EP 1261649 A2 20021204 - PROCESS FOR PRODUCING POLYPROPYLENE FROM C3 OLEFINS SELECTIVELY PRODUCED IN A FLUID CATALYTIC CRACKING PROCESS FROM A NAPHTHA/STEAM FEED
Title (en)
PROCESS FOR PRODUCING POLYPROPYLENE FROM C3 OLEFINS SELECTIVELY PRODUCED IN A FLUID CATALYTIC CRACKING PROCESS FROM A NAPHTHA/STEAM FEED
Title (de)
VERFAHREN ZUR HERSTELLUNG VON POLYPROPYLEN AUS C3-OLEFINEN DIE IN EINEM FLUIDISIERTEN KATALYTISCHEN KRACKVERFAHREN AUS EINEM NAPHTHA/DAMPF-STROM SELEKTIV HERGESTELLT WERDEN
Title (fr)
PROCEDE DE PRODUCTION DE POLYPROPYLENE A PARTIR D'OLEFINES C 3? PRODUITES SELECTIVEMENT DANS UN PROCESSUS DE CRAQUAGE CATALYTIQUE FLUIDE A PARTIR D'UNE ALIMENTATION EN NAPHTA/VAPEUR
Publication
Application
Priority
- US 0106685 W 20010301
- US 51755400 A 20000302
- US 51755100 A 20000302
- US 51750300 A 20000302
- US 51749700 A 20000302
Abstract (en)
[origin: WO0164763A2] A process for producing polymers from olefins selectively produced from a catalytically cracked or thermally cracked naphtha stream is disclosed herein. The naphtha stream is introduced into a process unit comprised of a reaction zone, a stripping zone, a catalyst regeneration zone, and a fractionation zone. The naphtha feedstream is contacted in the reaction zone with a catalyst containing from about 10 to 50 wt. % of a crystalline zeolite having an average pore diameter less than about 0.7 nanometers at reaction conditions which include temperatures ranging from about 500 DEG to 650 DEG C and a hydrocarbon partial pressure from about 10 to 40 psia. Vapor products are collected overhead and the catalyst particles are passed through the stripping zone on the way to the catalyst regeneration zone. Volatiles are stripped with stream in the stripping zone and the catalyst particles are sent to the catalyst regeneration zone where coke is burned from the catalyst, which is then recycled to the reaction zone. Overhead products from the reaction zone are passed to a fractionation zone where a stream of C3 products is recovered and a stream rich in C4 and/or C5 olefins is recycled to the stripping zone. The olefins can be further processed and polymerized to form a variety of polymer materials.
IPC 1-7
IPC 8 full level
C07B 61/00 (2006.01); C07C 4/06 (2006.01); C07C 11/06 (2006.01); C08F 2/00 (2006.01); C08F 4/18 (2006.01); C08F 10/00 (2006.01); C08F 10/06 (2006.01); C10G 11/05 (2006.01); C10G 11/08 (2006.01); C10G 11/18 (2006.01); C10G 51/02 (2006.01); C10G 57/02 (2006.01)
CPC (source: EP)
C10G 51/026 (2013.01); C10G 57/02 (2013.01); C10G 2400/20 (2013.01)
Citation (search report)
See references of WO 0164761A2
Designated contracting state (EPC)
AT BE CH CY DE DK ES FI FR GB GR IE IT LI LU MC NL PT SE TR
DOCDB simple family (publication)
WO 0164763 A2 20010907; WO 0164763 A3 20020131; AU 3999001 A 20010912; AU 3999101 A 20010912; AU 4191601 A 20010912; AU 4337901 A 20010912; CA 2400382 A1 20010907; CA 2400524 A1 20010907; CA 2400598 A1 20010907; CN 1406252 A 20030326; CN 1406253 A 20030326; CN 1406254 A 20030326; EP 1259555 A2 20021127; EP 1261648 A2 20021204; EP 1261649 A2 20021204; JP 2003525323 A 20030826; JP 2004516334 A 20040603; JP 2004516335 A 20040603; MX PA02008552 A 20030312; MX PA02008553 A 20030312; MX PA02008554 A 20030422; WO 0164760 A2 20010907; WO 0164760 A3 20020103; WO 0164761 A2 20010907; WO 0164761 A3 20020103; WO 0164762 A2 20010907; WO 0164762 A3 20020124
DOCDB simple family (application)
US 0106687 W 20010301; AU 3999001 A 20010301; AU 3999101 A 20010301; AU 4191601 A 20010301; AU 4337901 A 20010301; CA 2400382 A 20010301; CA 2400524 A 20010301; CA 2400598 A 20010301; CN 01805858 A 20010301; CN 01805862 A 20010301; CN 01805874 A 20010301; EP 01913235 A 20010301; EP 01914623 A 20010301; EP 01916344 A 20010301; JP 2001564252 A 20010301; JP 2001564253 A 20010301; JP 2001564255 A 20010301; MX PA02008552 A 20010301; MX PA02008553 A 20010301; MX PA02008554 A 20010301; US 0106684 W 20010301; US 0106685 W 20010301; US 0106686 W 20010301