CN107282131A - Carbon monoxide-olefin polymeric and its application in ethylene tetramerization - Google Patents
Carbon monoxide-olefin polymeric and its application in ethylene tetramerization Download PDFInfo
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- CN107282131A CN107282131A CN201610197151.XA CN201610197151A CN107282131A CN 107282131 A CN107282131 A CN 107282131A CN 201610197151 A CN201610197151 A CN 201610197151A CN 107282131 A CN107282131 A CN 107282131A
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J31/00—Catalysts comprising hydrides, coordination complexes or organic compounds
- B01J31/16—Catalysts comprising hydrides, coordination complexes or organic compounds containing coordination complexes
- B01J31/24—Phosphines, i.e. phosphorus bonded to only carbon atoms, or to both carbon and hydrogen atoms, including e.g. sp2-hybridised phosphorus compounds such as phosphabenzene, phosphole or anionic phospholide ligands
- B01J31/2404—Cyclic ligands, including e.g. non-condensed polycyclic ligands, the phosphine-P atom being a ring member or a substituent on the ring
- B01J31/2409—Cyclic ligands, including e.g. non-condensed polycyclic ligands, the phosphine-P atom being a ring member or a substituent on the ring with more than one complexing phosphine-P atom
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- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2/00—Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms
- C07C2/02—Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms by addition between unsaturated hydrocarbons
- C07C2/04—Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms by addition between unsaturated hydrocarbons by oligomerisation of well-defined unsaturated hydrocarbons without ring formation
- C07C2/06—Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms by addition between unsaturated hydrocarbons by oligomerisation of well-defined unsaturated hydrocarbons without ring formation of alkenes, i.e. acyclic hydrocarbons having only one carbon-to-carbon double bond
- C07C2/08—Catalytic processes
- C07C2/26—Catalytic processes with hydrides or organic compounds
- C07C2/36—Catalytic processes with hydrides or organic compounds as phosphines, arsines, stilbines or bismuthines
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2231/00—Catalytic reactions performed with catalysts classified in B01J31/00
- B01J2231/20—Olefin oligomerisation or telomerisation
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2531/00—Additional information regarding catalytic systems classified in B01J31/00
- B01J2531/60—Complexes comprising metals of Group VI (VIA or VIB) as the central metal
- B01J2531/62—Chromium
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- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2531/00—Catalysts comprising hydrides, coordination complexes or organic compounds
- C07C2531/16—Catalysts comprising hydrides, coordination complexes or organic compounds containing coordination complexes
- C07C2531/24—Phosphines
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Abstract
The invention discloses a kind of ethylene tetramerization carbon monoxide-olefin polymeric, including biphosphine ligand shown in Formulas I, transistion metal compound, containing aluminum cocatalyst and TBHP；R in formula1And R2It is each independently selected from alkyl, cycloalkyl or aryl；R3、R4、R5And R6It is each independently selected from aryl or cycloalkyl.The invention also discloses the method that ethylene tetramerization is carried out using above-mentioned composition.Catalyst according to the invention composition, it is possible to increase ethylene tetramerization activity, and 1 octene selectivity.
Description
Technical field
The present invention relates to ethylene oligomerization field, and in particular to a kind of carbon monoxide-olefin polymeric for ethylene tetramerization.This
Invention further relates to application of the carbon monoxide-olefin polymeric in ethylene tetramerization reaction.
Background technology
1- octenes are as important Organic Ingredients and chemical intermediate, mainly for the production of high-quality polyethylene (PE).
The LLDPE (LLDPE) produced by 1- octenes and ethylene copolymer can significantly improve PE items
Can, particularly have significantly to the mechanical performance of polyethylene, optical property and tear strength and impact strength
Improve, be very suitable for agricultural mulch films such as packaging film and greenhouse, canopy room etc., while 1- octenes also serve as plasticizer,
The intermediate of aliphatic acid, detergent alcohols and lube oil additive.
