eddie2314
Chemical
- Jan 3, 2013
- 2
Folks, your help is greatly appreciated on this one. I am involved in the design of an item for use on the international market and am struggling to define what code the basic design should adhere to.
The item is an indirect fired rotary kiln. It can be used in many industries. It consists of a combustion chamber fired by burners. The chamber is vented to atmosphere so no pressure code requirements here. Inside the chamber sits a rotating tube filled with solids. The solids are heated in the tube, and the resultant vapor goes out a vent at the end of the tube. However, the vapor is under back-pressure (approx 7psig, or near 0.5 barg).
I've been looking at ASME code and can see that because the MAWP is < 15psig i don't need to adhere to section VIII. I then looked at section IV for low pressure and it doesn't seem to fall under that either. In my interpretation the unit is not strictly a steam boiler (although the majority of vapour will be steam and minor quantities of hazardous compounds). So my question is, what code, if any, do i need to apply??
Also, i was considering two potential pressure control philosophies.
1. a manual butterfly valve locked in position to create a back-pressure (a restriction orifice basically). Set and forget during commissioning, with a high pressure alarm to interlock the system into shutdown should high pressure arise (the feed moisture is variable so the resulting gas pressure will also be variable but it's intended to set the restriction to be open sufficiently for worst case conditions).
2. a PCV adjusting to a set pressure (looks expensive given the temperatures and vent diameter - 700degC and 6inch). Again, a high pressure alarm would shut the system down.
I'm not fully sure if a pressure relief device is required (given the low pressures, the uncertainty over code requirements, the inclusion of a high pressure interlock already etc).What do you think? Thoughts welcome!
Thanks
The item is an indirect fired rotary kiln. It can be used in many industries. It consists of a combustion chamber fired by burners. The chamber is vented to atmosphere so no pressure code requirements here. Inside the chamber sits a rotating tube filled with solids. The solids are heated in the tube, and the resultant vapor goes out a vent at the end of the tube. However, the vapor is under back-pressure (approx 7psig, or near 0.5 barg).
I've been looking at ASME code and can see that because the MAWP is < 15psig i don't need to adhere to section VIII. I then looked at section IV for low pressure and it doesn't seem to fall under that either. In my interpretation the unit is not strictly a steam boiler (although the majority of vapour will be steam and minor quantities of hazardous compounds). So my question is, what code, if any, do i need to apply??
Also, i was considering two potential pressure control philosophies.
1. a manual butterfly valve locked in position to create a back-pressure (a restriction orifice basically). Set and forget during commissioning, with a high pressure alarm to interlock the system into shutdown should high pressure arise (the feed moisture is variable so the resulting gas pressure will also be variable but it's intended to set the restriction to be open sufficiently for worst case conditions).
2. a PCV adjusting to a set pressure (looks expensive given the temperatures and vent diameter - 700degC and 6inch). Again, a high pressure alarm would shut the system down.
I'm not fully sure if a pressure relief device is required (given the low pressures, the uncertainty over code requirements, the inclusion of a high pressure interlock already etc).What do you think? Thoughts welcome!
Thanks