排ガスのダクト中に噴霧したのち集塵器
例えばバグフィルタの濾布で補集することにより達成で
きる。本発明の人工土壌は酸性土壌と混合することによ
って土壌のpHを調整し、また比表面積が大きく多孔質
であるため土壌中に空気、水を貯えることが可能であり
保水性及び保肥力の改善を図ることが出来る。更に成分
中にはN,P,K,Ca,Mg,Feなどを含み、これ
らの成分が土壌中に溶出することによって肥料としての
働きも示す。The artificial soil is used in a granular or powdery form depending on whether the hydrate obtained is a hardened product or a slurry-like product. In the case of the curable hydration treatment, the raw material and water are mixed and kneaded, and then extrusion molding is carried out with a pelletizer or the like, and steam curing is performed to obtain granules sized to an arbitrary size. On the other hand, in the case of non-consolidating hydration treatment, a powdery hydrate is obtained by drying the hydrate slurry. Each hydrate obtained here was treated with SO 2 , NOx
And a method of treating with an exhaust gas containing O 2, for the granular material can be achieved by passing the exhaust gas to be charged into the reactor of a fixed bed or a fluidized bed type, also ducts of the exhaust gas for the powdery substance This can be achieved by spraying into the inside and then collecting with a dust collector, for example, a filter cloth of a bag filter. The artificial soil of the present invention adjusts the pH of the soil by mixing it with acidic soil, and since it has a large specific surface area and is porous, it is possible to store air and water in the soil and improve water retention and fertilizing power. Can be planned. Furthermore, the components include N, P, K, Ca, Mg, Fe, etc., and these components also function as fertilizers by being eluted into the soil.
【0014】本発明の好ましい実施態様を以下に要約し
て示す。 (1)石炭灰が平均粒径20〜30ミクロンのフライア
ッシュまたは火炉底に落下するクリンカーアッシュであ
る請求項2に記載の人工土壌の製造方法。 (2)石膏が無水石膏、半水石膏及び二水石膏から選ば
れる少なくとも一つである請求項1または請求項2に記
載の人工土壌の製造方法。 (3)石膏が流動層燃焼灰等の炉内脱硫剤及び使用済み
石灰系排ガス処理剤から選ばれる石膏を含む物質である
上記(2)に記載の人工土壌の製造方法。 (4)水和処理が硬化性水和処理または非固結性水和処
理である請求項1または請求項2に記載の人工土壌の製
造方法。 (5)硬化性水和処理が蒸気養生によるものである上記
(4)に記載の人工土壌の製造方法。 (6)硬化性水和処理を原料と水の混合割合(固液比)
を1:0.2〜1:0.99とに行う上記(4)または
(5)に記載の人工土壌の製造方法。The preferred embodiments of the present invention are summarized below. (1) The method for producing artificial soil according to claim 2, wherein the coal ash is fly ash having an average particle size of 20 to 30 μm or clinker ash that drops to the bottom of the furnace. (2) The method for producing artificial soil according to claim 1 or 2, wherein the gypsum is at least one selected from anhydrous gypsum, hemihydrate gypsum, and gypsum dihydrate. (3) The method for producing artificial soil according to (2) above, wherein the gypsum is a substance containing gypsum selected from in-furnace desulfurization agents such as fluidized bed combustion ash and used lime-based exhaust gas treatment agents. (4) The method for producing artificial soil according to claim 1 or 2, wherein the hydration treatment is a hardening hydration treatment or a non-consolidating hydration treatment. (5) The method for producing artificial soil as described in (4) above, wherein the hardening hydration treatment is by steam curing. (6) Curable hydration treatment mixed ratio of raw material and water (solid-liquid ratio)
The method for producing an artificial soil as described in (4) or (5) above, wherein the ratio is 1: 0.2 to 1: 0.99.