Traditional 1- production of octenes methods are ethylene oligomerization methods, and ethylene oligomerization technology is distributed according to Schulz-Flory,
1- octene products are not only obtained, while also have other alpha-olefins and a small amount of solid superpolymer, and purpose product 1-
The selectivity of octene is very low, no more than 30%.The SHOP methods (US3676523) that for example Shell companies use
Ethylene oligomerization reaction is carried out using nickel-metal catalyst system, 11% 1- octenes are can obtain；United States Patent (USP)
(US6184428) report uses a kind of nickel compound as catalyst ethylene oligomerization, the yield of 1- octenes
For 19%.Japan Patent JP2002121157 is reported carries out ethylene oligomerization reaction using zirconium metal catalyzer,
The content of wherein 1- octenes is about 15%.The ethylene tetramerization ternary catalyst systems reported recently can be with high selection
Synthesize 1- octenes, such as patent application CN1741850A (WO2004/056478A1), CN1741849A to property
(WO2004/056479A1)、CN101032695A、CN101351424A、CN101415494A、
CN1651142A, CN101291734A and patent application US2006/0128910A1 are disclosed and used
P-N-P parts and chromium coordination catalysis ethylene tetramerization, co-catalyst use aluminum alkoxide.Aluminum alkoxide (including first
Base aikyiaiurnirsoxan beta, modified methylaluminoxane etc.) as co-catalyst, it is too high to there is cost, the problem of consumption is excessive,
Large-scale application is when ethylene tetramerization, and it certainly will cause production cost high.Moreover, in the prior art, leading to
Often think that water is very unfavorable to ethylene tetramerization reaction process, therefore need to be strict controlled in process of production
Reacted in the environment of anhydrous and oxygen-free.This causes known ethylene tetramerizations all at present or oligomerisation reaction to technique
Requirement it is all very harsh, cause reaction process reaction trigger and repeatability it is all excessively poor.
The content of the invention
In view of the application containing Phosphine ligands in ethylene tetramerization, present inventor is led in ethylene tetramerization with catalyst
Domain has carried out research extensively and profoundly, it has surprisingly been found that ethene is including the biphosphine ligand shown in Formulas I, transition
Metallic compound, the lower progress ethene four of carbon monoxide-olefin polymeric effect containing aluminum cocatalyst and TBHP
Poly- reaction, on the contrary with higher reactivity, and reaction trigger it is rapid, operate steadily, reproducible, production
The selectivity of 1- octenes is also greatly improved in thing；TBHP is promoted anti-as organic peroxide
The progress answered, so as to overcome the technology prejudice of those skilled in the art, achieves unexpected technique effect.
According to the first aspect of the invention, it is related to a kind of ethylene tetramerization carbon monoxide-olefin polymeric, including Formulas I institute
The biphosphine ligand that shows, transistion metal compound, containing aluminum cocatalyst and TBHP；
R in formula1And R2It is each independently alkyl, cycloalkyl or aryl；R3、R4、R5And R6It is each independent
Ground is aryl or cycloalkyl.
According to the present invention, TBHP is introduced in carbon monoxide-olefin polymeric, catalytic activity is improved, with
And the selectivity of 1- octenes.
In a preferred embodiment of the present invention, the alkyl refers to C1-C20Straight or branched saturation alkane
Base, preferably C1-C10Straight or branched saturated alkyl, more preferably C1-C6Straight or branched saturated alkyl.Tool
Body, the alkyl can be selected from methyl, ethyl, n-propyl, isopropyl, normal-butyl, isobutyl group, Zhong Ding
Base, the tert-butyl group, n-pentyl, sec-amyl, isopentyl, n-hexyl, Sec-Hexyl, isohesyl, n-heptyl and its
Isomers etc.；It is preferably selected from methyl, ethyl, n-propyl, isopropyl, normal-butyl and isobutyl group.
In a preferred embodiment of the present invention, the cycloalkyl refers to C3-C10Cycloalkyl, preferably C3-
C6Cycloalkyl.Specifically, the alkyl may be selected from cyclopropyl, cyclopenta and cyclohexyl.
In a preferred embodiment of the present invention, the substitution refers to its of the alkyl, cycloalkyl or aryl
In one or more carbon atoms be selected from oxygen, nitrogen and sulphur hetero atom substitution.Wherein the one of the optional aryl
Carbon atom on individual or multiple rings is selected from the hetero atom substitution of oxygen, nitrogen and sulphur.Preferably, the aryl is by halogen
Element or C1-C20Alkyl replaces.
