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:

1. Washing of raw CO₂ gas
2. Compression of CO₂ gas(centrifugal compressor and screw compressor – 2 stages)
3. Purification and dehydration of CO₂ gas
4. Liquefaction of CO₂ gas (using a condenser operating with ammonia)
5. Distillation of liquid CO₂
6. Storage and loading stations

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.

• The plant produces food grade CO2 at a capacity of 250Te/day. The CO2 final product spec is 99.998% purity.

• The plant mainly consists of

  • 3 off Sulzer 3 stage compressors 560psig discharge
  • Water scrubber to remove soluble impurities
  • Charcoal bed to remove traces of sulphur and oil
  • Activated alumina bed dryer (2 off for regeneration)
  • Condenser to produce liquid CO2 using ammonia as refrigerant
  • Stripping column to remove entrained inert gases using recycled CO2

Product specification:

Water 10.0 ppm w/w max

Sulphur 0.1 ppm w/w max

Gaseous inerts 100 ppm v/v

Methanne10 ppm v/v max

Argon 1.0 ppm w/w max

Boron 0.1 ppm w/w max

Halogens 1.0 ppm w/w max

Carbonyls 1.0 ppm w/w max

Oil 2.0 ppm w/w max

Arsenic 0.0 ppm w/w max

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,

• 6,500 Nm3/hr capacity

• Updated PSA 2006

• Fuel in natural Gas with an end pressure of 17.5 bar

• Yogawa PLC System

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

• Estimate based on average annual electricity consumption figures published by the US Energy Information Administration with a peak load factor of 2.0.

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

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

• Estimate based on average annual electricity consumption figures published by the US Energy Information Administration with a peak load factor of 2.0.

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.

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.

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.

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;

• power 0.06-0.08 MWh/t;
• steam consumption needed only during startup
• 4bar steam generation (export) 1 – 1.27 t/t;
• 16bar steam generation 0.1-0.2 t/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

MAJOR UNITS

The plant consists of:

• Natural gas desulphurization
• Primary reformer (operates at 790°C and 30bar with the secondary reformer at 950°C)
• Secondary reformer with air compressors
• Natural gas desulphurization
• Primary reformer
• Secondary reformer with air compressors
• High and low temperature shift.
• CO2 removal
• Mechanization
• Syn gas compressor and air compressor
• Ammonia synthesis (reaction is 270 bar)
• Ammonia evaporation

1,170 barrel-per-day Fischer-Tropsch (FT) Gas-to-Liquid (GTL) Wax plant targeting the production of higher-value wax products.

Product Mix:

Naphtha: High purity liquid paraffins targeted for chemical feedstock, or chemicals such as solvents, lighter fluids

Distillate: Zero sulfur and high cetane, ideal performance-enhancing automotive diesel additive, or used as high purity liquid paraffins in chemicals such as solvents, detergents, or drilling fluids

J40 Low Melt and J55 Mid Melt Wax: Low and mid-melting point waxes are primarily used in candles, corrugated board, particle board, tires, PVC additives, pharmaceuticals and personal care and cosmeticsJ75 High Melt Wax: Used in PVC additives for extruders, hot-melt adhesives, inks paints and coatings, candle additives, and personal care and cosmetics

J100 Hard Wax: Used in hot melt adhesives, PVC lubricants, inks, paints and coating additives, asphalt additives, and personal care and cosmetics

• The facility is nearly (75%) finished construction with all new equipment fabricated in 2015.
• The SMR was originally built in 1993 and only operated for about 10 years. It has been completely overhauled and has zero hours since overhaul.
• The two FT reactors are 78,000 sq ft shell and tube exchangers with FT catalyst packed inside the tubes.  The reactors are 11’ diameter with 32’ long tubes which are rated for 500 psig at 500°F.
• All of the steam-generation equipment is included for capturing the FT reaction exotherm.
• Most of the downstream process-contact material of construction is 304Lstainless steel.
• There is no asbestos in this facility.
• This system is located on a major deep-water port with international shipping routes and is available for operation in place.

1,170 barrel-per-day Fischer-Tropes GTL Facility targeting the production of higher-value wax products.

The facility consists of the following sections:

• Steam-Methane Reformer: 46.5 MMSCFD Linde-designed Steam-Methane Reformer (SMR) facility including feed preparation, reformer, syngas cooling, steam generation, hydrogen separation, carbon dioxide removal section (amine section), and carbon dioxide compression for recycle. The facility has only 10 years of operation as a HyCO Plant (hydrogen and carbon monoxide production). The SMR was redesigned and upgraded by Linde in 2015 to supply the new GTL facility
• Fischer-Tropes Reaction Section: Two Fischer-Tropes reactors, each with78,000 sq ft shell and tube exchangers with FT catalyst packed inside the tubes. The reactors are 11’ diameter with 32’ long tubes which are rated for 500 psig at 500°F. All of the steam-generation equipment is included for capturing the FT reaction exotherm. All of the equipment was constructed in 2015 and most of the downstream process-contact material of construction is 304L stainless steel.
• Product Fractionation Section: The Fractionation Column is 3’ diameter by 90’ tall and is constructed of 304 stainless steel. It is rated for 50 psig/full vacuum at 650°F. It has four packed sections with four product “take-offs” (overheads, two side-draws, and bottoms). All associated equipment is included such as the feed heater, condenser, two accumulators, and four overheads product/reflux pumps included. This system was manufactured in 2015 and is almost entirely 304 stainless steel construction.
• Wax Upgrade Section: Two 4,000 gallon batch hydrogenation reactor systems; each with 100 gpm feed capabilities. The reactors are rated for 327 psig at 455°F. Two 218 sq ft Short-Path Distillation Units (SPDU) rated for 22 psig/FV @ 572°F. One 82 sq ft Wiped-Film Evaporator (WFE) rated for 22 psig/FV @ 572°F. All of these systems were manufactured in 2015 in modular construction units and are ready to ship. Virtually all of the process contact material of construction is 304 stainless steel or better. The facility was designed and delivered in modules, but was never constructed or operated.

