[go: up one dir, main page]

JPH03207497A - Treatment of sewerage sludge - Google Patents

Treatment of sewerage sludge

Info

Publication number
JPH03207497A
JPH03207497A JP2002926A JP292690A JPH03207497A JP H03207497 A JPH03207497 A JP H03207497A JP 2002926 A JP2002926 A JP 2002926A JP 292690 A JP292690 A JP 292690A JP H03207497 A JPH03207497 A JP H03207497A
Authority
JP
Japan
Prior art keywords
sludge
heat
treatment
sintering
sewage
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.)
Pending
Application number
JP2002926A
Other languages
Japanese (ja)
Inventor
Tsunetoshi Kochihira
東風平 玄俊
Kazuo Masuda
増田 和生
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.)
Nippon Steel Corp
Original Assignee
Sumitomo Metal Industries 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 Sumitomo Metal Industries Ltd filed Critical Sumitomo Metal Industries Ltd
Priority to JP2002926A priority Critical patent/JPH03207497A/en
Publication of JPH03207497A publication Critical patent/JPH03207497A/en
Pending legal-status Critical Current

Links

Landscapes

  • Treatment Of Sludge (AREA)

Abstract

(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。
(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.

Description

【発明の詳細な説明】 く産業上の利用分野〉 この発明は家庭排水、産業排水などから生しる下水汚泥
の処理方法に関するものである。
DETAILED DESCRIPTION OF THE INVENTION Industrial Application Field The present invention relates to a method for treating sewage sludge generated from domestic wastewater, industrial wastewater, and the like.

〈従来技術〉 国民の健康管理、衛生管理の向上を図るため、各地で下
水道の普及が進められている。下水処理場では、下水処
理に伴い多量の汚泥が発生し、その汚泥は一部では肥料
として活用されている例もあるが大部分は有効利用され
ずに、脱水後に埋立処分または脱水焼却後に埋立て処分
されている。
<Prior art> In order to improve people's health and hygiene management, sewage systems are being popularized in various regions. At sewage treatment plants, a large amount of sludge is generated as a result of sewage treatment, and although some sludge is used as fertilizer, the majority of the sludge is not used effectively and is disposed of in landfills after dewatering or in landfills after dewatering and incineration. It has been disposed of.

この汚泥には有機物が含まれており、燃料としての価値
はあるものの、高水分および取扱いの困難さ故に最終的
には投棄されているが、投棄場所の確保難という面から
見て国民的レベルより有効利用技術の確立が望まれてい
る。
Although this sludge contains organic matter and has value as fuel, it is ultimately dumped due to its high moisture content and difficulty in handling. Establishment of more effective utilization technology is desired.

第2図に示すのは、家庭下水の一般的な汚水処理設備の
例であり、上流側から順に沈砂池50、最初沈殿池51
、エアコンプレッサー52によるばっ気槽53、最終沈
殿池54を設け、初沈55および終沈56を脱水機57
により脱水して脱水ケーキ(汚泥)を得ている。この脱
水ケーキは、助燃剤等を添加して焼却するか、または埋
立て処分するのが主流となっている。
What is shown in Fig. 2 is an example of a general domestic sewage treatment facility, in order from the upstream side: a settling tank 50, a first settling tank 51.
, an aeration tank 53 using an air compressor 52, and a final sedimentation tank 54 are provided, and the initial sedimentation 55 and final sedimentation 56 are removed by a dehydrator 57.
Dehydrated cake (sludge) is obtained by dehydration. This dehydrated cake is generally either incinerated after adding a combustion improver or the like, or disposed of in a landfill.

なお、汚泥または排液の処理方法として従来次のような
ものが提案されている。
The following methods have been proposed as methods for treating sludge or wastewater.

■ 特公昭61−59800号公報(コークス乾式消火
設備による余剰汚泥の処理方法) これは、冷却塔に装入された赤熱コークスを循環冷却ガ
スにより冷却するコークス乾式消火設備において、冷却
塔の下部またはガス循環路から脱水処理した汚泥ケーキ
を吹き込んで処理し、余剰汚泥の処理、コークス冷却効
率の向上等を図ったものである。
■ Japanese Patent Publication No. 61-59800 (method for processing surplus sludge using coke dry extinguishing equipment) The dehydrated sludge cake is blown into the system through the gas circulation path to treat excess sludge and improve coke cooling efficiency.

