JPH02214599A - Method for drying water-containing solid - Google Patents
Method for drying water-containing solidInfo
- Publication number
- JPH02214599A JPH02214599A JP1035309A JP3530989A JPH02214599A JP H02214599 A JPH02214599 A JP H02214599A JP 1035309 A JP1035309 A JP 1035309A JP 3530989 A JP3530989 A JP 3530989A JP H02214599 A JPH02214599 A JP H02214599A
- Authority
- JP
- Japan
- Prior art keywords
- heat
- water
- drying
- heating medium
- air
- 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
Links
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 30
- 238000001035 drying Methods 0.000 title claims abstract description 29
- 239000007787 solid Substances 0.000 title claims abstract description 13
- 238000000034 method Methods 0.000 title claims description 13
- 239000000446 fuel Substances 0.000 claims abstract description 14
- 239000002351 wastewater Substances 0.000 claims abstract description 10
- 230000000717 retained effect Effects 0.000 claims abstract description 3
- 239000010865 sewage Substances 0.000 claims description 20
- 239000011343 solid material Substances 0.000 claims description 6
- 239000010802 sludge Substances 0.000 abstract description 17
- 239000000295 fuel oil Substances 0.000 abstract description 3
- 238000010438 heat treatment Methods 0.000 abstract 6
- 239000002912 waste gas Substances 0.000 abstract 1
- 230000029087 digestion Effects 0.000 description 4
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 4
- 230000001954 sterilising effect Effects 0.000 description 4
- 238000004659 sterilization and disinfection Methods 0.000 description 4
- 238000010586 diagram Methods 0.000 description 3
- 239000002699 waste material Substances 0.000 description 3
- 238000005273 aeration Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000003337 fertilizer Substances 0.000 description 2
- 230000008719 thickening Effects 0.000 description 2
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 1
- 229910052801 chlorine Inorganic materials 0.000 description 1
- 239000000460 chlorine Substances 0.000 description 1
- KYKAJFCTULSVSH-UHFFFAOYSA-N chloro(fluoro)methane Chemical compound F[C]Cl KYKAJFCTULSVSH-UHFFFAOYSA-N 0.000 description 1
- 239000000498 cooling water Substances 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- NBVXSUQYWXRMNV-UHFFFAOYSA-N fluoromethane Chemical compound FC NBVXSUQYWXRMNV-UHFFFAOYSA-N 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 241001148471 unidentified anaerobic bacterium Species 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
- Y02B—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
- Y02B30/00—Energy efficient heating, ventilation or air conditioning [HVAC]
- Y02B30/52—Heat recovery pumps, i.e. heat pump based systems or units able to transfer the thermal energy from one area of the premises or part of the facilities to a different one, improving the overall efficiency
-
- 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
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/30—Fuel from waste, e.g. synthetic alcohol or diesel
-
- 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
- Y02P70/00—Climate change mitigation technologies in the production process for final industrial or consumer products
- Y02P70/10—Greenhouse gas [GHG] capture, material saving, heat recovery or other energy efficient measures, e.g. motor control, characterised by manufacturing processes, e.g. for rolling metal or metal working
Landscapes
- Drying Of Solid Materials (AREA)
- Treatment Of Sludge (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は、下水処理排水の保有する熱を有効利用する含
水固形物の乾燥方法に関する。DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a method for drying water-containing solids that effectively utilizes the heat possessed by sewage treatment wastewater.
[従来の技術〕
現在の下水処理設備の概略を第2図に示すが、図に示す
ように、家庭の台所、風呂場、水洗便所等から排出され
るlη水は沈砂池10に集められて沈み易い塵、土砂が
取り除かれた後、最初沈澱池11に行き、沈んだ小さな
生汚泥が機械によって掻き集められて濃縮槽12に集め
られる。[Prior Art] An outline of current sewage treatment equipment is shown in Figure 2. As shown in the figure, lη water discharged from household kitchens, bathrooms, flush toilets, etc. is collected in a settling basin 10. After the easily settled dust and earth are removed, the sludge first goes to a sedimentation tank 11, where small pieces of settled raw sludge are scraped up by a machine and collected in a thickening tank 12.
