Available high suction pressure compression unit (5000 psi)

COMPRESSION UNIT ARIEL JGD-6, SPEED: 1000 RPM, HP: 3550 HP, FLOW RATE:10 MMSCFD, STROKE: 5.5 in, CLASS: JGD, NUMER OF THROWS: 6, RATED POWER: 6210 BHP, FRAME FRICTION POWER: 57 BHP, CYL FRICTION FACTOR: 0.95, GUIDE TYPE: SEPARATE, SPEED RATINGS: RATED PISTON SPEED : 1100 RPM, MAXIMUM SPEED: 1200 RPM, MINIMUM SPEED: 600 RPM

MOTOR CAT GE3612 LE GAS PETROLEUM ENGINE 3550 BHP-3785 BHP 100 RPM

V-12, 4 STROKE CYCLE, BORE: 300 mm (11.8 in), STROKE: 300 mm (11.8 in), DISPLACEMENT: 254 L (15,528 cu. in), ASPIRATION: TURBOCHARGED-AFTERCOOLED, DIGITAL ENGINE MANAGMENT; GOVERNOR AND PROTECTION ELECTRONIC (ADEM A3)

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(2) Mobile Substation For sale 30 MVA, 115/13.8 KV

1. POWER TRANSFORMER 2. TRAILER 3. HV SURGE ARRESTER 4. HV CAPACITIVE VOLTAGE TRANSFORMER 5. HYBRID SWITCHGEAR 6. OUTDOOR CIRCUT BREAKER ROOF BUSHING 7. CONTROL & PROTECTION PANEL 8. BATTERY CHARGER

GE TM2500 Derivative Gas Turbine (USED). NOT BROKERS. INFO@PRAIVA.COM

GE TM 2500 <10.000 HOURS SC Net Output (MW): 34.6 MW (50 HZ ) SC Net Output (MW): 37 MW ( 60 HZ )

2500 HP Electric, Ariel KBK/4 GAS COMPRESSOR UNIT AVAILABLE FOR SALE

. 2500 HP Electric, Ariel KBK/4 Compressors – Capacity ~12MMSCFD @ 40# sucti on / 900# discharge – (3 Units) (3) coolers for these units are currently located in at Alfa Laval (manufacturer of the coolers) maintenance has been performed by UEC on the units. (1) MCC Building - (1) VFD, sync transfer control and MV MCC with PFCC for 4 units (1) Virginia 12.47 kV to 4160/2402 V, 12000//22400 KVA Power Transformer with 400A NGR to support these units.

Available 8136 Kw Man Energy Solution Mgt6000

Available: 3 Units. Condition: New. Never Used. 50 Hz.

Used Solar Mars 100 turbines. not brokers. info@praiva.com

<10.000 hours 50 Hz Fuel: Gas Natural

BOILER CLEAVER BROOKS CB PACKAGED BOILERS, CB600-800, YEAR: 2011 FOR SALE.

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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