【0015】(7)蒸気養生を温度60〜180℃、相
対湿度100%の飽和水分下で数分〜数日間行う上記
(5)に記載の人工土壌の製造方法。 (8)非固結性水和処理が熱水養生によるものである上
記(4)に記載の人工土壌の製造方法。 (9) 非固結性水和処理を固液比が1:1〜1:20
の範囲となるように行う上記(4)または(8)に記載
の人工土壌の製造方法。 (10)熱水養生を60〜180℃の温度で水中に原料を
分散し原料が下部に沈降、硬化しないように攪拌しなが
ら数分〜十数時間処理することにより行う上記(8)に
記載の人工土壌の製造方法。 (11)SO2 、NOx及びO2 を含むガスによる処理は
SO2 、NOxをそれぞれ100ppm〜1vol%含
み、O2 を5〜21vol%含む温度80〜200℃の
ガスでSVが5〜50000h-1で水和物の乾燥重量1
kg当たりSO2及びNOxが少なくとも1モル接触す
るのに十分な時間処理することにより行う請求項2また
は上記(1)〜(10)の何れかに記載の人工土壌の製造
方法。(7) The method for producing an artificial soil as described in (5) above, wherein steam curing is carried out at a temperature of 60 to 180 ° C. and a saturated water content of 100% relative humidity for several minutes to several days. (8) The method for producing an artificial soil as described in (4) above, wherein the non-consolidating hydration treatment is by hot water curing. (9) The non-consolidating hydration treatment was performed at a solid-liquid ratio of 1: 1 to 1:20
The method for producing an artificial soil as described in (4) or (8) above, which is performed so as to fall within the range. (10) The method according to (8) above, wherein hot water curing is performed by dispersing the raw material in water at a temperature of 60 to 180 ° C. and treating it for several minutes to several tens of hours while stirring so that the raw material does not settle and harden in the lower part. Method for producing artificial soil. (11) The treatment with a gas containing SO 2 , NOx and O 2 includes SO 2 and NOx in an amount of 100 ppm to 1 vol% and O 2 in an amount of 5 to 21 vol% at a temperature of 80 to 200 ° C. and an SV of 5 to 50000 h −. 1 in 1 dry weight of hydrate
The method for producing an artificial soil according to claim 2 or any one of (1) to (10) above, which is carried out by treating for a time sufficient to bring at least 1 mol of SO 2 and NOx per kg.
【0016】[0016]
【実施例】以下実施例により本発明を更に詳細に説明す
るが、これに限定されるものではない。文中の部及び%
は重量基準である。 (実施例1)組成がSiO2 :60%、Al2 O3 :2
3%、CaO:4.3%、Fe2 O 3 :5.5%、Mg
O:2.4%、Na2 O:0.7%、K2 O:1.3
%、TiO2 :1.2%、S:0.2%、C:1.2%
で平均粒径が23ミクロンの石炭灰60部に消石灰30
部及び半水石膏10部(CaSO4 換算)を混合し、水
40部を加えて混練りした。次に5mmの孔径のダイス
で押し出し成形し常圧95℃の水蒸気中で12時間養生
を行った後、200℃で2時間乾燥し、水和硬化物を得
た。次にこの硬化物をSO2 1000ppm、NOx2
00ppm、CO 2 13vol%、O2 6vol%、H
2 O8vol%(残りはN2 )のガスでSV1000h
-1、130℃で100時間処理し表2に示す組成及び物
性を有する人工土壌を得た。この中で施肥成分として注
目した全Nの含有濃度は2.5%であった。The present invention will be described in more detail with reference to the following examples.
However, the present invention is not limited to this. Department in text and%
Is based on weight. (Example 1) Composition is SiO2: 60%, Al2O3: 2
3%, CaO: 4.3%, Fe2O 3: 5.5%, Mg
O: 2.4%, Na2O: 0.7%, K2O: 1.3
%, TiO2: 1.2%, S: 0.2%, C: 1.2%
And slaked lime 30 in 60 parts of coal ash with an average particle size of 23 microns
Parts and hemihydrate gypsum 10 parts (CaSOFour(Converted) mixed, water
40 parts were added and kneaded. Next, a die with a hole diameter of 5 mm
Extruded and cured in steam at 95 ° C for 12 hours
And dried at 200 ° C. for 2 hours to obtain a hydrated cured product.
