JPS5830381A - Treatment for incineration ash of sewage sludge - Google Patents

Treatment for incineration ash of sewage sludge

Info

Publication number
JPS5830381A
JPS5830381A JP56127771A JP12777181A JPS5830381A JP S5830381 A JPS5830381 A JP S5830381A JP 56127771 A JP56127771 A JP 56127771A JP 12777181 A JP12777181 A JP 12777181A JP S5830381 A JPS5830381 A JP S5830381A
Authority
JP
Japan
Prior art keywords
sewage sludge
incineration ash
ashes
waste liquid
ash
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
Application number
JP56127771A
Other languages
Japanese (ja)
Other versions
JPS6114100B2 (en
Inventor
Kazuo Okada
和男 岡田
Akitoshi Yamada
山田 昭捷
Hiroyasu Otsuka
大塚 博保
Morimasa Takesue
武末 守正
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Nittetsu Mining Co Ltd
Original Assignee
Nittetsu Mining Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Nittetsu Mining Co Ltd filed Critical Nittetsu Mining Co Ltd
Priority to JP56127771A priority Critical patent/JPS5830381A/en
Publication of JPS5830381A publication Critical patent/JPS5830381A/en
Publication of JPS6114100B2 publication Critical patent/JPS6114100B2/ja
Granted legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00Technologies for solid waste management
    • Y02W30/50Reuse, recycling or recovery technologies
    • Y02W30/91Use of waste materials as fillers for mortars or concrete

Landscapes

  • Gasification And Melting Of Waste (AREA)
  • Processing Of Solid Wastes (AREA)
  • Treatment Of Sludge (AREA)

Abstract

PURPOSE:To obtain aggregate of high strength by adding waste org. liq. to the incineration ashes of sewage sludge and granulating the ashes then calcining the granules. CONSTITUTION:In a method of adding waste org. liq. to the incineration ashes of sewage sludge and granulating and calcining said ashes, the waste org. liq. is added to said incineration ashes so as to adjust the content of the dry solid to 4-12wt%. After the ashes are granulated, the granules are calcined. A rotary kiln or the like is used for granulation and granules having 0.5-15mm. grain sizes are obtained.

Description

【発明の詳細な説明】 本発明は下水汚泥焼却灰の処理方法に関するものであっ
て、下水汚泥焼却灰を造粒後焼成して軽1(廻0で強1
丁シニの犬なる骨材を造るととを目的どする。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for treating sewage sludge incineration ash, in which the sewage sludge incineration ash is granulated and then fired to obtain
The purpose is to make dog aggregates.

下水処:f!IIJJ%から犬1廿に発生する下水汚泥
焼却灰i17.t、 、現在その一部がコンポストとじ
て有効利用されているが、大部分は海岸や陸上で埋立処
分されている。
Sewerage: f! Sewage sludge incineration ash generated per dog from IIJJ% i17. Currently, some of it is effectively used as compost, but most of it is disposed of in landfills on the coast or on land.

しかしこの処理方法も立地上の制限があって埋立処分は
次第に困難になりつ5ある。このため、下水汚泥4:N
(ζ却灰の有効利用法の開発が強く望まれている。
However, this treatment method also has location limitations, and landfill disposal is becoming increasingly difficult5. For this reason, sewage sludge 4:N
(There is a strong desire to develop a method for effectively using ash.

1一 本発明はこの四重に応じるために下水71i泥・j尭却
灰を造粒後・j!″1を成して軽晴−でi、iji 1
1(k:の犬なる骨利を造らんとして4111々研究を
行った。
11 In order to meet this quadruple requirement, the present invention uses sewage 71i mud, j, and ash after granulation. ``It's light and sunny with 1, i, iji 1
1 (k:) We conducted 4111 studies in an attempt to create a dog-like benefit.

その結果によると、下水7θθ:’+ ’I”’l’i
却灰に有機]l’rJm液を添加して造粒すると有(穴
T」廃液中の固形分がtl−′[定1γ]Σ囲のとき含
水量が少なく、強度の大々る造粒物がイ11られること
、およびjす1く17て111られ/也造粒物を焼1成
すれば比較的低い幀、成温庶でJt ’il↑の小さく
強IWの犬なる+l:d□);結粒状物/バi!−IC
〕れることを知姑した。
According to the results, sewage 7θθ:'+ 'I''l'i
It is possible to granulate by adding organic] l'rJm liquid to the waste ash (hole T). If the material is heated, and if the granulated material is fired, it will have a relatively low temperature and a small strong IW of Jt'il↑ at the temperature. □); Nodules/Bai! -IC
] I knew it would happen.

