Isotactic polypropylene produced from supercritical polymerization process
An isotactic, propylene technology, used in the production of bulk chemicals, etc.
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Embodiment S013-S0
[0180] Embodiment S013-S022: C3 monomer feed 14g / min, hexane solvent 80ml / min
[0181] The supercooling limit (SCL) is given by SCL=0.907x-99.64, where x is Tmp.
[0182] Slurry polymerized polypropylene (comparative example)
[0183] Tables 5, 6 and 7 describe prior art bulk slurry polymerized propylene homopolymers and their preparation conditions. The technology for producing propylene homopolymers via bulk slurry polymerization is based on conventional Ziegler-Natta catalysts as well as supported Metallocene catalysts are well documented in the literature.
[0184] ACHIEVE TM 1605, 3854 and 6025G1 are commercial homopolymers made in commercial reactors available from ExxonMobil Chemical Co., Houston, TX. Slurry Examples SL1-SL4 were similar to these ACHIEVE products. They were produced in similar commercial reactors, but the process conditions were adjusted to achieve different MFR and molecular weight (Mw by GPC) values, as shown in Table 6.
[0185] Table 5. Catal...
Embodiment S
[0201] Embodiment SL5 Embodiment SL6
[0202] Catalyst feed rate (g / hr) 4.9 3.4
[0203] Scavenger (TEAL) feed rate (ml / min) 4.6 4.5
[0204] (2wt% in hexane)
[0205] Leading reactor temperature (°C) 74 74
[0206] Lead Reactor Pressure (psig) 471.6 474.6
[0207] Lead reactor C3 feed (kg / hr) 79.5 79.6
[0208] Leading reactor H2 gas concentration (mppm) 1156 2986
[0209] Tail reactor temperature (°C) 68 68
[0210] Tail reactor pressure (psig) 421.7 421.2
[0211] Tail reactor C3 feed (kg / hr) 29.5 29.5
[0212] Tail reactor H2 gas concentration (mppm) 1314 3613
[0213] Leading reactor production rate (kg / hr) 28.5 22.7
[0214] Tail reactor production rate (kg / hr) 10.7 11.8
[0215] Total production rate (kg / hr) 39.1 34.5
[0216] Leading reactor residence time (hr) 2.56 2.85
[0217] Tail reactor residence time (hr) 1.87 1.86
[0218] Total residence time (hr) 4.4 4.7
[0219] The polymer is discharged from the reactor as a...
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