System and Method for Catalyst Preparation
US-2016325252-A1 · Nov 10, 2016 · US
US10030086B1 · US · B1
| Field | Value |
|---|---|
| Publication number | US-10030086-B1 |
| Application number | US-201715655929-A |
| Country | US |
| Kind code | B1 |
| Filing date | Jul 21, 2017 |
| Priority date | Jul 21, 2017 |
| Publication date | Jul 24, 2018 |
| Grant date | Jul 24, 2018 |
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Methods for determining the concentration of transition metal compounds in a solution containing more than one transition metal compound are described. Polymerization reactor systems providing real-time monitoring and control of the concentrations of the transition metal components of a multicomponent catalyst system are disclosed, as well as methods for operating such polymerization reactor systems.
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We claim: 1. A process for operating a polymerization reactor system, the process comprising: (I) contacting a catalyst system comprising a first transition metal compound, a second transition metal compound, an activator, and an optional co-catalyst, with an olefin monomer and an optional olefin comonomer in a reactor within the polymerization reactor system under polymerization reaction conditions to produce an olefin polymer; (II) determining a concentration of the first transition metal compound in a solution comprising the first transition metal compound and the second transition metal compound, the concentration determined via the steps of: (i) submitting a sample of the solution to a sample chamber; (ii) irradiating the sample in the chamber with a light beam at a wavelength in the UV-visible spectrum; and (iii) generating a sample absorbance profile of the sample, subtracting a reference absorbance profile of the second transition metal compound in a reference solution from the sample absorbance profile to result in a first transition metal compound absorbance profile, and correlating the first transition metal compound absorbance profile to a standard to determine the concentration of the first transition metal compound in the solution; and (III) adjusting a flow rate of the first transition metal compound into the reactor when the concentration of the first transition metal compound in the solution has reached a predetermined level. 2. The process of claim 1 , wherein the solution comprising the first transition metal compound and the second transition metal compound is: a feed stream to a catalyst preparation vessel; a liquid or homogeneous catalyst system; a solution prepared from a heterogeneous or supported catalyst system; or a solution prepared from a sample mixture from the reactor. 3. The process of claim 1 , wherein: the wavelength in step (ii) comprises wavelengths in the 300 nm to 600 nm range; the sample absorbance profile in step (iii) comprises an absorbance curve over a range of wavelengths; and the step of correlating is performed at a single wavelength. 4. The process of claim 1 , wherein: the first transition metal compound and the second transition metal compound independently comprise chromium, vanadium, titanium, zirconium, hafnium, or a combination thereof; the olefin monomer comprises a C 2 -C 24 olefin; and the polymerization reactor system comprises a solution reactor, a gas-phase reactor, a slurry reactor, or a combination thereof. 5. The process of claim 1 , wherein: the first transition metal compound is an unbridged metallocene compound; and the second transition metal compound is a bridged metallocene compound. 6. The process of claim 1 , wherein the second transition metal compound comprises two or more different second transition metal compounds. 7. The process of claim 1 , wherein: the catalyst system comprises a first metallocene compound, a second metallocene compound, an activator, and a co-catalyst; and the catalyst system is contacted with ethylene and an olefin comonomer comprising 1-butene, 1-hexene, 1-octene, or a mixture thereof. 8. The process of claim 1 , wherein the reference solution comprises the second transition metal compound and a hydrocarbon solvent. 9. The process of claim 8 , wherein: the hydrocarbon solvent comprises 1-hexene, isobutane, toluene, cyclohexene, or any combination thereof; and a weight ratio of the first transition metal compound to the second transition metal compound in the solution is in a range from about 1:50 to about 1:5. 10. The process of claim 1 , wherein: the sample absorbance profile, the reference absorbance profile, and the first transition metal compound absorbance profile independently comprise an absorbance curve over a range of wavelengths; and the standard comprises a calibration curve. 11. The process of claim 1 , wherein the solution comprising the first transition metal compound and the second transition metal compound is a feed stream to a catalyst preparation vessel, and the flow rate of the first transition metal compound into the reactor is controlled by adjusting a flow rate ratio of the first:second transition metal compound to the catalyst preparation vessel. 12. A polymerization reactor system comprising: (A) a reactor configured to contact a catalyst system with an olefin monomer and an optional olefin comonomer under polymerization reaction conditions to produce an olefin polymer; (B) a catalyst preparation vessel configured to contact a first transition metal compound, a second transition metal compound, an activator, and an optional co-catalyst to form the catalyst system; and (C) an analytical system configured to determine a concentration of the first transition metal compound in a solution comprising the first transition metal compound and the second transition metal compound present within the polymerization reactor system. 13. The reactor system of claim 12 , wherein the analytical system comprises an ultraviolet-visible spectrometer. 14. The reactor system of claim 13 , wherein the analytical system further comprises a filter assembly configured to filter a sample of the solution comprising the first transition metal compound and the second transition metal compound before analysis by the ultraviolet-visible spectrometer. 15. The reactor system of claim 12 , wherein the reactor system further comprises (D) a controller configured to control a flow rate of the first transition metal compound into the reactor based on the concentration determined by the analytical system. 16. The reactor system of claim 15 , wherein: the reactor system comprises a slurry reactor, a gas-phase reactor, a solution reactor, or a combination thereof; and the analytical system comprises an ultraviolet-visible spectrometer with an integrated computer system for measuring a sample absorbance profile of the first transition metal compound in the solution, for subtracting a reference absorbance profile of the second transition metal compound in a reference solution from the sample absorbance profile to result in a first transition metal compound absorbance profile, and for correlating the first transition metal compound absorbance profile to a standard to determine the concentration of the first transition metal compound in the solution. 17. The reactor system of claim 15 , wherein: the solution comprises the first transition metal compound, the second transition metal compound, and a hydrocarbon solvent; and the solution is a feed stream to the catalyst preparation vessel, and the controller controls the flow rate of the first transition metal compound into the reactor by adjusting a flow rate ratio of the first:second transition metal compound to the catalyst preparation vessel. 18. The reactor system of claim 15 , wherein the controller is configured to control the flow rate of the transition metal compound into the reactor based on the concentration determined by the analytical system in real-time. 19. The reactor system of claim 15 , wherein: the reactor system comprises two or more reactors, at least one of which is a loop slurry reactor; the polymerization reaction conditions comprise a reaction temperature in a range from about 60° C. to about 185° C., and a reaction pressure of less than about 1000 psig; the olefin polymer comprises an ethylene homopolymer, an ethylene/1-butene copolymer, an ethylene/1-hexene copolymer, or an ethylene/1-octene copolymer; and the first transition metal com
using ultraviolet light (G01N21/39 takes precedence) · CPC title
Homopolymers and copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond · CPC title
Controlling or regulating processes (controlling or regulating in general G05) · CPC title
Investigating relative effect of material at wavelengths characteristic of specific elements or molecules, e.g. atomic absorption spectrometry {(G01N21/72 takes precedence)} · CPC title
controlling the flow · CPC title
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