JPS62160200A - Pressure type activated sludge system - Google Patents
Pressure type activated sludge systemInfo
- Publication number
- JPS62160200A JPS62160200A JP61001928A JP192886A JPS62160200A JP S62160200 A JPS62160200 A JP S62160200A JP 61001928 A JP61001928 A JP 61001928A JP 192886 A JP192886 A JP 192886A JP S62160200 A JPS62160200 A JP S62160200A
- Authority
- JP
- Japan
- Prior art keywords
- power
- gas
- activated sludge
- fuel
- energy
- 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
- 239000010802 sludge Substances 0.000 title claims description 8
- 239000010865 sewage Substances 0.000 claims description 5
- 238000006243 chemical reaction Methods 0.000 claims description 3
- 239000002351 wastewater Substances 0.000 claims description 3
- 238000011084 recovery Methods 0.000 claims description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 16
- 238000000034 method Methods 0.000 abstract description 8
- 239000000446 fuel Substances 0.000 abstract description 7
- 238000002485 combustion reaction Methods 0.000 abstract description 5
- 239000007789 gas Substances 0.000 description 12
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 3
- 239000003245 coal Substances 0.000 description 3
- 238000002347 injection Methods 0.000 description 3
- 239000007924 injection Substances 0.000 description 3
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- 239000004568 cement Substances 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000003208 petroleum Substances 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- 239000003570 air Substances 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 238000009841 combustion method Methods 0.000 description 1
- 230000018044 dehydration Effects 0.000 description 1
- 238000006297 dehydration reaction Methods 0.000 description 1
- 229910001873 dinitrogen Inorganic materials 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000003337 fertilizer Substances 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 239000003921 oil Substances 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 230000001172 regenerating effect Effects 0.000 description 1
- 239000012783 reinforcing fiber Substances 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000013589 supplement Substances 0.000 description 1
- 238000004065 wastewater treatment Methods 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
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/10—Biological treatment of water, waste water, or sewage
Landscapes
- Exhaust Gas After Treatment (AREA)
- Activated Sludge Processes (AREA)
Abstract
Description
【発明の詳細な説明】
活性汚泥システムは汚水処理の有力な方法である。これ
を更に高効率化し、またコンパクトにするため、近年デ
ィープシャフトプロセスと称する深井戸状の孔で、高圧
で反応せしめるシステムが開発されている。これは高圧
にすることにより、水中の酸素の分圧も高くなり、反応
が促進され圧力が10気圧程度で10倍近くになってい
る。この場合は深井戸を屁ることか必要であり、また排
気としての過剰空気や炭酸ガス、窒素ガスなどは、その
まま大気圧に棄てられて、貴重な圧力エネルギーが無ダ
になっている。もちろん一部は汚水の循環動力となって
いるが、極めて効率の悪いものであり、また深井戸が地
質の関係などで困難で経費を要する場合もある。DETAILED DESCRIPTION OF THE INVENTION Activated sludge systems are a promising method of wastewater treatment. In order to make this process even more efficient and compact, a system called the deep shaft process has been developed in recent years, in which the reaction is carried out at high pressure in a deep well-shaped hole. By increasing the pressure, the partial pressure of oxygen in the water also increases, promoting the reaction and increasing the pressure nearly 10 times to around 10 atmospheres. In this case, it is necessary to fart into a deep well, and the excess air, carbon dioxide, nitrogen gas, etc. that are exhausted are simply dumped into atmospheric pressure, wasting valuable pressure energy. Of course, some of this is used to circulate sewage, but it is extremely inefficient, and deep wells may be difficult and expensive due to geological conditions.
また処理の結果発生するスラッチの処理は、別途に複雑
なシステムを要し、コストが高く経済性がよくない。Further, processing of slatch generated as a result of processing requires a separate complicated system, which is high in cost and not economical.
