TW588019B - Method for treatment of waste water by contacting activated sludge with sarcosine compounds - Google Patents

Method for treatment of waste water by contacting activated sludge with sarcosine compounds Download PDF

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Publication number
TW588019B
TW588019B TW090106617A TW90106617A TW588019B TW 588019 B TW588019 B TW 588019B TW 090106617 A TW090106617 A TW 090106617A TW 90106617 A TW90106617 A TW 90106617A TW 588019 B TW588019 B TW 588019B
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Taiwan
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sludge
activated sludge
treatment
sarcosine
waste water
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TW090106617A
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Chinese (zh)
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Toshio Ide
Akio Tamada
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Shikoku Chem
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    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00Biological treatment of water, waste water, or sewage
    • C02F3/02Aerobic processes
    • C02F3/12Activated sludge processes
    • 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
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/10Biological treatment of water, waste water, or sewage

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  • Life Sciences & Earth Sciences (AREA)
  • Biodiversity & Conservation Biology (AREA)
  • Microbiology (AREA)
  • Hydrology & Water Resources (AREA)
  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Activated Sludge Processes (AREA)

Abstract

The purpose of the present invention is to provide a treating method of waste water which enables forming activated sludge which allows excellent sedimentation and satisfactory treated water quality and reducing the amount of excess sludge generation. Sarcosine compounds are brought into contact with the activated sludge.

Description

588019 五、發明說明(1) [發明所屬 本發明係 設施中,形 之活性污泥 理較容易之 【習知之技 廢水處理 產生量之先 藥劑加入活 污泥與節省 7,1996 ) ° 有以高分子 等無機系凝 5-253589 號 的後段上設 各種活性污 道,Vol·21 生態研究會 上述之處 餘污泥的產 ,然而,其 之技術領域 關於一種在 成壓密性較 ,並且謀求 廢水處理方 術】 设加l中,形 前技術,眾 性污泥之方 能源」,田 另外,作為 凝集劑等之 集劑的添加 公報〕。再 置消化槽, 泥法中之污 ,No· 2, 1997 編,微生物 理方法,為 生量,嘗試 並不一定可 法 用等經濟性的問題。又 劑,具備有減少污泥容 果,但是,其並不能減 產業廢水處理設施和公共廢水處理 高之污泥凝聚,及形成沈積性優越 減少剩餘污泥的產生量,及維持管 成良好活性污泥及減少剩餘污中 所皆知係將微生物劑或酵素劑等 法,〔例如,「微生物處理中戏, 代榮一,節省能源,V 〇 1. 4 8, 夕 剩餘污泥之減量化的方法,被 0· 有機系凝集劑或聚氯化鋁、辟$案 f法,〔例如,曰本專利特;=1呂 ’藉由生物薄膜法或在活性、、〜 以謀求污泥的減量化,〔「 ’亏泥 /尼產生量」,界好雄,月刊下關在 •或者「進行變動和控制」微^水 之生態1 1,學會出版中心〕。物 了維持良好微生物活性,及滅I 以微生物劑或酵素劑等筚添 夕剩 以獲得滿足的效果,有產以加 二高分子凝集劑等之各種各樣^費 里,及提高沈積性之特點之停,集 J 5泥之產生量,也並不能提二2588019 V. Description of the invention (1) [In the facility of the invention to which the invention belongs, the activated sludge that is shaped is easier to be treated. [The conventional technology to generate the amount of wastewater produced by the prior treatment of wastewater is added to the activated sludge and saved 7,1996) ° Various types of activated sludges are set on the rear section of polymer-based inorganic system Ning No. 5-253589. The Vol · 21 Ecological Research Society mentioned above produces waste sludge. However, its technical field is about Seeking Wastewater Treatment Alchemy] Let's add a medium, a pre-form technology, a universal energy source of sludge ", Tian Tian, Additive Bulletin as an aggregating agent, etc.]. Then set up digestion tank, dirt in mud method, No. 2, 1997, microbiology method, for the amount of energy, try and may not be economically applicable. It also has the ability to reduce the capacity of sludge, but it can not reduce the sludge aggregation in industrial wastewater treatment facilities and public wastewater treatment, and it has excellent sedimentability to reduce the amount of excess sludge generated and maintain good tube formation activity. What is known in sludge and reduction of residual sewage is the method of using microbial agents or enzymes, [for example, "microbial treatment of Chinese opera, Dai Rongyi, energy saving, V 〇 1. 4 8, reduction of residual sludge Method, using organic flocculant or polyaluminum chloride as the method, [for example, Japanese patent special; = 1 Lu 'through the thin film method or the active, to reduce sludge "[" Deficiency of mud / Ni-Ni production ", Hao Xiong Xiong, monthly publication Shimonoseki or" make changes and control "micro-ecology of water 1 1, Institute of Publishing Center]. In order to maintain good microbial activity, and to reduce the use of microbial agents or enzymes, etc. to obtain the desired effect, there are a variety of high-molecular agglutinating agents, etc. to produce a variety of ferries, and improve the deposition The stop of features, the amount of mud produced by J 5 cannot be mentioned.

