国产精品久久7777777_A／O工藝處理制藥生產(chǎn)廢水_江蘇萬(wàn)尚|污水處理|廢氣治理-江蘇萬(wàn)尚環(huán)?？萍加邢薰?/title> <meta name="keywords" content="工藝,處理,制藥,生產(chǎn),廢水,亞?wèn)|,制藥,霍山," /> <meta name="description" content="亞?wèn)|制藥霍山有限公司，在生產(chǎn)過(guò)程中，排放各種廢水總計200t/d，通過(guò)對廢水水質(zhì)實(shí)測結果可知，該企業(yè)廢水生化性較好（生化比為0.4左右），適宜選用生物法處理，故在對種種生物處" /> <link rel="stylesheet" href="/templets/default/resouce/css/company/style.css" type="text/css" media="all" />  <meta http-equiv="Cache-Control" content="no-transform" /> <meta http-equiv="Cache-Control" content="no-siteapp" /> <script>var V_PATH="/";window.onerror=function(){ return true; };</script> </head> <body > <h1><a href="http://m.ngxyzm.com/">久久精品国产日本波多野结衣,久久水蜜桃亚洲AV无码精品麻豆,无码精品中文字幕一区二区三区,囯内精品久久人妻无码HD</a></h1> <div class="pl_css_ganrao" style="display: none;"><dfn id="prjxh"><th id="prjxh"></th></dfn><ol id="prjxh"><output id="prjxh"></output></ol><legend id="prjxh"><legend id="prjxh"></legend></legend><th id="prjxh"><legend id="prjxh"></legend></th><track 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href="/fangan/jiejuefangan/">工程設計方案</a></span> </div> </div> <article> <div id="y0k0gg0" class="wrapper" id="detailed"> 亞?wèn)|制藥霍山有限公司，在生產(chǎn)過(guò)程中，排放各種廢水總計200t/d，通過(guò)對廢水水質(zhì)實(shí)測結果可知，該企業(yè)廢水生化性較好（生化比為0.4左右），適宜選用生物法處理，故在對種種生物處理方法進(jìn)行比較的基礎上采取A/O工藝處理該廢水。<br /> <br /> <strong>1 </strong><strong>廢水的水量、水質(zhì)和處理要求</strong><br /> 亞?wèn)|制藥霍山有限公司，日排廢水為200t，因而設計處理水量為200m<sup>3</sup>/d，處理后的外排廢水各項指標必須達到GB 8978—1996的一級標準。<br /> 該公司生產(chǎn)廢水的污染物主要是有機物，實(shí)測廢水水質(zhì)情況及排放標準列于表1。<br /> 表1 生產(chǎn)廢水水質(zhì)及排放標準<br /> <table align="center" border="1" cellpadding="0" cellspacing="0"> <tbody> <tr> <td> 項目</td> <td> PH</td> <td> CODcr/（mg·L<sup>-1</sup>）</td> <td> BOD<sub>5</sub>/（mg·L<sup>-1</sup>）</td> <td> SS/（mg·L<sup>-1</sup>）</td> <td> 色度/倍</td> </tr> <tr> <td> 廢水水質(zhì)</td> <td> 4.73-6.87</td> <td> 427-3000</td> <td> 206-1070</td> <td> 52-363</td> <td> 80-4120</td> </tr> <tr> <td> 設計進(jìn)水水質(zhì)</td> <td> 6-9</td> <td> 2500</td> <td> 1000</td> <td> 250</td> <td> 3000</td> </tr> <tr> <td> 排放標準</td> <td> 6-9</td> <td> 100</td> <td> 30</td> <td> 70</td> <td> 50</td> </tr> </tbody> </table> <div style="clear:both;"> </div> <br /> <strong>2 </strong><strong>處理工藝選擇及工藝流程</strong><br /> 2.1 處理工藝選擇<br /> 本著(zhù)投資省、運行費用低、處理效果好的在原則，結合該公司的實(shí)際情況，選擇A／O工藝處理該廢水，厭氧部分COD、BOD降解率在40%—50%，為下一步的廢水處理提供了更加有利的條件，減少了好氧部分的壓力。厭氧部分沒(méi)有電耗和其他消耗，但可使好氧段減少曝氣時(shí)間近三分之一，更可減少投藥量，省電、省料、省工；根據實(shí)際運行情況還可以改為更先進(jìn)的SBR法，實(shí)現自動(dòng)化處理廢水。<br /> <br /> 2.2 處理工藝流程<br /> 處理工藝流程如圖1所示。<br /> 生產(chǎn)廢水首先經(jīng)格柵井，去除水中粗大顆粒物后，進(jìn)入調節池，在調節池內進(jìn)行水質(zhì)、水量調節，然后用污水泵打人A／O池。進(jìn)水量由流量計控制，經(jīng)過(guò)充分厭氧和好氧處理后，出水進(jìn)人二沉池進(jìn)行活性污泥、水分離，二沉池出水經(jīng)氣浮池以除去色度后，達標排放。