三効蒸発器の蒸発面積はどのように決定するのか？
Thread Content
立式列管式；ケーシング側、0.4MPaの飽和蒸気を投入し、90℃の凝縮水を排出；管程、25℃、5t/h 水投入；蒸発量を3t/hにするために、各効のヒーターの加熱面積が同じである場合、どれくらい必要か？簡単な計算手順は？また、第一効果での蒸気消費量はいくらですか？
どなたか詳しい方いますか？管程と殻程はそれぞれ2つの段階で計算するんでしょうか？
**Looking for Chemical Technology, Equipment & Solutions?** No Registration Required Broader Platform Exposure | Global Chemical Service Provider Connections
Submit Request — Free ConsultationThis 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.