本発明舎よ・、これらを改善するものであって、排ガス
中の過剰空気を利用して、この内に燃料を噴射して燃焼
せしめて高圧高温ガスを製り、これをガスタービンに、
導いて動力を発生し、この動力によってコンプレッサー
やポンプを駆動でき、加圧による余分な動力四の負担が
ない°。さらに余剰の動力は、その他の種々の用途に使
泪できる。The inventor of this invention aims to improve these by making use of the excess air in the exhaust gas, injecting fuel into it and combusting it to produce high-pressure, high-temperature gas, which is then used to power the gas turbine.
This power can be used to drive compressors and pumps, eliminating the burden of extra power due to pressurization. Furthermore, the surplus power can be used for various other purposes.
また活性汚泥法での発生スラッチ、今までは炉床で焼却
したり、肥料化したり種々の方法が試みられている。こ
の焼却は充分乾煙しないと自燃せず、その脱水乾釉プロ
セスが問題である。本発明では積極的に石油、ガス、石
炭などで助燃しても、このエネルギーは有効に動力とし
て活用されるので、動燃量を増大できて、未乾燥の含水
スラッチでも完全に焼却できる。この場合ふつうの助燃
法だけでなく、COMやCIA/Hのように、含水スラ
ッチ中に石油や石炭微粉を均一に混合して燃焼せしめる
こともできるうさらに排気のみならず、処理済みの汚水
の圧力エネルギーも、これを水力タービンに導いて動力
回収して、給水ポンプの駆動に活用ザるものとする。In addition, various methods have been tried to deal with the sludge produced in the activated sludge method, such as incinerating it in a hearth or turning it into fertilizer. This incineration does not self-combust unless it is sufficiently dried and smoked, and the dehydration and dry glazing process is a problem. In the present invention, even if oil, gas, coal, etc. are actively used to supplement combustion, this energy is effectively utilized as motive power, so the amount of dynamic fuel can be increased, and even undried water-containing sludge can be completely incinerated. In this case, in addition to the usual auxiliary combustion method, it is also possible to use COM and CIA/H, which uniformly mix petroleum or coal powder in the water-containing slatch and combust it. Pressure energy will also be guided to a hydraulic turbine to recover the power and be used to drive the water supply pump.
つぎに本方式では大量の空気が有効に働き、充分な過剰
空気が経済的に存在できているので、ふつうの活性汚泥
法では除去できない窒素分も、本システムでは相当部分
を減少できるう
つぎに図面によって詳細を説明すると、第1図において
、これは本発明の全体構造図であって、1′は汚水処理
用の反応器である。Next, in this system, a large amount of air works effectively and a sufficient amount of excess air can exist economically, so this system can reduce a considerable portion of the nitrogen content that cannot be removed with ordinary activated sludge methods. To explain the details in detail, FIG. 1 is an overall structural diagram of the present invention, and 1' is a reactor for treating sewage.
この反応器lの圧力は、ふつう10気圧前後とする。こ
のGM ?j9としては、細径の塔状圧力容器や、細径
の背の低い圧力容器の多数のハチの尖状の集合体や、ま
た圧力容器自身も、近年発達したセメント技術を利用し
て、セメント圧力容器とすることもできる。この内には
補強繊維としてカーボン、ガラス、スチールなどを使用
できる。図では圧力容器が3嘔の場合を示している。排
気ガスは水中で度応した後と昇し、水面より分離して頂
部に導かれる。このとき水滴が排気ガスに随伴する可能
性があるので、これを防ぐため出口に設けた2はセパレ
ータであって水滴を分離する。The pressure in this reactor I is usually around 10 atmospheres. This GM? J9 includes a small-diameter tower-shaped pressure vessel, a large number of bee-shaped aggregates of small-diameter, low-profile pressure vessels, and the pressure vessel itself is made of cement using recently developed cement technology. It can also be a pressure vessel. Carbon, glass, steel, etc. can be used as reinforcing fibers. The figure shows a case where the pressure vessel is 3 times. After the exhaust gas reacts in the water, it rises, separates from the water surface, and is led to the top. At this time, water droplets may accompany the exhaust gas, so to prevent this, a separator 2 is provided at the outlet to separate the water droplets.
