Dear All
Greetings
I need expert advice, suggestion and opinions regarding sour water stripping operation.
We have commissioned sour water stripper unit in June 2017. It was designed by STP and EPCC by Hualu china. Since start up we face so many issue regarding its stripped water quality. It was design to treat sour water coming from DHT and NHT units and its stripped water again recycle back 40 % to DHT and NHT as wash water while remaining 60% as effluent. In general operating manual the specifications of stripped water provided as as follows
01. H2S <100 ppm
02. NH3 <100 ppm
Both of the above parameters are meeting and within limits. Issue is that the quality required by DHt and NHT unit (UOP) have some requirements to use stripped water as wash water.
01. TDS < 3 ppm
02. Cl < 1 ppm
03. TSS < 1 ppm
Stripped water producing from our stripper has following parameters
01. TDS 50-80 ppm
02. TSS 10-20 ppm
03 Cl 5-15 ppm
04 H2S 5-10 ppm
With these specifications we unable to recycle back as wash water and all the stripped is discarded as effluent. Some time we only able to use blend of stripped water and condensate (20:80 ratio) to meet results but most of the time we are wasting our water. Management has serious concern about water shortage and continuously forcing us to reuse it. Please comment how we can reduce TDS, TSS, Sulphides in stripped water. Can TDS remove through stripping means where the will go as we have one output which is stripped water and other output is sour acid gas. So where this TDS going still confused. We don't have any technical support from designer and expertise inside refinery as well.
Please comment where we can reuse this water within refinery other than wash water in hydro processing units. How we can improve the quality of stripped water.