588019 五、發明說明(5) 槽内的剩餘污泥的減低率、及在SVI的指標中所表示之污 泥的沈積性及B0D除去率,以得嘴志料叙u 瓦干 以使凋查對廢水的處理能力的 影響力。 上述的試驗結果如表丨所示’由於添加肌 結果,可對剩餘污泥飛躍性的诘少。s^ 他隹注的减)。另外,可提高污泥的 沈私性’且B 0 D除去率也維括;士淮 、,γ 干也、再符问水準,亚可了解到對廢水 處理機能並未有阻害。 表1 添加劑 剩餘污泥的減低 率(°/〇) SV I (m 1 /g) B 0 D除去率 (%) 肌氨酸 35 152 97 肌氨酸鈉 33 155 ------ 98 肌氨酸鹽酸鹽 28 150 98 無 一 161 97 〔實施例2〕 -- ——-—— 在貫施例1中,肌氨酸鈉的添加濃度對曝氣槽的污泥重 量,以每1日量分別為〇.〇1及5重量%的比率加入廢水之 驗結果,如表2所示。 如依該試驗結果,添加濃度為0 01重量%時,剩餘污泥 僅稍微減低,添加濃度未及〇. 01重量%時,就無法預期 好的添加效果。 另一方面,5重量%的添加量,可得知有顯著污泥的減 低效果,但BOD除去率稍微減低。因此,如超過5重量%時 ,廢水處理機能會降低所以不佳。 、588019 V. Description of the invention (5) The reduction rate of the remaining sludge in the tank, and the sedimentability and BOD removal rate of the sludge indicated in the SVI index, in order to obtain the information about the dryness of the tiles and make the investigation Impact on wastewater treatment capacity. The test results described above are shown in Table 丨 'As a result of the addition of muscles, the residual sludge can be greatly reduced. s ^ he bet on minus). In addition, the intimacy of sludge can be improved, and the removal rate of B 0 D is also covered; Shihuai, γgan also meets the standards, and Yake understands that there is no obstacle to the wastewater treatment function. Table 1 Reduction rate of additive residual sludge (° / 〇) SV I (m 1 / g) B 0 D removal rate (%) Sarcosine 35 152 97 Sodium sarcosine 33 155 ------ 98 muscle Amino acid hydrochloride 28 150 98 None 161 97 [Example 2] ---------- In the first embodiment, the concentration of sodium sarcosine added to the sludge weight of the aeration tank, per 1 Table 2 shows the results of adding waste water at daily ratios of 0.01 and 5% by weight. According to the results of this test, when the added concentration is 0.011% by weight, the remaining sludge is only slightly reduced, and when the added concentration is less than 0.01% by weight, a good addition effect cannot be expected. On the other hand, it was found that the addition amount of 5% by weight had a significant sludge reduction effect, but the BOD removal rate was slightly reduced. Therefore, if it exceeds 5% by weight, the performance of the wastewater treatment is lowered, which is not preferable. ,

五、發明說明(6) 表2V. Description of the invention (6) Table 2

實施例3〕Example 3]