厭氧池、好氧池和氣浮池產(chǎn)生的污泥經(jīng)濃縮后進(jìn)入壓濾機，形成干泥餅外運填埋。二沉池的部分污泥進(jìn)行回流。<br /> <br /> <strong>3 </strong><strong>主要構筑物及設備</strong><br /> 3.1 主要構筑物及投資<br /> 主要構筑物及投資如表2所示。<br /> 表2 主要構筑物及投資<br /> <table align="center" border="1" cellpadding="0" cellspacing="0"> <tbody> <tr> <td> 序號</td> <td> 建筑物名稱(chēng)</td> <td> 數量</td> <td> 規格</td> <td> 結構</td> <td> 投資/萬(wàn)元</td> </tr> <tr> <td> 1</td> <td> 格柵井</td> <td> 1</td> <td> </td> <td> 磚混</td> <td> 0.40</td> </tr> <tr> <td> 2</td> <td> 調節池</td> <td> 1</td> <td> 8m×6m×4.5m</td> <td> 磚混</td> <td> 2.10</td> </tr> <tr> <td> 3</td> <td> 厭氧池</td> <td> 1</td> <td> 8m×9m×5.5m</td> <td> 鋼混</td> <td> 6.00</td> </tr> <tr> <td> 4</td> <td> 好氧池</td> <td> 2</td> <td> 8m×8m×5.5m</td> <td> 鋼混</td> <td> 8.50</td> </tr> <tr> <td> 5</td> <td> 二沉池</td> <td> 1</td> <td> 8m×3m×5.5m</td> <td> 鋼混</td> <td> 1.50</td> </tr> <tr> <td> 6</td> <td> 污泥濃縮池</td> <td> 1</td> <td> 2m×4m×3m</td> <td> 磚混</td> <td> 0.60</td> </tr> <tr> <td> 合計</td> <td> </td> <td> </td> <td> </td> <td> </td> <td> 19.1</td> </tr> </tbody> </table> <div style="clear:both;"> </div> <br /> 3.2 主要設備材料及投資<br /> 主要設備材料及投資如表3所示。<br /> 表3 主要設備、材料及投資<br /> <table align="center" border="1" cellpadding="0" cellspacing="0"> <tbody> <tr> <td style="width:56px;"> 序號</td> <td style="width:194px;"> 設備名稱(chēng)</td> <td style="width:66px;"> 數量</td> <td style="width:112px;"> 投資/萬(wàn)元</td> </tr> <tr> <td style="width:56px;"> 1</td> <td style="width:194px;"> 旋轉式曝氣攪拌兩用機</td> <td style="width:66px;"> 2</td> <td style="width:112px;"> 6.00</td> </tr> <tr> <td style="width:56px;"> 2</td> <td style="width:194px;"> 氣浮機</td> <td style="width:66px;"> 1</td> <td style="width:112px;"> 6.00</td> </tr> <tr> <td style="width:56px;"> 3</td> <td style="width:194px;"> 壓濾機</td> <td style="width:66px;"> 1</td> <td style="width:112px;"> 3.50</td> </tr> <tr> <td style="width:56px;"> 4</td> <td style="width:194px;"> 螺桿泵</td> <td style="width:66px;"> 1</td> <td style="width:112px;"> 04.0</td> </tr> <tr> <td style="width:56px;"> 5</td> <td style="width:194px;"> 加藥槽</td> <td style="width:66px;"> </td> <td style="width:112px;"> 0.80</td> </tr> <tr> <td style="width:56px;"> 6</td> <td style="width:194px;"> 加藥控制系統</td> <td style="width:66px;"> 1</td> <td style="width:112px;"> 0.80</td> </tr> <tr> <td style="width:56px;"> 7</td> <td style="width:194px;"> 電控系統</td> <td style="width:66px;"> 1</td> <td style="width:112px;"> 0.50</td> </tr> <tr> <td style="width:56px;"> 8</td> <td style="width:194px;"> 流量計</td> <td style="width:66px;"> 2</td> <td style="width:112px;"> 1.00</td> </tr> <tr> <td style="width:56px;"> 9</td> <td style="width:194px;"> 管道系統</td> <td