作者查詢 / Starvilo
作者 Starvilo 在 PTT [ ChemEng ] 看板的留言(推文), 共20則
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1F推: 我製程操作的確如此116.118.180.27 06/30 17:37
2F→: 實際跟理論還是有差距喔~~116.118.180.27 06/30 17:37
3F→: 例如可以11板攝取出溫度 12板也可116.118.180.27 06/30 17:38
4F→: 配合取樣分析,只有達產品純度需求116.118.180.27 06/30 17:39
5F→: 即可,最後在考慮節能操作,才是完美116.118.180.27 06/30 17:39
6F→: 現實中就是這樣操作116.118.180.27 06/30 17:40
7F→: 你說的都是理論而已116.118.180.27 06/30 17:40
1F推: 每板有每板的組成,溫度控制改變每板的223.138.12.102 06/05 05:54
2F→: 組成,並無特定找出最佳溫控,可以固定某223.138.12.102 06/05 05:54
3F→: 一點當作參考,223.138.12.102 06/05 05:54
2F推: 再沸器氣提量夠嗎116.118.180.27 06/01 18:34
2F→: 手閥全關應該就沒壓損問題?111.82.128.70 05/29 20:58
5F→: 目前無法理解出口壓小的原因223.139.177.236 05/30 17:42
12F→: 看過了V QQ223.139.177.236 05/30 19:18
16F→: 恩111.82.231.119 06/01 13:13
17F→: 壓力不夠易造成某些加熱在管線氣化111.83.186.243 06/01 17:47
18F→: 目前還是請廠商在pump 拆修看有無問題111.83.186.243 06/01 17:49
19F→: 確定pump問題,內部軸心腐蝕,更換正常223.137.23.125 06/06 00:44
21F→: 另外由於他是2段式pump,1-2段間的軸套損223.137.23.125 06/06 17:46
22F→: 耗,導致有回流,作虛功223.137.23.125 06/06 17:46
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