泥的減低率 SVI(ml/g) BOD除去率 (%) -~~~~---- (°/〇) ______ 160 97 33 ----~-~~一- 155 98 42 150 90 一 161 97 咸低剩餘污泥試驗。在同工廠的處理 叹施中’其運作條件,係以水量為丨〇 〇 〇m3 /曰,曝氣槽容 積為 1 0 0 0 m3 ’ 沈殿槽為 6〇〇 m3,心%為5〇〇〇[11§/1,b〇d 污 泥負荷為0· 20〜〇· 25kg-BOD/kg-SS。試驗期間為4個月, 刖面2個月’調查未添加肌氨酸鈉時的處理狀況,後面2個 月’以一週投與1次之比率,將肌氨酸鈉佔曝氣槽污泥重 量之1重量%之3 0 k g加入曝氣槽内,比較投入前後之廢水 的處理狀況。 上述的試驗結果如表3所示,脫水塊狀物的產生量在投 入後減低為27 %。又,BOD去除等之處理能力及污泥的沈 積性具有明顯改善傾向。 C:\2D-CODE\90-06\90106617.ptd 第9頁 588019 五、發明說明(7) 表3 分析項目 藥劑投入前(2個月 藥劑投入後(2個月 1)__ 流入水 處理水 去除率 流入水 處理水 去除率_ pH 7.3 7.4 7.3 7.3 BOD(mg/1) 940 26 97.2 950 15 98.4 COD(mg/1) 320 25 92.2 380 19 95 MLSS(mg/1) 5200 5100 SV30(%) 98 88 SVI(ml/g) 188 173 脫水塊狀物產生量(kg/曰) 4800 3500(減低率 27.1%) 脫水塊狀物含水率(% ) 87.8 85.5 脫水塊狀物固形分(kg/曰) 586 508 BOD污泥變化率(%) 62.3 53.4Sludge reduction rate SVI (ml / g) BOD removal rate (%)-~~~~ ---- (° / 〇) ______ 160 97 33 ---- ~-~~ -1-155 98 42 150 90 1 161 97 Salty low residual sludge test. In the same factory treatment, "the operating conditions are based on the water volume of 1000 m3 / said, the volume of the aeration tank is 1000 m3," the Shen Dian trough is 600 m3, and the heart% is 500. 〇 [11§ / 1, b〇d The sludge load was 0.220 ~ 0.25 kg-BOD / kg-SS. The test period was 4 months, and the surface of the noodles was investigated for 2 months 'without the addition of sarcosinate, and the next 2 months' was administered once a week at a rate of sarcosine in the aeration tank sludge 30 kg of 1% by weight is added to the aeration tank to compare the treatment status of wastewater before and after the input. The above test results are shown in Table 3. The amount of dehydrated lumps was reduced to 27% after the injection. In addition, the processing capacity of BOD removal and the like and the sludge depositability tend to be significantly improved. C: \ 2D-CODE \ 90-06 \ 90106617.ptd Page 9 588019 V. Description of the invention (7) Table 3 Before analysis of the project's pharmaceutical input (2 months after the pharmaceutical input (2 months 1)) __ Inflow water treatment water Removal rate Inflow water treatment water removal rate_ pH 7.3 7.4 7.3 7.3 BOD (mg / 1) 940 26 97.2 950 15 98.4 COD (mg / 1) 320 25 92.2 380 19 95 MLSS (mg / 1) 5200 5100 SV30 (%) 98 88 SVI (ml / g) 188 173 Dehydrated block production (kg / day) 4800 3500 (reduction rate 27.1%) Dehydrated block water content (%) 87.8 85.5 Dehydrated block solid content (kg / day) 586 508 BOD sludge change rate (%) 62.3 53.4

(注)B0D污泥變化率:脫水塊狀物固形分/流入水中的 B0D 〔實施例4〕 以流入水量為8 0 0 0 m3 /日、曝氣槽容積為3 0 0 0 m3、及 MLSS 為 2 0 0 0mg/l 之B0D 污泥負、荷為 0· 2kg-B0D/kg-SS 所運轉 之下水道處理場中,將肌氨酸納對曝氣槽污泥重量以每曰 0 · 1重量%之比率,利用定量泵連續加入污泥的回送線 内。 比較肌氨酸鈉投入前後的各2個月的廢水處理狀況之結 果,如表4所示。 如依所獲得試驗結果,具有明顯的剩餘污泥減低之效 果。(Note) Change rate of B0D sludge: solid content of dehydrated block / B0D of inflow water [Example 4] Inflow water volume is 8 0 0 0 m3 / day, aeration tank volume is 3 0 0 0 m3, and MLSS B0D sludge with a load of 2 0 0 0 mg / l and a load of 0.2 kg-B0D / kg-SS were run in a sewer treatment plant. Sodium sarcosine was added to the aeration tank sludge at a weight of 0 · 1 per day. The ratio of weight% is continuously added to the sludge return line by means of a fixed-rate pump. Table 4 shows the results of comparing the wastewater treatment status for each two months before and after the administration of sodium sarcosinate. According to the test results obtained, it has obvious effects of reducing the remaining sludge.

