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class="on"><a href="/index.php?catid=15">高氨氮廢水蒸氨工藝</a></li> </ul> <div id="cem2yu4aycae" class="clear"></div> </div> <div id="cem2yu4aycae" class="clear"></div> </div> </div> </div> <div id="cem2yu4aycae" class="clear"></div> <div id="cem2yu4aycae" class="nmain wow fadeInUp"> <div id="cem2yu4aycae" class="hxjsxq"> <div id="cem2yu4aycae" class="gy_bt1"> <h3>高氨氮廢水蒸氨工藝</h3> <em></em> </div> <div> <div style="margin:0px auto; width:800px"> </div> </div> <p><br/></p><p><strong><span style="font-family: 宋體;font-size: 14px"><span style="font-family:宋體">核心技術(shù)：</span></span></strong></p><p style="text-indent:28px"><span style=";font-family:宋體;font-size:14px"><span style="font-family:宋體">我司蒸氨塔結合氨吸收塔聯(lián)運工藝處理高氨氮廢水，選用我公司與天津大學(xué)聯(lián)合開(kāi)發(fā)、國內先進(jìn)導向篩板并結合波紋板規整填料對氨氣的高效吸收，實(shí)現達標排放。該氨氮廢水處理系統操作彈性大，在確保達標排放的前提下，可通過(guò)對循環(huán)吸收的控制，調節得到所需濃度（</span><span style="font-family:Calibri">5%</span><span style="font-family:宋體">～</span><span style="font-family:Calibri">20%</span><span style="font-family:宋體">）的工業(yè)氨水。</span></span></p><p style="text-indent:28px"><span style=";font-family:宋體;font-size:14px"><span style="font-family:宋體"><br/></span></span></p><p style="text-align:center"><span style=";font-family:宋體;font-size:14px"><span style="font-family:宋體"><img src="/data/upload/image/20220125/1643095758758693.png" title="1643095758758693.png" alt="image.png" width="614" height="374" style="width: 614px; height: 374px;"/></span></span></p><p><strong><span style="font-family: 宋體;font-size: 14px"><span style="font-family:宋體">技術(shù)優(yōu)勢：</span></span></strong></p><p style="margin-top:2px;line-height:147%"><span style=";font-family:宋體;line-height:147%;font-size:14px"><span style="font-family:Calibri">1</span><span style="font-family:宋體">、雙塔蒸氨工藝不存在氣相采出料液的二次過(guò)冷凝，節省了冷卻水的用量與冷凝液在提濃段對蒸汽的損耗，更有利于蒸氨塔的穩定運行；蒸汽耗量?jì)H需 </span><span style="font-family:Calibri">80-100kg/</span><span style="font-family:宋體">噸水，同比傳統工藝可節省蒸汽</span><span style="font-family:Calibri">30%</span><span style="font-family:宋體">。</span></span></p><p style="margin-top:2px;line-height:147%"><span style=";font-family:宋體;line-height:147%;font-size:14px"><span style="font-family:Calibri">2</span><span style="font-family:宋體">、雙塔蒸氨的方式，通過(guò)氨水回流罐所逸散出來(lái)的不凝氣在氨吸收塔內部進(jìn)行三級循環(huán)噴淋吸收產(chǎn)出合格的氨水，該種方式可以保證氨水純度，相對于在氨水回流罐采出氨水的方式，有效的防止了液泛現象對于氨水純度的影響，同時(shí)，第三級噴淋采用一次水進(jìn)行噴淋，可以使不凝氣中的氨氮含量降到最低，生產(chǎn)裝置區域內部不會(huì )有過(guò)于明顯的氨氣味道。</span></span></p><p style="margin-top:2px;line-height:147%"><span style=";font-family:宋體;line-height:147%;font-size:14px"><span style="font-family:Calibri">3</span><span style="font-family:宋體">、塔盤(pán)材質(zhì)選用導向塔板，防止高懸浮物高</span><span style="font-family:Calibri">COD</span><span style="font-family:宋體">的料液對塔板造成堵塞。</span></span></p><p style=";text-autospace:none;line-height:150%"><span style=";font-family:宋體;font-size:14px"><span style="font-family:Calibri">4</span><span style="font-family:宋體">、導向</span></span><span style=";font-family:宋體;font-size:14px"><span style="font-family:宋體">塔板與泡罩、浮閥等鼓泡型塔板不同，汽、液接觸是在罩內進(jìn)行的，特別是撞擊分離板后，汽、液破碎、混合強度加大，且相接觸界面被多次更新，汽、液接觸面積大為增加，致使罩內傳質(zhì)、傳熱效率很高。研究證明：罩外噴射出的液滴與汽體接觸表面積更大，使傳質(zhì)更充分，這樣整個(gè)塔板空間均成為有效傳質(zhì)區，因此傳質(zhì)效率較高，一般比浮閥等要高出</span></span><span style=";font-family:宋體;font-size:14px"><span style="font-family:Calibri">15%</span></span><span style=";font-family:宋體;font-size:14px"><span style="font-family:宋體">以上。</span></span></p><p style="text-align: center;"><img src="/data/upload/image/20220125/1643095826136552.png" title="1643095826136552.png" alt="image.png"/></p> </div> </div> <div id="cem2yu4aycae" class="footer"> <div id="cem2yu4aycae" class="container" > <div id="cem2yu4aycae" class="col-md-4"> <h3>聯(lián)系我們</h3> <em></em> <div id="cem2yu4aycae" class="l_x"> <p>綜合電話(huà)：022-84890098<br/></p><p>公司郵箱：913500445@qq.com</p><p>公司地址：天津市空港經(jīng)濟區西七道科大訊飛智匯谷9層<br/></p><p><br/></p> </div> </div> <div id="cem2yu4aycae" class="col-md-42"> <h3>關(guān)于我們</h3> 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