一方、沈澱した汚泥が取り除かれた汚水は曝気槽13に
よって混入された活性汚泥と共に曝気し微生物によって
分解され、最終沈澱池14によって沈んだ汚物を排除し
、滅菌池15で塩素によって滅菌された後、海に放流さ
れている。On the other hand, the sewage from which the settled sludge has been removed is aerated with activated sludge mixed in in the aeration tank 13 and decomposed by microorganisms, the settled sewage is removed in the final settling tank 14, and the sewage is sterilized with chlorine in the sterilization tank 15. , are discharged into the sea.
一方、上記最初沈澱池11曝気槽13及び最終沈澱池1
4によって集められた汚泥は濃縮槽12で濃縮された後
、第一消化槽16及び第二消化槽17に搬送され、ガス
と消化汚泥に分解され、ガスはガスタンク18に集めら
れ、消化汚泥は汚泥貯留槽19を通った後、脱水設備2
0によって脱水した後含水汚泥として排出される。On the other hand, the first settling tank 11 aeration tank 13 and the final settling tank 1
The sludge collected in step 4 is concentrated in a thickening tank 12, and then transported to a first digestion tank 16 and a second digestion tank 17, where it is decomposed into gas and digested sludge.The gas is collected in a gas tank 18, and the digested sludge is After passing through the sludge storage tank 19, the dewatering equipment 2
After being dehydrated by 0, it is discharged as water-containing sludge.
しかしながら、上記滅菌池15から放流されている排水
の温度は真冬でも12℃程度あり、十分な熱源であるに
も関わらず利用されず、場合によっては温排水の公害源
となる等の問題点を引き起こしていた。However, the temperature of the waste water discharged from the sterilization pond 15 is around 12 degrees Celsius even in the middle of winter, and although it is a sufficient heat source, it is not used, and in some cases, there are problems such as the heated waste water becoming a source of pollution. was causing it.
また、上記第−及び第二の消化槽16.17においては
、通常の嫌気性菌を用いるので反応を促進するため高温
度に保持する必要があり、この為該消化槽16.17で
生じたガスを一旦ガスタンク18に貯留した後ボイラー
設備21によって燃焼して蒸気を発生させ、該蒸気を上
記消化槽16.17に送り込んで加熱する構造となって
いるので、発生したガス(主としてメタンガス)を有効
に利用していないという問題点があった。In addition, in the above-mentioned first and second digestion tanks 16.17, since ordinary anaerobic bacteria are used, it is necessary to maintain the temperature at a high temperature to promote the reaction. The structure is such that the gas is temporarily stored in the gas tank 18 and then combusted by the boiler equipment 21 to generate steam, which is then sent to the digestion tank 16, 17 and heated, so that the generated gas (mainly methane gas) is The problem was that it was not being used effectively.
本発明はこのような事情に鑑みなされたもので、下水処
理設備で発生する排水の保有する熱を有効に利用した下
水処理設備を提供することを目的とする。The present invention was made in view of the above circumstances, and an object of the present invention is to provide a sewage treatment facility that effectively utilizes the heat contained in the waste water generated in the sewage treatment facility.
上記目的に沿う請求の範囲第1項記載の含水固形物の乾
燥方法は、下水処理設備から発生する排水の保有熱をヒ
ートポンプを使用して回収し、該回収した熱によって空
気を加温し、該加温した空気によって上記下水処理設備
から発生する含水固形物を乾燥するようにして構成され
ている。The method for drying water-containing solids according to claim 1, which meets the above object, uses a heat pump to recover the retained heat of wastewater generated from sewage treatment equipment, and uses the recovered heat to heat the air. The heated air is configured to dry water-containing solids generated from the sewage treatment equipment.
そして、請求の範囲第2項記載の含水固形物の乾燥方法
は、請求の範囲第1項記載の含水固形物の乾燥方法にお
いて、ヒートポンプの動力源は下水処理設備から発生す
るガスを燃料とするガスタービンあるいはガスエンジン
等の熱機関で構成されている。The method for drying a water-containing solid material according to claim 2 is the method for drying a water-containing solid material according to claim 1, wherein the power source of the heat pump is fueled by gas generated from a sewage treatment facility. It consists of a heat engine such as a gas turbine or gas engine.