Was. Next, this cured product is21000ppm, NOx2
00ppm, CO 213vol%, O26vol%, H
2O8vol% (the rest is N2) Gas SV1000h
-1And composition shown in Table 2 after treatment at 130 ° C for 100 hours
The artificial soil having the property was obtained. In this, apply as fertilizer component
The content concentration of the total N observed was 2.5%.
【0017】この人工土壌を用いて、ほうれんそうの栽
培を行った。市販の畑の土とバーミキュライトを1:1
で混合したもの、市販の畑の土と本発明の人工土壌を
1:1及び3:1で混合したものを土壌として鉢植えし
ビニールハウスの中で約2カ月間栽培した。その結果を
表3に示す。何れの場合も追肥を与えなかった。Spinach was cultivated using this artificial soil. Commercial field soil and vermiculite 1: 1
The mixture of 1) and the mixture of the commercially available field soil and the artificial soil of the present invention in a ratio of 1: 1 and 3: 1 were potted as soil and cultivated in a greenhouse for about 2 months. Table 3 shows the results. No topdressing was given in any case.
【0018】[0018]
【表2】 [Table 2]
【0019】[0019]
【表3】 表3に示されるように、本発明の人工土壌を土壌に混合
することによって肥料を与えなくても適正に栽培出来る
ことがわかる。[Table 3] As shown in Table 3, it can be seen that by mixing the artificial soil of the present invention with the soil, proper cultivation can be performed without applying fertilizer.
【0020】(実施例2)原料及び水を実施例1で使用
した石炭灰20部、消石灰20部及び使用済み石灰系排
ガス処理剤(組成がSiO2 :25%、AlO3 :9.
6%、CaO:26%、Fe2 O3 :2.4%、Mg
O:0.8%、Na2 O:0.2%、K2 O:0.6
%、S:11.2%、C:1.0%、T−N:1.9
%)60部及び水45部に変えた以外は実施例1と同様
に処理して人工土壌Aを得た。このものの全N分を分析
した結果、2.3%であった。また含水率は33%であ
った。(Example 2) 20 parts of coal ash and 20 parts of slaked lime used as the raw material and water in Example 1 and a used lime type exhaust gas treating agent (composition: SiO 2 : 25%, AlO 3 : 9.
6%, CaO: 26%, Fe 2 O 3: 2.4%, Mg
O: 0.8%, Na 2 O: 0.2%, K 2 O: 0.6
%, S: 11.2%, C: 1.0%, TN: 1.9.
%) The artificial soil A was obtained by the same treatment as in Example 1 except that 60 parts and 45 parts of water were used. As a result of analyzing the total N content of this product, it was 2.3%. The water content was 33%.
【0021】(実施例3)生石灰30部を75℃の熱水
500部中に投入し攪拌しながら20分後に実施例1で
使用した石炭灰50部及び二水石膏20部(CaSO4
換算)を加え温度95℃に保って12時間養生し、脱水
後150℃で2時間乾燥して粉状の水和物を得た。この
粉体を、バグフィルタを備えた反応器中に吹き込みSO
2 2000ppm、NOx600ppm、CO2 13v
ol%、O2 10vol%、H2 O10vol%、(残
りはN2 )の組成、温度100℃のガスと接触させ(バ
グフィルタ層でのSVは20000h-1)粉状の人工土
壌Bを得た。このものの全Nを分析した結果、1.2%
であった。(Example 3) 30 parts of quicklime was added to 500 parts of hot water at 75 ° C., and after stirring for 20 minutes, 50 parts of coal ash used in Example 1 and 20 parts of gypsum dihydrate (CaSO 4
(Calculated) was added and the mixture was kept at a temperature of 95 ° C. for 12 hours, dehydrated and dried at 150 ° C. for 2 hours to obtain a powdery hydrate. Blowing this powder into a reactor equipped with a bag filter, SO
2 2000ppm, NOx 600ppm, CO 2 13v
ol%, O 2 10 vol%, H 2 O 10 vol%, (remainder is N 2 ) and contact with a gas at a temperature of 100 ° C. (SV in the bag filter layer is 20000 h −1 ) to obtain a powdery artificial soil B. It was As a result of analyzing the total N of this product, 1.2%
Met.