次に実験した結果について説明する、 実1険に1tit用しノζ+lす%却灰の相数けllj
 ’N−%で表わして2131表の如〜イ、のであね、
斗だ使用し/ζ;イ1’ #・;燦1条液であるアルコ
ール廃液の物r l/I:Itニー1第2表の如きもの
である。
Next, I will explain the results of the experiment.
' Expressed as N-%, it is as shown in the 2131 table.
It is an alcoholic waste liquid that is used as a liquid, as shown in Table 2.

第2表 焼却灰にアルコール廃液を種々の割合に添加して造粒し
、造粒物の含水率および圧潰強度とアルコール層液添加
量との関係を求め、第1図の結果をイiすだ。ここに圧
潰強度とは造粒物の強度測定法の一神で測定した強度で
あって、−粒の造粒物を板上に匿き、その試料の上に板
をのせ、その上から加重をかけてどの程度の加重で破壊
するかを試)倹する方法である。
Table 2 Alcohol waste liquid was added to the incineration ash in various proportions and granulated, and the relationship between the moisture content and crushing strength of the granulated material and the amount of alcohol layer liquid added was determined, and the results shown in Figure 1 were compared. is. Here, the crushing strength is the strength measured using one of the methods for measuring the strength of granules. This is a method of saving money (testing the amount of force required to destroy the object).

第1図において、■は圧潰強度とアルコール廃液添加量
との関係を、2は水分含有量とアルコール廃液添加1肩
との1ツ4係を示す。次に第2図において1,2および
3はそれぞれ得られる焼成物の比重が1.、O,]、、
2および1.4の場合を示す。
In FIG. 1, ■ indicates the relationship between the crushing strength and the amount of alcohol waste liquid added, and 2 indicates the relationship between the water content and the amount of alcohol waste liquid added. Next, in FIG. 2, 1, 2, and 3 indicate the specific gravity of the fired product obtained, respectively. ,O,],,
2 and 1.4 are shown.

以上は有機質廃液としてアルコール廃液を使用した場合
であるが、パルプ廃液、例えば第3表に示すような性状
のSP法による蒸解廃液第3表 を使用し7た場合でも同じ、1こうな結果が111られ
/−6第1図および第2図から下水f’i泥も1.1.
却灰に対し有機質廃液を、その乾燥固形分が/1〜12
 i’1ij7j: 9Kになるように添加し、造わt
すればa水率が少々く、圧潰強度の犬なる造粒物が・r
;LらJ′へ この造粒物を焼成すれば、・+rli 
rJ、Cの犬々る・(バー結4′)ン状物がf(jられ
ることが詔められる。
The above is a case where alcohol waste liquid is used as the organic waste liquid, but the same result can be obtained even if pulp waste liquid, for example cooking waste liquid from the SP method with the properties shown in Table 3, is used. 111/-6 From Figures 1 and 2, sewage f'i mud is also 1.1.
Organic waste liquid is added to the ash, and its dry solid content is /1 to 12.
i'1ij7j: Added to make 9K.
Then, a granulated material with a slightly lower water content and a higher crushing strength will be obtained.
;L to J' If this granulated material is fired, ・+rli
It is admonished that rJ, C's (bar knot 4')-like thing is f(j).

次に上記方法で造ったt+j);枯枝4u物、市11%
、の人T軽坦骨材および川砂にポルトランドセメント合
し、モルタル試.1・台を行った結果を第4表に示す。
Next, t+j) made using the above method: 4 u of dead branches, 11% city
Mix portland cement with light aggregate and river sand, and test mortar. Table 4 shows the results of 1 test.

