KR101746030B1 - Solid catalyst for polyketone polymerization and its manufacturing method - Google Patents

Solid catalyst for polyketone polymerization and its manufacturing method Download PDF

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KR101746030B1
KR101746030B1 KR1020160014194A KR20160014194A KR101746030B1 KR 101746030 B1 KR101746030 B1 KR 101746030B1 KR 1020160014194 A KR1020160014194 A KR 1020160014194A KR 20160014194 A KR20160014194 A KR 20160014194A KR 101746030 B1 KR101746030 B1 KR 101746030B1
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bis
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methoxyphenyl
phosphine
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신혜미
심재윤
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주식회사 효성
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    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G67/00Macromolecular compounds obtained by reactions forming in the main chain of the macromolecule a linkage containing oxygen or oxygen and carbon, not provided for in groups C08G2/00 - C08G65/00
    • C08G67/02Copolymers of carbon monoxide and aliphatic unsaturated compounds
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J31/00Catalysts comprising hydrides, coordination complexes or organic compounds
    • B01J31/16Catalysts comprising hydrides, coordination complexes or organic compounds containing coordination complexes
    • B01J31/18Catalysts comprising hydrides, coordination complexes or organic compounds containing coordination complexes containing nitrogen, phosphorus, arsenic or antimony as complexing atoms, e.g. in pyridine ligands, or in resonance therewith, e.g. in isocyanide ligands C=N-R or as complexed central atoms
    • B01J31/1845Catalysts comprising hydrides, coordination complexes or organic compounds containing coordination complexes containing nitrogen, phosphorus, arsenic or antimony as complexing atoms, e.g. in pyridine ligands, or in resonance therewith, e.g. in isocyanide ligands C=N-R or as complexed central atoms the ligands containing phosphorus
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J37/00Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
    • B01J37/0009Use of binding agents; Moulding; Pressing; Powdering; Granulating; Addition of materials ameliorating the mechanical properties of the product catalyst
    • B01J37/0018Addition of a binding agent or of material, later completely removed among others as result of heat treatment, leaching or washing,(e.g. forming of pores; protective layer, desintegrating by heat)
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    • C07ORGANIC CHEMISTRY
    • C07FACYCLIC, CARBOCYCLIC OR HETEROCYCLIC COMPOUNDS CONTAINING ELEMENTS OTHER THAN CARBON, HYDROGEN, HALOGEN, OXYGEN, NITROGEN, SULFUR, SELENIUM OR TELLURIUM
    • C07F9/00Compounds containing elements of Groups 5 or 15 of the Periodic Table
    • C07F9/02Phosphorus compounds
    • C07F9/28Phosphorus compounds with one or more P—C bonds
    • C07F9/50Organo-phosphines
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07FACYCLIC, CARBOCYCLIC OR HETEROCYCLIC COMPOUNDS CONTAINING ELEMENTS OTHER THAN CARBON, HYDROGEN, HALOGEN, OXYGEN, NITROGEN, SULFUR, SELENIUM OR TELLURIUM
    • C07F9/00Compounds containing elements of Groups 5 or 15 of the Periodic Table
    • C07F9/02Phosphorus compounds
    • C07F9/28Phosphorus compounds with one or more P—C bonds
    • C07F9/50Organo-phosphines
    • C07F9/5022Aromatic phosphines (P-C aromatic linkage)

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Abstract

The present invention relates to a Group 8 transition metal compound; (Bis (2-methoxyphenyl) phosphine (cyclohexane-1,1-diyl bis (methylene)) bis (bis (2-methoxyphenyl) phosphine) ligand having a Group 15 element and an anion of an acid having a pKa of 4 or less Wherein the Group 8 transition metal compound is palladium acetate and the anion of the acid with a pKa of 4 or less is selected from the group consisting of trifluoroacetic acid, trifluoromethanesulfonic acid, p-toluenesulfonic acid, and sulfuric acid One kind thereof.
On the other hand, the polyketone polymerization ligand of the present invention can be produced by reacting a bis (bis (2, 2-dimethyl-1,3-dioxane-5,5-diyl) bis (methylene) Methoxyphenyl) phosphine), thereby making it possible to apply various ligands to polyketone polymerization.

