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Facilities For Sale

500 STPD NITRIC ACID PLANT

Plant Capacity : 500 STPD
Age : Installed in 174
Stopped operations in 2010
Footprint : 
Technology Provider : The plant uses the Weatherly high-pressure process with air compressor discharge pressure of 154.54 psia at 348 ºF, convert pressure at 137 psig and absorption pressure at 140 psig.


THERMAL DESALINATION UNITS Mechanical Vapor Compression (MVC)


Plant Capacity : 17,280 m3/day or 120 m3/hour/unit 
Age : Installed in 2000, Stopped operations in April 2019 
Footprint : 35m x 70m 
Technology Provider : IDE 
Thermal Desalination with Mechanical Vapor Compression (MVC) technology used for Seawater 



GTE (Glycerin to Epichlorohydrin) Plant

Plant Capacity : 12000 ton-per-year
Age : Commissioned in 2012 and shut down in 2013.
Footprint : 
Technology Provider : DBO (Desmet Ballestra Oleo)



Secondary Aluminum Production from recycling scrap

Plant Capacity : 50.000 ton-per-year
Age : 2019
Footprint : 5000 m2 (Land),  1690 m2 (Facilities)
Technology Provider : 



Bio Oil, Bio Gas, & Charcoil Plant

Plant Capacity : 1800 ton-per-year
Age : 2019
Footprint : 
Technology Provider :  



FREEZE CONCENTRATION PLANT 


Plant Capacity : 17.000 POUNDS-PER HOUR 
Age : 2019
Footprint : 
Technology Provider :  GEA MESSO PT











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500 TPD NITRIC ACID PLANT FOR SALE

 Used 500 STPD Nitric Acid Plant built in 1974. This Nitric Acid Plant uses synthesis by oxidizing ammonia to make nitrogen dioxide, then absorbed over a catalyst and water to form nitric acid. New major equipment was installed during 1994 - 2013. Atmospheric air is filtered and compressed in a centrifugal compressor, which is driven by a hot gas expander and steam turbine. Liquid ammonia is vaporized, superheated and filtered and is joined by the compressed air stream in a double mixing operation based on orificing. The combined ammonia-air mixture enters the converter where the ammonia stream ignites and burns very rapidly to form nitric oxide and water vapor. The hot reaction products and excess air leaving the converter pass through a waste heat boiler and heat exchanger to: cool the process gas before entering the cooler condenser; recover heat be the generation of steam; and recover power by heating the tail gas for use in the hot gas expander. Partially cooled process gas enters

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