氧化溝外文翻譯

1、<p><b>　　外文資料翻譯</b></p><p>　　Oxidation ditches</p><p>　　1. Introduction </p><p>　　Oxidation ditch and continuous circular aeration tank, deformation is one of the a

2、ctivated sludge process. Oxidation ditch sewage treatment technology is successfully developed by the Dutch in the 1950 s and health engineering. Put into use in the Netherlands for the first time since 1954. Due to its

3、good effluent water quality, steady operation, convenient management and other technical characteristics, has been widely used both at home and abroad in domestic sewage and industrial wastewater tr</p><p>　

4、　The types of the oxidation ditch has been widely applied at present include: pass, oxidation ditch, the Carrousel oxidation ditch, Mr. Bell oxidation ditch, T oxidation ditch, three groove type oxidation ditch, and the

5、integration of DE type oxidation ditch and oxidation ditch. The oxidation ditch because of the differences on the structure and operation, so each has its characteristics. This paper will mainly introduce Carrousel’s str

6、ucture, the mechanism of the oxidation ditch, the existence q</p><p>　　2. The structure of Carrousel oxidation ditch </p><p>　　Carrousel oxidation ditch is DHV Company developed in 1967 by the D

7、utch. On the basis of the original Carrousel oxidation ditch DHV EIMCO it’s patented in the United States Company and created the Carrousel 2000 System, realizes the higher requirements of biological denitrification and

8、phosphorus removal function. By far the world has more than 850Carrousel oxidation ditch and Carrousel 2000 System is running. </p><p>　　Carrousel oxidation ditch with directional control of aeration and agi

9、tation device, the mixture transfer horizontal velocity, which was stirring the mixture of circulating in the oxidation ditch channels closed. Oxidation ditch has special hydraulic flow state, therefore, has the characte

10、ristics of both the completely mixed reactor and has the characteristic of push flow reactor, groove exists obvious dissolved oxygen concentration gradient. Oxidation ditch cross section is rectangular or trape</p>

11、<p>　　3. The mechanism of Carrousel oxidation ditch </p><p>　　3.1 Carrousel oxidation ditch sewage treatment principle </p><p>　　The original Carrousel oxidation ditch process with reflu

12、x sludge sewage directly into the oxidation ditch System. Dissolved oxygen in surface aerator make mixture the DO concentration increased to about 2 ~ 3 mg/L. Under the condition of the fully mixed oxygen, get enough dis

13、solved oxygen to remove BOD microbial; at the same time, nitrate and nitrite, ammonia was oxidized to at this point, the mixture in aerobic condition. By aeration zone in the downstream of the aerator, water turbulence s

14、tat</p><p>　　3.2 Carrousel Moseley oxidation ditch the influence factors of biological nitrogen removal </p><p>　　Influence factors of phosphorus removal from Carrousel Moseley oxidation ditch i

15、s primarily a sludge age, nitrate concentration and substrate concentration. Research shows that when the total sludge age of 8 ~ 10 d, the lion's share of the activated sludge phosphorus content is 4% of the dried s

16、ludge quantity, 11% of the quality of heterotrophic bacteria, but when sludge in sludge age more than 15 d maximum phosphorus content significantly decreased, but cannot meet the maximum phosphorus remova</p><

17、p>　　4. Carrousel Moseley oxidation ditch existing problems and solutions </p><p>　　Though Carrousel Moseley oxidation ditch have effluent water quality is good, strong ability to resist impact load, high

18、efficiency of nitrogen removal and sludge is stable, power consumption province, easy to automatic control, etc. However, in the actual operation process, a series of problems still exist. </p><p>　　4.1 Slud

19、ge bulking problem </p><p>　　When carbohydrates in the waste water is more, N, P content in imbalance, low pH, high oxidation ditch in sludge load, dissolved oxygen concentration, dredge not free and easy to

20、 sludge bulking caused by filamentous bacteria sex; Non filamentous bacteria mainly in wastewater sludge bulking sludge load at high temperature is low. Microbial load is high, the bacteria absorb a large amount of nutri

21、ents, because of the low temperature, metabolic speed is slow, product storage on a large amount of hi</p><p>　　Aiming at the cause of sludge bulking, can adopt different countermeasures: caused by a lack of

22、 oxygen, high water temperature, can increase air or cut into the water to lighten the load, or decrease the MLSS (control sludge return flow), reduce oxygen demand; Such as sludge loading is too high, can improve the ML