Description

TECHNICAL FIELD [0001] The present invention relates to a polyketone polymerization catalyst and a method for producing the same,

TECHNICAL FIELD The present invention relates to a polyketone polymerization catalyst having a high activity in a polyketone polymerization catalyst, and a polymerization catalyst ligand which is simple in structure and simple in production process and easy to mass-synthesize in a commercial manner, and a process for producing the same.

The polymerization catalyst used in the production of polyketones generally consists of a system of Pd (II) / Bidentate Phosphine Ligand / Acid. (Pd (OAc) 2-BDOMPP-TFA) system commercialized by Shell in 1999 is a representative example.

Figure 112016012254409-pat00001

1,3-bis [bis (2-methoxyphenyl) phosphino] propane (F.wt: 532.54 g / mol)

The development of highly active polymerization catalysts used in the production of polyketones is centered on the modification of bidentate phosphine ligands among the three components of the catalyst. (2-methoxyphenyl) phosphine] propane, 3,3-bis [bis- (2-methoxyphenyl) Phenylmethyl] -1,5, -dioxa-spiro [5,5] undecane, and the like are known. On the average, they exhibit a polymerization activity of more than 2 times as much as the BDOMPP system. However, since lithium is used in the synthesis, it is a dangerous reaction that can be synthesized only on a laboratory scale, so that commercial mass synthesis is not easy and expensive.

Figure 112016012254409-pat00002

(F.wt .: 560.59 g / mol), 2,2-dimethoxy-1,3-bis [di (2-methoxyphenyl)

Figure 112016012254409-pat00003

[5,5] undecane (International Patent Publication No. WO 01 / 02463A1) (F.wt: 672.73 g) was added to a solution of 3,3-bis [bis- (2- methoxyphenyl) phosphanylmethyl] -1,5-dioxa-spiro [ / mol)

(Bis (methylene)) bis (bis (2-methoxyphenyl) phosphine) ligand is easy to mass-produce commercially, and Shell 2 < / RTI > polymerization activity than BDOMPP, a commercially available ligand. It is possible to develop a polyketone highly active catalyst. It is necessary to develop a ligand exhibiting a polymerization activity equal to or higher than that of the ligand.

Figure 112016012254409-pat00004

Bis (bis (2-methoxyphenyl) phosphine (F.wt: 672.73 g / mol)

Korea Patent No. 1,546,034 Korea Patent Publication No. 2010-0041305

The present invention aims at providing a novel ligand (cyclohexane-1,1-diylbis (methylene)) bis (bis (2-methoxyphenyl) phosphine having a high polymerization activity.

According to a preferred embodiment of the present invention, a Group 8 transition metal compound; (Bis (2-methoxyphenyl) phosphine (cyclohexane-1,1-diyl bis (methylene)) bis (bis (2-methoxyphenyl) phosphine) ligand having a Group 15 element and an anion of an acid having a pKa of 4 or less Wherein the Group 8 transition metal compound is palladium acetate and the anion of the acid with a pKa of 4 or less is selected from the group consisting of trifluoroacetic acid, trifluoromethanesulfonic acid, p-toluenesulfonic acid, and sulfuric acid One kind thereof.

According to another preferred embodiment of the present invention, a solvent is added to the Group 8 transition metal compound; Bis (bis (2-methoxyphenyl) phosphine (cyclohexane-1,1-diylbis (methylene)) bis (bis (2-methoxyphenyl) phosphine) which is a ligand having a Group 15 element and an anion of an acid having a pKa of 4 or less are added, To form a three-component complex, removing the solvent from the three-component complex, freezing at a temperature below -10 ° C to form a single crystal, and grinding the single crystal to form a solid phase catalyst. A method for producing a ketone polymerization catalyst is provided.

