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Browse our inventory of complete processing plants available for purchase.
Browse our inventory of complete processing plants available for purchase.
Showing 10 of 10 matching plants. Search: "Power".
Combined heat and power cogeneration system, it was built in 2000 and started up in 2001, it was shutdown in early 2016, the engines have operated for 36,300 hours and 34,000 hours
6.72 Megawatt gas fired combined heat and power cogeneration system, system includes:
5000 kg/hr Cochran single pass waste heat recovery boiler, inlet temperature 160 degrees C, outlet 186 degrees C (saturated steam @ 10.5 barg), heat transfer duty 2934 +- 15%, specific gravity/density 0.95 kg/m3, specific heat 1.00 kCal/kg.C, with economiser
2 x 3360.8 Kw (4201 kVA) gas engine driven electrical generator, engine manufactured by Waukesha (Dresser), model #16VAT27GL, serial #C-80859/1 & C-80859/2, SAA #2000-168, natural gas fired, continuous, comp ratio 9/1, min.WKI 91, ignition timing (BTDC) 11-02, service 4650 HP (3469 Kw), altitude limit 500 feet (152 meter), governed speed 1000 rpm, 0.80mm valve intake & exhaust clearance, firing order 1R-1L-4R-4L-7R-7L-6R-6L-8R-8L-5R-5L-2R-2L-3R-3L, AC generator (alternator) manufactured by Leroy Somer, type LSA-56-BM65-6P, serial #167056-2, IP 23, 3360.8 Kw, 4201 kVA power rating, 11000 volt, 220.5 Amp, 3 phase, 50 Hz, 1000 rpm, excitation AREP, all mounted on a carbon steel skid
oil lubrication, cooling water system, MCC control panels, some ductwork,
3.2 MW Gas Fired Co-Generation combined heat and power plant. With (4) 800 KW Caterpillar natural gas-fired, after-cooled, lean burn 3516 90 LE reciprocating engine generator sets each rated at 820kWe output at 480V at the generator terminals.
This chp plant is in excellent condition. All four generators operate at a base load of 700KW, though are capable and have run at their 800KW nameplate. All units are operated on a 24/7 basis with very little downtime for anything other than scheduled maintenance.
5,250 KW, 50 Cycle, Escher Wyss steam turbine generator set, with extraction.
Turbine:
Escher Wyss
Type REA 1600
Designed for 5,240 KW
Rpm: 6,600
Inlet Pressure: 36 Kp/SqCm @ 410 degrees C
Extraction 1 - non controlled 2800 Kg/H
Extraction 2 - controlled 27,000 Kg/H, pressure 11-14 Kp/SqCm
Generator:
Type 14S250
6600 KVA
COS Phi 0.8
Voltage: 11 KV, 50 Hz
"Green Energy" CHP Steam Power Plant Uses Alternative Methane-based Natural Gas Biofuels Like Biogas & Landfill Gas Also Burns Natural Gas Gas Fired Power Generation of 10 Megawatts (MW)
This biogas cogen plant is the largest of the smaller scale combined heat and power systems IPP has available for sale. This 10 megawatt (10,200 kw) thermal power station uses Rankine cycle process to produce energy that could supply electricity to ~2,000 - 6,000 residential customers* and includes:
Deltak gas fired boiler - burns landfill, bio-gas, methane & natural gas
steam powered turbine
10 MW electric power generator by Ideal Electric Co.
Complete control room
Complete documentation available including manuals, drawings, inspection and operational data reports
Built in 1996-1998, this steam power plant started operating in 1998. The previous use was for combined heat and power generation from biogas feed sourced from a landfill. The prior owner shut this chp plant down when its bio gas supply increased dramatically and it decided to replace the gas based power plant with a larger capacity landfill gas power plant. Contact IPP for operational data, documentation, complete equipment list
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This biogas cogen plant is the largest of the smaller scale combined heat and power systems IPP has available for sale. This 10 megawatt (10,200 kw) thermal power station uses Rankine cycle process to produce energy that could supply electricity to ~2,000 - 6,000 residential customers* and includes:
Deltak gas fired boiler - burns landfill, bio-gas, methane & natural gas
steam powered turbine
10 MW electric power generator by Ideal Electric Co.
Complete control room
Complete documentation available including manuals, drawings, inspection and operational data reports
Built in 1996-1998, this steam power plant started operating in 1998. The previous use was for combined heat and power generation from biogas feed sourced from a landfill. The prior owner shut this chp plant down when its bio gas supply increased dramatically and it decided to replace the gas based power plant with a larger capacity landfill gas power plant.
1 on 1 power train configuration
1 Gas turbine, 1 Steam turbine, 1 HRSG
2 x GSUT
1 x 115 kV / 23 kV transformer
1 x 115 kV/ 6.9 kV Aux transformer
2 x 6.9 kV/ 400V Aux transformer
Demin + RO water treatment
Steam delivery: 20 ton/ hr, 1.3 barg superheated steam to an Industrial User
GE MS6001FA w/ DLN2.6 combustion NG fired OpFlex Auto Tune, speed 5,200 rpm, Output 64.0 MW
GE 7A6 Air cooled generator, Output 83.6 MVA, Armature volts 11.5 kV, 50 Hz, 2 Poles, 3 phase , Speed 3000 rpm
Facility Details
90,000 sq. ft. OSD Manufacturing Site
Designed for tablets, capsules, powders, and sachets, this Oral Solid Dose (OSD) manufacturing facility is immediately available for redeployment/operation. The facility was previously operated under US FDA regulations until its idling in 2025.
