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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 25 of 65 matching plants.
Complete 800.000 tpa Sustainable aviation fuel (SAF) plant comprising of:
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?
Plant is designed to purify, condense, liquefy, and store raw carbon dioxide gas (CO₂) at the site. Production capacity is 15 tons/hour design, possible up to 16,5-17 tons/hour. Purity is 99.995%
Main process steps:
The plant has a production capacity of 35 000 tons Phthalic Anhydride (PA) per year on a continuous seven days per week basis.
Raw material orthoxylene (o-Xylene, 1,2-dimethylbenzene) is mainly imported by ship to the tank storage at the jetty. Orthoxylene is pumped by pipeline to the site. The reaction is strongly exothermic and the reaction heat is recovered generating steam in an integrated WHB (Waste Heat Boiler). The tail gases from the processes are incinerated in a catalytic incinerator (Catox) where complete combustion takes place leaving only effluent CO2 and water.
The exothermic reaction develops substantial amounts of excess heat. Surplus heat is cooled off with a liquidized salt mix made up by potassium nitrate and sodium nitrate, which in turn is cooled with water and hence no thermal oils is present in the WHB. Reaction occurs in potentially explosive areas in all process steps.
The plant handles hydrocarbons at elevated temperatures and pressures and has the potential for pool fires, explosion and gas jet fires. There is however not sufficient quantity of light hydrocarbons to give rise to the inherent potential for a vapor cloud explosions. There is generally a good standard of remote isolation valves provided in the raw material supply as well as in process units.
A rare opportunity is now available to acquire a fully integrated petrochemical complex in Southeast Asia, designed for high-volume production of olefins and downstream polymers. This strategically located asset includes a world-scale naphtha cracker, aromatics production, and polymer plants—allowing buyers to enter or expand within the polyethylene (PE) and polypropylene (PP) markets with remarkable speed and significantly reduced capital cost.
For companies holding long naphtha feedstock positions or seeking immediate entry into ethylene, propylene, and polyethylene production, this facility offers a fast-track route to revenue generation:
| Segment | Capacity (t/yr) | | --- | --- | | Ethylene | 480,000 | | Propylene | 240,000 | | Butadiene | 70,000 | | Benzene | 90,000 | | Toluene | 50,000 | | Mixed Xylenes | 30,000 | This complex efficiently converts naphtha into high-value light olefins and aromatics, creating a competitive platform for polymer production and downstream chemicals.
| Polymer Plant | Capacity (t/yr) | | --- | --- | | Polypropylene (PP) | 300,000 | | Linear Low-Density PE (LLDPE) | 160,000 | | High-Density PE (HDPE) | 160,000 | | New PE Plant (commissioned ~July/Aug 2024, closing Feb 2025) | 250,000 | | Total PE Capacity | 570,000 |
The site is engineered to consume its own ethylene and propylene, feeding 570 kt of polyethylene and 300 kt of polypropylene—minimizing dependence on external feedstock and maximizing operating efficiency.
Unlike a greenfield build that requires years of permitting, engineering, construction, utilities development, workforce building, and commissioning—this asset already exists, operates, and is proven.
Producers supplying Asia-Pacific, India, Middle East, or export PE/PP global trade lanes can rapidly scale output and capture demand in fast-growing regions.
The site can be dismantled and relocated to your home country or industrial platform, preserving:
A relocation project can be:
Speed-to-market matters—this acquisition allows:
Confidential discussions are now open for:
Started as 2 burners in parallel-Dual pressure plant; 3-9 barg; initial capacity was 700 tpd at 100%
-1982: Revamped with Uhde engineering
-2002: MDR increased at 980 tpd at 100%
-2003: Installation of a basket inside both burners to test N20 catalyst developed by owner
-2005: Increase N20 catalyst quantity in both burners
-2007-08: MDR increased to 100 td at 100% (steam turbine speed increased to 5920 rm)
-2012: Replacement of burner basket with new design
-2017: Replacement of burner basket with new design
Formaldehyde Plant (Reichhold Design using metal oxide catalyst).