23、SS, in order to adjust the load, when necessary to stop water, boring exposure for a period of time; Can be adjusted by adding the nitrogen fertilizer, phosphate fertilizer, mixture of </p><p>　　4.2 Bubble p

24、roblem </p><p>　　Due to water with a large number of oil, processing System can't effectively remove it completely, part of the oil concentration in the sludge, turn the brush oxygen filling mixing, prod

25、uce a large number of bubbles; The sludge age slightly long, sludge aging, also easy to produce foam. With surface spray water or remove foam deforming agent, deforming agent commonly used engine oil, kerosene, silicone

26、oil, turnover of 0.5 ~ 1.5 mg/L. By increasing the sludge concentration in aeration or reduced</p><p>　　4.3 Sludge up-floating problem </p><p>　　When the oil content in waste water is too large,

27、 qualitative light, the whole System in the process of operation can't well control the residence time in the second pond, easy cause lack of oxygen, produce sludge up-floating decay; When the aeration time is too lo

28、ng, high nitrification occurred in the pool, the nitrate concentration is high, in the second pond, prone to denitrification, produce nitrogen gas, sludge floating; In addition, the oil content in the waste water is too

29、large, the slud</p><p>　　After sludge floating water shall be suspended, break or removal of the sludge, ascertain the reason, adjust the operation. Sludge settle ability is poor, can dosing coagulant or ine

30、rt material, improve the precipitation; Such as water load should be reduced into water or step back flow; Such as the sludge particles small can decrease the aerator speed; Denitrification is found, should reduce air, i

31、ncreasing the backflow or mud; Sludge decay is found, should increase air, and clean up mud, hydra</p><p>　　4.4 And uneven velocity of sludge deposition problem </p><p>　　In Carrousel Moseley ox

32、idation ditch, for its unique mixing and processing results, the mixture must be circulating in the groove at a certain velocity. It is generally believed that the minimum flow rate should be 0.15 m/s, the average veloci

33、ty of sedimentary does not occur should be 0.3 ~ 0.5 m/s. Oxidation ditch aeration equipment generally brush turn for aeration and aeration rotary brush turns the submerged depth of 250 ~ 300 mm, submerged depth of the w

34、heel is 480 ~ 530 mm. With oxidation </p><p>　　Upstream or downstream equipped with guide plate is to improve the velocity distribution, the effective method to improve aerobic capacity, and the most conveni

35、ent measures. Guide plate installed upstream from the rotary axis of turn (brush) 4.0 (upstream), the guide plate height of water depth of 1/5 ~ 1/6, and perpendicular to the surface installation; Downstream of the guide

36、 plate is installed in is apart from the wheel turn (brush) axis of 3.0 m. Guide plate material can be made of metal or </p><p>　　In addition, through setting underwater in the aerator upstream driver can al

37、so turn on aeration brush at the bottom of the low speed region mixture flow circulation play a positive role, so as to solve oxidation ditch of velocity is low, the sludge sedimentation problem. Set the underwater vehic

38、le is dedicated to promoting mixture operation mode of oxidation ditch can be more flexible; to save energy and improve efficiency is of great significance. </p><p>　　5. The development of Carrousel oxidatio

39、n ditch </p><p>　　Due to biological nitrogen removal in sewage treatment standard requirements more and stricter, Carrousel Moseley oxidation ditch also got further development. At present, the research and

40、application more consists of the following two types: type micro porous aeration Carrousel 2000 System, Carrousel 3000 System. </p><p>　　5.1 Microporous aeration Carrousel 2000 System </p><p>　　

41、Microporous aeration Carrousel 2000 System using Microporous aeration (oxygen supply equipment for blower), the Microporous aeration device can produce a large number of tiny air bubble diameter of 1 mm or so, which grea

42、tly improved the bubble surface area, and makes the pool volume increase certain cases total oxygen transfer (such as pool depth increases the mass transfer efficiency will be higher). According to the current technical

43、ability of blower manufacturer, pool the effective depth of </p><p>　　5.2 Carrousel 3000 System </p><p>　　Carrousel 3000 System is in front of the Carrousel 2000 System combined with a biologica

44、l selection area. The biological selection area is the screening of strains with high organic load, suppress the growth of filamentous bacteria, and improve the removal rate of each pollutant, the subsequent process prin