不発l町はこれらの知見に基くものであって、下水汚泥
焼却灰に対して有4’+lt ノlfロ発液を、その乾
燥固形物が4〜−、1.2−if−!Hi′腎に庁る3
1:うに添加し2、含水率を調整して造粒した後、焼成
するととを714.7徴表する下水汚泥焼却灰の処理方
法である。
The unexploded city is based on these findings, and the dry solid matter is 4'+lt, 1.2-if-! Hi'kidney 3
1: This is a method for treating sewage sludge incineration ash, in which sea urchin is added, 2, the water content is adjusted, granulation is performed, and then the ash is calcined.

本発明において、下水から汚泥を凝集し、沈澱゛させて
脱水せしめるエイ′1:で消石灰を添力[7する場合は
汚泥中に1f7化ノノルシウl、の含有1j−1−が多
く4−リ、造粒′吻を高?!Mで、焼成する際融i’4
 1−、易くなる/こめ、汚泥中の酸化ノノルシウノ、
−+A1ri ]、り 9( Jゾ、下のものを(jJ
i。
In the present invention, sludge from sewage is coagulated, precipitated, and dehydrated by adding slaked lime to the sludge. , granulation'proboscis high? ! M, melting i'4 during firing
1-, it becomes easier / oxidation of rice and sludge,
-+A1ri], ri 9(Jzo, the one below (jJ
i.

川することが9寸しい。It's 9 inches long to go to the river.

造fI′2物の,lI+,、放湯D′1゛は焼成物の比
重,有+]し質廃液の添加4.′11合,炉内):辺囲
気,J風1+V時間によりj,lij庁るが、大体10
00〜12000Cの間である。
lI+, of the manufactured fI'2 product, D'1' is the specific gravity of the fired product, +] Addition of waste liquid 4. '11, in the furnace): The surrounding air, J wind 1 + V time varies depending on the time, but approximately 10
It is between 00 and 12000C.

場合ではバインダーとしての効−唄が弱くなり、造粒物
の強度が十分でなく、寸だ12重量螢以上では焼成物の
比重が犬になり、かつ所望の比重のものを得ようとすれ
ば、比較的高いn,、! (95で焼jib lる必・
皮がある。
In some cases, the effect as a binder becomes weak, the strength of the granulated product is insufficient, and if the specific gravity of the fired product exceeds 12%, and if you try to obtain the desired specific gravity, , relatively high n,,! (I have to burn it at 95.
It has skin.

有機ノシ℃廃液としてはエチルアルコール製造の際、副
生ずるアルコール廃液、木材をSP法などにより蒸解す
る際副生するパルプ廃液外どが使用される。
As the organic porcelain waste liquid, alcohol waste liquid produced as a by-product during the production of ethyl alcohol, and pulp waste liquid produced as a by-product when wood is digested by the SP method, etc. are used.

本発明においては、通常の皿形造粒機などを用いて43
’l却灰と有機質廃液との混合物を造粒し、直杆05〜
15脆皆度の大きさの造粒物を造る。
In the present invention, using a normal dish-shaped granulator or the like,
'l The mixture of incinerated ash and organic waste liquid is granulated and directly
A granulated material having a size of 15 brittleness is made.

そして造粒物の水分が20〜25πになるように含水率
を調整して造粒することが9寸しい。またこの:<’j
 %R7’I勿をす(z成するにC1°、ロータリーキ
ルンなどを使j11シて行なうことも出来るが、本発明
でd:有機′?jlをバインダーとして・lt+・用し
ているため、加熱過イ“1″て造粒物の粉化が起り易く
、また下水汚泥焼却灰に1融着し易い組成で構成されて
いるため、特)ff4昭55−75522号、特願昭5
5−103166号の気流焼成方法および炉を用いれば
造粒物を投入初期に急速に加熱することができるので、
造粒物の表面は直ちに焼結せしめられ、粉化が少々く、
造粒物相互は、融着することなく、比重の軽い焼成物を
コ告ることかできる。
It is recommended that the moisture content of the granulated product be adjusted to be 20 to 25π during granulation. Also this:<'j
%R7'I needless to say (z can also be done using C1°, rotary kiln, etc., but in the present invention, since d:organic'?jl is used as a binder, heating is not necessary. Because it is composed of a composition that easily causes pulverization of the granulated material and easily fuses with sewage sludge incineration ash, it is particularly suitable for
By using the airflow firing method and furnace of No. 5-103166, the granules can be rapidly heated at the initial stage of charging.
The surface of the granules is immediately sintered, and there is little pulverization.
The granules do not fuse to each other, making it possible to produce a fired product with a light specific gravity.