■ 特開昭61−271098号公報(排水汚泥の焼却
処理方法) これは、リンを含む排水汚泥の焼却処理前に、汚泥とカ
ルシウム化合′JIyJ(例えばCaCOa)を混合し
、安定なリン酸カルシウムを生或して焼却炉およびサイ
クロン等におけるタリンカートラブル、腐食を防止する
ようにしたものである。
■ JP-A-61-271098 (Incineration treatment method for wastewater sludge) In this method, before incineration of wastewater sludge containing phosphorus, sludge and a calcium compound 'JIyJ (for example, CaCOa) are mixed to produce stable calcium phosphate. It is designed to prevent trouble and corrosion of the coals in incinerators, cyclones, etc.

■ 特公昭63−45639号公報(有機性廃液の処理
方法) これは、有機物とリンを含む廃液の嫌気好気活性汚泥法
において、濃縮初沈汚泥と濃縮余剰汚泥を混合すると同
時または混合直後に、鉄塩化合物および消石灰Ca (
OH) zを添加し、次いで脱水処理し、脱水時の分離
液中のリン濃度を低下させるものである。
■ Japanese Patent Publication No. 63-45639 (Method for treating organic waste liquid) This is an anaerobic and aerobic activated sludge method for waste liquid containing organic matter and phosphorus, in which concentrated primary settled sludge and concentrated surplus sludge are mixed at the same time or immediately after mixing. , iron salt compounds and slaked lime Ca (
OH) is added and then dehydrated to reduce the phosphorus concentration in the separated liquid during dehydration.

〔この発明が解決しようとする課題〕[Problems to be solved by this invention]

前述のような従来の汚泥処理法の場合、次のような問題
点がある。
In the case of the conventional sludge treatment method as described above, there are the following problems.

(i)埋立て処分法 (イ)地下水汚染の可能性がある。(i) Landfill disposal law (b) There is a possibility of groundwater contamination.

(口)埋立て場所の確保が困難である。(Explanation) It is difficult to secure a landfill site.

(ハ)有用成分が効率良く利用されない。(c) Useful ingredients are not utilized efficiently.

(11)焼却処分法 (イ)設備費が高価となる。(11) Incineration disposal method (b) Equipment costs are high.

(口)ランニングコストカ高い。(Mouth) Running costs are high.

(ハ)有用或分が資源として利用されない。(c) A certain amount of useful material is not used as a resource.

(ni)コークス乾式消火設備の利用 コークス品質の影響があり、大量処理が困難である。(ni) Use of coke dry fire extinguishing equipment It is difficult to process large quantities due to the influence of coke quality.

従来の汚泥処理法には以上のような問題点があり、■衛
生的である。■安価である、■資源として有効利用でき
るの条件を満足する下水汚泥の処理方法の開発は、国民
的要求であるといえる。
Conventional sludge treatment methods have the above-mentioned problems: ■ They are unhygienic. It can be said that the development of a treatment method for sewage sludge that satisfies the following conditions: ■It is inexpensive; and ■It can be used effectively as a resource.

この発明は、このような事情に鑑みてなされたもので、
その目的は汚水処理後の汚泥を衛生的に、かつ安価に処
理できると共に、有用戒分を完全に、かつ大量に資源と
して再利用することのできる下水汚泥の処理方法を提供
することにある。
This invention was made in view of these circumstances,
The purpose is to provide a method for treating sewage sludge that can hygienically and inexpensively treat sludge after sewage treatment, and that can completely and reuse a large amount of useful substances as resources.

〔課題を解決するための手段〕[Means to solve the problem]

本発明は、第l図に示すように、家庭下水などの汚水処
理設Oi1から排出された脱水ケーキ(汚泥)2に生石
灰CaOを加えて混練機3により混練し、この混練機3
において生石灰の水和反応および水和時の反応熱により
加熱乾燥して加熱処理ダスト4を得、この加熱処理ダス
ト4を焼結設備5の焼結原料6の一部として使用する。
As shown in FIG. 1, in the present invention, quicklime CaO is added to a dehydrated cake (sludge) 2 discharged from a sewage treatment facility Oi1 such as domestic sewage, and the mixture is kneaded by a kneader 3.
In the hydration reaction of quicklime and the reaction heat during hydration, the heat-treated dust 4 is heated and dried, and this heat-treated dust 4 is used as a part of the sintering raw material 6 of the sintering equipment 5.