In a preferred embodiment of the present invention, the aryl refers to C5-C20Monocyclic or multiring aromatic
Group, specifically, the aryl may be selected from phenyl, naphthyl and pyridine radicals.Substituted aryl such as substituted-phenyl etc..
In some preferred embodiments of the present invention, the transistion metal compound can be commonly used in the art
Transistion metal compound, such as chromium, molybdenum, iron, titanium, the preferably compound of zirconium or nickel, chromium chloride, levulinic
At least one of ketone chromium, isooctyl acid chromium or three (tetrahydrofuran) chromium trichlorides etc..
In some preferred embodiments of the present invention, aluminium and transition metal compound in co-catalyst of the present invention
The mol ratio of metal is 30 in thing:1-1000:1, preferably 100:1-800:1, more preferably 200:1-500:1,
Such as 200:1-300:1, or 300:1-500:1.The mol ratio of the part and transistion metal compound is 0.5:1-
2:1.In the scope, composition has higher activity and selectivity.
In some preferred embodiments of the present invention, machine solvent is further includeed in the composition.To have
The weight of machine solvent is calculating benchmark, and the weight of the TBHP contained in the carbon monoxide-olefin polymeric contains
Measure as 25-1000ppm；More preferably 150-750ppm, most preferably 250-500ppm.
In a preferred embodiment of the invention, the organic solvent be selected from hexahydrotoluene, heptane, hexamethylene,
Ether, tetrahydrofuran, benzene,toluene,xylene and dichloromethane, preferably hexahydrotoluene or heptane.
In certain embodiments of the present invention, it is described to be selected from alkyl aluminum compound and alkoxy containing aluminum cocatalyst
Aluminium compound, preferably alkyl aluminum compound.
The present invention some preferred embodiment in, the aluminum alkoxide be C1-C4Alkylaluminoxane, its
Middle C1-C4Alkyl is the alkyl of straight or branched；Preferably, described aikyiaiurnirsoxan beta is selected from MAO, changed
Property MAO, ethylaluminoxane and isobutyl aluminium alkoxide；More preferably MAO.The alkyl calorize
The formula of compound is AlWnYm, wherein n is 1-3 integer, and m is 0-2 integer, and m+n etc.
In 3, when there is multiple W, it may be the same or different, and be each independently straight or branched C1-C8Alkyl；
When there is multiple Y, it may be the same or different, and be each independently selected from halogen, preferably chlorine and/or bromine；Enter one
Preferably, described alkyl aluminum compound is selected from trimethyl aluminium, triethyl aluminum, tri-propyl aluminum, triisobutyl to step
At least one of aluminium, tri-n-hexyl aluminum, tri-n-octylaluminium, diethylaluminum chloride and ethylaluminium dichloride, more
It is preferred that trimethyl aluminium, triethyl aluminum and/or triisobutyl aluminium.
In some preferred embodiments of the present invention, in the carbon monoxide-olefin polymeric, the part, transition
The amount of metallic compound and co-catalyst is catalytic amount.In a specific embodiment, with composition
Volume is calculating benchmark, and the content of the biphosphine ligand is 2-500 μm of ol/L, preferably 5-50 μm ol/L；Institute
It is 2-500 μm of ol/L, preferably 5-50 μm ol/L to state the content of transistion metal compound；.
Second embodiment of the present invention is related to a kind of ethylene tetramerization technique, is included in above-mentioned catalyst combination
In the presence of thing, ethylene tetramerization reaction is carried out.
In a preferred embodiment of the invention, the reaction temperature of the ethylene tetramerization reaction is 0-200 DEG C, excellent
It is 10-100 DEG C to select reaction temperature, and more preferably reaction temperature is 30-60 DEG C；Reaction pressure 0.1-20MPa.
In general, as ethylene pressure increased activity is raised.
, can be by biphosphine ligand, transition gold in the carbon monoxide-olefin polymeric in the ethylene tetramerization reaction of the present invention
Category compound, co-catalyst and TBHP are pre-mixed for any two or three, then again with it is another
Plant or two kinds are added in reaction system together；Or by biphosphine ligand, transistion metal compound, co-catalyst
These four components are added directly into reaction system with TBHP；Or biphosphine ligand, transition is golden
Belong to after compound, co-catalyst and TBHP these four components premix, directly add as a mixture
Enter in reaction system.And organic solvent can be added in the mixed process of any one above-mentioned hybrid mode.
