A chemical engineer must calculate the maximum safe operating temperature of a high-pressure gas reaction vessel. The vessel is a stainless-steel cylinder that measures 23.0 cm wide and 27.6 cm high. The maximum safe pressure inside the vessel has been measured to be 8.60 MPa. For a certain reaction the vessel may contain up to 0.959 kg of dinitrogen difluoride gas. Calculate the maximum safe operating temperature the engineer should recommend for this reaction. Write your answer in degrees Celsius. Round your answer to 3 significant digits. temperature: I °C ?

Chemistry for Engineering Students
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Author:Lawrence S. Brown, Tom Holme
Publisher:Lawrence S. Brown, Tom Holme
Chapter11: Chemical Kinetics
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A chemical engineer must calculate the maximum safe operating temperature of a high-pressure gas reaction vessel. The
vessel is a stainless-steel cylinder that measures 23.0 cm wide and 27.6 cm high. The maximum safe pressure inside the
vessel has been measured to be 8.60 MPa.
For a certain reaction the vessel may contain up to 0.959 kg of dinitrogen difluoride gas. Calculate the maximum safe
operating temperature the engineer should recommend for this reaction. Write your answer in degrees Celsius. Round
your answer to 3 significant digits.
temperature: ] °C
Ox10
?
Transcribed Image Text:A chemical engineer must calculate the maximum safe operating temperature of a high-pressure gas reaction vessel. The vessel is a stainless-steel cylinder that measures 23.0 cm wide and 27.6 cm high. The maximum safe pressure inside the vessel has been measured to be 8.60 MPa. For a certain reaction the vessel may contain up to 0.959 kg of dinitrogen difluoride gas. Calculate the maximum safe operating temperature the engineer should recommend for this reaction. Write your answer in degrees Celsius. Round your answer to 3 significant digits. temperature: ] °C Ox10 ?
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