45、ciple with Carrousel 2000 System. </p><p>　　Carrousel 's considerable improvement in performance in 3000 Systems: one is to increase the pool is deep, can reach 7.5 ~ 8 m, concentric circles type, wall s

46、haring, reduce cover an area of an area, reduce cost and at the same time could improve the ability of resistance to low temperature (up to 7 ℃); Second, the clever design of the aeration equipment, table under exposure

47、machine installation guide tube, suction oxygen mixture, using underwater propeller flow problem; Three is the use of the</p><p>　　6. Conclusion </p><p>　　Carrousel oxidation ditch due to the ph

48、osphorus denitrogenation ability, with good resistance to impact load capacity and convenient operation and management, has been widely used. But due to the development of science and technology and the progress of the s

49、ociety, the technology will further improve. The author thinks: Carrousel Moseley oxidation ditch of future research will be mainly reflects in the following respects. </p><p>　　1) Combined with biological m

50、embrane method, research and development model organism Carrousel Moseley oxidation ditch. Amount of microorganisms which can not only improve unit reactor, thereby increasing organic load, and the biofilm itself </p&

51、gt;<p>　　With A built-in A/O System to strengthen the denitrification effect. </p><p>　　2) Improve Carrousel Moseley oxidation ditch in the activity of microorganisms. Such as add EM specificity in th

52、e oxidation ditch, put iron make microorganism domestication into biological iron and activated carbon increase zoogloea form and improve resistance to toxic shock, etc. </p><p>　　3) Improve the Carrousel Mo

53、seley oxidation ditch equipment performance and monitoring technology. Improve the performance of table exposure machine, underwater propeller, reduce maintenance workload; using multi-objective monitoring technology suc

54、h as DO and ORP and frequency conversion technology is the future Carrousel Moseley oxidation ditch science run way. </p><p>　　4) Improve Carrousel Moseley oxidation ditch can cold resistant, high toxicity,

55、reduce area and project cost. Membrane theory application, deep water power condition and the process performance of hardy in order to reduce the project cost, improving the resistance to toxicity can provide the possibl

56、e direction. </p><p><b>　　中文翻譯</b></p><p><b>　　氧化溝</b></p><p><b>　　1.前言</b></p><p>　　氧化溝又名連續(xù)循環(huán)曝氣池，是活性污泥法的一種變形。氧化溝污水處理工藝是20世紀50年代由荷蘭衛(wèi)

57、生工程研究所研制成功的。自從1954年在荷蘭的首次投入使用以來。由于其出水水質(zhì)好、運行穩(wěn)定、管理方便等技術(shù)特點，已經(jīng)在國內(nèi)外廣泛的應(yīng)用于生活污水和工業(yè)污水的治理。</p><p>　　目前應(yīng)用較為廣泛的氧化溝類型包括：帕斯韋爾氧化溝、卡魯塞爾氧化溝 、奧貝爾氧化溝、T型氧化溝（三溝式氧化溝）、DE型氧化溝和一體化氧化溝。這些氧化溝由于在結(jié)構(gòu)和運行上存在差異，因此各具特點。本文將主要介紹卡羅塞爾氧化溝的結(jié)構(gòu)、機理、

58、存在的問題及其最新發(fā)展。</p><p>　　2.卡羅塞爾氧化溝的結(jié)構(gòu)</p><p>　　卡羅塞爾氧化溝是1967年由荷蘭的DHV公司開發(fā)研制。在原卡羅塞爾氧化溝的基礎(chǔ)上DHV公司和其在美國的專利特許公司EIMCO又發(fā)明了卡羅塞爾2000系統(tǒng)，實現(xiàn)了更高要求的生物脫氮和除磷功能。至今世界上已有850多座卡羅塞爾氧化溝和卡羅塞爾 2000系統(tǒng)正在運行。</p><p&g

59、t;　　卡羅塞爾氧化溝使用定向控制的曝氣和攪動裝置，向混合液傳遞水平速度，從而使被攪動的混合液在氧化溝閉合渠道內(nèi)循環(huán)流動。因此氧化溝具有特殊的水力學(xué)流態(tài)，既有完全混合式反應(yīng)器的特點，又有推流式反應(yīng)器的特點，溝內(nèi)存在明顯的溶解氧濃度梯度。氧化溝斷面為矩形或梯形，平面形狀多為橢圓形，溝內(nèi)水深一般為2.5～4.5ｍ，寬深比為2:1，亦有水深達7m的，溝中水流平均速度為0.3m/s。氧化溝曝氣混合設(shè)備有表面曝氣機、曝氣轉(zhuǎn)刷或轉(zhuǎn)盤、射流曝氣器、導(dǎo)