Available for operation in-place (Allentown, PA USA) or relocation globally.
Process Description:
The Formaldehyde plant (P501) is designed to produce formaldehyde by the catalytic conversion of methanol and oxygen controlled recycle gas. Formaldehyde is produced by the direct oxidation of methanol from the Methanol Storage Tank and Piping (P502). Emissions from the methanol storage tank and piping, during truck unloading, are captured by the Methanol Vapor Recovery System (C502). Emissions not captured by the vapor recovery system are fugitive emissions (Z550). The catalytic conversion reaction is carried out with the aid of a catalyst, which consists of molybdenum and iron oxides. The process gas is passed through the catalyst, contained in a multiple tube unit called the converter. It both heats the air-methanol mixture to the reaction temperature in the upper part of the catalyst tube and removes the heat of the reaction in the lower part. The formalin gases, which leave the converter, are cooled in an after-cooler where low-pressure steam is produced. The cooled gases enter an absorber where the formaldehyde is absorbed into water to produce up to a 53.0% Formaldehyde solution. In order to reach desired production rates, it is necessary to operate the plant under recycle conditions. Part of the gas mixture leaving the absorber stack is returned to a recycle tank where it is mixed with fresh air, at a controlled rate, to maintain oxygen content of 10 — 10.5% by volume. The remaining unused gas mixture goes to the Natural Gas fired (FML541) Catalytic Oxidizer (C501) where it is preheated and oxidized, in the presence of a catalyst, to harmless byproducts. These byproducts are released to the atmosphere through the Formaldehyde Incinerator Stack (5501).
Notes: Shut down in 2024. Documentation is incomplete.
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
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
Solid Separations:
Saccharified mash is then sent to the sugar clarification system. Paddle screens and centrifuges are used to filter out spent grain solids and wash sugar from the spent grains in a 3-stage counter current wash. Liquid sugar is pumped to 121,000-gallon SS storage tanks and solids are sent to rotary drum dyer for final drying.
Fermentation begins with bacterial propagation through a sanitary seed train consisting of two 44 gallon seed tanks, two 2000 gallon seed tanks and finally a 28,500 gallon seed tank before being mixed with liquid sugar in four 285,000 gallon fermenters. During fermentation broth is continuously stripped from the fermenters and passed through an Alfa Laval ultra filtration skid separating the biologics from the fermentation broth which are sent back to fermenter. Filtrate is pumped to the distillation unit where Butanol and Acetone are distilled off through a series of distillation columns and passed through a 3-effect evaporation system before heading to final product storage
Other notable features include an on-site wastewater treatment facility rated for 157,000 gallons per day and full product testing and microbiological laboratory.
Other potential uses included: high protein feed products, renewable biochemicals, single cell proteins, sustainable aviation fuel, food grade organic acids and industrial/GNS alcohols.
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,
(4) Rieter (Maag) Underwater strand pelletizers ( M-USG 900 V)
Viscosity: 200-500 Pas viscosity.
Pellet dimension of (2.1x2.8)mm x 2.8 mm lg. +/- 10%
No. of Strands: 90
Capacity:
Minimum: 3200 kg/h
Nominal: 5000 kg/h
Maximum: 6900 kg/h
Melt density 1.18 g/cm3,
Solid density 1.34 g/cm3.
Melt temperature 285-290°C.
Cooling length before cut: 1.5m
Max strand speed of 220 m/min (minimum speed 100 m/min)
The polymerization plant (PPU) has a capacity of 225,000 tons per year and is a Unipol technology plant, with two gas phase reactors, so can produce homopolymers, random copolymers and impact copolymers.
The extruder is a Coperion ZSK300, with a 5.5MW Loher main motor and associated transformer. The extruder also has a Maag polymer pump, Gottfert on-line rheometer, and electric hot oil systems for the die plate and barrel.