焼結原料は、鉄鉱石7、石灰石8、コー−クス9からな
り、これらに加熱処理ダスト4を添加した後、混練機1
0で混練し、焼結機11で焼結した焼結鉱12を高炉1
3に装入する。
The sintering raw materials consist of iron ore 7, limestone 8, and coke 9, and after adding heat-treated dust 4 to these, they are mixed in a kneader 1.
The sintered ore 12 mixed in the blast furnace 1 and sintered in the sintering machine 11 is
Charge to 3.

汚水処理設備lおよび焼結設m5には一般的に用いられ
ている設備を用いることができる。
Generally used equipment can be used for the sewage treatment equipment l and the sintering equipment m5.

〈作 用〉 (1)汚泥と生石灰を混練することにより、CaO +
HzO →Ca(OH)z+ Qkcalの水和反応に
より汚泥中の水分が低減されると共に゛、永和時の反応
熱により余剰水分が蒸発し、特別な加熱源なしに汚泥を
加熱乾燥できる。また、これと同時に細菌は加熱により
死滅する。
<Function> (1) By kneading sludge and quicklime, CaO +
The water content in the sludge is reduced by the hydration reaction of HzO → Ca(OH)z+ Qkcal, and excess water is evaporated due to the reaction heat during hydration, making it possible to heat and dry the sludge without a special heating source. At the same time, the bacteria are also killed by heating.

(j1)加熱処理ダストを焼結原料として使用すること
により、消石灰Ca (OH) z分が石灰石の一部と
して利用され、石灰石の使用量を低減できる。また、消
石灰は微粉原料の造粒剤として作用し、焼結工程での生
産性が向上する。
(j1) By using heat-treated dust as a sintering raw material, slaked lime Ca (OH) z is used as a part of limestone, and the amount of limestone used can be reduced. In addition, slaked lime acts as a granulating agent for the fine powder raw material, improving productivity in the sintering process.

(iii)加熱処理ダスト中の消石灰分はコークスの燃
焼性を改善し、また有機或分は燃焼することにより粉コ
ークスの一部となり、焼結用コークス原単位の低減を図
れる。
(iii) The slaked lime content in the heat-treated dust improves the combustibility of coke, and the organic content becomes part of coke powder by burning, thereby reducing the coke consumption for sintering.

なお、汚泥と生石灰の混合比は、発熱量、経済性などの
面から適宜決定されるが、重量比で1=1が好ましい。
The mixing ratio of sludge and quicklime is appropriately determined from the viewpoint of calorific value, economical efficiency, etc., but it is preferable that the weight ratio is 1=1.

また、加熱処理ダストの焼結原料への添加比率は25%
以下となる。焼結鉱の製造に際しては自溶性焼結鉱とな
らしめるため、鉄鉱石だけでなく石灰石も原料として使
用し、本発明では加熱処理ダスト中の消石灰分が石灰石
の一部として利用されるが、25%より多く添加すると
原料中の石灰分が過剰となり、焼結鉱の品質が低下する
In addition, the addition ratio of heat-treated dust to the sintering raw material is 25%.
The following is true. In the production of sintered ore, not only iron ore but also limestone is used as a raw material in order to make it a self-soluble sintered ore, and in the present invention, the slaked lime content in the heat-treated dust is used as part of the limestone. If more than 25% is added, the lime content in the raw material will be excessive and the quality of the sintered ore will deteriorate.

く実 施 例〉 これは、汚水処理設備1からの脱水ケーキ2に生石灰C
aOを重量比1:lで混合し、得られた加熱処理ダスト
4を焼結設備5で焼結した例であり、次表のような結果
が得られた。
Practical example> This is a case where quicklime C is added to the dehydrated cake 2 from the sewage treatment equipment 1.
This is an example in which aO was mixed at a weight ratio of 1:l and the resulting heat-treated dust 4 was sintered in a sintering equipment 5, and the results shown in the following table were obtained.