C:\2D-CODE\90-06\90106617.ptd 第10頁 588019 五、發明說明(8) 又,藥劑的投入前後,用顯微鏡觀察活性污泥相,投入 後絲狀細菌和放射線ii較少,另一方面,p h丨1 〇 ^丨n a和 vorti cel la等良性的後生動物與原生動物具有增殖現象。 即添加肌氨酸納之結果,可得知廢水處理中由於有用的高 次微生物的增殖,因而可加強活性污泥的捕食作用,促進 剩餘污泥的減量化。 表4 分析項目 藥劑投入前(2個月 藥劑投入後(2個月 ) 流入水 處理水 去除率 流入水 處理水 去除率 pH 6.8 7 6.8 7 B〇D(mg/1) 150 5 96.7 165 4 97.6 C0D(mg/l) 125 4 96.8 133 4 97_ MLSS(mg/l) 2000 1900 _ SV30(%) 26 24 _ SVI(ml/g) 130 126 _ 脫水塊狀物產生量(kg/曰) 5210 3880(減低率25 _—- 脫水塊狀物含水率(%) 79.5 78.1 脫水塊狀物固形分(kg/曰) 1068 850(減低率 20.4@i_ Philodina - vort icel la + _ + + _— Epi stylis + .+ + + 一 放射線菌3) + — _—-— 絲狀細菌(021N) + (注)-未發現 +少 + +較多 + + +相當多C: \ 2D-CODE \ 90-06 \ 90106617.ptd Page 10 588019 V. Description of the invention (8) In addition, before and after the dosage of the agent, observe the activated sludge phase with a microscope, there are fewer filamentous bacteria and radiation ii after the dosage. On the other hand, benign metazoans and protozoa such as ph 丨 1 〇 ^ 丨 na and vorti cel la have proliferation phenomena. That is, as a result of the addition of sarcosine, it can be known that in the wastewater treatment, due to the proliferation of useful higher-order microorganisms, the predation effect of activated sludge can be enhanced, and the reduction of excess sludge can be promoted. Table 4 Analysis project before pharmaceutical input (2 months after pharmaceutical input (2 months) Inflow water treatment water removal rate Inflow water treatment water removal rate pH 6.8 7 6.8 7 BOD (mg / 1) 150 5 96.7 165 4 97.6 C0D (mg / l) 125 4 96.8 133 4 97_ MLSS (mg / l) 2000 1900 _ SV30 (%) 26 24 _ SVI (ml / g) 130 126 _ Dehydrated mass production (kg / day) 5210 3880 (Reduction rate 25 _—- Dehydrated block moisture content (%) 79.5 78.1 Dehydrated block solid content (kg / day) 1068 850 (Reduction rate 20.4@i_ Philodina-vort icel la + _ + + _ — Epi stylis +. + + + A radioactive bacterium 3) + — _ —- — filamentous bacteria (021N) + (Note)-not found + less + + more + + + quite a lot

C:\2D-CODE\90-06\90106617.ptd 第11頁 588019 五、發明說明(9) 【發明之效果】 依據本發明方法,使活性污泥接觸肌氨酸系化合物,由 於活性污泥之捕食作用的提高結果,因而可提高廢水處理 的能力,另外,能夠對剩餘污泥的產生量有飛躍性的減 低,並對廢水處理設備之維持管理較容易,並且可以大幅 降低維持管理的費用。C: \ 2D-CODE \ 90-06 \ 90106617.ptd Page 11 588019 V. Description of the invention (9) [Effects of the invention] According to the method of the present invention, the activated sludge is brought into contact with sarcosine compounds. As a result of the increase in predation, the capacity of wastewater treatment can be improved. In addition, the amount of excess sludge can be reduced drastically, and the maintenance and management of wastewater treatment equipment is easier, and the cost of maintenance and management can be greatly reduced .

C:\2D-raDE\90-06\90106617.ptcl 第12頁 588019 圖式簡單說明 C:\2D-CODE\90-06\90106617.ptd 第 13 頁C: \ 2D-raDE \ 90-06 \ 90106617.ptcl page 12 588019 Schematic description C: \ 2D-CODE \ 90-06 \ 90106617.ptd page 13

Claims (1)

588 pl9— 修 yy. 90106617 年月日 修正 替換 ........ 範贵一 1. 一種廢水處理方法,其特徵為,當使活性污泥接觸肌 氨酸系化合物,對於活性污泥(固形換算),每1日以肌氨 酸系化合物0. 01〜5重量%的比例接觸。588 pl9— Repair yy. Correction and replacement on the date of 90106617 ... Fan Guiyi 1. A method of wastewater treatment, characterized in that when activated sludge is contacted with sarcosine-based compounds, for activated sludge 01〜5 重量 % 的 比 接触。 (Solid conversion), every 1 day with a sarcosine-based compound 0. 01 ~ 5% by weight ratio of contact. \\A326\總檔\90\90106617\90106617(替換)-l.ptc 第14頁\\ A326 \ Total files \ 90 \ 90106617 \ 90106617 (replace) -l.ptc Page 14
TW090106617A 2000-03-21 2001-03-21 Method for treatment of waste water by contacting activated sludge with sarcosine compounds TW588019B (en)

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JPS588919B2 (en) * 1975-08-23 1983-02-18 イデミツコウサン カブシキガイシヤ Odei Hensei Taino Seizouhouhou
JPS61197094A (en) * 1985-02-25 1986-09-01 Idemitsu Petrochem Co Ltd Treatment of waste water
DE3902626C2 (en) * 1989-01-30 1994-12-22 Schreiber Berthold Processes for biological wastewater treatment
JP3167021B2 (en) * 1998-06-10 2001-05-14 環境エンジニアリング株式会社 Method for treating organic wastewater and chemicals used in the method

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