Andy2005
Industrial
- Feb 7, 2005
- 2
I wonder if anyone can help? I'm currently carrying out a project on factors that affect rapid gravity filter performance in water treatment, and one aspect I'm looking at in particular is the effect of solids loading.
In order to calculate solids loading, I believe I need to convert the influent turbidity value (in NTU) to mg/l suspended solids. Several values have been suggested to me as being 'the conversion factor that you use' however, I'm struggling to find any literature that supports any of the claims. Examples of what I have been told are:
1.5 if converting raw water turbidity to mg/l ss.
2.0 if converting interstage turbidity to mg/l ss.
I have also seen a model that uses 1.1 as the conversion factor. Please can somebody clarify what are the correct values to use, and if possible the title of a reference book or paper that supports the claim?
Many thanks...Andy
In order to calculate solids loading, I believe I need to convert the influent turbidity value (in NTU) to mg/l suspended solids. Several values have been suggested to me as being 'the conversion factor that you use' however, I'm struggling to find any literature that supports any of the claims. Examples of what I have been told are:
1.5 if converting raw water turbidity to mg/l ss.
2.0 if converting interstage turbidity to mg/l ss.
I have also seen a model that uses 1.1 as the conversion factor. Please can somebody clarify what are the correct values to use, and if possible the title of a reference book or paper that supports the claim?
Many thanks...Andy