JP3246509B1 - Treatment facilities for hydrous sludge - Google Patents
Treatment facilities for hydrous sludgeInfo
- Publication number
- JP3246509B1 JP3246509B1 JP2001172198A JP2001172198A JP3246509B1 JP 3246509 B1 JP3246509 B1 JP 3246509B1 JP 2001172198 A JP2001172198 A JP 2001172198A JP 2001172198 A JP2001172198 A JP 2001172198A JP 3246509 B1 JP3246509 B1 JP 3246509B1
- Authority
- JP
- Japan
- Prior art keywords
- sludge
- kiln
- hydrous
- hydrous sludge
- cement
- 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.)
- Expired - Lifetime
Links
- 239000010802 sludge Substances 0.000 title claims abstract description 55
- 239000004568 cement Substances 0.000 claims abstract description 24
- 239000002994 raw material Substances 0.000 claims abstract description 11
- 239000002002 slurry Substances 0.000 claims description 4
- 238000004519 manufacturing process Methods 0.000 claims description 3
- 239000000463 material Substances 0.000 claims description 2
- 238000005086 pumping Methods 0.000 claims description 2
- 238000010438 heat treatment Methods 0.000 claims 1
- 238000002347 injection Methods 0.000 claims 1
- 239000007924 injection Substances 0.000 claims 1
- 239000010801 sewage sludge Substances 0.000 abstract description 10
- 238000001035 drying Methods 0.000 abstract description 8
- 239000000654 additive Substances 0.000 abstract description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 6
- 230000000996 additive effect Effects 0.000 abstract description 2
- 230000000694 effects Effects 0.000 abstract 1
- ODINCKMPIJJUCX-UHFFFAOYSA-N Calcium oxide Chemical compound [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 description 6
- 238000000034 method Methods 0.000 description 4
- 239000010865 sewage Substances 0.000 description 4
- 239000000292 calcium oxide Substances 0.000 description 3
- 235000012255 calcium oxide Nutrition 0.000 description 3
- 235000019645 odor Nutrition 0.000 description 3
- 239000003337 fertilizer Substances 0.000 description 2
- AXCZMVOFGPJBDE-UHFFFAOYSA-L calcium dihydroxide Chemical compound [OH-].[OH-].[Ca+2] AXCZMVOFGPJBDE-UHFFFAOYSA-L 0.000 description 1
- 239000000920 calcium hydroxide Substances 0.000 description 1
- 235000011116 calcium hydroxide Nutrition 0.000 description 1
- 229910001861 calcium hydroxide Inorganic materials 0.000 description 1
- 238000004332 deodorization Methods 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 238000010304 firing Methods 0.000 description 1
- 229910001385 heavy metal Inorganic materials 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000002689 soil Substances 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
Classifications
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P40/00—Technologies relating to the processing of minerals
- Y02P40/10—Production of cement, e.g. improving or optimising the production methods; Cement grinding
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/40—Valorisation of by-products of wastewater, sewage or sludge processing
Landscapes
- Treatment Of Sludge (AREA)
- Curing Cements, Concrete, And Artificial Stone (AREA)
Abstract
【要約】
【目的】 下水汚泥等の含水汚泥を、乾燥、添加剤添加
等の前処理を施すことなく、効率的に最終処分する。
【構成】 含水汚泥を、直接、乾式キルン2の窯尻部分
2A又は仮焼炉に導入して焼却する。
【効果】 含水汚泥を、乾燥することなく、また、添加
剤を用いて前処理することなく、直接、既存の簡易な焼
却設備である乾式キルンに投入してセメント原料と共に
焼却処理することができる。キルンに投入された含水汚
泥は、その殆どが水分と有機成分であるため、焼却によ
り残留する灰分はごく微量であり、セメントクリンカー
の品質に影響を及ぼすこともなく、通常運転を行える。Abstract: [Object] To efficiently dispose of hydrous sludge such as sewage sludge without final treatment such as drying and addition of additives. [Structure] A hydrous sludge is directly introduced into a kiln bottom portion 2A of a dry kiln 2 or a calciner to be incinerated. [Effect] The hydrous sludge can be directly injected into a dry kiln, which is an existing simple incinerator, and incinerated with the cement raw material without drying and without pretreatment using an additive. . Since most of the hydrous sludge introduced into the kiln is water and organic components, the amount of ash remaining after incineration is very small, and normal operation can be performed without affecting the quality of cement clinker.