【0022】(実施例4)実施例2において得られたス
ラリの一部を脱水後150℃で乾燥して水分を25%と
しディスクペレッターで押し出し成形した後、再度15
0℃で2時間乾燥してペレット状の硬化物を得た。この
硬化物を実施例1のガス組成で温度を100℃、SVを
500h-1と変えた以外は実施例1と同様の条件でガス
処理し人工土壌Cを得た。このものの全N濃度は3%で
あった。(Example 4) A part of the slurry obtained in Example 2 was dehydrated and then dried at 150 ° C to adjust the water content to 25%, and extrusion molding was carried out by a disc pelleter.
It was dried at 0 ° C. for 2 hours to obtain a pellet-shaped cured product. This cured product was gas-treated under the same conditions as in Example 1 except that the temperature was 100 ° C. and the SV was changed to 500 h −1 with the gas composition of Example 1 to obtain artificial soil C. The total N concentration of this product was 3%.
【0023】(実施例5)ボイラ火炉底から採取したク
リンカーアッシュ(粒径1.0mm以下、組成Si
O2 :63%、Al2 O3 :18%、CaO:5.6
%、MgO:3.5%、Fe2 O3 :6.2%、Na2
O:0.3%、K2 O:0.6%、S:0.4%、C:
0.6%)60部に消石灰20部と無水石膏20部を混
合し水40部を加えて混練りした。この混練り物を5m
mの孔径のダイスで押し出し成形した後、オートクレー
ブに入れて、150℃の水蒸気中で12時間養生した。
次にこの成形物を200℃で乾燥し実施例1と同様の方
法でガス処理し人工土壌Dを得た。このものの全N濃度
は0.3%であった。(Embodiment 5) Clinker ash (particle size 1.0 mm or less, composition Si
O 2 : 63%, Al 2 O 3 : 18%, CaO: 5.6
%, MgO: 3.5%, Fe 2 O 3 : 6.2%, Na 2
O: 0.3%, K 2 O: 0.6%, S: 0.4%, C:
(0.6%) 60 parts were mixed with 20 parts of slaked lime and 20 parts of anhydrous gypsum and 40 parts of water was added and kneaded. This kneaded product is 5m
After extrusion molding with a die having a pore size of m, it was placed in an autoclave and cured in steam at 150 ° C. for 12 hours.
Next, this molded product was dried at 200 ° C. and gas-treated in the same manner as in Example 1 to obtain artificial soil D. The total N concentration of this product was 0.3%.
【0024】(実施例6)実施例1で用いた石炭灰20
部に消石灰10部及び流動層炉内脱硫使用済み剤70部
(組成がSiO2 :15%、Al2 O3 :5.2%、F
e2 O3 :4.6%、CaO:22%、MgO:2.3
%、Na2 O:0.5%、K2 O:0.6%、S:3.
1%、C:2.1%)、水50部を加え、実施例1と同
様の方法で処理して人工土壌Eを得た。このものの全N
濃度は1.2%であった。Example 6 Coal ash 20 used in Example 1
10 parts of slaked lime and 70 parts of spent desulfurization agent in fluidized bed furnace (composition: SiO 2 : 15%, Al 2 O 3 : 5.2%, F
e 2 O 3 : 4.6%, CaO: 22%, MgO: 2.3
%, Na 2 O: 0.5%, K 2 O: 0.6%, S: 3.
1%, C: 2.1%), and 50 parts of water were added and treated in the same manner as in Example 1 to obtain artificial soil E. All N of this thing
The concentration was 1.2%.
【0025】(参考例)実施例2〜6で得られた人工土
壌A〜Eを用い、各々を畑の土と1:1に混合した土壌
で実施例1と同様に、ほうれんそうの栽培を行った。結
果を表4に示す。(Reference Example) Spinach cultivation was carried out in the same manner as in Example 1 except that the artificial soils A to E obtained in Examples 2 to 6 were mixed with the soil of the field in a ratio of 1: 1. It was The results are shown in Table 4.