60、管式曝氣器和提升管式曝氣機等，近年來配合使用的還有水下推動器。</p><p>　　3. 卡羅塞爾氧化溝的機理</p><p>　　3.1 卡羅塞爾氧化溝處理污水的原理</p><p>　　最初的普通卡羅塞爾氧化溝的工藝中污水直接與回流污泥一起進入氧化溝系統(tǒng)。表面曝氣機使混合液中溶解氧DO的濃度增加到大約2～3mg/L。在這種充分摻氧的條件下，微生物得到足夠的溶解氧

61、來去除BOD；同時，氨也被氧化成硝酸鹽和亞硝酸鹽，此時，混合液處于有氧狀態(tài)。在曝氣機下游，水流由曝氣區(qū)的湍流狀態(tài)變成之后的平流狀態(tài)，水流維持在最小流速，保證活性污泥處于懸浮狀態(tài)（平均流速>0.3m/s）。微生物的氧化過程消耗了水中溶解氧，直到DO值降為零，混合液呈缺氧狀態(tài)。經(jīng)過缺氧區(qū)的反硝化作用，混合液進入有氧區(qū)，完成一次循環(huán)。該系統(tǒng)中，BOD降解是一個連續(xù)過程，硝化作用和反硝化作用發(fā)生在同一池中。由于結(jié)構(gòu)的限制，這種氧化溝雖然可

62、以有效的去處BOD，但除磷脫氮的能力有限。</p><p>　　3.2 卡羅塞爾氧化溝除磷脫氮的影響因素</p><p>　　影響卡羅塞爾氧化溝除磷的因素主要是污泥齡、硝酸鹽濃度及基質(zhì)濃度。研究表明，當總污泥齡為8~10d時活性污泥中的最大磷含量為其干污泥量的4%，為異養(yǎng)菌體質(zhì)量的11%，但當污泥齡超過15d時污泥中最大含磷量明顯下降，反而達不到最大除磷效果。因此，一味延長污泥齡（例如20

63、d、25d、30d）是沒有必要的，宜在8~15d范圍內(nèi)選用。同時，高硝酸鹽濃度和低基質(zhì)濃度不利于除磷過程。</p><p>　　4. 卡羅塞爾氧化溝存在的問題及解決方法</p><p>　　盡管卡羅塞爾氧化溝具有出水水質(zhì)好、抗沖擊負荷能力強、除磷脫氮效率高、污泥易穩(wěn)定、能耗省、便于自動化控制等優(yōu)點。但是，在實際的運行過程中，仍存在一系列的問題。</p><p>　　

64、4.1 污泥膨脹問題</p><p>　　當廢水中的碳水化合物較多，N、P含量不平衡，pH值偏低，氧化溝中污泥負荷過高，溶解氧濃度不足，排泥不暢等易引發(fā)絲狀菌性污泥膨脹；非絲狀菌性污泥膨脹主要發(fā)生在廢水水溫較低而污泥負荷較高時。微生物的負荷高，細菌吸取了大量營養(yǎng)物質(zhì)，由于溫度低，代謝速度較慢，積貯起大量高粘性的多糖類物質(zhì)，使活性污泥的表面附著水大大增加，SVI值很高，形成污泥膨脹。</p><

65、p>　　針對污泥膨脹的起因，可采取不同對策：由缺氧、水溫高造成的，可加大曝氣量或降低進水量以減輕負荷，或適當降低MLSS（控制污泥回流量），使需氧量減少；如污泥負荷過高，可提高MLSS，以調(diào)整負荷，必要時可停止進水，悶曝一段時間；可通過投加氮肥、磷肥，調(diào)整混合液中的營養(yǎng)物質(zhì)平衡（BOD5：N：P=100：5：1）；pH值過低，可投加石灰調(diào)節(jié)；漂白粉和液氯（按干污泥的0.3%~0.6%投加），能抑制絲狀菌繁殖，控制結(jié)合水性污泥膨脹。

