HCBBS Forum (日本語)
Submit Chemical Projects / Find Solutions
Amplify Your Requirements on a Broader Chemical Platform *Engineering · Technology · Equipment · Solutions*
Submit Request

空分装置の熱交換器の抵抗はどう計算するか

2015-11-21View Original

Thread Content

低圧板式熱交換器の抵抗はどのように計算するのか、汚染窒素の板式熱交換器の抵抗というのは、上塔の圧力から水冷塔の圧力を引いた値なのでしょうか?一般的にはどのくらいで、25KPaは高いですか?低圧板式熱交換器の抵抗が小さいかどうかを判断するには、どの値を見ればよいのでしょうか?
Reply #22015-11-23
私は普段、このように計算します。塔内圧力-塔下部の頂部圧力+塔下部の抵抗=プレート型抵抗(空気通路)。他の部分は、皆さん自身で計算してみてください~~

Submit a Project

**Looking for Chemical Technology, Equipment & Solutions?** No Registration Required Broader Platform Exposure | Global Chemical Service Provider Connections

Submit Request — Free Consultation

Disclaimer

This is an automated machine translation of the original thread. Some technical terms may have inaccuracies; the original text shall prevail. Click "View Original" at the top right to access the source page, which supports IP-based automatic real-time language translation. Please watch out for contact details and sales inducements to prevent fraud. All content and translations are for reference only, representing solely the poster's personal views. For enquiries, email service@hcbbs.com.