Description
【0001】[0001]
【産業上の利用分野】本発明は含水汚泥の処理設備に係
り、特に、セメントクリンカーの製造設備に併設され
て、下水汚泥等の含水汚泥を、乾燥、添加剤添加等の前
処理を施すことなく、効率的に最終処分する処理設備に
関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a facility for treating hydrous sludge , and more particularly to a facility for manufacturing cement clinker.
The present invention relates to a treatment facility for efficiently disposing of hydrated sludge such as sewage sludge without final treatment such as drying and addition of additives.
【0002】[0002]
【従来の技術】下水処理場から排出される下水汚泥等の
汚泥の処理法としては、古来、肥料として利用される場
合もあったが、汚泥に重金属類が含有されていること、
及び、肥料としての利用では処理量があまりに少ないこ
となどの理由から、最近では、陸上埋立て及び海上投棄
が主流となっている。しかしながら、下水処理場からの
下水汚泥排出量は、首都圏を中心に、近年、増々増加傾
向にあり、陸上埋立てや海上投棄処分のための処分場の
不足、更には、環境汚染防止上の制約を受けて、汚泥処
理は焼却処分に移行しているのが現状である。この汚泥
の焼却方法としては、既にいくつかの方法が提案されて
いる。2. Description of the Related Art Sludge such as sewage sludge discharged from a sewage treatment plant has been used as fertilizer since ancient times. However, sludge contains heavy metals.
In recent years, land reclamation and sea dumping have become the mainstream for reasons such as the amount of treatment used for fertilizer is too small. However, the amount of sewage sludge discharged from sewage treatment plants has been increasing in recent years, especially in the Tokyo metropolitan area, and there is a shortage of landfills for land reclamation and marine dumping. Due to restrictions, sludge treatment has been shifted to incineration. Several methods have already been proposed for incineration of this sludge.
【0003】[0003]
【発明が解決しようとする課題】しかしながら、従来の
焼却炉による汚泥焼却方法では、焼却に先立ち汚泥を乾
燥する必要がある。また、乾燥排ガスを脱臭する必要も
ある。このため、焼却コスト、乾燥コスト及び脱臭コス
トが嵩み、処理コストが高くつくという欠点がある。However, in the conventional sludge incineration method using an incinerator, it is necessary to dry the sludge before incineration. It is also necessary to deodorize the dried exhaust gas. For this reason, there are drawbacks that incineration costs, drying costs, and deodorization costs are increased, and processing costs are high.
【0004】汚泥の乾燥に生石灰を用い、汚泥中の水分
と生石灰との反応で消石灰を生成させると共に、反応熱
を利用して残留水分を乾燥させることにより汚泥を空気
圧送可能な状態に乾燥させ、乾燥物をセメント原料とし
て利用する方法も提案されているが、この方法でも、汚
泥の乾燥のために生石灰を添加する必要があるという不
具合がある。[0004] Quick lime is used to dry sludge, slaked lime is generated by the reaction of water in the sludge with quick lime, and residual moisture is dried by using heat of reaction to dry the sludge into a state capable of being sent by air. Although a method of using a dried product as a cement raw material has been proposed, this method also has a disadvantage that quicklime needs to be added for drying sludge.
【0005】本発明は上記従来の問題点を解決し、下水
汚泥等の含水汚泥を、乾燥、添加剤添加等の前処理を施
すことなく、効率的に最終処分する処理設備を提供する
ことを目的とする。The present invention has been made to solve the above-mentioned conventional problems and to provide a treatment facility for efficiently final disposal of hydrated sludge such as sewage sludge without performing pretreatment such as drying and addition of additives. Aim.
【0006】[0006]
【課題を解決するための手段】請求項1に記載の含水汚
泥の処理設備は、原料ミルで粉砕されたセメント原料を
予熱するプレヒータと、このプレヒータが窯尻部分に接
続されて、予熱された上記セメント原料を焼成する乾式
キルンとを有するセメントクリンカーの製造設備に併設
される含水汚泥の処理設備であって、含水スラリー状の
含水汚泥を貯留する汚泥タンクと、この汚泥タンク内の
上記含水汚泥を圧送する圧送ポンプと、この圧送ポンプ
に接続されて上記含水汚泥を上記乾式キルン内へと直接
投入する配管とを備えてなり、かつ上記配管が上記窯尻
部または仮焼炉に接続されていることを特徴とするもの
である。 A hydrous soil according to claim 1.
The mud processing equipment uses cement raw material pulverized by a raw material mill.
