Procatalyst and polymerization process using the same
US-2018265604-A1 · Sep 20, 2018 · US
US12466901B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-12466901-B2 |
| Application number | US-202017630802-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jul 30, 2020 |
| Priority date | Jul 31, 2019 |
| Publication date | Nov 11, 2025 |
| Grant date | Nov 11, 2025 |
A practical reading order for non-experts. Skip the full description unless you need deep technical detail.
What the patent document calls the invention.
A short plain-language summary of the technical disclosure.
Who owns or filed the patent and who is credited as inventor.
Filing, priority, publication, and grant dates set the timeline.
The legal scope of protection — read this for what is actually claimed.
Technology tags used to group this patent with similar filings.
Prior art links and similar publications in this corpus.
Official abstract text for this publication.
Processes of polymerizing olefin monomers and catalyst systems. The catalyst systems include a non-hydrogen-generating post-metallocene procatalyst; a co-catalyst; and a hydrogenation procatalyst having the formula Cp 2 TiX n TiCp 2 or Cp 2 TiX n , in which each Cp is cyclopentadienyl substituted with at least one (C 1 -C 10 )alkyl; each X is independently monoanionic or neutral, wherein each X is independently (C 1 -C 40 )hydrocarbon, (C 1 -C 40 )heterohydrocarbon, (C 1 -C 40 )hydrocarbyl, (C 1 -C 40 )heterohydrocarbyl, or a halogen atom; and n is 1 or 2.
Opening claim text (preview).
The invention claimed is: 1 . A catalyst system comprising: a non-hydrogen-generating post-metallocene procatalyst; a co-catalyst; and a hydrogenation procatalyst having the formula Cp 2 TiX 2 TiCp 2 or Cp 2 TiX n , where: each Cp is cyclopentadienyl optionally substituted with at least one (C 1 -C 10 ) alkyl; each X is independently (C 1 -C 40 )hydrocarbon, (C 1 -C 40 )heterohydrocarbon, (C 1 -C 40 )hydrocarbyl, (C 1 -C 40 )heterohydrocarbyl, or a halide; and n is 1 or 2; wherein the non-hydrogen-generating post-metallocene procatalyst is a metal-ligand complex according to formula (I): where: M is a metal selected from titanium, zirconium, or hafnium, the metal being in a formal oxidation state of +2, +3, or +4; n is 0, 1, or 2; when n is 1, X 1 is a monodentate ligand or a bidentate ligand; when n is 2, each X 1 is independently a monodentate ligand; each X 1 that is a monodentate ligand is independently halide, unsubstituted (C 1 -C 20 )hydrocarbyl, unsubstituted (C 1 -C 20 )hydrocarbyl, C(O)O—, or R K R L N—, where each of R K and R L is independently an unsubstituted (C 1 -C 20 )hydrocarbyl; L is a diradical selected from the group consisting of (C 1 -C 40 )hydrocarbylene, (C 1 -C 40 )heterohydrocarbylene, —Si(R C ) 2 -, —Si(R C ) 2 OSi(R C ) 2 -, —Si(R C ) 2 C(R C ) 2 -, —Si(R C ) 2 Si(R C ) 2 -, —Si(R C ) 2 C(R C ) 2 Si(R C ) 2 -, —C(R C ) 2 Si(R C ) 2 C(R C ) 2 -, —N(R N )C(R C ) 2 -, —N(R N )N(R N )-, and —C(R C ) 2 N(R N )C(R C ) 2 -, each Z is independently selected from —O—, —S—, —N(R N )-, or —P (R P )-; R 1 , R 2 , R 3 , R 4 , R 5 , R 6 , R 7 , R 8 , R 9 , R 10 , R 11 , R 12 , R 13 , R 14 , R 15 , and R 16 are independently selected from the group consisting of —H, (C 1 -C 40 )hydrocarbyl, (C 1 -C 40 )heterohydrocarbyl, —Si(R C ) 3 , —Ge(R C ) 3 , —P(R P ) 2 , —N(R N ) 2 , —OR C , —SR C , —NO 2 , —CN, —CF 3 , R C S(O)—, R C S(O) 2 —, —N═C(R C ) 2 , R C C(O)O—, R C OC(O)—, R C C(O)N(R)—, (R C ) 2 NC(O)—, halide, radicals having formula (XI), radicals having formula (XII), and radicals having formula (XIII): where: each of R 31 -R 35 , R 41 -R 48 , and R 51 -R 59 is independently selected from —H, (C 1 -C 40 )hydrocarbyl, (C 1 -C 40 )heterohydrocarbyl, —Si(R C ) 3 , —Ge(R C ) 3 , —P(R P ) 2 , —N(R N ) 2 , —OR C , —SR C , —NO 2 , —CN, —CF 3 , R C S(O)—, R C S(O) 2 —, (R C ) 2 C═N—, R C C(O)O—, R C OC(O)—, R C C(O)N(R N )-, (R C ) 2 NC(O)—, or halide; and wherein the non-hydrogen-generating post-metallocene procatalyst is unsupported and the hydrogenation procatalyst is unsupported. 