The polyketone polymerization ligand of the present invention can be produced by reacting a polyketone polymerization ligand ((2,2-dimethyl-1,3-dioxane-5,5-diyl) bis (methylene)) bis Phenyl) phosphine), which makes it possible to apply various ligands during polyketone polymerization.

Hereinafter, the present invention will be described.

The present invention relates to a Group 8 transition metal compound; A ligand having a Group 15 element; And an anion of an acid having a pKa of 4 or less, and provides a polyketone polymerization catalyst.

Examples of the Group 8 transition metal compounds include complexes of palladium, nickel, cobalt, iron, rhodium, ruthenium, osmium, iridium or platinum. Specific examples thereof include nickel acetate, nickel acetyl acetate, palladium acetate, (Diethylamine) palladium, palladium sulfate, cobalt acetate, cobalt acetylacetate, ruthenium acetate, ruthenium acetylacetate, ruthenium acetylacetate, trifluoromethanesulfonic acid, Ruthenium, and the like, but are not limited thereto.

Among these Group VIII transition metal compounds, a transition metal compound which is inexpensive and economically preferable is a nickel compound, and a preferable transition metal compound from the viewpoint of yield and molecular weight of polyketone is a palladium compound, and from the viewpoint of improving catalytic activity and intrinsic viscosity It is most preferred to use palladium acetate.

In general, examples of ligands having a Group 15 element include 2,2-bipyridyl, 4,4-dimethyl-2,2-bipyridyl, 2,2- (2,2-dimethyl-1,3-dioxane-5,5-diyl) bis (methylene) bis (bis (2-methoxyphenyl) phosphine), 1,2- (Diphenylphosphino) ethane, 1,3-bis (diphenylphosphino) propane, 1,4-bis (diphenylphosphino) Di (2-methoxyphenyl) phosphine] propane, 1,3-bis [di (2-methoxyphenyl) Bis (diphenylphosphino) benzene, 1,2-bis [(diphenylphosphino) phenyl] phosphine] propane, 1,2-bis (diphenylphosphino) cyclohexane, Bis [[di (2-methoxy-4-sulfonic acid sodium-phenyl) -phosphoric acid methyl] benzene, 1,2- Methyl] benzene, 1,1-bis (diphenylphosphino) ferrocene, 2-hydroxy-1,3 And phosphorus ligands such as bis [di (2-methoxyphenyl) phosphino] propane and 2,2-dimethyl-1,3-bis [di (2-methoxyphenyl) But is not limited thereto.

Among them, preferred ligands (b) having a Group 15 element are phosphorus ligands having an atom of Group 15, and particularly preferred ligands in terms of the yield of polyketone are ((2,2-dimethyl- Bis (di (2-methoxyphenyl) phosphino] propane, 1, 3-dioxane-5,5-diyl) bis (methylene) bis Bis [di (2-methoxyphenyl) phosphino] methyl] benzene in view of molecular weight of polyketone and 2-hydroxy- Propane and 2,2-dimethyl-1,3-bis [di (2-methoxyphenyl) phosphino] propane. In view of safety without requiring an organic solvent, Phenyl] phosphino] methyl] benzene, which is easy to synthesize and has a large amount of (meth) And preferred in terms of economy are 1,3-bis (di Carbonyl phosphino) propane, 1,4-bis (diphenylphosphino) butane.

In the present invention, a ligand (cyclohexane-1,1-diylbis (methylene)) bis (bis (2-methoxyphenyl) phosphine used in a polymerization catalyst is used. The method is as follows.