66、</p><p><b>　　4.2 泡沫問題</b></p><p>　　由于進水中帶有大量油脂，處理系統(tǒng)不能完全有效地將其除去，部分油脂富集于污泥中，經(jīng)轉(zhuǎn)刷充氧攪拌，產(chǎn)生大量泡沫；泥齡偏長，污泥老化，也易產(chǎn)生泡沫。用表面噴淋水或除沫劑去除泡沫，常用除沫劑有機油、煤油、硅油，投量為0.5~1.5mg/L。通過增加曝氣池污泥濃度或適當減小曝氣量，也能有效控制泡沫產(chǎn)生。

67、當廢水中含表面活性物質(zhì)較多時，易預(yù)先用泡沫分離法或其他方法去除。另外也可考慮增設(shè)一套除油裝置。但最重要的是要強水資源管理理，減少含油過高廢水及其它有毒廢水的進入。</p><p>　　4.3 污泥上浮問題</p><p>　　當廢水中含油量過大，整個系統(tǒng)泥質(zhì)變輕，在操作過程中不能很好控制其在二沉池的停留時間，易造成缺氧，產(chǎn)生腐化污泥上??；當曝氣時間過長，在池中發(fā)生高度硝化作用，使硝酸鹽濃度

68、高，在二沉池易發(fā)生反硝化作用，產(chǎn)生氮氣，使污泥上?。涣硗?，廢水中含油量過大，污泥可能挾油上浮。</p><p>　　發(fā)生污泥上浮后應(yīng)暫停進水，打碎或清除污泥，判明原因，調(diào)整操作。污泥沉降性差，可投加混凝劑或惰性物質(zhì)，改善沉淀性；如進水負荷大應(yīng)減小進水量或加大回流量；如污泥顆粒細小可降低曝氣機轉(zhuǎn)速；如發(fā)現(xiàn)反硝化，應(yīng)減小曝氣量，增大回流或排泥量；如發(fā)現(xiàn)污泥腐化，應(yīng)加大曝氣量，清除積泥，并設(shè)法改善池內(nèi)水力條件。<

69、/p><p>　　4.4 流速不均及污泥沉積問題</p><p>　　在卡羅塞爾氧化溝中，為了獲得其獨特的混合和處理效果，混合液必須以一定的流速在溝內(nèi)循環(huán)流動。一般認為，最低流速應(yīng)為0.15m/s，不發(fā)生沉積的平均流速應(yīng)達到0.3~0.5m/s。氧化溝的曝氣設(shè)備一般為曝氣轉(zhuǎn)刷和曝氣轉(zhuǎn)盤，轉(zhuǎn)刷的浸沒深度為250~300mm，轉(zhuǎn)盤的浸沒深度為480~ 530mm。與氧化溝水深（3.0~3.6m）相

70、比，轉(zhuǎn)刷只占了水深的1/10~1/12，轉(zhuǎn)盤也只占了1/6~1/7，因此造成氧化溝上部流速較大（約為0.8~1.2m，甚至更大），而底部流速很?。ㄌ貏e是在水深的2/3或3/4以下，混合液幾乎沒有流速），致使溝底大量積泥（有時積泥厚度達1.0m），大大減少了氧化溝的有效容積，降低了處理效果，影響了出水水質(zhì)。</p><p>　　加裝上、下游導(dǎo)流板是改善流速分布、提高充氧能力的有效方法和最方便的措施。上游導(dǎo)流板安裝在

71、距轉(zhuǎn)盤（轉(zhuǎn)刷）軸心4.0處（上游），導(dǎo)流板高度為水深的1/5~1/6，并垂直于水面安裝；下游導(dǎo)流板安裝在距轉(zhuǎn)盤（轉(zhuǎn)刷）軸心3.0m處。導(dǎo)流板的材料可以用金屬或玻璃鋼，但以玻璃鋼為佳。導(dǎo)流板與其他改善措施相比，不僅不會增加動力消耗和運轉(zhuǎn)成本，而且還能夠較大幅度地提高充氧能力和理論動力效率。</p><p>　　另外，通過在曝氣機上游設(shè)置水下推動器也可以對曝氣轉(zhuǎn)刷底部低速區(qū)的混合液循環(huán)流動起到積極推動作用，從而解決氧