これにより排気はドライガスとして出て行く。3は燃焼
室であって、この内で燃料を燃焼せしめて高温高圧ガス
とする。このとき別にスラッチ含有水噴射弁を設けて、
同時に転勤燃焼せしめることができる。またはスラッチ
含有水中にCOM 、CWMのように、石油や゛微粉炭
を一様に混合して燃焼せしめることもできる。4は燃料
噴射弁であるっ5はスラッチ含有水噴射弁である。6は
ガスタービンである。場合によってはスラッチは別途に
処理し、ガスタービンは単なる低温の排気エキスパンダ
ーとして、一部の動力回収にのみ使用し、熱焼室3をよ
めてシステムを簡素化することもできる。7は発電機で
ある。8は空気のコンプレッサーである。9は駆動電動
灘である。10はガスタービン6の排気熱を利用して、
燃焼室3えの空気を予熱する再生熱交換器である。11
は給水ポンプであって、種々の物を含んだ汚水を高圧に
するため、ダイヤフラムポンプを使用するう12は水力
タービンであって、処理済みの汚水の圧力エネルギーを
回収して、給水ポンプ11の駆動の補助をする。13は
給水ポンプ11の駆1II71電動機である。As a result, the exhaust gas exits as dry gas. 3 is a combustion chamber in which fuel is combusted to produce high-temperature, high-pressure gas. At this time, a separate slatch-containing water injection valve is installed,
At the same time, they can be transferred and fired. Alternatively, petroleum or pulverized coal may be uniformly mixed in slatch-containing water, such as COM or CWM, and then burned. 4 is a fuel injection valve and 5 is a slatch-containing water injection valve. 6 is a gas turbine. In some cases, the slatch may be treated separately, the gas turbine may be used as a mere low-temperature exhaust expander for only part of the power recovery, and the thermal combustion chamber 3 may be eliminated to simplify the system. 7 is a generator. 8 is an air compressor. 9 is a driving electric nada. 10 uses the exhaust heat of the gas turbine 6,
This is a regenerative heat exchanger that preheats the air in the combustion chamber 3. 11
12 is a water supply pump that uses a diaphragm pump to pressurize wastewater containing various substances. 12 is a water turbine that recovers the pressure energy of the treated wastewater and supplies it to the water supply pump 11. Assists with driving. 13 is a drive 1II71 electric motor of the water supply pump 11.
第1図は本発明の全体構造図である。 FIG. 1 is an overall structural diagram of the present invention.
Claims (1)
水処理システムで、排気および排水のエネルギーを利用
して動力を回収する加圧式活性汚泥システム。[Claims] A sewage treatment system in which sewage is placed in a pressurized container and activated sludge, the reaction of which is promoted by pressurized air, is applied to the sewage, and power is generated by using the energy of exhaust and wastewater. Pressurized activated sludge system for recovery.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP61001928A JPS62160200A (en) | 1986-01-08 | 1986-01-08 | Pressure type activated sludge system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP61001928A JPS62160200A (en) | 1986-01-08 | 1986-01-08 | Pressure type activated sludge system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPS62160200A true JPS62160200A (en) | 1987-07-16 |
Family
ID=11515266
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP61001928A Pending JPS62160200A (en) | 1986-01-08 | 1986-01-08 | Pressure type activated sludge system |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS62160200A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US8156662B2 (en) * | 2006-01-18 | 2012-04-17 | Earthrenew, Inc. | Systems for prevention of HAP emissions and for efficient drying/dehydration processes |
-
1986
- 1986-01-08 JP JP61001928A patent/JPS62160200A/en active Pending
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US8156662B2 (en) * | 2006-01-18 | 2012-04-17 | Earthrenew, Inc. | Systems for prevention of HAP emissions and for efficient drying/dehydration processes |
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