mkuppe
Chemical
- Jun 19, 2012
- 5
Hello all,
I'm requesting a clarification on the API 570 literature. I'm attempting to classify piping in a plant that produces 200 proof ethanol for fuel. For the most part everything is pretty clear but I'm getting mixed interpretations from others about certain piping circuits. For example, at the top of the rectifier column, 190 proof ethanol vapor is travelling through a pipe. The temperature of the product is above the boiling point (obviously) but well below the auto-ignition temperature. I'm inclined to believe that as per the guidelines in API 570 section 6.3.4.2b, this qualifies the pipe as a Class 1 since the atomospheric boiling point is below the operating temperature. However, I've had others tell me that this would be a Class 3 pipe, but I'm skeptical since we are operating well above the flash point. Any thoughts or clarification would be greatly appreciated. Thank you.
I'm requesting a clarification on the API 570 literature. I'm attempting to classify piping in a plant that produces 200 proof ethanol for fuel. For the most part everything is pretty clear but I'm getting mixed interpretations from others about certain piping circuits. For example, at the top of the rectifier column, 190 proof ethanol vapor is travelling through a pipe. The temperature of the product is above the boiling point (obviously) but well below the auto-ignition temperature. I'm inclined to believe that as per the guidelines in API 570 section 6.3.4.2b, this qualifies the pipe as a Class 1 since the atomospheric boiling point is below the operating temperature. However, I've had others tell me that this would be a Class 3 pipe, but I'm skeptical since we are operating well above the flash point. Any thoughts or clarification would be greatly appreciated. Thank you.