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Methods for preparing a fluorided chromium catalyst can include a step of calcining a supported chromium catalyst at a peak calcining temperature to produce a calcined supported chromium catalyst, followed by contacting the calcined supported chromium catalyst at a peak fluoriding temperature with a

Methods for preparing a fluorided chromium catalyst can include a step of calcining a supported chromium catalyst at a peak calcining temperature to produce a calcined supported chromium catalyst, followed by contacting the calcined supported chromium catalyst at a peak fluoriding temperature with a vapor comprising a fluorine-containing compound to produce the fluorided chromium catalyst. The peak fluoriding temperature can be at least 50° C. less, and often from 200° C. to 500° C. less, than the peak calcining temperature. Polymers produced using the fluorided chromium catalyst can have a beneficial combination of higher melt index, narrower molecular weight distribution, and lower long chain branch content.

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1. A process to produce a fluorided chromium catalyst, the process comprising: (a) calcining a supported chromium catalyst at a peak calcining temperature to produce a calcined supported chromium catalyst; and(b) contacting the calcined supported chromium catalyst at a peak fluoriding temperature wi

1. A process to produce a fluorided chromium catalyst, the process comprising: (a) calcining a supported chromium catalyst at a peak calcining temperature to produce a calcined supported chromium catalyst; and(b) contacting the calcined supported chromium catalyst at a peak fluoriding temperature with a vapor comprising a fluorine-containing compound to produce the fluorided chromium catalyst;wherein the peak fluoriding temperature is at least about 50° C. less than the peak calcining temperature. 2. The process of claim 1, wherein: the peak calcining temperature is in a range from about 725° C. to about 900° C.;the peak fluoriding temperature is in a range from about 300° C. to about 675° C.;the peak fluoriding temperature is from about 100° C. to about 600° C. less than the peak calcining temperature; orany combination thereof. 3. The process of claim 1, wherein: the peak calcining temperature is in a range from about 600° C. to about 871° C.;the peak fluoriding temperature is in a range from about 300° C. to about 500° C.;the peak fluoriding temperature is from about 200° C. to about 500° C. less than the peak calcining temperature; orany combination thereof. 4. The process of claim 1, wherein the fluorided chromium catalyst comprises fluorided chromium/silica, fluorided chromium/silica-titania, fluorided chromium/silica-titania-magnesia, fluorided chromium/silica-alumina, fluorided chromium/alumina, fluorided chromium/phosphated alumina, or a combination thereof. 5. The process of claim 1, wherein the fluorine-containing compound comprises a fluorocarbon. 6. The process of claim 1, wherein the fluorine-containing compound comprises perfluorohexane, perfluoroacetic anhydride, tetrafluoroethane, or a combination thereof. 7. The process of claim 1, wherein the fluorided chromium catalyst comprises: from about 0.1 to about 10 wt. % chromium; andfrom about 0.25 to about 8 wt. % fluorine. 8. The process of claim 1, wherein step (a) and step (b) are performed in an oxidizing atmosphere. 9. The process of claim 1, wherein: the contacting in step (b) is performed for a time period ranging from about 10 minutes to about 6 hours; andthe fluorine-containing compound is present in the vapor for less than about 25% of the contacting time period in step (b). 10. The process of claim 1, wherein the fluorided chromium catalyst has: a pore volume in a range from about 1 to about 5 mL/g; anda surface area in a range from about 200 to about 550 m2/g. 11. The process of claim 1, wherein the surface area of the fluorided chromium catalyst produced by the process is at least about 10% greater than a surface area of a fluorided chromium catalyst obtained by performing the contacting step at the peak calcining temperature. 12. The process of claim 1, wherein a catalyst activity of the fluorided chromium catalyst produced by the process is at least about 10% greater than that of a fluorided chromium catalyst obtained by performing the contacting step at the peak calcining temperature, under the same polymerization conditions. 13. An olefin polymerization process, the olefin polymerization process comprising: (i) calcining a supported chromium catalyst at a peak calcining temperature to produce a calcined supported chromium catalyst;(ii) contacting the calcined supported chromium catalyst at a peak fluoriding temperature with a vapor comprising a fluorine-containing compound to produce a fluorided chromium catalyst, wherein the peak fluoriding temperature is from about 100° C. to about 600° C. less than the peak calcining temperature; and(iii) contacting the fluorided chromium catalyst and an optional co-catalyst with an olefin monomer and an optional olefin comonomer in a polymerization reactor system under polymerization conditions to produce an olefin polymer. 14. The olefin polymerization process of claim 13, wherein: the olefin monomer comprises ethylene or propylene; andthe polymerization reactor system comprises a slurry reactor, a gas-phase reactor, a solution reactor, or a combination thereof. 15. The olefin polymerization process of claim 13, wherein: the fluorided chromium catalyst and a co-catalyst are contacted with ethylene and an olefin comonomer comprising a C3-C10 alpha-olefin; andthe polymerization reactor system comprises a loop slurry reactor. 16. The olefin polymerization process of claim 13, wherein: a number of long chain branches per 1,000,000 total carbon atoms of the olefin polymer is less than that of an olefin polymer obtained without using step (ii) of the process, under the same polymerization conditions;a HLMI of the olefin polymer is less than that of an olefin polymer obtained without using step (ii) of the process, under the same polymerization conditions;a ratio of Mw/Mn of the olefin polymer is greater than that of an olefin polymer obtained without using step (ii) of the process, under the same polymerization conditions;a ratio of I21/I10 of the olefin polymer is greater than that of an olefin polymer obtained without using step (ii) of the process, under the same polymerization conditions; orany combination thereof. 17. The olefin polymerization process of claim 13, wherein: a HLMI of the olefin polymer is greater than that of an olefin polymer obtained by using a fluorided chromium catalyst activated at a temperature of about 650-700° C., under the same polymerization conditions;a ratio of Mw/Mn of the olefin polymer is less than that of an olefin polymer obtained by using a fluorided chromium catalyst activated at a temperature of about 650-700° C., under the same polymerization conditions;a number of long chain branches (LCB's) per 1,000,000 total carbon atoms of the olefin polymer is less than that of an olefin polymer obtained by using a fluorided chromium catalyst activated at a temperature of about 650-700° C., under the same polymerization conditions; orany combination thereof. 18. The olefin polymerization process of claim 13, wherein the olefin polymer is an ethylene homopolymer, an ethylene/1-butene copolymer, an ethylene/1-hexene copolymer, or an ethylene/1-octene copolymer. 19. The olefin polymerization process of claim 18, wherein the olefin polymer is characterized by: a HLMI in a range from about 2 to about 70 g/10 min;a density in a range from about 0.92 to about 0.96 g/cm3;a ratio of Mw/Mn in a range about 6 to about 25;a ratio of Mz/Mw in a range from about 6 to about 12; andless than or equal to about 10 LCB's per 1,000,000 total carbon atoms.