dh328
Chemical
- Dec 2, 2009
- 10
Hi,
Recently we have faced a problem in operation of our ethylene refrigerant compressor. Although the compressor is working below full capacity, turbine governor valve is fully opened but steam flow is 18 ton/hr compared to full load steam consumption of 30 ton/hr. we have washed the blades and they are clean. Turbine after first stage pressure is 2.2 kg/cm2G (pretty less than max. allowable). main steam pressure is 15 kg/cm2G and it is surprising that steam pressure after throttling valve is 7.5 kg/cm2G. I think that throttling valve parts are loosen or damaged. some colleagues say that strainer in throttle valve may be chocked. what do you think?
what is solution?
Recently we have faced a problem in operation of our ethylene refrigerant compressor. Although the compressor is working below full capacity, turbine governor valve is fully opened but steam flow is 18 ton/hr compared to full load steam consumption of 30 ton/hr. we have washed the blades and they are clean. Turbine after first stage pressure is 2.2 kg/cm2G (pretty less than max. allowable). main steam pressure is 15 kg/cm2G and it is surprising that steam pressure after throttling valve is 7.5 kg/cm2G. I think that throttling valve parts are loosen or damaged. some colleagues say that strainer in throttle valve may be chocked. what do you think?
what is solution?