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降压孔板是如何降压的? 降压孔板降压原理其实是运用了能量守恒定律: 一定体积、一定能量,一定温度的物质在经过扩经段以后,体积增大,能量减小(这里主要指压力能),温度降低。 另外补充下降压孔板中为何设计为多孔样式,其主要目的在于均匀分布,最大限度的降低对操作的波动,最终达到烟气经三旋和临界喷嘴后顺利返回烟道的工况。查看更多
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沸腾炉出渣方式选择? 连续排渣用得比较多,还有一条看你用的什么原料,含硫多少,如果渣量大的话可以增加一个排渣孔查看更多
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关于工业环保的法律法规? 环保法律法规是比较好查的了,不像安全的;安全的好多法规还要去买才能下载。查看更多
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机械密封 PLAN52密封方案,冬季密封油温度进口大于出口 ...? 介质温度低,对密封液进行冷却,自然是进口低,出口高了。 问题是进密封温度是60.5,怎么可能?这么高 ... 密封罐的表面温度,我们怀疑是密封液没有循环起来。 查看更多
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新扩建的汽油加氢改造中加热炉在反应器之后? 几个反应器呀,有可能是那种选择性加氢的,两个反应器的吧查看更多
哪位大侠有2006年石化燕山的ASPEN培训教材? 能给我发一份吗? jackli111000 谢谢!谢谢!查看更多
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有机硅行业的前景怎么样?欢迎大家积极参与,畅所欲言。? 欢迎来发言领财富! @654262293 @lrxlrxlrxlrx @王天泽 @优点呆 @经典 @催化一粟 @沙漠里的游鱼 @李家小弟 @恶贯满盈 @tclz007 @o.k. @co2leaks @傻傻小木头 @zqwqiwu123 @bt饮水思源 @qq172424245 查看更多
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93%超声波酸浓仪不准? 改下出口管,出口管要高于酸浓仪,目的是让酸浓仪充分浸泡在酸里面,测量出来的数据才准确。查看更多
分光光度法标准曲线最后两点偏低什么原因,怎么避免? 标准样稀释过程中出现偏差,每次稀释溶液样必须选择母液进行。查看更多
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抽滤时滤饼很黏稠,过滤速度很慢,怎么办? 收益匪浅查看更多
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水封槽的设置多少合适? 本文由 盖德化工论坛 转载自互联网 有人说水封槽一般五十米设置一个,这么设置的目的是什么?为什么要设置多个水封槽?注:是甲醇制取甲醛工业中使用的。查看更多
请高手帮忙,空分装置区应设置蒸汽管道,用于阀门解冻或 ...? 设置蒸汽管道的主要原因是: 当装置长时间停车时,需要把冷箱内的低温液体排掉。 如果直接排放,存在一定的安全问题:一是低温液体对人产生冻伤的危险性,二是氧气局部浓缩易发生火灾的危险性,三是氮气、氩气局部浓缩使人窒息的危险性。 所以通常都是气化后放空。 低温液体气化需要热量,一般用蒸汽作为热源;实在没有,用原料空压机后的空气也可以查看更多
横河DCS VP 系统? 亲,你这个问题很难回答啊,要具体问题具体分析啊查看更多
反渗透膜怎么处理? 帮我联系一下啊!查看更多
换热器两侧流体的温度和温差问题? 对的,:):):):):):):)查看更多
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如何进行含有机磷废水的处理? 原帖由 cdpulin 于 2008-6-26 09:55 发表 有机膦,直接混凝几乎不起作用,如果用吸附的办法则处理成本太高。有机膦首先得用氧化使其产生水解转变成正磷酸盐,再用混凝剂进行脱除。如果含量不是特别高,也可以用厌氧的方法使其转变成正磷,再进行去除。 ... 有机膦首先得用氧化使其产生水解转变成正磷酸盐,再用混凝剂进行脱除。 学习了啊 查看更多
丹麦酒店的低碳高招? https:///thread-1283022-1-6.html 依靠人的运动产生电能的例子很多,见上帖查看更多
求助换热器设计问题? 我这两天再找防共鸣板的例子和该结构详图,非常抱歉我居然在我的50g资料库里没有留下以前我做过的vendor's drawings. 唉,那阵子我刚有宝宝脑袋不好用了,连这个也没有备份。 防共鸣板(de-resonating baffle)是多孔的一块板使得流体的频率和设备管束的固有频率分开,通常first mode 在换热器的45%左右位置,second mode & higher 在81%换热器位置。 please refer to: https:///securel2/designmanual/dmcontent/c7.3.pdf design manuel c7.3 design lnprovements c7.3.3 • add deresonating baffles. acoustic vibration placing deresonating baffles in all heat exchanger crosspasses can noise, increase the acoustic frequency, thus eliminating any acoustic continued vibration problem. these deresonating baffles should be parallel to both the direction of crossflow and the centerline of the tubes, so that they do not materially alter the thermal and hydraulic performance of the heat exchanger. often, tubes must be removed to install deresonating baffles; installation should be done carefully to ensure that outer edges of the deresonating baffles are at least 3 to 5 in. (76 to 127 mm) from the shell. incorrect placement of deresonating baffles can seriously affect performance of heat exchangers