Figure 112016012254409-pat00005

The ligand can be synthesized through the following four steps. First, diethyl malonate and 1,5-dibromopentane are boiled under sodium ethoxide and ethanol, and then reduced under lithium aluminum hydride and tetrahydrofuran to synthesize 1,1-cyclohexane dimethanol. And reacted with tosyl chloride under pyridine to give the leaving group. The ligand can be obtained by reacting it with 2-methoxyphenylphosphine and sodium hydride under dimethylsulfoxide. Each step is subjected to purification steps such as column chromatography and recrystallization, and the purity of each step can be confirmed by nuclear magnetic resonance analysis.

On the other hand, examples of the anion of the acid having a pKa of 4 or less include an anion of an organic acid having a pKa of 4 or less such as trifluoroacetic acid, trifluoromethanesulfonic acid, or p-toluenesulfonic acid; Anions of inorganic acids having a pKa of 4 or less such as perchloric acid, sulfuric acid, nitric acid, phosphoric acid, heteropoly acid, tetrafluoroboric acid, hexafluorophosphoric acid, and fluorosilicic acid; And anions of boron compounds such as trispentafluorophenylborane, trisphenylcarbenium tetrakis (pentafluorophenyl) borate, and N, N-dimethylarinium tetrakis (pentafluorophenyl) borate. It does not.

Particularly, the anion of an acid having a pKa of 4 or less, which is preferred in the present invention, is trifluoroacetic acid, which makes it possible to produce a polyketone having a high catalytic activity and a high intrinsic viscosity.

In the present invention, a polyketone polymer having a number average molecular weight of 100 to 200,000, particularly 20,000 to 90,000, as measured by gel permeation chromatography is particularly preferable. The physical properties of the polymer are determined according to the molecular weight, depending on whether the polymer is a copolymer or a terpolymer and, in the case of a terpolymer, the properties of the second hydrocarbon part. The melting point of the total of the polymers used in the present invention is 175 ° C to 300 ° C, and generally 210 ° C to 270 ° C. The intrinsic viscosity (LVN) of the polymer measured by HFIP (hexafluoroisopropyl alcohol) at 60 DEG C using a standard tubular viscosity measuring apparatus is 0.5 dl / g to 10 dl / g, preferably 0.8 dl / g to 4 dl / g, More preferably, it is 1.0 dl / g to 2.5 dl / g. If the intrinsic viscosity is less than 1.0 dl / g, the mechanical properties are deteriorated. If the intrinsic viscosity exceeds 2.5 dl / g, the workability is deteriorated.

On the other hand, the molecular weight distribution of the polyketone is preferably 1.5 to 2.5, more preferably 1.8 to 2.2. When the ratio is less than 1.5, the polymerization yield decreases. When the ratio is 2.5 or more, the moldability is poor. In order to control the molecular weight distribution, it is possible to adjust proportionally according to the amount of the palladium catalyst and the polymerization temperature. That is, when the amount of the palladium catalyst is increased or when the polymerization temperature is 100 ° C or higher, the molecular weight distribution becomes larger.

On the other hand, the present invention provides a process for producing the above polyketone polymerization catalyst.

(Cyclohexane-1,1-diylbis (methylene)) bis (bis (2-methoxyphenyl) phosphine and a pKa of 4 Or less, and then the mixture is stirred to form a three-component complex.

At this time, the solvent is not particularly limited, but acetone is preferably used.

The bis (bis (2-methoxyphenyl) phosphine (cyclohexane-1,1-diylbis (methylene)) bis (bis (2-methoxyphenyl) phosphine, which is a ligand having the Group 8 transition metal compound and the Group 15 element, Examples of the anion of an acid are as described above.

Then, the solvent is removed from the three-component complex formed as described above.

In the present invention, a rotary evaporator is used to remove the solvent, but the present invention is not limited thereto.

The solution from which the solvent has been removed is frozen at a temperature of -10 ° C or lower, and then left standing for a predetermined time to form a single crystal.

On the other hand, the solution used for crystallization can be reused by concentrating with a rotary evaporator.

Then, the formed single crystal is washed several times with an inert hydrocarbon solvent such as hexane or heptane, and then pulverized to form a solid catalyst.