Ethylene tetramerization is carried out using carbon monoxide-olefin polymeric of the present invention, after reaction terminates, gas phase is carried out
Chromatogram and mass spectral analysis.The product of acquisition mainly includes C6And C8, there is a small amount of C4、C10、C12Deng α-alkene
Hydrocarbon；The selectivity of 1- octenes in four poly- products can reach more than 70%.As a result show, catalyst activity is most
Height can be more than 1 × 108g·mol(Cr)-1·h-1More than.High molecular polymer is few.
In the present invention, especially in the pilot scale and industrial processes of ethylene tetramerization, the catalysis of the present invention is used
Agent composition, can effectively be catalyzed ethylene tetramerization reaction, and carbon monoxide-olefin polymeric has the reactivity of superelevation, and
Reaction trigger it is rapid, operate steadily, it is reproducible.
The present invention is using containing biphosphine ligand, transistion metal compound, containing aluminum cocatalyst and TBHP
Carbon monoxide-olefin polymeric in the presence of carry out ethylene tetramerization reaction, TBHP is as having among reaction
Machine peroxide, can be with the pilot scale and industrial processes that accelerate reaction speed, especially ethylene tetramerization
The selectivity of 1- octenes is significantly carried in effectively catalysis ethylene tetramerization reaction, the reactivity with superelevation, product
Height, and reaction trigger it is rapid, operate steadily, it is reproducible.The ethylene tetramerization or oligomerisation catalyst body reported
System, its reaction condition is often required that and carried out under the conditions of anhydrous and oxygen-free, and catalyst of the present invention, is being had
In the presence of machine peroxide-TBHP, on the contrary with higher reactivity, and reaction triggers
Rapidly, operate steadily, it is reproducible, achieve beneficial effect.
Embodiment
The following example is only used for that the present invention is described in detail, it will be appreciated that the scope of the present invention is not
It is limited to these embodiments.
In an embodiment of the present invention：Part used is reacted by substitution alkynes and diphenyl phosphine chloride, Jin Er
Prepared in the presence of titanium catalyst.
Nuclear magnetic resonance is detected using Bruker companies of Switzerland AV400MHz nuclear magnetic resonance chemical analysers.
Gas-chromatography is detected using the chromatograph of Hewlett-Packard 5890.
Mass spectrum is detected using U.S.'s Finnigan company's T race DSQ type gas chromatograph-mass spectrometers.
Embodiment 1
Using 300mL stainless steel polymeric kettles.Autoclave is heated to 80 DEG C, nitrogen displacement number is used after vacuumizing
It is secondary, it is then charged with ethene displacement once, is down to design temperature.1 μm of ol biphosphine ligand is sequentially added at 40 DEG C
(wherein R1For methyl, R2For ethyl, R3、R4、R5And R6Be phenyl), 1 μm of ol chromium trichloride,
Co-catalyst triethyl aluminum, TBHP and organic solvent hexahydrotoluene, the cumulative volume of mixed liquor
For 100mL, counted on the basis of the weight of organic solvent, the weight content of TBHP is 25ppm,
The mol ratio of aluminium and chromium is 300.Reaction pressure 4.0MPa is controlled, ethene is passed through, ethylene tetramerization reaction is carried out.
After reaction 0.5 hour, system is cooled to room temperature, gaseous products is collected in aerometer measuring tank, liquid-phase product
Collect in conical flask, measure laggard promoting the circulation of qi analysis of hplc.Data are shown in Table 1.
Embodiment 2
Be the same as Example 1, difference is, the weight content of TBHP is 150ppm.Data are shown in
Table 1.
Embodiment 3
Be the same as Example 1, difference is, the weight content of TBHP is 250ppm.Data are shown in
Table 1.
Embodiment 4
Be the same as Example 1, difference is, the weight content of TBHP is 500ppm.Data are shown in
Table 1.
Embodiment 5
Be the same as Example 1, difference is, the weight content of TBHP is 750ppm.Data are shown in
Table 1.