72、化溝底部流速低、污泥沉積的問題。設(shè)置水下推動器專門用于推動混合液可以使氧化溝的運行方式更加靈活，這對于節(jié)約能源、提高效率具有十分重要的意義。</p><p>　　5. 卡羅塞爾氧化溝的發(fā)展</p><p>　　由于污水處理標準中對除磷脫氮的要求越來越嚴格，卡羅塞爾氧化溝也得到了進一步的發(fā)展。目前，研究及應(yīng)用較多的包括以下兩種類型：微孔曝氣型卡羅塞爾2000系統(tǒng)、卡羅塞爾3000系統(tǒng)。<

73、;/p><p>　　5.1 微孔曝氣型卡羅塞爾2000系統(tǒng)</p><p>　　微孔曝氣型卡羅塞爾2000系統(tǒng)采用微孔曝氣（供氧設(shè)備為鼓風(fēng)機），微孔曝氣器可產(chǎn)生大量直徑為1mm左右的微小氣泡，這大大提高了氣泡的表面積，使得在池容積一定的情況下氧轉(zhuǎn)移總量增大（如池深增加則其傳質(zhì)效率將更高）。根據(jù)目前鼓風(fēng)機生產(chǎn)廠家的技術(shù)能力，池的有效水深最大可8m，因此可根據(jù)不同的工藝要求選取合適的水深。傳統(tǒng)氧化

74、溝的推流是利用轉(zhuǎn)刷、轉(zhuǎn)碟或倒傘型表曝機實現(xiàn)的，其設(shè)備利用率低、動力消耗大。微孔曝氣型卡羅塞爾2000系統(tǒng)則采用了水下推流的方式，即把潛水推進器葉輪產(chǎn)生的推動力直接作用于水體，在起推流作用的同時又可有效防止污泥的沉降。因而，采用潛水推進器既降低了動力消耗，又使泥水得到了充分地混合。</p><p>　　5.2 卡羅塞爾3000系統(tǒng)</p><p>　　卡羅塞3000系統(tǒng)是在卡羅塞爾2000系

75、統(tǒng)前再加上一個生物選擇區(qū)。該生物選擇區(qū)是利用高有機負荷篩選菌種，抑制絲狀菌的增長，提高各污染物的去除率，其后的工藝原理同卡羅塞爾2000系統(tǒng)。</p><p>　　卡羅塞爾3000系統(tǒng)的較大提高表現(xiàn)在：一是增加了池深，可達7.5~8m，同心圓式，池壁共用，減少了占地面積，降低造價同時提高了耐低溫能力（可達7℃）；二是曝氣設(shè)備的巧妙設(shè)計，表曝機下安裝導(dǎo)流筒，抽吸缺氧的混合液，采用水下推進器解決流速問題；三是使用了先

76、進的曝氣控制器QUTE（它采用一種多變量控制模式）。四是采用一體化設(shè)計，從中心開始，包括以下環(huán)狀連續(xù)工藝單元：進水井和用于回流活性污泥的分水器；分別由四部分組成的選擇池和厭氧池。這之外是有三個曝氣器和一個預(yù)反硝化池的卡羅塞爾2000系統(tǒng)（如圖2 所示）。五是圓形一體化的設(shè)計使得氧化溝不需額外的管線，即可實現(xiàn)回流污泥在不同工藝單元間的分配。</p><p><b>　　6. 結(jié)論</b><

77、;/p><p>　　卡羅塞爾氧化溝由于具有良好的出磷脫氮能力、抗沖擊負荷能力和運行管理方便等優(yōu)點，已經(jīng)得到了廣泛的應(yīng)用。但由于科技的發(fā)展和社會的進步，該工藝必將得到進一步的提高。作者認為：卡羅塞爾氧化溝的未來研究方向?qū)⒅饕w現(xiàn)在以下幾方面。</p><p>　　1) 結(jié)合生物膜法，研究和開發(fā)生物模型卡羅塞爾氧化溝。這樣不僅可以提高單位反應(yīng)器的微生物總量，從而提高有機負荷，而且生物膜本身<

78、;/p><p>　　具有的內(nèi)置A/O系統(tǒng)強化了脫氮效果。</p><p>　　2) 不斷提高卡羅塞爾氧化溝中微生物的活性。例如在氧化溝中投加EM專一菌種、投入鐵鹽使微生物馴化成生物鐵、投入活性炭增強菌膠團的形成并提高耐毒性沖擊等。</p><p>　　3) 提高卡羅塞爾氧化溝設(shè)備性能和監(jiān)控技術(shù)。提高表曝機、水下推進器的性能，減少維修工作量；利用DO、ORP等多目標監(jiān)