Preheater to preheat and this preheater
Continued, dry type of firing the preheated cement raw material
Attached to cement clinker manufacturing facility with kiln
Equipment for the treatment of hydrous sludge,
A sludge tank for storing hydrated sludge, and
A pump for pumping the above-mentioned hydrous sludge;
The sludge is directly connected to the dry kiln
And a pipe for charging, and the pipe is
Characterized by being connected to a part or a calciner
It is.
【0007】請求項2に記載の含水汚泥の処理設備は、
請求項1に記載の配管が、上記窯尻部の側面に接続され
ていることを特徴とするものである。 [0007] The treatment facility for hydrous sludge according to claim 2 is characterized in that:
The piping according to claim 1 is connected to a side surface of the kiln bottom.
It is characterized by having.
【0008】以下、図面を参照して本発明を詳細に説明
する。Hereinafter, the present invention will be described in detail with reference to the drawings.
【0009】[0009]
【発明の実施の形態】図1は本発明の含水汚泥の処理設
備の一実施形態を示す模式的な断面図である。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS FIG. 1 shows an apparatus for treating hydrous sludge according to the present invention.
FIG. 2 is a schematic cross-sectional view showing one embodiment of the equipment .
【0010】本実施例においては、含水汚泥(例えば、
下水処理場の沈降汚泥)を、含水スラリー状のまま、乾
式キルンの窯尻部分に直接投入して焼却する。即ち、下
水処理場から排出された下水汚泥等の含水汚泥は、ま
ず、汚泥受入設備から一旦、圧送ポンプP1 を備える配
管11を経て汚泥タンク1に貯留し、この汚泥タンク1
から随時圧送ポンプP2 を備える配管12を経て乾式ロ
ータリーキルン2の窯尻部分2Aよりキルン1内に直接
投入する。[0010] In this embodiment, hydrated sludge (for example,
The settled sludge of the sewage treatment plant) is directly poured into the kiln bottom of the dry kiln and incinerated in the form of a wet slurry. That is, water sludge or the like sewage sludge discharged from a sewage treatment plant, first, once the sludge receiving facility, and stored in the sludge tank 1 via a pipe 11 with a pressure pump P 1, the sludge tank 1
Directly charged into the kiln 1 from the kiln inlet part 2A of the dry rotary kiln 2 through the pipe 12 with a needed pressure pump P 2 from.
【0011】このロータリーキルン2の窯尻部分の上部
には、サスペンションプレヒータ3が連設されており、
図示しない原料ミルで粉砕されたセメント原料を、この
プレヒータ3で予熱した後、ロータリーキルン2の窯尻
部分2Aに投下し、キルン2内で焼成してセメントクリ
ンカーを製造するように構成されている。A suspension preheater 3 is connected to the upper part of the kiln bottom of the rotary kiln 2.
A cement raw material pulverized by a raw material mill (not shown) is preheated by the preheater 3, then dropped into the kiln tail portion 2A of the rotary kiln 2, and fired in the kiln 2 to produce a cement clinker.
【0012】従って、ロータリーキルン2の窯尻部分2
Aに投入された含水汚泥は、加熱されたセメント原料と
共に焼成され、セメントクリンカーとして排出される。Therefore, the kiln bottom part 2 of the rotary kiln 2
The hydrous sludge charged in A is fired together with the heated cement raw material and discharged as cement clinker.
【0013】このように、含水汚泥を配管圧送して直接
焼却処理する場合には、臭気等の問題が生起することも
ない。As described above, in the case where the hydrated sludge is pressure-fed to the pipe and directly incinerated, problems such as odor do not occur.
【0014】なお、仮焼炉を有するセメント焼成設備の
場合にあっては、含水汚泥を仮焼炉に投入して焼却する
ようにしても良い。In the case of a cement burning facility having a calciner, hydrous sludge may be put into a calciner and incinerated.
【0015】本含水処理設備を用いて含水汚泥を処理す
るに際しては、既存の乾式キルンに、その運転条件を特
に変更することなく含水汚泥を投入して焼却処分するの
が好ましく、この点からは、投入する含水汚泥を所定値
以下とする必要がある。Treating hydrated sludge using the hydrate treatment equipment
In this case, it is preferable to incinerate and dispose hydrated sludge into the existing dry-type kiln without particularly changing its operating conditions.From this point, it is necessary to reduce the amount of hydrated sludge to be supplied to a predetermined value or less. .
