WHY STRIP FOUL CONDENSATES? ABSTRACT - TAPPIGet A Quote
mmBtu per short ton kg CO 2 per mmBtu g CH 4 per mmBtu g N 2O per mmBtu kg CO 2 per short ton g CH 4 per short ton g N Blast Furnace Gas: Fuel Gas: 0.001388 59.00 3.0 0.60 0.08189 0.004164 0.000833 Propane Gas: 0.002516 61.46 3.0 : 0.60 0.15463 0.007548 0.001510Get A Quote
31/05/2005 · This stream consists of the underflow from the primary condenser W 3 (12.98 ton/hr, 419 ppmw methanol) and the underflow from the turpentine decanter W 5 (9.7 ton/hr, 16,248 ppmw methanol) Wastewater stream W 7 (10.78 ton/hr, 9900 ppmw methanol) resulting from (8.20 ton/hr of fresh water that is added to condense a vapor stream (2.58 ton/hr, 41,360 ppmw methanol)Get A Quote
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them to destroy 10.2 pounds of methanol (MeOH) per oven dry ton of pulp (ODTP) (5.1 kilograms per oven dry megagram of pulp). Unbleachedmills will have to destroy 6.6 pounds per ODTP (3.3 kg/Mg). Most mills built or upgraded since 1980 have had a condensate stripping system installed as an integral part of the overall mill process. Many older mills have now added a foul condensate stripper toGet A Quote
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