At this time, the particle size of the ground solid catalyst is preferably 5 nm to 100 μm, and when the particle size is within the above range, the catalytic activity is excellent.

A method of producing polyketone using the solid catalyst for polyketone polymerization produced through the above-described process will be described.

In the present invention, a polyketone is prepared by copolymerizing carbon monoxide and an ethylenically unsaturated compound in the presence of the solid catalyst for polyketone polymerization.

At this time, it is preferable to use a gas phase polymerization method as the polymerization method, and the reactor used in the polymerization can be used as it is or in a known manner.

The polymerization temperature is not particularly limited and is generally 40 to 180 占 폚, preferably 50 to 120 占 폚. The pressure at the time of polymerization is not particularly limited, and is generally from normal pressure to 20 MPa, preferably from 4 to 15 MPa.

On the other hand, examples of the ethylenically unsaturated compound copolymerized with the carbon monoxide include ethylene, propylene, 1-butene, 1-hexene, 4-methyl-1-pentene, -Olefins such as tetradecene, 1-hexadecene, and vinylcyclohexane; Alkenyl aromatic compounds such as styrene and? -Methylstyrene; But are not limited to, cyclopentene, norbornene, 5-methylnorbornene, 5-phenylnorbornene, tetracyclododecene, tricyclododecene, tricyclo undecene, pentacyclopentadecene, pentacyclohexadecene, Cyclic olefins such as cyclododecene; Vinyl halides such as vinyl chloride; Acrylic acid esters such as ethyl acrylate and methyl acrylate, but are not limited thereto. These ethylenically unsaturated compounds may be used singly or as a mixture of plural kinds.

Of these, preferred ethylenically unsaturated compounds are? -Olefins, more preferably? -Olefins having 2 to 4 carbon atoms, and most preferably ethylene.

The charging ratio of the carbon monoxide and the ethylenic unsaturated compound is not particularly limited, but it is preferably adjusted to 1: 1 to 1: 2.

Hereinafter, the present invention will be described concretely with reference to Examples. However, the following Examples are merely illustrative of one embodiment of the present invention, and the scope of the present invention is not limited by the following Examples.

Comparative Example 1

≪ Step 1 > Preparation of ternary complex

8.3035 g (13.12 mmol) of ((2,2-dimethyl-1,3-dioxane-5,5-diyl) bis (methylene) bis (bis (2- methoxyphenyl) phosphine) was added to 5 L of acetone solvent (12.50 mmol) of palladium acetate was added to the mixture and stirred for 30 minutes to completely dissolve the mixture. The two components , 14.25 g (124.9 mmol) of trifluoroacetic acid was added, and the mixture was stirred for 30 minutes to form a three-component complex.

≪ Step 2 > Preparation of solid catalyst

The three-component complex solution prepared in Step 1 was evaporated using a rotary evaporator until the total volume became 1 L, and then 1 L of hexane or heptane was added slowly to the remaining solution so that the solution was not mixed with the acetone solution. Thereby forming a solution layer.

Then, store in a frozen state at -10 ° C or lower. After standing for 1 day in the frozen state, a reddish yellow single crystal was obtained. The obtained single crystals were washed with hexane at room temperature and then ground to a size of 1 mu m or less using a micronizer to prepare a solid catalyst.

Example 1

≪ Step 1 > Preparation of ternary complex

8.3035 g (13.12 mmol) of bis (bis (2-methoxyphenyl) phosphine (cyclohexane-1,1-diylbis (methylene)) bis (13.12 mmol) was added to 5 L of acetone solvent and the mixture was stirred for 30 minutes in a magnetic stirrer Then, 2.8061 g (12.50 mmol) of palladium acetate was added, and the mixture was completely dissolved by stirring for 30 minutes. After dissolution of the two components was confirmed, trifluoroacetic acid 14.25 g (124.9 mmol) of trifluoroacetic acid was added, and the mixture was stirred for 30 minutes to form a three-component complex.