請求の範囲第1項記載の含水固形物の乾燥方法において
は、下水処理設備から発生ずる排水の熱をヒートポンプ
によって回収し、この熱によって空気を加温し、そして
該空気によって含水固形物を乾燥している。In the method for drying hydrated solids according to claim 1, heat of waste water generated from sewage treatment equipment is recovered by a heat pump, air is heated by this heat, and hydrated solids are dried by the air. are doing.
請求の範囲第2項記載の含水固形物の乾燥方法において
は、ヒートポンプの動力源は下水処理設備から発生する
ガスを燃料とする熱機関によって構成されている。従っ
て、余分な電力が不要となる。In the method for drying a water-containing solid material as set forth in claim 2, the power source of the heat pump is constituted by a heat engine that uses gas generated from sewage treatment equipment as fuel. Therefore, no extra power is required.
続いて、添付した図面を参照しつつ、本発明を具体化し
た実施例につき説明し、本発明の理解に供する。Next, embodiments embodying the present invention will be described with reference to the attached drawings to provide an understanding of the present invention.
ここに、第1図は本発明の実施例に係る含水固形物の乾
燥方法を適用した装置の概略構成を示すブロック図であ
る。Here, FIG. 1 is a block diagram showing a schematic configuration of an apparatus to which a method for drying a water-containing solid material according to an embodiment of the present invention is applied.
第1図に示すように、まず第1図に示す滅菌池15から
排出される放流水を一旦熱交換用のプール22に入れた
後に放流する。As shown in FIG. 1, first, the discharged water discharged from the sterilization pond 15 shown in FIG. 1 is once put into the heat exchange pool 22 and then discharged.
上記プール22には熱交換用のパイプが配置されて内部
に水等の熱媒■がポンプ23によって別の熱交換機24
との間を循環するようになっている。A heat exchange pipe is arranged in the pool 22, and a heat medium such as water is pumped into the pool 22 by a pump 23 to another heat exchanger 24.
It is designed to circulate between
上記熱交換機24内にはフロン等の熱媒■が循環するよ
うになって上記プール22に貯留された放流水の熱を上
記水等の熱媒1に伝え、該水等の熱媒Iから熱を上記フ
ロン等の熱媒■に伝えている。In the heat exchanger 24, a heat medium such as fluorocarbon is circulated, and the heat of the discharged water stored in the pool 22 is transferred to the heat medium 1 such as water, and from the heat medium I such as water. The heat is transferred to the heat medium (2) such as the above-mentioned Freon.
該熱媒■は圧縮機25によって加圧されて凝縮器26に
よって予備乾燥室内の空気を加温し、膨張弁27を介し
て上記熱交換機24に戻り降温して熱を吸収する。なお
、上記熱交換機24、圧縮機25、凝縮器26及び膨張
弁27を有してヒートポンプが構成されている。The heat medium (1) is pressurized by the compressor 25, heats the air in the pre-drying chamber by the condenser 26, returns to the heat exchanger 24 via the expansion valve 27, cools it, and absorbs heat. Note that the heat exchanger 24, compressor 25, condenser 26, and expansion valve 27 constitute a heat pump.
一方、上記凝縮器26では、乾燥室の一例である予備乾
燥室28と接続されるバイブ29.30を介して循環す
る空気が略60〜80℃程度に加熱され、その空気でも
って第1図の前記した脱水設備20から排出される含水
固形物の一例である含水汚物(脱水汚泥ともいう)を予
備乾燥するようにしている。On the other hand, in the condenser 26, the air circulating through the vibrator 29.30 connected to the pre-drying chamber 28, which is an example of a drying chamber, is heated to about 60 to 80 degrees Celsius, and the air is heated to approximately 60 to 80 degrees Celsius. Water-containing waste (also referred to as dehydrated sludge), which is an example of water-containing solids discharged from the above-mentioned dewatering equipment 20, is pre-dried.