with two-phase flow on the shell side by causing an undesirable separation of the phases. although xist does not handle deresonating baffles, a discussion is provided in stv-4 [31 and by barrington [4, 5j. a few guidelines in the literature describe the size, thickness, or placement of deresonating baffles to prevent acoustic resonance in shell-and-tube heat exchangers. chen [61 recommends dividing the exchanger with deresonating baffles to create acoustic frequencies as different from one another as possible. in this way, higher damping is achieved due to the interaction of individual chambers; any resonance is localized and the number of baffles minimized. following this recommendation, figure c7.3-1 shows that, to affect the first five modes, the best position for a single baffle is about 0.05 d off the centerline. the resulting characteristic lengths are 55 and 45 percent of the shell diameter, which are most effective in suppressing the first mode. on the other hand, if two baffles are used, they should be placed about 0.05 d on one side of the centerline and 0.32d on the other. this arrangement produces characteristic lengths of 18, 37, and 45 percent of the shell diameter. because the acoustic frequencies are inversely proportional to the characteristic length, the resulting frequencies are increased by 5.6, 2.7, and 2.2 times the acoustic frequency without the deresonating baffles. figure c7.3-1. recommended placement of deresonating baffles. blevins [7] cautions that for a deresonating baffle to be effective, it must be capable of reflecting a sound wave. such an observation implies a baffle with more mass than the surrounding shellside fluid. the baffle thickness must be greater than b b sf b x t (c7.3-1) change the shell diameter. although often not the most attractive approach, a change in the shell diameter can alter the acoustic frequency; however, it may also cause a significant and unacceptable change in the thermal and hydraulic performance of the heat exchanger. changing the shell diameter is less effective than adding deresonating baffles. avoid a frequency match. on those rare occasions when the acoustic and tube natural frequencies nearly match, the acoustic frequency should be changed by adding deresonating baffles or the tube natural frequency should be changed by shortening the maximum unsupported span length. shortening the span is more effective, if allowable pressure drop permits. c7.3.3 acoustic vibration noise, continued first deresonating baffle second deresonating baffle mode 1 2 3 4 5 0.45 d s 0.37 d s 0.18 d s 哎呀!就htri 有一份对于该软件的资料详细的介绍了htri的振动分析的warning, analysis region: https:///securel1/so ... ls/fundamentals.pdf (对不起,这是htri的copy right. 这份fundamentals 是我极力推荐给用htri的设计人员的软件入门资料,必读。) i recommend a paper for heat exchanger accoustic vib:查看更多
生物质秸秆炭化炉 的结构设计与试验研究,摘要? 你是要这篇文献?查看更多
捣固焦炉标准温度? 也是根据焦饼最终温度能达到950-1050℃来确定标准温度。由于锥度一般小于20,所以基本不考虑机焦温差。根据实际生产情况由于机侧敞炉门时间长,也可机侧稍高于焦侧(慎重)。查看更多
简介
职业:江苏威名石化有限公司 - 工艺技术员
学校:长江大学 - 化工
地区:辽宁省
个人简介:人生贵知心,定交无暮早。查看更多
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