≪ Step 2 > Preparation of solid catalyst

The three-component complex solution prepared in Step 1 was evaporated using a rotary evaporator until the total volume became 1 L, and then 1 L of hexane or heptane was added slowly to the remaining solution so that the solution was not mixed with the acetone solution. Thereby forming a solution layer.

Then, store in a frozen state at -10 ° C or lower. After standing for 1 day in the frozen state, a reddish yellow single crystal was obtained. The obtained single crystals were washed with hexane at room temperature and then ground to a size of 1 mu m or less using a micronizer to prepare a solid catalyst.

The polymerization activity test results are shown in Table 1.

division Production (g) Activity (kg / gPd / hr) I.V. (dL / g) BD (g / ml) Tm (占 폚) Pd cont. (Ppm) Comparative Example 1 159.4 14.828 2.178 0.099 219.1 6.9 Example 1 163.5 15.206 2.384 0.093 220.9 10.4

Example 1 using the novel ligand (cyclohexane-1,1-diylbis (methylene)) bis (bis (2-methoxyphenyl) phosphine showed superior amount of acid yield and excellent catalytic activity as compared with Comparative Example 1 .

Claims (3)

Group 8 transition metal compounds;
Bis (bis (2-methoxyphenyl) phosphine (cyclohexane-1,1-diyl bis (methylene)) bis (bis (2-methoxyphenyl) phosphine having the following structural formula and having a Group 15 element
anions of acids with a pKa of 4 or less;
≪ RTI ID = 0.0 > polyketone < / RTI >
Figure 112016012254409-pat00006

The method according to claim 1,
Wherein said Group 8 transition metal compound is palladium acetate,
Wherein the anion of the acid having a pKa of 4 or less is one selected from the group consisting of trifluoroacetic acid, trifluoromethanesulfonic acid, p-toluenesulfonic acid and sulfuric acid.
A Group 8 transition metal compound in a solvent; Bis (bis (2-methoxyphenyl) phosphine and an acid of an acid having a pKa of 4 or less, which is a ligand having a Group 15 element, which is cyclohexane-1,1-diylbis (methylene) Forming a ternary complex;
Removing the solvent from the three-component complex, and then freezing at a temperature of -10 ° C or lower to form a single crystal; And
Pulverizing the single crystal to form a solid catalyst;
≪ / RTI >

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR102134158B1 (en) * 2019-03-18 2020-07-15 효성화학 주식회사 Manufacturing method of polyketone using solid acids
KR20200126502A (en) * 2019-04-30 2020-11-09 효성화학 주식회사 Manufacturing method of polyketone using solid acids
CN115819753A (en) * 2022-11-02 2023-03-21 黄河三角洲京博化工研究院有限公司 Polyketone polymerization method

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003504172A (en) 1999-07-06 2003-02-04 シエル・インターナシヨネイル・リサーチ・マーチヤツピイ・ベー・ウイ Catalyst composition and use thereof

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003504172A (en) 1999-07-06 2003-02-04 シエル・インターナシヨネイル・リサーチ・マーチヤツピイ・ベー・ウイ Catalyst composition and use thereof

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR102134158B1 (en) * 2019-03-18 2020-07-15 효성화학 주식회사 Manufacturing method of polyketone using solid acids
KR20200126502A (en) * 2019-04-30 2020-11-09 효성화학 주식회사 Manufacturing method of polyketone using solid acids
KR102179648B1 (en) 2019-04-30 2020-11-18 효성화학 주식회사 Manufacturing method of polyketone using solid acids
CN115819753A (en) * 2022-11-02 2023-03-21 黄河三角洲京博化工研究院有限公司 Polyketone polymerization method
CN115819753B (en) * 2022-11-02 2024-03-29 黄河三角洲京博化工研究院有限公司 Polymerization method of polyketone

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