この予備乾燥の手段としては例えば、コンヘアによって
上記含水汚物を徐々に搬送しながら、熱風に当てるよう
にしても良いし、気流と対向させる方向から徐々に含水
汚物を落下させるようにしても良い。As a means for this pre-drying, for example, the water-containing waste may be exposed to hot air while being gradually conveyed by a hair dryer, or the water-containing waste may be gradually dropped from a direction facing the airflow.
この後、予備乾燥室28で水分がある程度除去された汚
泥は、高温乾燥室31に送られる。この高温乾燥室31
には焼却炉32からの排ガスが導入され200〜600
℃の高温ガスによって完全に乾燥するようになっている
。Thereafter, the sludge from which some moisture has been removed in the pre-drying chamber 28 is sent to the high-temperature drying chamber 31. This high temperature drying room 31
Exhaust gas from the incinerator 32 is introduced into the
It is designed to be completely dried using high-temperature gas at ℃.
一方、この高温乾燥室31によって完全に乾燥した汚泥
は一部が上記焼却炉32の燃料として使用され、他の乾
燥汚泥は肥料あるいは他の燃料として使用される。On the other hand, a part of the sludge completely dried in the high-temperature drying chamber 31 is used as fuel for the incinerator 32, and the other dried sludge is used as fertilizer or other fuel.
この場合、他の燃料として使用する場合には、上記予備
乾燥された汚泥を一定の型に入れて成形した後、上記高
温乾燥室31に入れることも可能である。また、肥料と
して使用する場合には上記高温乾燥室31から排出され
る汚泥と焼却炉32から排出される灰とを混合すること
も可能である上記実施例においては、−旦放流水をブー
ル22に入れて熱媒である水に熱を伝導するようにした
が、直接ブール22の中に熱交換用のパイプを入れてフ
ロン等からなる熱媒■を加熱するすることも可能であり
、更には滅菌室15の中に熱交換用のパイプを配置し、
上記ブール22を省略することも可能である。In this case, if the sludge is to be used as another fuel, the pre-dried sludge may be placed in a certain mold and shaped, and then placed in the high-temperature drying chamber 31. Furthermore, when used as fertilizer, it is also possible to mix the sludge discharged from the high temperature drying chamber 31 with the ash discharged from the incinerator 32. Although it is possible to directly insert a heat exchange pipe into the boule 22 to heat a heat medium made of chlorofluorocarbon or the like, A heat exchange pipe is placed in the sterilization chamber 15,
It is also possible to omit the Boolean 22 described above.
また、熱媒■の圧縮機を回転されるモータとして第2図
に示すようにガスタンク18に貯留されたメタンガスを
燃料とするタービンあるいはガスエンジンで回転させる
ことも可能であり、更にはポンプ23及び熱風ファン3
3の回転駆動源を上記ガスを燃料とするタービンあるい
はエンジン等の熱機関で回転させることも可能である。It is also possible to rotate the compressor of the heat medium (1) by a turbine or gas engine that uses methane gas stored in the gas tank 18 as fuel, as shown in FIG. hot air fan 3
It is also possible to rotate the rotational drive source No. 3 with a heat engine such as a turbine or an engine that uses the above gas as fuel.
なお、上記高温乾燥室31からの排ガスは上記焼却炉3
2の予熱空気の加熱源としても良いし、あるいは予備乾
燥室28に送られる空気を更に高温にするための熱源と
して使用することも可能であり、上記ガスを燃料とした
熱機関を使用した場合には、該機関の排気ガスの保有す
る熱及び冷却水の保有する熱を他の熱源としてを効利用
することが可能である。Note that the exhaust gas from the high temperature drying chamber 31 is transferred to the incinerator 3.
It can be used as a heat source for the preheated air in step 2, or it can be used as a heat source to further raise the temperature of the air sent to the pre-drying chamber 28. When a heat engine using the above gas as fuel is used. In this case, it is possible to effectively utilize the heat possessed by the exhaust gas and the heat possessed by the cooling water of the engine as other heat sources.
上記の如く構成することによってプール22から放流さ
れる排水の温度は若干下がることになるなお、上記予備
乾燥の後に、上記ガスを燃料とする遠赤外線を発するヒ
ーターを設け、該ヒーターによって乾燥する乾燥機を設
けることも可能である。By configuring as described above, the temperature of the wastewater discharged from the pool 22 is slightly lowered. Furthermore, after the preliminary drying, a heater that emits far infrared rays using the gas as fuel is provided, and the drying process is performed by the heater. It is also possible to provide a machine.