【0016】例えば、90〜100t/hrの割合でセ
メントクリンカーを生産しているロータリーキルンに通
常の下水汚泥を導入して焼却処分する場合、下水汚泥の
投入量は9〜10t/hrとし、製造されるセメントク
リンカーの重量に対して1/9〜1/11程度の含水汚
泥を投入するようにするのが好ましい。For example, when ordinary sewage sludge is introduced into a rotary kiln producing cement clinker at a rate of 90 to 100 t / hr and incinerated, the sewage sludge is supplied at a rate of 9 to 10 t / hr. It is preferable to add about 1/9 to 1/11 of the hydrous sludge based on the weight of the cement clinker.
【0017】[0017]
【作用】本発明によれば、含水汚泥を、乾燥することな
く、また、添加剤を用いて前処理することなく、直接、
既存の簡易な焼却設備である乾式キルンに投入してセメ
ント原料と共に焼却処理することができる。キルンに投
入された含水汚泥は、その殆どが水分と有機成分である
ため、焼却により残留する灰分はごく微量であり、セメ
ントクリンカーの品質に影響を及ぼすこともなく、通常
運転を行える。加えて、含水汚泥を配管圧送して直接焼
却処理しているので、臭気等の問題が生起することもな
い。 According to the present invention, hydrated sludge is directly dried without drying and without pretreatment with an additive.
It can be put into a dry kiln, which is an existing simple incineration facility, and incinerated with cement raw materials. Since most of the hydrous sludge introduced into the kiln is water and organic components, the amount of ash remaining after incineration is very small, and normal operation can be performed without affecting the quality of cement clinker. In addition, hydrated sludge is pumped by piping and directly baked.
Odors and other problems may not occur.
No.
【0018】[0018]
【実施例】以下に具体的な実施例を挙げて、本発明をよ
り詳細に説明する。The present invention will now be described in more detail with reference to specific examples.
【0019】実施例1 下記表1に示す組成の下水汚泥を、図1に示す如く、乾
式キルン(90〜100t/hrのセメントクリンカー
を生産している乾式キルン)の窯尻から1〜10t/h
rの量で投入して、通常運転を行ったところ、セメント
クリンカーの品質に何ら影響を及ぼすことなく、安定な
運転を行うことができ、汚泥を含水スラリーのまま、前
処理することなく、直接最終処分することができた。Example 1 As shown in FIG. 1, sewage sludge having the composition shown in Table 1 below was used in a kiln of a dry kiln (a dry kiln producing a cement clinker of 90 to 100 t / hr) at a rate of 1 to 10 t / h. h
When the normal operation was carried out by adding the amount of r, the stable operation can be performed without any influence on the quality of the cement clinker, and the sludge is directly contained in the water-containing slurry without pretreatment. Final disposal was possible.
【0020】[0020]
【表1】 [Table 1]
【0021】なお、仮焼炉に導入した場合も同様にセメ
ントクリンカーの品質に何ら影響を及ぼすことなく、安
定な運転を行うことができ、汚泥を含水スラリーのま
ま、前処理することなく、直接最終処分することができ
た。In addition, when introduced into a calciner, a stable operation can be similarly performed without any influence on the quality of cement clinker, and the sludge can be directly used as a water-containing slurry without pretreatment. Final disposal was possible.
【0022】[0022]
【発明の効果】以上詳述した通り、本発明の含水汚泥の
処理設備によれば、下水汚泥などの含水汚泥を、乾燥や
添加剤添加等の前処理を施すことなく、また、環境汚染
の問題もなく、既存の乾式キルンで直接焼却処理するこ
とにより、効率的かつ低コストに最終処分することがで
きるとともに、汚泥焼却灰はセメントクリンカーとして
経済的に最終処理することができる。 As described in detail above, the hydrous sludge of the present invention
According to the treatment equipment , effluent sludge such as sewage sludge can be directly incinerated in an existing dry kiln without pretreatment such as drying and addition of additives, and without environmental pollution. And low-cost final disposal , while sludge incineration ash is used as cement clinker.
It can be economically processed.
【0023】また、含水汚泥を配管圧送して直接焼却処
理しているので、臭気等の問題が生起することもない。 [0023] In addition, the wet sludge is pressure-fed to the pipe and directly incinerated.
As a result, problems such as odor do not occur.
【図1】本発明の含水汚泥の処理設備の一実施形態を示
す模式的な断面図である。FIG. 1 is a schematic cross-sectional view showing an embodiment of a treatment facility for hydrous sludge of the present invention.
