⭐ 欢迎来到虫虫下载站！ | 📦 资源下载 📁 资源专辑 ℹ️ 关于我们
⭐ 虫虫下载站
📤 上传资源

📄 6_2.asp

📁 《管式加热炉设计计算程序》本程序依据《管式加热炉规范》 SY/T0538-2004进行开发而成。适用于油田、长输管道圆筒型管式加热炉（包括丁头管、翅片管）的热力计算、水力计算、阻力计算及强度计算。
💻 ASP
字号:
🔍 
<!--#include file="dbconn.asp"-->
<!--#include file="inc/checkchange.inc"-->
<!--#include file="inc/QZF.CSS"-->
<!--#include file="9_06.asp"-->
<html>
<head>
<meta http-equiv="Content-Language" content="zh-cn">
<meta http-equiv="Content-Type" content="text/html; charset=gb2312">
<meta name="GENERATOR" content="Microsoft FrontPage 4.0">
<meta name="ProgId" content="FrontPage.Editor.Document">
<title>管式加热炉工艺设计书</title>
</head>
<body>

<p align="center"><font face="华文新魏" size="7"><b>六、</b></font><font face="华文新魏" size="7"><b>炉管压力降计算</b></font></p>


<%
th=Session.Contents("th")
 if th="00" then 
 response.write"<p align='center'><a href='index.asp'><font color='#000064'>请输入设计号！&gt;&gt;&gt;</font> </a></p>" 
 Response.End 
 end if
th=Session.Contents("th")