本発明によれば、造粒′吻の含水−111が少なく、強
度の大きな造粒物がイ(イらJするので、乾す、ヤシの
際、熱量を低減せしめることができるばかりでなく、造
粒物の粉化、破壊を防止することができる。寸だ比較的
低い焼成温度で比重が小さく、強IJムーの大きな焼成
物を造ることができるので、市[]1シの人工:lj’
Y量骨材と同居或はそれ以上の品質のものがq:t、 
c−、れ、その工業的価値は大である。
According to the present invention, since the water content of the granulation proboscis is small and the granulated material has high strength, it is possible to not only reduce the amount of heat during drying and processing, but also to It is possible to prevent the pulverization and destruction of grains.It is possible to make fired products with low specific gravity and large strong IJ mu at a relatively low firing temperature.
The quality of the same or higher than Y amount aggregate is q:t,
c-, its industrial value is great.

実施例 下水処理場から初出する下水ill泥のi:t’、ξ却
灰(その組成は第1表と同じ)を200メツシュ通過9
0 %に粉砕し、その劫7却灰粉砕I吻] 00 IT
l閏雪’r’I iにン、1(7、第2表に示すアルコ
ール廃液を20叩171°部添加混合しさらに水を20
重用部添加して含水惜を調整j7、皿型造粒(伜により
0.3〜3.5胡の造粒物を作った後乾燥した。次にコ
ノ造粒物〕を% #;!ri lln 55−7552
2号竪摺り炉による気流焼成法に」:り耐高温度105
0℃で焼成した。
Example: Sewage ill mud initially discharged from a sewage treatment plant i:t', ξ ash (its composition is the same as in Table 1) was passed through 200 meshes9
0% and its kalpa 7 ash crushing] 00 IT
1 (7) Add 20 parts of the alcohol waste shown in Table 2 and mix with 171 parts, and then add 20 parts of water.
Adjust the moisture content by adding a heavy part, and add the dish-shaped granulation (a granulation of 0.3 to 3.5% depending on the size and drying. Next, the granulation) to % #;!ri lln 55-7552
For air flow firing method using No. 2 vertical furnace: High temperature resistance 105
It was fired at 0°C.

とのようにして(4%だ焼成′1勿の粒げVをハ周°1
1にした結果、第4表に示すような比重の軽い高強度の
人工illl骨量が得られた。丼たこの焼成物を用いて
モルタル強度を測定したところ川砂を骨材として場合と
同等の強if(を示した。
(4% firing'1)
1, an artificial illumination bone mass with low specific gravity and high strength as shown in Table 4 was obtained. When the mortar strength was measured using the baked product of the rice bowl octopus, it showed the same strength as when using river sand as the aggregate.

なおこの実施例において造粒の際に第3表に示す如きパ
ルプ廃液を用いても上記と同様の結果がイ(1られた。
In this example, even if the pulp waste liquid shown in Table 3 was used during granulation, the same results as above were obtained.

4、■1面の曲中′h、説明 第1図および第21!XIは本発明の実験語用を示すも
のであって、第1図は下水汚泥シa’、q ]211灰
の造粒物におけるアルコール廃液の添加11:と造粒物
の圧油強度並びに造粒物の水分含)Yl:との関係を示
すものであり、図中1は圧α1強度とアル:ノール廃添
加量惜の関件、2は水分含有+11とアルコール廃液添
加量の関係を示し、第21ツICLアルコール廃液添加
量゛とI焼成温度の関係を示すものである。第2図中1
゜2、および3はそれぞれ焼成物の比重1.0.]、、
2および1.4を示す。
4.■ Song 'h' on side 1, explanation Figure 1 and Figure 21! XI shows the experimental terminology of the present invention, and Figure 1 shows the addition of alcohol waste liquid to the granulated product of sewage sludge shea', q]211 ash, the pressure oil strength of the granulated product, and the In the figure, 1 shows the relationship between the pressure α1 intensity and the amount of alcohol waste added, and 2 shows the relationship between the water content +11 and the amount of alcohol waste added. , 21 shows the relationship between the amount of ICL alcohol waste added and the firing temperature. 1 in Figure 2
゜2 and 3 are the specific gravity of the fired product, respectively, 1.0. ],,
2 and 1.4 are shown.

