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培養過(guò)程中投加部分成熟AGS可有效縮短好氧顆?；瘯r(shí)間，AGS的投加時(shí)間點(diǎn)是快速培養的關(guān)鍵控制因素，它決定了活性污泥顆?；c投加AGS之后加速顆?；瘍刹糠值臅r(shí)間分布。投加點(diǎn)控制在10 min時(shí)可有效維持接種AGS的穩定性，使其不經(jīng)解解體過(guò)程而直接作為新生顆粒的晶核及載體，較好地發(fā)揮了AGS的作用。</span></div> <div> </div> <div> <span style="font-size:16px;">二、好氧顆粒污泥處理化工廢水的應用研究</span></div> <div> </div> <div> <span style="font-size:16px;">結論:通過(guò)在模擬污水中逐步提高實(shí)際廢水的比例，于44 d后成功馴化出高適應性AGS。馴化過(guò)程中AGS始終處在顆?；c解體的動(dòng)態(tài)平衡過(guò)程中，雖然伴隨著(zhù)大顆粒的破碎，但AGS始終較好地維持了自身的顆粒狀結構，并表現出良好的沉降性能。馴化過(guò)程中反應器對主要污染物的去除效果亦有波動(dòng)，但隨著(zhù)AGS逐漸適應實(shí)際廢水水質(zhì)，反應器對COD、TIN及TP的去除率最終均上升至90%以上，表現出較強的污染物去除能力。試驗結果表明AGS良好的沉降性能及高耐毒性能實(shí)現對苯甲酸芐酯廢水的無(wú)害化治理。</span></div> <div> </div> <div> <span style="font-size:16px;">三、高氨氮、連續流中好氧顆粒污泥的穩定性研究</span></div> <div> </div> <div> <span style="font-size:16px;">結論:通過(guò)逐步提高氮負荷（0.8~1.1 kg/m³·d），連續流中的AGS在63 d的運行時(shí)間里較好地維持了其顆粒狀結構。雖然氮負荷的增加對AGS的穩定性有一定沖擊，導致AGS的理化特性及對污染物的去除效果出現波動(dòng)，但AGS通過(guò)改變自身形態(tài)、分泌更多EPS等逐漸適應了新水質(zhì)，對COD及TP的去除率最終上升至約90%及100%。雖然反應器對TIN的去除效果并不穩定，最終去除率亦不足70%，但高氨氮環(huán)境能抑制微生物的過(guò)快生長(cháng)，使得顆?；c解體的動(dòng)態(tài)平衡更易維持。試驗結束時(shí)的AGS表現出比接種AGS更加光滑、致密的結構，表明AGS能在高氨氮、連續流環(huán)境下保持其穩定性。</span></div> <div> </div> <div> <span style="font-size:16px;">四、設置生物選擇段的SBR中好氧顆粒污泥的培養</span></div> <div> </div> <div> <span style="font-size:16px;">結論:（1）在吸取第一次培養失敗的經(jīng)驗基礎上，利用選擇壓法、并設置厭氧生物選擇器及投加活性炭惰性載體進(jìn)行AGS的培養，第3 d時(shí)反應器內即可觀(guān)察到新生的生物膜及AGS，21 d時(shí)幾乎全部以菌膠團及AGS形式存在，未出現第一次培養時(shí)的蚊蠅幼蟲(chóng)大量繁殖及污泥膨脹現象。表明厭氧生物選擇器的設置及活性炭的投加有利于A(yíng)GS的快速形成。（2）隨著(zhù)回流量的增大，系統的穩定性受到一定沖擊，造成污泥的理化特性及出水水質(zhì)的異常波動(dòng)。但是，微生物可通過(guò)增加或減少EPS的分泌以適應新的環(huán)境，使得22 d開(kāi)始污泥理化特性逐漸趨穩?；亓鲗е禄旌弦蝴}度的增加導致一些絮體難以下沉，從而造成出水SS的升高及污泥齡的減小，導致出水氨氮和SS的波動(dòng)。