【表4】 (土壌の混合比は1:1)[Table 4] (Soil mixing ratio is 1: 1)
【0026】(実施例7)実施例2で得た人工土壌Aを
畑の土に対して10wt%添加し男爵イモ、二十日大根
による栽培試験を行った。結果を表5に示す。(Example 7) The artificial soil A obtained in Example 2 was added to the field soil in an amount of 10% by weight, and a cultivation test was carried out using baron potatoes and radish radish. The results are shown in Table 5.
【0027】(比較例1)土壌改良剤効果の比較例とし
て、堆肥を土に対して10wt%として、実施例7と同
様の栽培試験を行った。比較例1の栽培試験結果を表5
に示す。(Comparative Example 1) As a comparative example of the effect of the soil improver, the same cultivation test as in Example 7 was conducted using 10% by weight of compost as soil. Table 5 shows the cultivation test results of Comparative Example 1.
Shown in
【0028】(比較例2)土壌改良剤効果の比較例とし
て、無肥料の土についても実施例7と同様の栽培試験を
行った。比較例2の栽培試験結果を表5に示す。(Comparative Example 2) As a comparative example of the effect of the soil improver, the same cultivation test as in Example 7 was carried out on fertilizer-free soil. Table 5 shows the results of the cultivation test of Comparative Example 2.
【0029】[0029]
【表5】 [Table 5]
【0030】[0030]
【発明の効果】以上述べたように本発明の人工土壌は比
較的安価な原料または従来廃棄物と考えられていたもの
を利用して容易に製造され、植物栽培時における土壌の
pH、保水性保肥力の改善を行うことができ、それ自体
が肥料としての役割を果たすため、本発明の工業的価値
は非常に大きい。Industrial Applicability As described above, the artificial soil of the present invention is easily produced by using relatively inexpensive raw materials or what was conventionally considered as waste, and the soil pH and water retention at the time of plant cultivation are maintained. The industrial value of the present invention is very great because it can improve the fertilizing ability and can itself serve as a fertilizer.
───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 庁内整理番号 FI 技術表示箇所 B01D 53/74 B01J 20/04 C (72)発明者 森 邦広 北海道札幌市豊平区美しが丘4条9丁目2 番1号北海道電力株式会社総合研究所内 (72)発明者 上野 務 北海道札幌市豊平区美しが丘4条9丁目2 番1号北海道電力株式会社総合研究所内 (72)発明者 斎藤 和敏 北海道札幌市厚別区下野幌テクノパーク1 丁目2番14号 株式会社エコニクス内 (72)発明者 中館 史行 北海道札幌市厚別区下野幌テクノパーク1 丁目2番14号 株式会社エコニクス内 (72)発明者 多谷 淳 東京都千代田区丸の内二丁目5番1号 三 菱重工業株式会社内 (72)発明者 藤田 浩 広島県広島市西区観音新町四丁目6番22号 三菱重工業株式会社広島研究所内 (72)発明者 小串 泰之 広島県広島市西区観音新町四丁目6番22号 三菱重工業株式会社広島研究所内 (72)発明者 木下 達之 広島県広島市西区観音新町四丁目6番22号 三菱重工業株式会社広島研究所内─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 6 Identification number Reference number within the agency FI Technical indication location B01D 53/74 B01J 20/04 C (72) Inventor Kunihiro Mori 4 Mihogaoka, Toyohira-ku, Sapporo, Hokkaido 4-9 2-2-1 Hokkaido Electric Power Co., Inc. Research Center (72) Inventor Tsutomu Ueno 4-9-1, Migamioka, Toyohira-ku, Sapporo-shi, Hokkaido Hokkaido Electric Power Co. Research Center (72) Inventor Kazutoshi Saito Hokkaido Sapporo 1-14 Shimonoboro Techno Park, Atsubetsu-ku, Yokohama-shi Econics Co., Ltd. (72) Inventor, Fumiyuki Nakadate 1-2-14 Shimotono-Poro Techno Park, Atsubetsu-ku, Sapporo-shi, Hokkaido (72) Inventor Atsushi Taya, Chiyoda, Tokyo 2-5-1 Marunouchi Ward Sanryo Heavy Industries Co., Ltd. (72) Inventor Hiroshi Fujita Hiroshima Hiroshima 4-6-22 Kannon-Shinmachi, Nishi-ku, Hiroshima Research Institute, Mitsubishi Heavy Industries, Ltd. (72) Inventor, Yasuyuki Kogushi, 4-6-22, Kannon-Shinmachi, Nishi-ku, Hiroshima, Hiroshima (72) Inventor, Tatsu Kinoshita 4-6-22 Kannon-shinmachi, Nishi-ku, Hiroshima-shi, Hiroshima Prefecture Mitsubishi Heavy Industries Ltd. Hiroshima Research Institute
Claims (2)
石灰系排ガス処理剤に消石灰・生石灰及び石膏から選ば
れた少なくとも一つを混合し、水和処理することを特徴
とする人工土壌の製造方法。1. An artificial soil characterized by mixing at least one selected from slaked lime / quick lime and gypsum with a used lime-based exhaust gas treating agent after being used as a desulfurizing / denitrifying agent and hydrating the mixture. Production method.