style="width:66px;"> 1</td> <td style="width:112px;"> 1.50</td> </tr> <tr> <td style="width:56px;"> 10</td> <td style="width:194px;"> 填料、支架</td> <td style="width:66px;"> </td> <td style="width:112px;"> 4.00</td> </tr> <tr> <td style="width:56px;"> 合計</td> <td style="width:194px;"> </td> <td style="width:66px;"> </td> <td style="width:112px;"> 24.5</td> </tr> </tbody> </table> <div style="clear:both;"> </div> <br /> 3.3 運行費用<br /> 運行費用0.45元/m<sup>3</sup>。其中電費0.20元/m<sup>3</sup>；人員工資0.10元/m<sup>3</sup>；維護費0.05元/m<sup>3</sup>。<br /> <br /> <strong>4 </strong><strong>系統的啟動(dòng)和運行結果</strong><br /> <br /> 4.1 系統的啟動(dòng)<br /> 該系統啟動(dòng)時(shí)，取用合肥市某污水處理廠(chǎng)濃縮污泥，直接放入厭氧池和好氧池，加入生產(chǎn)廢水進(jìn)行調試運行，經(jīng)過(guò)10d的調試，系統得以穩定運行，并交付使用。厭氧池水力停留時(shí)間為48h，好氧池水力停留時(shí)間為12h；二沉池水力停留時(shí)間為12h。<br /> <br /> <br /> 4.2 系統運行結果<br /> 該系統于2003年10月建成并開(kāi)始系統調試，系統正常運行兩個(gè)月后，2003年12月申請環(huán)保部門(mén)驗收，驗收監測結果見(jiàn)表4。<br /> 表4 系統進(jìn)出水驗收監結果<br /> <table align="center" border="1" cellpadding="0" cellspacing="0"> <tbody> <tr> <td> 日期</td> <td> 項目</td> <td> PH</td> <td> CODcr/（mg·L<sup>-1</sup>）</td> <td> BOD<sub>5</sub>/（mg·L<sup>-1</sup>）</td> <td> SS/（mg·L<sup>-1</sup>）</td> <td> 色度/倍</td> </tr> <tr> <td> 12-27</td> <td> 處理前<br /> 處理后<br /> 去除率/%</td> <td> 5.74<br /> 7.48</td> <td> 959<br /> 53<br /> 95.5</td> <td> 760<br /> 5.4<br /> 99.3</td> <td> 309<br /> 5.0<br /> 98.4</td> <td> 4120<br /> 45<br /> 98.9</td> </tr> <tr> <td> 12-28</td> <td> 處理前<br /> 處理后<br /> 去除率/%</td> <td> 6.27<br /> 7.42</td> <td> 426<br /> 72<br /> 84.1</td> <td> 291<br /> 7.4<br /> 97.5</td> <td> 97<br /> 5.6<br /> 94.2</td> <td> 160<br /> 8<br /> 95.0</td> </tr> <tr> <td> 12-29</td> <td> 處理前<br /> 處理后<br /> 去除率/%</td> <td> 4.73<br /> 7.51</td> <td> 3000<br /> 33<br /> 98.9</td> <td> 1070<br /> 10<br /> 99.0</td> <td> 363<br /> 4.8<br /> 98.7</td> <td> 1280<br /> 8<br /> 99.4</td> </tr> </tbody> </table> <div style="clear:both;"> </div> 由表4的連續監測結果看，系統進(jìn)水PH4.73-6.27，SS為97-363mg/L，CODcr為426-3000mg/L，BOD<sub>5</sub>為291-1070mg/L，色度為160-4120倍時(shí)，出水PH為7.42，SS去除率達94.2%以上，CODcr平均去除率為92.5%，BOD<sub>5</sub>去除率97.5%以上，色度去除率95.0%以上。系統抗沖擊負荷能力強，系統出水穩定，各項指標均達到GB 8978—1996的一級標準。<br /> 工程的實(shí)際運行中也發(fā)現一些問(wèn)題，一是污泥匯流泵功率小，無(wú)法有效回流污泥造成污泥流失；二是曝氣機葉輪、軸承、軸套、密封圈等易損壞，使用時(shí)間不久就要更換。<br /> <strong>5 </strong><strong>結論</strong><br /> 綜上所述可得出以下結論：<br /> （1）只要系統正常運行，操作管理規范，A/O工藝處理中成藥廢水實(shí)際可行，處理效果好，出水水質(zhì)穩定，各項指標均達到GB 8978—1996的一級標準。<br /> （2）工程投資和運行費用適中。<br /> （3）自動(dòng)化程度較高，便于操作管理。<br /> （4）系統耐沖擊負荷高，對進(jìn)水水質(zhì)的波動(dòng)具有較好的適應性，運行穩定可靠。<br /> （5）部分設備有待重新選擇，以使系統更加完善。 </div> <div id="iasokee" class="wrapper 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