Table 1. Results of Terpolymerization as a Function of Input Content of High α-olefins

Run No.a	High α-olefin (mol/L)		Yield Before Soxhlet (g)	Yield After Soxhlet (g)	Catalytic Activityb	Mwc (×10-3)	Mnc (×10-3)	MWDc
1	1-Hexene	0.2	7.00	0.32	384	153	49	3.1
2		0.4	7.12	1.30	1560	147	45	3.2
3		0.6	8.74	4.23	5076	115	36	3.2
4		0.8	8.13	3.94	4728	136	40	3.4
5	1-Octene	0.2	7.11	0.41	492	203	67	3.0
6		0.4	6.87	2.02	2424	180	58	3.1
7		0.6	7.32	2.68	3216	142	41	3.5
8		0.8	7.66	4.21	5052	131	41	3.2
9	1-Decene	0.2	5.18	2.12	2544	266	78	3.4
10		0.4	7.56	5.46	6552	251	83	3.0
11		0.6	9.21	7.89	9468	197	59	3.3
12		0.8	14.33	11.75	14100	161	52	3.1
13	1-Dodecene	0.2	6.42	0.94	1308	210	60	3.5
14		0.4	9.27	3.21	3852	214	63	3.4
15		0.6	8.26	5.34	6408	205	60	3.4
16		0.8	9.81	4.62	5544	190	59	3.2

Polymerization conditions: ethylene=0.4 mol/L, DVB=0.2 mol/L, 50°C, 20 min, 500 rpm, 300 mL stainless autoclave, rac-Et(Ind)₂ZrCl₂=2.5 μmol, Al/Zr=500, and B/Zr=1.5.
Kg of polymer/(mol of catalyst·h.).
cDetermined by GPC data.