Claims (1)

【特許請求の範囲】[Claims] 下水汚泥焼却灰に対して、有機質廃液を、その乾燥1・
1.1形分が4〜12重邦:%に々るように添加し、含
水率を調+1白して造粒した後、焼成するととを特徴と
する下水汚泥焼却灰の処理方法。
For sewage sludge incineration ash, organic waste liquid is dried 1.
1. A method for treating sewage sludge incineration ash, which comprises adding 4 to 12% of sewage sludge incineration ash, adjusting the moisture content by +1, granulating it, and then firing it.
JP56127771A 1981-08-17 1981-08-17 Treatment for incineration ash of sewage sludge Granted JPS5830381A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP56127771A JPS5830381A (en) 1981-08-17 1981-08-17 Treatment for incineration ash of sewage sludge

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP56127771A JPS5830381A (en) 1981-08-17 1981-08-17 Treatment for incineration ash of sewage sludge

Publications (2)

Publication Number Publication Date
JPS5830381A true JPS5830381A (en) 1983-02-22
JPS6114100B2 JPS6114100B2 (en) 1986-04-17

Family

ID=14968282

Family Applications (1)

Application Number Title Priority Date Filing Date
JP56127771A Granted JPS5830381A (en) 1981-08-17 1981-08-17 Treatment for incineration ash of sewage sludge

Country Status (1)

Country Link
JP (1) JPS5830381A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS60210552A (en) * 1984-04-04 1985-10-23 日本碍子株式会社 Manufacture of lightweight aggregate from sludge
JP2010012406A (en) * 2008-07-03 2010-01-21 Oji Paper Co Ltd Ash treatment method

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0195368U (en) * 1987-12-16 1989-06-23

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS60210552A (en) * 1984-04-04 1985-10-23 日本碍子株式会社 Manufacture of lightweight aggregate from sludge
JPH0132180B2 (en) * 1984-04-04 1989-06-29 Ngk Insulators Ltd
JP2010012406A (en) * 2008-07-03 2010-01-21 Oji Paper Co Ltd Ash treatment method

Also Published As

Publication number Publication date
JPS6114100B2 (en) 1986-04-17

Similar Documents

Publication Publication Date Title
Huang et al. Application of water treatment sludge in the manufacturing of lightweight aggregate
US5268131A (en) Method for making light weight ceramic particles
RU2109705C1 (en) Method of processing ash dust and sludge from waste water treatment, method of preparing light filler, and light ball-like filler
CN104261802B (en) A kind of mud flyash high-strength ceramic granule and preparation method thereof
CN102050586B (en) Method for producing silicate cement by utilizing urban sewage plant sludge
CN104724897A (en) Sludge dewatering conditioning agent and use method thereof
CN111732357A (en) System and method for preparing lightweight aggregate by using fly ash and municipal sludge
JPH11217576A (en) Co-fuel for cement calcination and its production
CN1109850A (en) Method for producing haydite from refuse or mud
JPS5830381A (en) Treatment for incineration ash of sewage sludge
JP3178821B1 (en) Manufacturing method of building and construction blocks
JP5319254B2 (en) Method for firing sludge granulated product and method of using the same
JP3068036B2 (en) Manufacturing method of lightweight artificial aggregate
JPH06247756A (en) Production of lightweight aggregate using dehydrated sludge as raw material
JPS6114099B2 (en)
KR100687627B1 (en) Method for solidifying sewage sludge
CN112341237A (en) Method for firing light ceramsite by using waste casting resin sand
JPS62221484A (en) Method for treating shredder dust
CN112679222A (en) Resource disposal method for sludge drying incineration granulation
TWI440610B (en) Method for generating sludge sludge
RU2186047C2 (en) Method of hollow filling agent producing
JP2008137820A (en) Method for production of artificial aggregate
JPH07941A (en) Method for molding incineration ash
JPS6013891A (en) Assistant fuel for cement calcination and method for using the same
JPS62100470A (en) Manufacture of tile from sewage-treated sludge