請求の範囲第1項記載の含水固形物の乾燥方法は以上の
説明からも明らかなように、下水処理設備から発生ずる
放流水の熱を有効に利用して含水固形物の乾燥を行って
いるので、従来、重油等の燃料が不要となる。As is clear from the above description, the method for drying water-containing solids according to claim 1 effectively utilizes the heat of discharged water generated from sewage treatment equipment to dry water-containing solids. Therefore, conventional fuel such as heavy oil is not required.
更には、下水処理設備からの排水の温度が下がるので、
これに伴う温排水の問題が無くなる。Furthermore, the temperature of wastewater from sewage treatment equipment decreases,
This eliminates the problem of hot water drainage.
請求の範囲第2項記載の含水固形物の乾燥方法において
は、ヒートポンプの動力源に該下水処理設備から発生す
るガスを燃料とする熱機関によって回転駆動されている
ので、より外部からの燃料等あるいは電気等を使用する
ことなく設備の運転が行える。In the method for drying a water-containing solid material as set forth in claim 2, since the heat pump is rotationally driven by a heat engine that uses gas generated from the sewage treatment equipment as fuel, the heat pump is rotated by a heat engine that uses gas generated from the sewage treatment equipment as fuel, so that it is possible to use more external fuel, etc. Alternatively, equipment can be operated without using electricity or the like.
第1図は本発明に係る含水固形物の乾燥方法を適用した
装置の概略ブロック図、第2図は従来例に係る下水処理
設備の概略ブロック図である。
〔符号の説明]FIG. 1 is a schematic block diagram of an apparatus to which the method for drying water-containing solids according to the present invention is applied, and FIG. 2 is a schematic block diagram of a conventional sewage treatment facility. [Explanation of symbols]
Claims (2)
ポンプを使用して回収し、該回収した熱によって空気を
加温し、該加温した空気によって上記下水処理設備から
発生する含水固形物を乾燥することを特徴とする含水固
形物の乾燥方法。(1) Use a heat pump to recover the retained heat of the wastewater generated from the sewage treatment equipment, heat the air with the recovered heat, and use the heated air to remove the hydrated solids generated from the sewage treatment equipment. A method for drying a water-containing solid material.
るガスを燃料とする熱機関である請求の範囲第1項記載
の含水固形物の乾燥方法。(2) The method for drying water-containing solids according to claim 1, wherein the power source of the heat pump is a heat engine that uses gas generated from sewage treatment equipment as fuel.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1035309A JPH02214599A (en) | 1989-02-14 | 1989-02-14 | Method for drying water-containing solid |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1035309A JPH02214599A (en) | 1989-02-14 | 1989-02-14 | Method for drying water-containing solid |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH02214599A true JPH02214599A (en) | 1990-08-27 |
Family
ID=12438195
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1035309A Pending JPH02214599A (en) | 1989-02-14 | 1989-02-14 | Method for drying water-containing solid |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH02214599A (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH06343996A (en) * | 1993-06-07 | 1994-12-20 | Toa Kankyo Service Kk | Sludge treatment device |
| CN104788004A (en) * | 2015-04-14 | 2015-07-22 | 南通天蓝环保能源成套设备有限公司 | Sludge low-temperature drying device |
| CN107285593A (en) * | 2017-07-06 | 2017-10-24 | 四川天润德环境工程有限公司 | A kind of sewage source heat pump and equipment associated with sludge drying |
-
1989
- 1989-02-14 JP JP1035309A patent/JPH02214599A/en active Pending
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH06343996A (en) * | 1993-06-07 | 1994-12-20 | Toa Kankyo Service Kk | Sludge treatment device |
| CN104788004A (en) * | 2015-04-14 | 2015-07-22 | 南通天蓝环保能源成套设备有限公司 | Sludge low-temperature drying device |
| CN107285593A (en) * | 2017-07-06 | 2017-10-24 | 四川天润德环境工程有限公司 | A kind of sewage source heat pump and equipment associated with sludge drying |
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