から選ばれた少なくとも一つに消石灰・生石灰及び石膏
から選ばれた少なくとも一つを混合し、水和処理した後
SO2 、NOx及びO2 を含有するガスで処理すること
を特徴とする人工土壌の製造方法。2. At least one selected from coal ash and a used lime-based exhaust gas treating agent is mixed with at least one selected from slaked lime / quick lime and gypsum, and after hydration treatment, SO 2 , NOx and O are mixed. A method for producing an artificial soil, which comprises treating with a gas containing 2 .
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP7013948A JPH08205672A (en) | 1995-01-31 | 1995-01-31 | Production of artificial soil |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP7013948A JPH08205672A (en) | 1995-01-31 | 1995-01-31 | Production of artificial soil |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH08205672A true JPH08205672A (en) | 1996-08-13 |
Family
ID=11847437
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP7013948A Withdrawn JPH08205672A (en) | 1995-01-31 | 1995-01-31 | Production of artificial soil |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH08205672A (en) |
-
1995
- 1995-01-31 JP JP7013948A patent/JPH08205672A/en not_active Withdrawn
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN102000481B (en) | Method for treating desulfurization ash | |
CA1258059A (en) | Preparation process of desulfurizing and denitrating agents | |
JP2776895B2 (en) | Bonding agent manufacturing method, as well as underground building materials, building component raw materials, mortar and concrete bonding agent components or rapid setting components | |
Garea et al. | Fly-ash/calcium hydroxide mixtures for SO2 removal: structural properties and maximum yield | |
US5560894A (en) | Process for treatment of exhaust gas | |
KR20140092699A (en) | Sludge solidified agent and menufacturing method of artificial soil usign the same | |
JP2002241183A (en) | Porous ceramic particle and its production process | |
JPH0975747A (en) | Method for caking photocatalyst | |
JPH08205672A (en) | Production of artificial soil | |
JP3717969B2 (en) | Fertilizer manufacturing method | |
GB2171685A (en) | Steam power station clarification sludge used for wet desulphurisation of waste gases | |
Houte et al. | Desulfurization of flue gases in a fluidized bed of modified limestone | |
US5403808A (en) | Sorbents for flue gas desulfurization | |
JP2753194B2 (en) | Ground improvement material and ground improvement method | |
JPH08182999A (en) | Treatment of sewerage sludge and sewerage sludge-treated material | |
JPH06198127A (en) | Waste gas treating device | |
JPH0669477B2 (en) | Deodorant | |
JP2547260B2 (en) | Exhaust gas treatment method | |
EP0181088A1 (en) | A process for the manufacture of a quick setting high strength hardening composition | |
AU753464B2 (en) | Method for making manufactured aggregates from coal combustion by-products | |
JP2952227B2 (en) | Method for producing exhaust gas treatment agent | |
JP2547901B2 (en) | Mud treatment agent and treatment method | |
SU709139A1 (en) | Absorber for purifying gases from sulfur oxides | |
JPH07102320B2 (en) | Exhaust gas treatment agent manufacturing method and exhaust gas treatment method | |
SU1664774A1 (en) | Method of producing granulated lime fertilizers |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
A300 | Withdrawal of application because of no request for examination |
Free format text: JAPANESE INTERMEDIATE CODE: A300 Effective date: 20020402 |