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Product Thermal Capacity: 1 - 20 t/h
Working Pressure: 0.7 - 2 Mpa
Product Thermal Capacity: 20 - 110 t/h
Working Pressure: 1.25 - 5.3 Mpa
Product Thermal Capacity: 2 – 20t/h
Working Pressure: 1 - 2.5 MPA
Product Thermal Capacity: 4 - 35 t/h
Working Pressure: 1.0 - 2.5 MPA
If condensate isn’t returned to the boiler, the steam system must make up the loss with cold, untreated, raw water that has to be prepared for boiler operation. This preparation has a cost. The make-up water also contains substantially less BTU content that must be …
Boiler load - the capacity of a steam boiler - is often rated as boiler horse powers, lbs of steam delivered per hour, or BTU. Lbs Steam delivered per Hour. Large boiler capacities are often given in lbs of steam evaporated per hour under specified steam conditions. BTU - British Thermal Units
For steam mains drainage, the condensate load for each drain trap is typically 1% of the steam capacity of the main based on drain points at 50 m intervals, and with good insulation. For most drain points, sizing the trap to pass twice the running load at the working pressure (minus any backpressure) will allow it to cope with the start-up load.
Return Condensate to the Boiler When steam transfers its heat in a manufacturing process, heat exchanger, or heating coil, it reverts to a liquid phase called condensate. An attractive method of improving your power plant’s energy efficiency is to increase the condensate return to the boiler.
Returning hot condensate to the boiler makes sense for several reasons. As more condensate is returned, less make-up water is required, saving fuel, make-up water, and chemicals and treatment costs. Less condensate discharged into a sewer system reduces disposal costs. Return of high purity condensate also reduces energy losses due to boiler
Condensate pumps are typically sized at three times (3x) normal condensing or evaporation rate. These guidelines are based upon design and operating experience. However, upon proper application, units can be sized at two times (2x) the condensing or evaporation rate.
Related Topics . Air Conditioning - Air Conditioning systems - heating, cooling and dehumidification of indoor air for thermal comfort; Related Documents . Air - Composition and Molecular Weight - Dry air is a mechanical mixture of nitrogen, oxygen, argon and several other gases in minor amounts; Air - Density at varying pressure and constant temperatures - Figures and tables showing changes
As I mentioned in my earlier post regarding about Steam Trap, while selecting a steam trap the most important data required is the condensate load.. This data is generally provided by the process department but as a piping engineer too should be in a position to estimate the condensate loads initially.
Condensate Receiving & Condensate Flash Recovery tank design. Abstract : Condensate receiving tank or condensate mound is one of the simple equipment in sugar industry and other process industries. If we provide common condensate flash recovery tank then no need to provide individual mounds for each evaporation or heating bodies like juice heaters, evaporator bodies, pans .. etc.
Dec 08, 2017· Steam condensate calculation covering: steam and condensate systems steam and condensate piping steam and condensate manifolds steam
Exchangers, Heat Pipes, Industrial Pumps, Water Heaters, Water Softeners, Boiler Seminars, Services & Parts. 8 Common Boiler Formulas BR = (1 / CC) * BC BR = (1 / 8.6) * 10,000 BR = 1,163#/hr Where, BR Blowdown rate BC Boiler capacity in #/hr NOTE – To convert the previous example from #/lb to GPM’s follow the following conversion:
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