第1表 加熱処理結果 第2表 加熱処理ダストの焼結使用結果 これらの表から、汚泥を加熱乾燥、殺菌し、焼結工程に
おいて生産率の向上、コークス原単位および石灰石使用
量の低減を図れることがわかる。
Table 1 Heat treatment results Table 2 Results of sintering heat treated dust From these tables, it is possible to heat dry and sterilize sludge, improve production rate, and reduce coke consumption and limestone consumption in the sintering process. I understand that.

なお、下水汚泥の処理可能量を試算してみると次のよう
になる。
A trial calculation of the amount of sewage sludge that can be treated is as follows.

■前提 粗鋼量7,000 KT/年の一貫製鉄所焼結鉱必要量
 :800(KT/月〕 焼結原料必要量:890(KT/月)  (800 x
1/0.9) 加熱処理ダスト添加量:45〔κT/月〕(890X5
%) ■汚泥処理量 45κTXI/1.8 (歩留り) =2 5  (K
T/月〕■処理可能人口 〔発明の効果〕 前述のとおり、この発明に係る下水汚泥の処理方法は、
汚泥に生石灰を混合して加熱処理ダストを得、この加熱
処理ダストを焼結原料の一部として使用するようにした
ため、汚泥を加熱乾燥・殺菌できると共に、加熱処理ダ
スト中の消石灰分、有機成分により生産率の向上、コー
クス原単位および石灰石使用量の低減を図ることができ
、汚水処理後の汚泥を衛生的に、かつ安価に処理できる
と共に、有用或分を完全に、かつ大量に資源として有効
に再利用し、無害化させることができる。
■Assumed amount of crude steel 7,000 KT/year Required amount of sintered ore for integrated steelworks: 800 (KT/month) Required amount of sintering raw material: 890 (KT/month) (800 x
1/0.9) Heat treatment dust addition amount: 45 [κT/month] (890X5
%) ■Sludge treatment amount 45κTXI/1.8 (yield) = 2 5 (K
T/month]■Population that can be treated [Effects of the invention] As mentioned above, the method for treating sewage sludge according to this invention is as follows:
By mixing quicklime with sludge to obtain heat-treated dust and using this heat-treated dust as part of the sintering raw material, the sludge can be heated to dry and sterilized, and the slaked lime content and organic components in the heat-treated dust can be reduced. It is possible to improve the production rate, reduce the coke consumption rate and the amount of limestone used, and the sludge after sewage treatment can be treated hygienically and inexpensively, and the useful portion can be completely and in large quantities used as a resource. It can be effectively reused and rendered harmless.

【図面の簡単な説明】[Brief explanation of drawings]

第1図は、この発明に係る下水汚泥の処理方法を示すシ
ステムフロー図、第2図は一般的な汚水処理設備のシス
テムフロー図である。 1・・・汚水処理設備、2・・・脱水ケーキ(汚泥)3
・・・混練機、   4・・・加熱処理ダスト5・・・
焼結設備、  6・・・焼結原料7・・・鉄鉱石、  
 8・・・石灰石9・・・コークス、   ■0・・・
混練機11・・・焼結機、   12・・・焼結鉱13
・・・高炉
FIG. 1 is a system flow diagram showing a sewage sludge treatment method according to the present invention, and FIG. 2 is a system flow diagram of a general sewage treatment facility. 1... Sewage treatment equipment, 2... Dehydrated cake (sludge) 3
...Kneading machine, 4...Heating treatment dust 5...
Sintering equipment, 6...Sintering raw material 7...Iron ore,
8... Limestone 9... Coke, ■0...
Kneader 11...Sintering machine, 12...Sintered ore 13
...blast furnace

Claims (1)

【特許請求の範囲】[Claims] (1)汚泥に生石灰を混合して水和反応および水和時の
反応熱により加熱処理ダストを得、この加熱処理ダスト
を焼結原料の一部として使用することを特徴とする下水
汚泥の処理方法。
(1) Treatment of sewage sludge characterized by mixing quicklime with sludge to obtain heat-treated dust through hydration reaction and reaction heat during hydration, and using this heat-treated dust as part of the sintering raw material. Method.
JP2002926A 1990-01-10 1990-01-10 Treatment of sewerage sludge Pending JPH03207497A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2002926A JPH03207497A (en) 1990-01-10 1990-01-10 Treatment of sewerage sludge

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2002926A JPH03207497A (en) 1990-01-10 1990-01-10 Treatment of sewerage sludge

Publications (1)