Embodiment 6
Be the same as Example 1, difference is, the weight content of TBHP is 1000ppm.Data
It is shown in Table 1.
Embodiment 7
Be the same as Example 1, difference is, the weight content of TBHP for 500ppm and aluminium with
The mol ratio of chromium is 200.Data are shown in Table 1.
Embodiment 8
Be the same as Example 1, difference is, the weight content of TBHP for 500ppm and aluminium with
The mol ratio of chromium is 500.Data are shown in Table 1.
Embodiment 9
Be the same as Example 1, difference is, the weight content of TBHP is 500ppm and reaction
Temperature is 30 DEG C.Data are shown in Table 1.
Embodiment 10
Be the same as Example 1, difference is, the weight content of TBHP is 500ppm and reaction
Temperature is 60 DEG C.Data are shown in Table 1.
Embodiment 11
Be the same as Example 1, difference is, the weight content of TBHP is 500ppm and R1For
Normal-butyl, R2For cyclohexyl, R3、R4、R5And R6It is phenyl.Data are shown in Table 1.
Embodiment 12
Be the same as Example 1, difference is, the weight content of TBHP is 500ppm and R1For
The tert-butyl group, R2For cyclopenta, R3、R4、R5And R6It is phenyl.Data are shown in Table 1.
Embodiment 13
Be the same as Example 1, difference is, the weight content of TBHP is 500ppm and R1、
R2、R3、R4、R5And R6It is phenyl.Data are shown in Table 1.
Embodiment 14
Be the same as Example 1, difference is, the weight content of TBHP is 500ppm and R1For
Cyclopropyl, R2For phenyl, R3、R4、R5And R6It is phenyl.Data are shown in Table 1.
Embodiment 15
Be the same as Example 1, difference is, the weight content of TBHP is 500ppm R1For first
Base, R2For ethyl, R3、R4、R5And R6It is cyclohexyl.Data are shown in Table 1.
Comparative example 1
Be the same as Example 1, difference is that the weight content of TBHP is 0ppm.Data are shown in Table 1.
Table 1
It can see by the data of table 1, the bar that carbon monoxide-olefin polymeric of the invention exists in TBHP
Under part, catalytic activity increases on the contrary, and shows good catalytic activity and the selectivity of 1- octenes.Obtain
In product, the selectivity of 1- octenes is up to more than 70%.
It should be noted that embodiment described above is only used for explaining the present invention, do not constitute to this hair
Bright any limitation.By referring to exemplary embodiments, invention has been described, it should be appreciated that its
In used word be descriptive and explanatory vocabulary, rather than limited vocabulary.Can be by regulation at this
The present invention is modified in the range of invention claim, and without departing substantially from the scope of the present invention and essence
The present invention is revised in refreshing.Although the present invention described in it is related to specific method, material and reality
Example is applied, it is not intended that the present invention is limited to wherein disclosed particular case, on the contrary, the present invention is expansible
To other all methods and applications with identical function.
Claims (10)
1. a kind of ethylene tetramerization carbon monoxide-olefin polymeric, including biphosphine ligand, transition metal compound shown in Formulas I
Thing, containing aluminum cocatalyst and TBHP；
R in formula1And R2It is each independently alkyl, cycloalkyl or aryl；R3、R4、R5And R6It is each independent
Ground is aryl or cycloalkyl.
2. composition according to claim 1, it is characterised in that the alkyl is C1-C20Straight chain or
The saturated alkyl of side chain, preferably C1-C10The saturated alkyl of straight or branched, more preferably C1-C6Straight chain or branch
The saturated alkyl of chain；And/or the cycloalkyl is C3-C10Cycloalkyl, preferably C3-C6Cycloalkyl；And/or institute
Aryl is stated for C5-C20Monocyclic or polycyclic aryl；And/or, the alkyl, wherein the one of cycloalkyl or aryl
Individual or multiple carbon atoms are selected from the hetero atom substitution or unsubstituted of oxygen, nitrogen and sulphur, and preferably described aryl is by halogen
Or C1-C20Alkyl replaces or unsubstituted.