2 . A catalyst system comprising: a non-hydrogen-generating post-metallocene procatalyst; and Cp 2 TiX 2 treated with an aluminum alkyl species, where: each Cp is cyclopentadienyl substituted with at least one (C 1 -C 10 ) alkyl; each X is independently (C 1 -C 40 )hydrocarbon, (C 1 -C 40 )heterohydrocarbon, (C 1 -C 40 )hydrocarbon anion, (C 1 -C 40 )heterohydrocarbon anion, or a halide; wherein the non-hydrogen-generating post-metallocene procatalyst is a metal-ligand complex according to formula (I): where: M is a metal selected from titanium, zirconium, or hafnium, the metal being in a formal oxidation state of +2, +3, or +4; n is 0, 1, or 2; when n is 1, X 1 is a monodentate ligand or a bidentate ligand; when n is 2, each X 1 is independently a monodentate ligand; each X 1 that is a monodentate ligand is independently halide, unsubstituted (C 1 -C 20 )hydrocarbyl, unsubstituted (C 1 -C 20 )hydrocarbyl, C(O)O—, or R K R L N—, where each of R K and R L is independently an unsubstituted (C 1 -C 20 )hydrocarbyl; L is a diradical selected from the group consisting of (C 1 -C 40 )hydrocarbylene, (C 1 -C 40 )heterohydrocarbylene, —Si(R C ) 2 -, —Si(R C ) 2 OSi(R C ) 2 -, —Si(R C ) 2 C(R C ) 2 -, —Si(R C ) 2 Si(R C ) 2 -, —Si(R C ) 2 C(R C ) 2 Si(R C ) 2 -, —C(R C ) 2 Si(R C ) 2 C(R C ) 2 -, —N(R N )C(R C ) 2 -, —N(R N )N(R N )-, and —C(R C ) 2 N(R N )C(R C ) 2 -, each Z is independently selected from —O—, —S—, —N(R N )-, or —P (R P )-; R 1 , R 2 , R 3 , R 4 , R 5 , R 6 , R 7 , R 8 , R 9 , R 10 , R 11 , R 12 , R 13 , R 14 , R 15 , and R 16 are independently selected from the group consisting of —H, (C 1 -C 40 )hydrocarbyl, (C 1 -C 40 )heterohydrocarbyl, —Si(R C ) 3 , —Ge(R C ) 3 , —P(R P ) 2 , —N(R N ) 2 , —OR C , —SR C , —NO 2 , —CN, —CF 3 , R C S(O)—, R C S(O) 2 —, —N═C(R C ) 2 , R C C(O)O—, R C OC(O)—, R C C(O)N(R)—, (R C ) 2 NC(O)—, halide, radicals having formula (XI), radicals having formula (XII), and radicals having formula (XIII): where: each of R 31 -R 35 , R 41 -R 48 , and R 51 -R 59 is independently selected from —H, (C 1 -C 40 )hydrocarbyl, (C 1 -C 40 )heterohydrocarbyl, —Si(R C ) 3 , —Ge(R C ) 3 , —P(R P ) 2 , —N(R N ) 2 , —OR C , —SR C , —NO 2 , —CN, —CF 3 , R C S(O)—, R C S(O) 2 —, (R C ) 2 C═N—, R C C(O)O—, R C OC(O)—, R C C(O)N(R N )-, (R C ) 2 NC(O)—, or halide; and wherein the non-hydrogen-generating post-metallocene procatalyst is unsupported and the Cp 2 TiX 2 treated with an aluminum alkyl species is unsupported. 3 . The catalyst system of claim 2 , wherein the aluminum alkyl species comprises alkylaluminoxane, modified alkylaluminoxane, or an aluminum alkyl having the formula AlR 3 wherein each R is independently (C 1 -C 40 )hydrocarbon (C 1 -C 40 )heterohydrocarbon, (C 1 -C 40 )hydrocarbyl, (C 1 -C 40 )heterohydrocarbyl, or a halide. 4 . The catalyst system of claim 2 , wherein the aluminum alkyl species is the reaction product of AlR 3 and water, alcohol, silanol, or a Lewis base. 5 . The catalyst system of claim 4 , wherein the Lewis base is pyridine or mono-substituted alkylamine, disubstituted alkylamine, or tri-substituted alkylamine. 6 . The catalyst system of claim 2 , wherein the aluminum alkyl species is diisobutylaluminum oxide (DIBAO or DIBAL-O) or Isobutylaluminoxane (IBAO). 7 . The catalyst system of claim 1 , wherein the catalyst system further comprises an impurity scavenger. 8 . The catalyst system of claim 1 , wherein each X is a substituted benzyl or substituted heteroarylbenzyl. 9 . The catalyst system of claim 1 , wherein X is selected from the group consisting of: 10 . The catalyst system of claim 1 , wherein the non-hydrogen-generating post-metallocene procatalyst produces less than or equal to 1 ppm of hydrogen under polymerization conditions. 11 . The catalyst system of claim 2 , wherein the catalyst system further comprises an impurity scavenger. 12 . The catalyst system of claim 2 , wherein each X is a substituted benzyl or substituted heteroarylbenzyl. 13 . The catalyst system of claim 2 , wherein X is selected from the group consisting of: 14 . The catalyst system of claim 2 , wherein the non-hydrogen-generating post-metallocene procatalyst produces less than or equal to 1 ppm of hydrogen under polymerization conditions.
Recycling of unreacted starting or intermediate materials · CPC title
Ethene · CPC title
in combination with an organoaluminium compound · CPC title
Low molecular weight, e.g. <100,000 Da. · CPC title
Heteroatom-substituted Cp, i.e. Cp or analog where at least one of the substituent of the Cp or analog ring is or contains a heteroatom · CPC title
Related publications grouped by family.
Answers are generated from the same data shown on this page.