There are six, 280t capacity pellet silos downstream of the extruder, three with air spinner container loading spouts.
There are also another 280t silo, one 140t silo and three 70t silos.
There are also six air blowers for the dilute phase conveying of the pellets from the extruder to the silos or between silos.
There are also two Atlas Copco GA132 compressors to drive the air spinners and silo purging.
There is also a Refinery Grade Propylene (RGP) purification system which includes a Propylene Treatment Plant (PTP) which contains alumina bed driers, a de-ethaniser column, and a de-butaniser column. The PTP supplies treated RGP to a propane-propylene splitter (PPS). The PPS is a heat pump design for minimum utilities demand.
The PTP has a RGP feed capacity of 26 t/hr, whilst the PPS has an RGP feed capacity of 16 t/hr at 70% propylene to produce 11 t/hr polymer grade propylene (PGP) at 98% recovery and 99.0% purity.
The PPU, extruder and PPS were commissioned in September 1991.
The PTP was commissioned in April 1995.
There is a fibre glass cooling water tower comprised of four 15MW cells and three 450kW water circulation pumps. This was commissioned in October 2010.
Plant Capacity: 150,000 MTPY
Commissioned: February 2001
Shut Down: January 2013
Associated with the 4000,000 MTPY VCM Plant -IPP Stock #600847
This 150 kmta PVC Plant uses licensed technology from Ineos Vinyl. The process employs “closed-lid” and VCM stripping technology. The reactors are designed to remain closed in between batches and unreacted VCM is removed with a stripping column for recycle.
Engineering was by Technip and the plant started up in 2001. The last major turnaround was in September, 2012 and the plant was shut down in December, 2012.
The plant produces K57, K66-R-G-F, and K70 grades
Complete EDC/VCM plant available as well.
All field instrumentation is electronic. Redundant Micromotion flow meters are used for critical fluid measurements, even on lines up to 6” diameter.
Utility systems include instrument air compressors (3), nitrogen booster compressor, major electrical transformers (11), thermal oxidizers (2), waste water treatment facility, and fire water pumps (3).
70 TPD PET - SSP Plant It is a facility that manufactures high-IV PET chips suitable for various bottle production by reacting low-IV PET chips produced in a melt polymerization process in a solid state to have high crystallinity and removing moisture and acetaldehyde.
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.
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)
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
Click Here to View this Video on Youtube
3100 Gallon (12 M3), 25 bar Buss Loop Hydrogenation Reactor System
12 m³ 1.4439 SS Hydrogenation Reactor system, BUSS LOOP reactor, -1/25 bar@ 200 ° C, max operating pressure 16 bar@ 105°C . Gebr. Quast/Gothe KG, SN # 2603 total volume 13.143 l. System includes a 114 m² 1.4439 SS heat exchanger , -1/25 bar internal, jkt -1/6 bar @ 200°C, manuf. Gessner Apparatebau GmbH /Germany, volume 870 l pipes, 1.139 l shell, dia 700 mm, 5 m length , connected to AW 413 double jacket pipe, 1.4571 SS 10 bar@ 120°C, 5 l both sides; a 30,6 m² 1.4571 SS Vicarb plate heat exchanger , 8 bar@110°C, 70 l each side, SN # D 3660; and a 995 l 1.4571 SS pressure tank -1/26 bar @ 200°C, used as Hydrogen buffer tank, manufactured By Weisstaler, SN 38644.
The natural gas feedstock is first preheated and de‐sulphurized (382°C/25bar), absorption is carried out over Zinc oxide granules, and then reacted with steam to produce a reformed gas/steam mixture at 860°C temperature and 21 bar pressure.