3. composition according to claim 1 or 2, it is characterised in that the alkyl be selected from methyl,
Ethyl, n-propyl, isopropyl, normal-butyl, isobutyl group, sec-butyl, the tert-butyl group, n-pentyl, sec-amyl,
Isopentyl, n-hexyl, Sec-Hexyl, isohesyl, n-heptyl and its isomers；Be preferably selected from methyl, ethyl,
N-propyl, isopropyl, normal-butyl and isobutyl group；And/or, the cycloalkyl is selected from cyclopropyl, cyclopenta and ring
Hexyl；And/or the aryl is selected from phenyl, naphthyl and pyridine radicals.
4. the composition according to any one of claim 1-3, it is characterised in that enter in the composition
One step includes organic solvent, preferably using the weight of the organic solvent as calculating benchmark, contains in the composition
TBHP weight content be 25-1000ppm, preferably 150-750ppm, be most preferably
250-500ppm。
5. the composition according to any one of claim 1-4, it is characterised in that in the co-catalyst
The mol ratio of aluminium and metal in transistion metal compound is 30:1-1000:1, preferably 100:1-800:1, more preferably
For 200:1-500:1；And/or, the mol ratio of the part and transistion metal compound is 0.5:1-2:1.
6. composition according to claim 5, it is characterised in that the transistion metal compound is optional
At least one of compound from chromium, molybdenum, iron, titanium, zirconium or nickel, preferably chromium chloride, chromium acetylacetonate,
At least one of isooctyl acid chromium and three (tetrahydrofuran) chromium trichlorides.
7. the composition according to any one of claim 1-6, it is characterised in that the co-catalysis containing aluminium
Agent is selected from least one of alkyl aluminum compound and alkoxy aluminum compound, preferably is selected from trimethyl aluminium, triethyl group
Aluminium, tri-propyl aluminum, triisobutyl aluminium, tri-n-hexyl aluminum, tri-n-octylaluminium, diethylaluminum chloride, dichloride
At least one of aluminium ethide, MAO, ethylaluminoxane and modified methylaluminoxane.
8. the composition according to any one in claim 4-7, it is characterised in that the organic solvent
Selected from hexahydrotoluene, heptane, hexamethylene, ether, tetrahydrofuran, benzene,toluene,xylene and dichloromethane
At least one of alkane.
9. a kind of method of ethylene tetramerization, is included in the ethylene tetramerization according to any one of claim 1-8
In the presence of carbon monoxide-olefin polymeric, ethylene tetramerization reaction is carried out.
10. method according to claim 9, it is characterised in that the reaction temperature of the ethylene tetramerization reaction
Spend for 0-200 DEG C, preferably 10-100 DEG C, more preferably 30-60 DEG C；Reaction pressure 0.1-20MPa；With/
Or, using the volume of composition as calculating benchmark, the content of the biphosphine ligand is 2-500 μm of ol/L, preferably 5-
50μmol/L；The content of the transistion metal compound is 2-500 μm of ol/L, preferably 5-50 μm ol/L.
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113600244A (en) * | 2021-08-06 | 2021-11-05 | 山东京博石油化工有限公司 | Catalyst for synthesizing 1-octene and application thereof |
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| WO2009074203A1 (en) * | 2007-12-12 | 2009-06-18 | Linde Ag | Catalyst composition for oligomerization of ethylene oligomerization process and method for its preparation |
| CN101605605A (en) * | 2007-01-18 | 2009-12-16 | Sk能源株式会社 | Ethene four gathers catalyst systems and uses this catalyst system to prepare the method for 1-octene |
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2016
- 2016-03-31 CN CN201610197151.XA patent/CN107282131B/en active Active
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101605605A (en) * | 2007-01-18 | 2009-12-16 | Sk能源株式会社 | Ethene four gathers catalyst systems and uses this catalyst system to prepare the method for 1-octene |
| WO2009074203A1 (en) * | 2007-12-12 | 2009-06-18 | Linde Ag | Catalyst composition for oligomerization of ethylene oligomerization process and method for its preparation |
Non-Patent Citations (1)
| Title |
|---|
| 陈泽森等: "《水性建筑涂料生产技术》", 31 January 2007, 北京：中国纺织出版社 * |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113600244A (en) * | 2021-08-06 | 2021-11-05 | 山东京博石油化工有限公司 | Catalyst for synthesizing 1-octene and application thereof |
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