污泥空心桨叶烘干设备询价�?参数-价格-中国粉体罐�/title>

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} }); function showliuyan(me, showtype){ if(showtype==0){ //$("#Content").val($("#Content").attr('placeholder')); Content= document.getElementById('PopMsgFrom').Content.getAttribute('placeholder'); document.getElementById('PopMsgFrom').Content.value=Content; } if(showtype==1){ // $("#Content").val($(me).text()); alert($(me).text()); document.getElementById('PopMsgFrom').Content.value=$(me).text(); } $(".fxp").css("display","flex"); } function close_popwin(){ $(".fxp").css("display","none"); // 关闭虚拟电话后的留言� $(".dhxj").css("display","none"); $(".dhxjbox").css("display", "none"); $(".dhxjbox2").css("display", "none"); return false; } </script>  <div class="cpjs"> <div class="cpjs_tab"> <div class="js_cpjj" style="border-bottom: 3px solid #1479d7; color: #1479d7;">产品介绍</div> <div class="js_cxd">创新炸�/div> <div class="js_xgfa">相关方案</div> <div class="js_xgzl">相关资料</div> <div class="js_yhpl">用户评论</div> <div class="js_gsdt">公司动�?/div> <div class="js_wsj">问商宵�/div> </div> <script> $(function(){ // 切换 $(".cpjs_tab a").click(function(){ $(".cpjs_tab a").css({"color":"#4F5862","border-bottom-color":"transparent"}); $(this).css({"color":"#1479d7","border-bottom-color":"#1479d7"}); }); }); </script>  <div class="cpjj"> <p>污泥<strong>空心桨叶烘干讽�/strong>备询价书</p><p>请贵公司设计下例2个设施的污泥烘干设施工艺，并对闪蒸式和圆筒烘干式进行工艺、投资及运行成本等方面进行比较。对工艺设备进行报价，提供工艺的总装布置图、土建设计资料、三电公辅设计资料、�/p><p>1）转底炉设施</p><p>原料：炼钢OG及RH污泥 、连铸水处理污泥、热轧污�?/p><p>总计20.34万t/a，含水率35％，烘干至含水率1％。物料密度约1.2t/m3、�/p><p>年作业时间：312.5天（年作�?500小时）、�/p><p>2）OG泥压块设於�/p><p> 原料：炼钢OG及RH污泥7.69万t/a，含水率35％，烘干至含水率1％。物料密度约1.2t/m3、�/p><p>年作业时间：350天，每天工作6，年作业2100小时、�/p><p>注：该项目本身可产生3万m3/h的热空气，温度约330℃、�/p><p> 蒸汽24.5t/h，压�?.25MPa，温�?50℃、�/p><p>能源条件——煤气：</p><p>湛江钢铁工程内可以提供本项目使用的煤气种类是转炉煤气或混合煤气（焦炉与高炉煤气混合）二种，选用时可以取其中任意一种、�/p><p> 1. 混合煤气９�/p><p>(a) 成分�?7.95%焦炉煤气�?2.05%高炉煤气合成，焦炉煤气中焦油处理至≤5mg/m3，硫化氢处理�?0mg/m3：�/p><p>(b) 低热倻�~7524kJ/m3：�/p><p>(c) 压力�?nbsp;16~22kPa（指送至含铁固废处理中心项目区域处）：�/p><p>(d) 温度：常温；</p><p> (e) 湿度：水份饱和、�/p><p>�?）干煤气成份如表1�?９�/p><p>高炉煤气干煤气成份表�?�?</p><p> </p><table cellspacing="0" cellpadding="0"><tbody><tr class="firstRow"><td width="174"><p style="TEXT-ALIGN: center">干煤气成仼�/p></td><td width="174"><p style="TEXT-ALIGN: center">平均值（％）</p></td><td width="174"><p style="TEXT-ALIGN: center">波动范围（％（�/p></td></tr><tr><td width="174"><p style="TEXT-ALIGN: center">CO</p></td><td width="174"><p style="TEXT-ALIGN: center">23.279</p></td><td width="174"><p style="TEXT-ALIGN: center">20.8�?3.4</p></td></tr><tr><td width="174"><p style="TEXT-ALIGN: center">CO2</p></td><td width="174"><p style="TEXT-ALIGN: center">25.055</p></td><td width="174"><p style="TEXT-ALIGN: center">22.0�?6.5</p></td></tr><tr><td width="174"><p style="TEXT-ALIGN: center">H2</p></td><td width="174"><p style="TEXT-ALIGN: center">5.349</p></td><td width="174"><p style="TEXT-ALIGN: