Prarancangan Pabrik Etilbenzena Dari Etilena dan Benzena Dengan Proses UNOCAL/UOP Kapasitas 200.000 Ton/Tahun

• मुख्य लेखकों: Nashruddin, Muhammad (लेखक), , Emi Erawati, S.T., M.Eng (लेखक), , M. Mujiburohman, S.T., M.T., Ph.D (लेखक)
• स्वरूप: पुस्तक
• प्रकाशित: 2015.
• विषय: Thesis; NonPeerReviewed
• ऑनलाइन पहुंच: Connect to this object online

Ethylbenzene plant design capacity of 200,000 tons per year from ethylene and benzene will use the Unocal/UOP process using Fixed Bed Reactor Multitube with an operating temperature of 180-199.94oC and pressure of 5 atm. The reaction takes place in the phase of preparing ethylbenzene gases, irrevers...