</span></div> <div> </div> <div> <span style="font-size:16px;">五、失穩好氧顆粒污泥在SBR中的修復</span></div> <div> </div> <div> <span style="font-size:16px;">結論：</span></div> <div> <span style="font-size:16px;"> （1）在SBR中接種發(fā)生絲狀菌膨脹的AGS，通過(guò)逐步縮短沉降時(shí)間及降低C/N比，19 d時(shí)大部分顆粒表面已經(jīng)比較光滑，25 d時(shí)AGS在反應器中已占主導，30d時(shí)完全實(shí)現好氧顆?；?。44 d后重新培養出形狀規則、外部光滑、結構致密的AGS，SVI、平均粒徑及顆?；史謩e為65.77ml/g、1.42 mm及95.19%。</span></div> <div> <span style="font-size:16px;"> （2）接種AGS極不穩定，修復過(guò)程中部分接種大顆粒經(jīng)歷了先解體后重新顆?；倪^(guò)程，且解體的顆粒污泥可以作為新顆粒污泥形成的晶核及載體，因而修復時(shí)間（約30 d）稍短于直接利用活性污泥培養AGS。 </span></div> <div> <span style="font-size:16px;"> （3）正常情況下反應器對污染物具有較好的處理效果，出水COD在11 d后趨于穩定，始終維持在80mg/L以下，去除率保持在90%以上；前40 d內出水TP始終處于波動(dòng)狀態(tài)，但TP的去除率基本保持在70%以上，41 d以后出水TP趨于穩定，出水TP維持在0.67 mg/L以下、去除率在96%以上；前39 d內出水TIN和NH4+-N處于波動(dòng)狀態(tài)，出水TIN在40 d以后趨于穩定、去除率保持在88%以上。</span></div> <div> </div> <div> <span style="font-size:16px;">六、不同生物選擇段的SBR中好氧顆粒污泥的特性</span></div> <div> </div> <div> <span style="font-size:16px;">結論：</span></div> <div> <span style="font-size:16px;">（1）生物選擇段的設置能夠有效抑制絲狀菌的生長(cháng)，并能較好的維持AGS的穩定性。不同好氧選擇段下AGS的SV30/SV5保持在0.93以上，SVI在40ml/g以下，MLVSS/MLSS維持在0.70左右，EPS在40 mg/g MLVSS左右，PN/PS在1.3~2.0之間，含水率約為98%；不同厭氧選擇段下AGS的SV30/SV5保持在0.92以上，SVI在40ml/g以下，MLVSS/MLSS維持在0.67左右，EPS在44 mg/g MLVSS左右，PN/PS在1.4~1.8之間，含水率約為97.5%。</span></div> <div> <span style="font-size:16px;"> （2）不同選擇段下反應器對污染物均具有較好的去除效果。不同好氧選擇段下反應器對COD、TP、TIN及NH4+-N的去除率分別保持在98%、90%、77%及82%以上；不同厭氧選擇段下反應器對COD、TP、TIN及NH4+-N的去除率分別保持在97%、85%、75%及75%以上。雖然好氧選擇段下污染物的去除效果要略高于厭氧選擇段，但厭氧選擇段可有效降低運行能耗。</span></div> </p> <div id="crmh0qv" class="page"> <p>上一篇：<a href='/xinwenzixun/243.html'>污水處理廠(chǎng)春節值班7大注意事項</a> </p> <p>下一篇：<a href='/xinwenzixun/245.html'>污泥處理主要設備及系統組成</a> </p> <a href="javascript:void(0);" title="折帶式過(guò)濾機" class="back" onClick="javascript:history.back(-1);">返回</a> </div> </div> </div> </div>  </div> </div>  <div id="hizxggx" class="footclear"></div> <div id="w6kjhdm" class="foot"> <div id="piwjktj" class="fmain"> <div id="tpbkgw7" 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