center">3.2�?.5</p></td></tr><tr><td width="174"><p style="TEXT-ALIGN: center">N2</p></td><td width="174"><p style="TEXT-ALIGN: center">46.302</p></td><td width="174"><p style="TEXT-ALIGN: center">45.0�?3.0</p></td></tr><tr><td width="174"><p style="TEXT-ALIGN: center">CH4</p></td><td width="174"><p style="TEXT-ALIGN: center">0.015</p></td><td width="174"><p style="TEXT-ALIGN: center">0.0�?.1</p></td></tr></tbody></table><p>（b）计算低热值：3260 kJ/m3 （波动范围：±5％）</p><p>（c）温 度：常温：�/p><p>（d）压 力：�?.50±0.50kPa（指煤气柜出入口处的压力）；</p><p>（e）含尘量：≤5mg/m3：�/p><p>（f）湿 度：水份饱和、�/p><p>�?）干煤气成份如表1�?９�/p><p>焦炉煤气干煤气成份表�?�?</p><p> </p><table cellspacing="0" cellpadding="0"><tbody><tr class="firstRow"><td width="171"><p style="TEXT-ALIGN: center">干煤气成仼�/p></td><td width="171"><p style="TEXT-ALIGN: center">平均值（％）</p></td><td width="171"><p style="TEXT-ALIGN: center">波动范围（％（�/p></td></tr><tr><td width="171"><p style="TEXT-ALIGN: center">CO</p></td><td width="171"><p style="TEXT-ALIGN: center">5.9</p></td><td width="171"><p style="TEXT-ALIGN: center">5.3�?.5</p></td></tr><tr><td width="171"><p style="TEXT-ALIGN: center">CO2</p></td><td width="171"><p style="TEXT-ALIGN: center">2.1</p></td><td width="171"><p style="TEXT-ALIGN: center">1.9�?.4</p></td></tr><tr><td width="171"><p style="TEXT-ALIGN: center">H2</p></td><td width="171"><p style="TEXT-ALIGN: center">58.8</p></td><td width="171"><p style="TEXT-ALIGN: center">57.1�?0.6</p></td></tr><tr><td width="171"><p style="TEXT-ALIGN: center">N2</p></td><td width="171"><p style="TEXT-ALIGN: center">3.8</p></td><td width="171"><p style="TEXT-ALIGN: center">2.2�?.4</p></td></tr><tr><td width="171"><p style="TEXT-ALIGN: center">CH4</p></td><td width="171"><p style="TEXT-ALIGN: center">25.6</p></td><td width="171"><p style="TEXT-ALIGN: center">24.7�?6.5</p></td></tr><tr><td width="171"><p style="TEXT-ALIGN: center">C2H4</p></td><td width="171"><p style="TEXT-ALIGN: center">2.3</p></td><td width="171"><p style="TEXT-ALIGN: center">2.1�?.4</p></td></tr><tr><td width="171"><p style="TEXT-ALIGN: center">C2H6</p></td><td width="171"><p style="TEXT-ALIGN: center">0.9</p></td><td width="171"><p style="TEXT-ALIGN: center">0.7�?.0</p></td></tr><tr><td width="171"><p style="TEXT-ALIGN: center">C3H6</p></td><td width="171"><p style="TEXT-ALIGN: center">0.2</p></td><td width="171"></td></tr><tr><td width="171"><p style="TEXT-ALIGN: center">O2</p></td><td width="171"><p style="TEXT-ALIGN: center">0.4</p></td><td width="171"><p style="TEXT-ALIGN: center">0.0�?.0</p></td></tr></tbody></table><p>（b）计算低热值：18520kJ/m3（波动范围：18000�?8850 kJ/m3）；</p><p>（c）温 度：常温：�/p><p>（d）压 力：</p><p>低压焦炉煤气管网：～6.30±0.15kPa（指煤气柜出入口处的压力）；</p><p>加压焦炉煤气管网�?1~12kPa</p><p>（e）湿 度：水份饱和：�/p><p>（f）含不纯物的数量如表1�?９�/p><p>焦炉煤气含不纯物表表1�?</p><p> </p> </div>  <div class="cxd"> <div class="cxd_tit"><span></span>创新炸�/div> <p style=" color: #333; 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