From blending and tableting to fluid bed drying, pan coating, and packaging, this facility has it all. With GMP-compliant workflows, serialized packaging lines, a DEA vault, and robust utilities, the system is built for high-output, regulated production with minimal ramp-up.
Suitable Uses
Manufacturing Assets
Dispensing / Weighing
Milling / Sieving
Blending / Mixing
Precision Dispensing & Weighing Equipment
Granulation
Drying (for wet granulation)
Milling & Particle Size Control Equipment
Compression / Tableting
Tablet Coating
Encapsulation
Final Dose Formation Equipment
In-Process Testing (IPT)
Bottling / Blister Packaging
Final Quality Control (QC) Testing
Storage / Warehousing
Utilities & Site Infrastructure
Control & Support Systems
Special Features
Plant Layout Overview
Main Floor: 65,860 Sq. Ft.
Second Floor: 26,794 Sq. Ft.
Total: 92,654 sq. ft.
Why This Plant?
NEW From Cancelled Project!
Using “excess air + solid sulfur” incineration process, the obtained sulfur dioxide gas concentration is about 12%~15%. Control the reasonable sulfur incineration temperature to ensure complete combustion of sulfur.
Using our proprietary technology for solid sulfur feed system, so that the sulfur incinerator temperature is stable, the sublimation sulfur is less in the flue gas. The plant is designed with negative pressure air blowing system, which has good operating environment, and sulfur yield is high.
Using automatic continuous discharging centrifuge, which is a continuous automatic operation, is safe and reliable, saving manpower.
The low concentration sulfuric acid waste liquid is used for production of Magnesium Sulfate products, so the plant has no waste liquid effluent discharge.
Perfect design of exhaust gas treatment. In the waste gas, SO2 concentration is less than 50mg/Nm3（SO2≤50mg/Nm3）.
The air is filtration by air filter, and then is feed into air compressor, the air is compressed by air compressor and is feed into sulfur incinerator, the air burning with solid sulfur and obtain sulfur dioxide gas (SO2).
The solid sulfur is fed into sulfur incinerator by solid sulfur feeder, the solid sulfur is mixed with air and burning in the sulfur incinerator, and obtain sulfur dioxide gas (SO2), and release a lot of heat at the same time.
S + O2 = SO2 + Q
A part of sulfur dioxide reaction with oxygen and get sulfur trioxide.
2SO2 + O2 = 2SO3 -Q
After burning, the hot flue gas is enter the flue gas buffer tank, and then is enter the cooling pipe, using circulating water to cooling the flue gas, the flue gas is cooling to 50~60℃ and then is feed into flue gas scrubber, through bubble washing to remove SO3 of flue gas. After the flue gas scrubber, using stage of separator to separation and removal of entrained droplets of flue gas. The scrubbing obtained dilute sulfuric acid is collected and used to produce Magnesium Sulfate by-product. The purified sulfur dioxide gas is sent (through pipeline) to sodium Metabisulfite synthesis section.
SO3 + H2O = H2SO4
Put solid soda ash (Na2CO3) into the soda ash batching kettle of sodium Metabisulfite synthesis section, add water and mother liquor (the filter liquor) of sodium Metabisulfite centrifuge and mixed into suspension, and then pumping the suspension into sodium Metabisulfite synthesis reactors, and feeds clean sulfur dioxide gas successively into the first stage, second stage and third stage synthesis reactors, after synthesis reaction, get sodium Metabisulfite suspension in the first stage synthesis reactor. The reaction tail gas is discharged from the third stage synthesis reactor, and is lead into the scrubbing tower for treatment.
Na2CO3 + 2SO2 = Na2S2O5 + CO2
The Sodium Metabisulfite suspension is discharged from the first stage synthesis reactor and stored into slurry tank, and then from the slurry tank feed into centrifugal, through centrifugal separation and get wet solid Sodium Metabisulfite, which is content 3~5% water, feed the wet Sodium Metabisulfite into hot air dryer (airflow drier), and through cyclone separators, get Sodium Metabisulfite products. The filtrate is collected into the acid mother liquor tank, reused for soda ash solution batching kettle. The drying use hot air comes from the waste heat recovery jacket of sulfur incinerator. After drying, the tail gas is send into tail gas absorption column.
The tail gas countercurrent contact with soda ash solution, the sulfur dioxide gas in the tail gas was absorbed by soda ash solution, the tail gas was cleaned and emptying **(SO2≤50mg/Nm3)**. The absorption solution reused for soda ash solution batching.
In the flue gas scrubber of sulfite dioxide purification section, the sulfite trioxide is absorbed by water and get concentration of 50~60% dilute sulfuric acid liquid waste, which is used to produce Magnesium sulfate heptahydrate by-products.
MgO + H2SO4 + 6H2O = MgSO4·7H2O
maximum proven capacity = 1.16 kt ammonia per day
feedstock: natural gas 50bar,
specific consumption 0.62-0.64 Tm³/t
energy/utilities: natural gas 5bar 0.35-0.37 Tm³/t;
CO2 emission 2.0-2.1 t/t
last major TARs: 2021 (reformer tubes exchange, syngas line renovation, catalyst change, turbines & compression overhaul, incl. 2.5-yearly DLRG (pressure equipment directive) inspections), 2019 (DCS migration user interface, SLPC, CUI measures, incl. 10-yearly DLRG inspections), 2017, 2014, 2011
The plant consists of:
Estimated Rate for the (2) Lines: 1,000 - 5,000 lbs/hour (material dependent)
Estimated Rate for the line: 1,000 - 7,000 lbs/hour (material dependent)