───────────────────────────────────────────────────── フロントページの続き (72)発明者 石崎 倫朗 福岡県北九州市八幡西区洞南町1番地1 三菱マテリアル株式会社セメント開発 センター内 (56)参考文献 特開 平3−98700(JP,A) 特公 平3−13181(JP,B2) 特公 昭59−38175(JP,B2) (58)調査した分野(Int.Cl.7,DB名) C02F 11/00 - 11/20 C04B 7/24 C04B 7/44 F23G 5/00 - 7/14 ──────────────────────────────────────────────────続 き Continuation of the front page (72) Inventor Toshiro Ishizaki 1-Donan-cho, Yawata-nishi-ku, Kitakyushu-shi, Fukuoka 1 Within the Mitsubishi Materials Corporation Cement Development Center (56) References JP-A-3-98700 (JP, A) JP 3-13181 (JP, B2) JP-B-59-38175 (JP, B2) (58) Fields investigated (Int. Cl. 7 , DB name) C02F 11/00-11/20 C04B 7/24 C04B 7/44 F23G 5/00-7/14
Claims (2)
熱するプレヒータと、このプレヒータが窯尻部分に接続
されて、予熱された上記セメント原料を焼成する乾式キ
ルンとを有するセメントクリンカーの製造設備に併設さ
れる含水汚泥の処理設備であって、 含水スラリー状の含水汚泥を貯留する汚泥タンクと、こ
の汚泥タンク内の上記含水汚泥を圧送する圧送ポンプ
と、この圧送ポンプに接続されて上記含水汚泥を上記乾
式キルン内へと直接投入する配管とを備えてなり、かつ
上記配管が上記窯尻部または仮焼炉に接続されているこ
とを特徴とする含水汚泥の処理設備。 (1) Preparing a cement raw material pulverized by a raw material mill.
Heating preheater and this preheater is connected to the kiln bottom
The dry key that fires the preheated cement material
Installed in a cement clinker manufacturing facility
A sludge tank for storing wet sludge in the form of a wet slurry.
Pump for pumping the above-mentioned wet sludge in the sludge tank
And the wet sludge connected to the pump
And a pipe for direct injection into the kiln, and
Make sure that the above piping is connected to the kiln bottom or calciner.
And a facility for treating hydrous sludge.
れていることを特徴とする請求項1に記載の含水汚泥の
処理設備。 2. The pipe is connected to a side of the bottom of the kiln.
The hydrous sludge according to claim 1, wherein
Processing equipment.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2001172198A JP3246509B1 (en) | 2001-06-07 | 2001-06-07 | Treatment facilities for hydrous sludge |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2001172198A JP3246509B1 (en) | 2001-06-07 | 2001-06-07 | Treatment facilities for hydrous sludge |
Related Parent Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP08254995A Division JP3344448B2 (en) | 1995-04-07 | 1995-04-07 | Sludge treatment method |
Publications (2)
Publication Number | Publication Date |
---|---|
JP3246509B1 true JP3246509B1 (en) | 2002-01-15 |
JP2002052397A JP2002052397A (en) | 2002-02-19 |
Family
ID=19013860
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2001172198A Expired - Lifetime JP3246509B1 (en) | 2001-06-07 | 2001-06-07 | Treatment facilities for hydrous sludge |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP3246509B1 (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US8141501B2 (en) | 2005-08-26 | 2012-03-27 | Mitsubishi Materials Corporation | Method and facility for disposing wet sludge |
JP7513098B2 (en) | 2020-08-07 | 2024-07-09 | 日本電信電話株式会社 | Optical coupling device and optical coupling system |
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JP5157052B2 (en) * | 2005-08-19 | 2013-03-06 | 住友大阪セメント株式会社 | Low moisture content sludge transportation method and equipment, and cement manufacturing facility |
JP4926781B2 (en) * | 2007-03-27 | 2012-05-09 | 住友大阪セメント株式会社 | High moisture content waste treatment method and treatment equipment |
AT509221B1 (en) * | 2009-12-28 | 2011-07-15 | Holcim Technology Ltd | METHOD FOR ASSESSING PHOSPHORUS-BASED ALTERNATIVE FUELS IN CEMENT MANUFACTURE |
CN104949128B (en) * | 2014-09-10 | 2017-10-27 | 方向 | A kind of fixed-end forces method |
CN104197339A (en) * | 2014-09-11 | 2014-12-10 | 陆骏 | Combined body of composite type rotating sludge incineration kiln and reciprocating type sludge incineration kiln |
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2001
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US8141501B2 (en) | 2005-08-26 | 2012-03-27 | Mitsubishi Materials Corporation | Method and facility for disposing wet sludge |
JP7513098B2 (en) | 2020-08-07 | 2024-07-09 | 日本電信電話株式会社 | Optical coupling device and optical coupling system |
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