Publication Number Publication Date
JPH03207497A true JPH03207497A (en) 1991-09-10

Family

ID=11542946

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2002926A Pending JPH03207497A (en) 1990-01-10 1990-01-10 Treatment of sewerage sludge

Country Status (1)

Country Link
JP (1) JPH03207497A (en)

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7731859B2 (en) 2006-07-10 2010-06-08 Ronald Eugene Woodruff Process for conditioning sewage sludge
JP2011000549A (en) * 2009-06-19 2011-01-06 Nippon Steel Corp Method of recycling wastewater sludge discharged from coal-fired power plant
CN102030450A (en) * 2010-09-30 2011-04-27 首钢总公司 Method for utilizing municipal sludge as raw material of steel industrial sintering ore
CN103866119A (en) * 2013-12-31 2014-06-18 首钢总公司 Energy-saving additive for sintering and application thereof
CN104060092A (en) * 2013-09-24 2014-09-24 攀钢集团攀枝花钢铁研究院有限公司 Biochemical sludge processing method
CN106191427A (en) * 2016-08-09 2016-12-07 重庆大学 A kind of municipal sludge mixes resource utilization method with useless fabric
CN106590811A (en) * 2016-11-22 2017-04-26 中冶节能环保有限责任公司 Method for significantly reducing discharge of sintering flue gas inhalable particles and fine particles

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7731859B2 (en) 2006-07-10 2010-06-08 Ronald Eugene Woodruff Process for conditioning sewage sludge
JP2011000549A (en) * 2009-06-19 2011-01-06 Nippon Steel Corp Method of recycling wastewater sludge discharged from coal-fired power plant
CN102030450A (en) * 2010-09-30 2011-04-27 首钢总公司 Method for utilizing municipal sludge as raw material of steel industrial sintering ore
CN104060092A (en) * 2013-09-24 2014-09-24 攀钢集团攀枝花钢铁研究院有限公司 Biochemical sludge processing method
CN103866119A (en) * 2013-12-31 2014-06-18 首钢总公司 Energy-saving additive for sintering and application thereof
CN106191427A (en) * 2016-08-09 2016-12-07 重庆大学 A kind of municipal sludge mixes resource utilization method with useless fabric
CN106590811A (en) * 2016-11-22 2017-04-26 中冶节能环保有限责任公司 Method for significantly reducing discharge of sintering flue gas inhalable particles and fine particles
CN106590811B (en) * 2016-11-22 2018-03-20 中冶节能环保有限责任公司 A kind of method for substantially reducing sintering flue gas pellet and fine particle discharge

Similar Documents

Publication Publication Date Title
US5435923A (en) Method for the treatment of sewage sludge and the like
WO2004046050A1 (en) Method for disinfecting and stabilizing organic wastes with mineral by-products
JPH07503178A (en) Exhaust treatment method
JP2803855B2 (en) Sewage sludge recycling system
US3440166A (en) Waste treatment process with recycling flocculating agents
JPH03207497A (en) Treatment of sewerage sludge
Tenney et al. The use of fly ash in conditioning biological sludges for vacuum filtration
JPH1177095A (en) Livestock manure processing system
JPS6328492A (en) Treatment of waste liquid of stack gas scrubbing
CN1068847A (en) Sludge briquettes made from biochemical sludge
JP3356859B2 (en) Sludge treatment method
JPH07275895A (en) Wastewater-treatment without dilution
JPH01310799A (en) Method and apparatus for mixing treatment of sewage and garbage
JP4387040B2 (en) Soil improver and / or organic fertilizer and method for producing the same
JP2696146B2 (en) Wastewater and sludge treatment methods
CN112142279A (en) Thermal power plant calcium carbonate sludge regeneration treatment agent and process
CN110127974A (en) A kind of salt sewage sludge harmlessness minimizing recycling treatment process
JP2006315885A (en) Recycled fertilizer and its manufacturing method
JPS6082192A (en) Treatment of organic sludge
JPH0650505A (en) Desulfurizing agent used both for fuel and manufacture thereof
JP2789154B2 (en) Sludge treatment method
JPS5838229B2 (en) How to dispose of waste
JPS63134589A (en) Treatment of organic water-containing sludge
JPS62197382A (en) Aerobic fermentation
JPH08299997A (en) Treatment of sludge and device therefor