The reforming reaction is basically the reaction between a hydrocarbon and steam to produce carbon monoxide and hydrogen. In the presence of excess steam these basic products are modified to produce quantities of carbon dioxide and methane, giving a reformed gas consisting of methane, carbon dioxide, carbon monoxide and hydrogen.
The reformed gas/steam mixture is then cooled, separated from process condensate and passed into the make‐up gas compressor where the gas is compressed (36°C /17bar) to a high pressure (113°C/49bar) to be injected into the methanol synthesis loop.
With Carbon Dioxide Additions, the external supply of carbon dioxide is mixed with the high pressure gases from the make‐up gas compressor before injection into the synthesis loop.
Synthesis gases are circulated at high flow rates through a methanol synthesis catalyst held at moderate temperatures (135°C/52bar) where hydrogen reacts with carbon monoxide and carbon dioxide to produce gaseous methanol.
Cooling of the circulated gas condenses crude liquid methanol which is bled from the system and sent to crude storage. The remaining gases are then replenished with make‐up gas before entering the synthesis gas circulator to pass round the loop again.
Inert gases (methane) present in the reformed gas accumulate in the loop and are bled from the system to be burnt as fuel.
The crude methanol contains small concentrations of other organic chemicals synthesized in the methanol converter.
The crude product is then taken from storage, fractionated in two distillation columns and the pure methanol passed to purified product storage tanks.
This all stainless steel, dual-column distillation system was designed by Sabic to separate and purify up to 18 mt/hr of toluene from a complex mixture including isomers, Bisphenol-A, and water. The system consists of a feed tank, vaporizer, pre-flash vessel, upper column, lower column, two column reboilers, and two overhead condensers with vacuum jets.
Subsystem from Complete Bisphenol A (BPA) Plant, IPP Stock #600363
190 Acre API Manufacturing Plant Complex Grimsby, England, UK
This world-class, fully integrated API manufacturing site, formerly operated by Novartis, includes over 1,200m3 of total reactor vessel capacity across three distinct production buildings, available for sale or lease as a whole site or individual buildings for operation in-place. The facility could be utilized for pharmaceutical and animal health API manufacturing or repurposed for specialty/fine chemical manufacturing, flavors and fragrances, or agrochemicals.
VIDEO: https://www.youtube.com/watch?v=AUWUHnAyWos&list=PLRlhdb05DXKR4eyHsLOkB6NzTyh2R4YCE
The site is located adjacent to the river Humber and between the Immingham and Grimsby port facilities, less than 5 minutes from downtown Grimsby, 25 minutes from Humberside Airport, 2.5 hours from Manchester Airport, 3.5 hours from London Heathrow.
Inside the fenceline is approximately 100 acres, with significant development land and infrastructure available inside the fence. There is an additional approximately 90 acres of agricultural land outside the fenceline.
Facility has the capabilities to perform various chemical synthesis, including hydrogenation, Grignard/Friedel-Crafts Reactions, Azide, and Tin Chemistries.
Building 110: Multi-product, Multi-purpose facility (ca. 1993)
Building 120: Mixed High Volume, Multi-Purpose Facility (ca. 1994/2007)
Building 150: High Volume, Multi-Product Facility (ca. 2004/2007)
Each building has its own dedicated solvent storage and recovery, in-process lab spaces, workshops, and offices.
Site Utilities:
The production buildings are supported by the following non-production infrastructure:
Warehousing:
The facility was not used in production of of plant/animal extracts, fermentation, penicilin, beta-lactams, steroids, hormonals, or cytoxic compounds.
UNUSED state-of-the-art highly flexible small molecule manufacturing facility constructed in 2011The facility is capable of producing around 400kg of API per year, allowing for the production of batches from lead to candidate through to Phase III and commercial launch quantities. This is the potential capacity, in a configuration of people working in 2x7h on 5 days, but this tool could be operated on a 24x7 basis if needed, in which case higher levels of output could be achieved. Production capacity remains dependent on the type and number of synthesis steps.
PILOT PLANT