Structure-controllable polymethylene macro-molecule initiating agent and preparation method and application thereof
A technology of macromolecular initiator and polymethylene, which is applied in the field of polymethylene macroinitiator, can solve the problems of group conversion and preparation of macromolecular initiator, etc.
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Embodiment 1
[0047] The preparation of the macroinitiator based on polyolefin with controllable structure of the present invention:
[0048] (1) Preparation of main chain terminal hydroxyl polyolefin
[0049] In a dry 500mL three-neck flask equipped with a reflux condenser, pass N 2 Add 3113g (0.242mol) of trimethylthionyl chloride under the state, add 7.55g (0.315mol) of NaH, add dry 250mL toluene with a syringe, reflux for 5h, filter the obtained gray suspension to obtain the toluene of ylide solution (concentration is 0.6mmol / mL).
[0050] In a dry 500mL three-necked flask equipped with a magnetic stirrer and a reflux condenser, N 2 Add 300mL (0.18mol) of the above-mentioned ylide toluene solution through a syringe under protection, stir at room temperature, and quickly add 0.60mL (0.60mmol) of BH 3 ·SMe 2 (Yi Lide / BH 3 ·SMe 2 molar ratio = 300), slowly warming up to 75°C. After reacting for 1 hour, cool down to room temperature, add 0.40 g (3.60 mmol) trimethylammonium oxide dih...
Embodiment 2~ Embodiment 12
[0054] The preparation of the controllable polymethylene macromolecular initiator of structure of the present invention:
[0055] Operation is basically the same as embodiment 1. The difference is that PM 1 -OH consumption, the type and amount of compound (I) in the esterification reaction process, the type and amount of catalyst, reaction solvent, reaction temperature, and reaction time are not completely the same as in Example 1. The structure-controllable polymethylene macroinitiator PM was obtained by the reaction 1 -(X) 2 . Wherein, X is Cl or Br, and the subscript "2" outside the brackets means two Xs.
[0056] The specific experimental conditions and polymer characterization data are shown in Table 1:
[0057] Table 1
[0058]
[0059] Note: PM 1 The amount of -OH is 0.67g (0.76mmol, 1 equiv.); the amount of solvent is 30mL; the conversion rate of the group is ~100%;
[0060] Obtain structure controllable polymethylene macromolecule initiator PM in embodiment...
Embodiment 10
[0063] The preparation of the polyolefin-based macromolecular initiator with controllable structure of the present invention:
[0064] (1) Preparation of main chain terminal hydroxyl polyolefin
[0065] Operation is basically the same as embodiment 1. The difference is that BH 3 ·SMe 2 The dosage is 0.4mL (0.4mmol) (Yet / BH 3 ·SMe 2 Molar ratio=600), the consumption of trimethylammonium oxide dihydrate is 0.27g (2.4mmol). To obtain the main chain terminal hydroxyl polyolefin PM 2 -OH(M n (GPC) = 1800 g / mol, PDI = 1.08, hydroxyl content = 0.35 mmol / g).
[0066] (2) Esterification reaction
[0067]In a dry 100mL round-bottomed flask with a condenser and a magnetic stirrer, add 3.0g (1.05mmol OH, 1 equiv.) of the product PM obtained above under nitrogen protection 2 -OH, 1.5mL (10.5mmol, 12equiv.) Catalyst triethylamine (TEA) and 120mL of toluene, stirring and dissolving at 90°C and cooling down to room temperature, then slowly dripping 5.0mL (51.8mmol, 12.2 equiv.) comp...
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