Methods of preparing a catalyst
AssigneeChevron Phillips Chemical Company LP
InventorsEric D. Schwerdtfeger, Max P. McDaniel, Ted H. Cymbaluk, Jeremy M. Praetorius, Kathy S. Clear, Alan L. Solenberger
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AssigneeChevron Phillips Chemical Company LP
InventorsEric D. Schwerdtfeger, Max P. McDaniel, Ted H. Cymbaluk, Jeremy M. Praetorius, Kathy S. Clear, Alan L. Solenberger
Estimating the term…
A method comprising calcining a catalyst precursor comprising chromium and a silica support material at a temperature in the range of from about 95° C. to about 400° C. in a bed fluidized by a gas flowing at a volumetric flow rate of from about 2.5 to about 30 times the settled volume of the bed per minute to form a calcined catalyst precursor. A method comprising calcining a catalyst precursor comprising chromium and silica at a temperature in the range of from about 95° C. to about 400° C. with a gas flowing through the bed at a gas hourly space velocity of from about 15 to about 200 per hour. A method comprising calcining a catalyst precursor comprising chromium and silica at a temperature in the range of from about 95° C. to about 400° C. with a gas flowing through the bed at a weight hourly space velocity of from about 1.9 to about 240 per hour.
A method comprising calcining a catalyst precursor comprising chromium and a silica support at a temperature in the range of from about 95° C. to about 400° C. in a bed fluidized by a gas flowing at a volumetric flow rate of from about 2.5 to about 30 times the settled volume of the bed per minute to form a calcined catalyst precursor.
A method comprising calcining a catalyst precursor comprising chromium and silica at a temperature in the range of from about 95° C. to about 400° C. with a gas flowing through the bed at a gas hourly space velocity, defined as gas flow rate divided by reactor volume, of from about 15 to about 200 per hour.
A method comprising calcining a catalyst precursor comprising chromium and silica at a temperature in the range of from about 95° C. to about 400° C. with a gas flowing through the bed at a weight hourly space velocity, defined as mass flow of gas divided by mass of catalyst, of from about 1.9 to about 240 per hour.
Dependencies are inferred from the claim text.