set rs=server.createobject("adodb.recordset")
 sql ="select * from 6 where (th='"&th&"')"
 rs.open sql,conn,1,1
th=rs("th")
m=rs("m")
n=rs("n")
w=rs("w")
di=rs("di")
l=rs("l")
le=rs("le")
rtpj=rs("rtpj")
u=rs("u")
uu=rs("uu")
re=rs("re")
f=rs("f")
pf=rs("pf")
m1=rs("m1")
n1=rs("n1")
w1=rs("w1")
di1=rs("di1")
l1=rs("l1")
le1=rs("le1")
rtpj1=rs("rtpj1")
u1=rs("u1")
uu1=rs("uu1")
re1=rs("re1")
f1=rs("f1")
pf1=rs("pf1")
h12=rs("h12")
pf2=rs("pf2")
p=rs("p")
%> 
<p align="center"><font face="宋体" size="3">设计号：<%=th%></font></p>
<p align="center">
<input type=button onclick="vbscript:buildDoc '',4" value="生成word">
<div align="center">
  <center>
<table border="1" id="myData" width="800">
  <tr>
    <td width="33" align="center">序号</td>
    <td width="202" align="center">名称</td>
    <td width="48" align="center">符号</td>
    <td width="48" align="center">单位</td>
    <td width="287" align="center">计算公式及数据来源</td>
    <td width="142" align="center">结果</td>
  </tr>
  <tr>
    <td width="33">　</td>
    <td width="202">一、辐射炉管阻力计算</td>
    <td width="48">　</td>
    <td width="48">　</td>
    <td width="287">　</td>
    <td width="142">　</td>
  </tr>
  <tr>
    <td width="33">1</td>
    <td width="202">辐射炉管管程数</td>
    <td width="48">m</td>
    <td width="48">程</td>
    <td width="287">　</td>
    <td width="142"><%=m%></td>
  </tr>
  <tr>
    <td width="33">2</td>
    <td width="202">每程辐射炉管根数</td>
    <td width="48">n</td>
    <td width="48">根</td>
    <td width="287">　</td>
    <td width="142"><%=n%></td>
  </tr>
  <tr>
    <td width="33">2</td>
    <td width="202">系数</td>
    <td width="48">w</td>
    <td width="48">-</td>
    <td width="287">180°急弯管为45</td>
    <td width="142"><%=w%></td>
  </tr>
  <tr>
    <td width="33">4</td>
    <td width="202">辐射炉管内径</td>
    <td width="48">di</td>
    <td width="48">mm</td>
    <td width="287">　</td>
    <td width="142"><%=di%></td>
  </tr>
  <tr>
    <td width="33">5</td>
    <td width="202">辐射炉管长度</td>
    <td width="48">l</td>
    <td width="48">m</td>
    <td width="287">　</td>
    <td width="142"><%=l%></td>
  </tr>
  <tr>
    <td width="33">6</td>
    <td width="202">辐射炉管当量长度</td>
    <td width="48">le</td>
    <td width="48">m</td>
    <td width="287">　</td>
    <td width="142"><%=le%></td>
  </tr>
  <tr>
    <td width="33">7</td>
    <td width="202">原油密度</td>
    <td width="48">p</td>
    <td width="48">-</td>
    <td width="287">　</td>
    <td width="142"><%=rtpj%></td>
  </tr>
  <tr>
    <td width="33">8</td>
    <td width="202">辐射炉管内原油流速</td>
    <td width="48">u</td>
    <td width="48">m/s</td>
    <td width="287">　</td>
    <td width="142"><%=u%></td>
  </tr>
  <tr>
    <td width="33">9</td>
    <td width="202">原油粘度</td>
    <td width="48">r</td>
    <td width="48">Pa.s</td>
    <td width="287">　</td>
    <td width="142"><%=uu%></td>
  </tr>
  <tr>
    <td width="33">10</td>
    <td width="202">原油雷诺数</td>
    <td width="48">Re</td>
    <td width="48">-</td>
    <td width="287">　</td>
    <td width="142"><%=re%></td>
  </tr>
  <tr>
    <td width="33">11</td>
    <td width="202">水力摩擦系数</td>
    <td width="48">f</td>
    <td width="48">-</td>
    <td width="287">　</td>
    <td width="142"><%=f%></td>
  </tr>
  <tr>
    <td width="33">12</td>
    <td width="202">辐射炉管总阻力</td>
    <td width="48">pf</td>
    <td width="48">MPa</td>
    <td width="287">　</td>
    <td width="142"><%=pf%></td>
  </tr>
  <tr>
    <td width="33">　</td>
    <td width="202">二、对流炉管阻力计算</td>
    <td width="48">　</td>
    <td width="48">　</td>
    <td width="287">　</td>
    <td width="142">　</td>
  </tr>
  <tr>
    <td width="33">1</td>
    <td width="202">炉管管程数</td>
    <td width="48">m</td>
    <td width="48">程</td>
    <td width="287">　</td>
    <td width="142"><%=m1%></td>
  </tr>
  <tr>
    <td width="33">2</td>
    <td width="202">每程对流炉管根数：</td>
    <td width="48">n</td>
    <td width="48">根</td>
    <td width="287">　</td>
    <td width="142"><%=n1%></td>
  </tr>
  <tr>
    <td width="33">3</td>
    <td width="202">系数</td>
    <td width="48">w</td>
    <td width="48">-</td>
    <td width="287">　</td>
    <td width="142"><%=w1%></td>
  </tr>
  <tr>
    <td width="33">4</td>
    <td width="202">对流炉管内径</td>
    <td width="48">di</td>
    <td width="48">mm</td>
    <td width="287">　</td>
    <td width="142"><%=di1%></td>
  </tr>
  <tr>
    <td width="33">5</td>
    <td width="202">对流炉管长度</td>
    <td width="48">l</td>
    <td width="48">m</td>
    <td width="287">　</td>
    <td width="142"><%=l1%></td>
  </tr>
  <tr>
    <td width="33">6</td>
    <td width="202">对流炉管当量长度</td>
    <td width="48">le</td>
    <td width="48">m</td>
    <td width="287">　</td>
    <td width="142"><%=le1%></td>
  </tr>
  <tr>
    <td width="33">7</td>
    <td width="202">原油密度</td>
    <td width="48">p</td>
    <td width="48">-</td>
    <td width="287">　</td>
    <td width="142"><%=rtpj1%></td>
  </tr>
  <tr>
    <td width="33">8</td>
    <td width="202">对流炉管内原油流速</td>
    <td width="48">u</td>
    <td width="48">m/s</td>
    <td width="287">　</td>
    <td width="142"><%=u1%></td>
  </tr>
  <tr>
    <td width="33">9</td>
    <td width="202">原油粘度</td>
    <td width="48">r</td>
    <td width="48">Pa.s</td>
    <td width="287">　</td>
    <td width="142"><%=uu1%></td>
  </tr>
  <tr>
    <td width="33">10</td>
    <td width="202">原油雷诺数</td>
    <td width="48">Re</td>
    <td width="48">-</td>
    <td width="287">　</td>
    <td width="142"><%=re1%></td>
  </tr>
  <tr>
    <td width="33">11</td>
    <td width="202">水力摩擦系数</td>
    <td width="48">f</td>
    <td width="48">-</td>
    <td width="287">　</td>
    <td width="142"><%=f1%></td>
  </tr>
  <tr>
    <td width="33">12</td>
    <td width="202">对流炉管总阻力</td>
    <td width="48">pf</td>
    <td width="48">MPa</td>
    <td width="287">　</td>
    <td width="142"><%=pf1%></td>
  </tr>
  <tr>
    <td width="33">　</td>
    <td width="202">三、高差阻力计算</td>
    <td width="48">　</td>
    <td width="48">　</td>
    <td width="287">　</td>
    <td width="142">　</td>
  </tr>
  <tr>
    <td width="33">1</td>
    <td width="202">进口标高与工艺管线标高之差</td>
    <td width="48">H<font size="1">12</font></td>
    <td width="48">m</td>
    <td width="287">　</td>
    <td width="142"><%=h12%></td>
  </tr>
  <tr>
    <td width="33">2</td>
    <td width="202">高差阻力</td>
    <td width="48">pf2</td>
    <td width="48">MPa</td>
    <td width="287">　</td>
    <td width="142"><%=pf2%></td>
  </tr>
  <tr>
    <td width="33">　</td>
    <td width="202">四、总阻力</td>
    <td width="48">　</td>
    <td width="48">　</td>
    <td width="287">　</td>
    <td width="142">  &nbsp;  </td>
  </tr>
  <tr>
    <td width="33">1</td>
    <td width="202">总阻力</td>
    <td width="48">p</td>
    <td width="48">MPa</td>
    <td width="287">　</td>
    <td width="142"><%=p%></td>
  </tr>
</table>
  </center>
</div>
</body>
</html>
<%
rs.close                       
set rs=nothing 
conn.close                       
set conn=nothing
response.write"<p align='center'><a href='6_1.asp?change=ture'><font color='#000064'>重新计算！&gt;&gt;&gt;</font> </a></p>" 
response.write"<p align='center'><a href='mulu.asp'><font color='#000064'>返回&gt;&gt;&gt;</font> </a></p>" 
%>

⌨️ 快捷键说明

复制代码 Ctrl + C
搜索代码 Ctrl + F
全屏模式 F11
切换主题 Ctrl + Shift + D
显示快捷键 ?
增大字号 Ctrl + =
减小字号 Ctrl + -