More Details

• The Fischer-Tropes Reaction Section, the Product Fractionation Section, and the Wax Upgrade Section were all manufactured in 2015 and have never been operated. All of the equipment downstream of the FT Reactors is constructed of 304L stainless steel or better alloys.
• The process is being kept under a nitrogen blanket. All electric motors are being “bumped” weekly or they have been removed and are in climate- controlled storage.
• The DCS is by Yokagawa and it is completely programmed and ready to install. The hardware is still at Yokagawa.
• There is no asbestos in this facility.
• Many spare parts are available.
• This system is located on a major deep-water port with international shipping routes.

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).

Capacity:

• 600 tons/day (25 tons/hr)

Raw Materials:

• CO2 supplied from a Long Residue Gasification Plant
• Liquid NH3 supplied from an Ammonia Production Plant

Product:

• Pelletized urea (carbonic acid diamide)
• The product is surface-modified - using URESOFT® 150 agent  to avoid  agglomeration. The typical content of this agent is 0.4% by weight.

1,250 TPD Ammonia Plant Equipment Available

Compressors

212808 - Clark-Model #4M9-7-P, rotary air compressor

• Capacity: 24,979 ACFM
• Direct driven by steam turbine through gear reducer
• HP=8920/RPM 538
• 7 stages, 2670 critical speed
• 14.07 PSIA / PD-86.0 PSIA (1st Stage: Air)

212809 - Clark Model #2M8-6, CS rotary air compressor

• Capacity: 4,079 ACFM
• Driven by a steam turbine through a gear reducer
• 8920 hp / 10211 rpm
• 6stages 6500 rpm critical 10211 rpm
• PS-8.5 PSIA / PD-490 PSIA (2nd Stage: Air)

212812 - Clark Model #2BF-7(5), CS Centrifugal

• Capacity:611  ACFM, rated for 16930 hp/10585 rpm
• Driven by Turbine/Gear
• PS-1,796 PSIA / PD-2,530 PSIA (1st Stage: SynGas)

212813 - Clark Model #2BF-7, CS Centrifugal

• Capacity: 1,326ACFM, rated for 16930 hp
• Driven by Turbine/Gear
• PS-904 PSIA / PD-1,816 PSIA (2nd Stage: SynGas)

212814 - Clark Model #2BC-8, CS Centrifugal

• Capacity: 3,528 ACFM , rated for 16930 hp
• Driven by turbine/gear
• PS-358 PSIA / PD-914 PSIA (3rd Stage: SynGas)

212815 - Clark Model #2M8-5, CS Centrifugal

• Capacity: 4,284 ACFM, rated for 9185 hp
• Driven by turbine/gear
• 5 stages - 10,438 rpm speed/1,000 rpm max/6650 critical
• PS-140 PSIA / PD-230 PSIA (1st Stage: Refrigeration)

212816-Clark Model #4M8-7, CS Centrifugal

• Capacity 11,763 ACFM  rated for 918 5hp
• Driven by turbine/gear
• 7 stages, 5875 rpm speed/6220 rpm max/3000 critical
• PS-29 PSIA / PD-143 PSIA (2nd Stage: Refrigeration)

Ammonia Converter

212801- Struthers Wells

• Capacity: 19,135 Gallons
• 7’ d x 75’l (overall)
• 2,600 PSI (Haldor Topsoe: S-200)
• Shell thickness 4.125"/ Head thickness 3.125"

Gears

212811 - General Electric Model #S-234-BG

• Input RPM-5,380 / Output RPM-10,211
• HP-4,862

212818 - General Electric Model #S-234-BH

• Input RPM-5,875 / Output RPM-10,413
• rated for 1.78 ratio
• HP-3,267
• Clockwise rotation
• Gear and pinion

212819 - Lufkin Model #D290C

• Input RPM 1,749/ Output RPM-74
• Rated for 23.33:1 ration
• HP 155

95078 - General Electric Model #SI-458-A

• Input RPM-4,860 / Output RPM-10,585
• HP-20,000

Turbines

212810 - Model #3TDFOV2

• CS, horizontal multi stage condensing turbine
• Manufactured by Worthington
• RPM-5,650
• HP-9,800
• Inlet-540 PSIG
• Rotation clock wise
• 5 stage rateau (double 4th & 5th stage)

212817 - Model #3TDFOV2

• CS, horizontal condensing turbine
• Manufactured by Worthington
• 5 stage rateau (double flow 4th & 5th stage)
• RPM-6,175
• HP-10,100
• Inlet PSI-150 @ 450° max
• Exhaust-4” of Hg  ABS. at 128°F
• Rotation clockwise

212820 - Unused spare turbine rotor for Terry Turbine model GAF6

Heat Exchangers

282825

• 5,290 sq. ft Horizontal
• Manufactured by Struthers Wells
• CS Shell / CS Tubes / CS Heads
• 100 PSI Shell / 2,600 PSI Tubes (@600°F)
• Single pass Shell and Tube

212823

• 5,955 sq. ft Horizontal
• Manufactured by Heatran
• CS Shell / CS Tubes / CS Heads
• 2,600 PSI Shell / 2,600 PSI Tubes  (@600°F)
• Single Pass shell and tube

212821/212822

• 11,300 sq. ft., Horizontal
• Manufactured by Heatran
• CS Shell / CS Tubes / CS Heads
• 2,600 PSI Shell / 2,600 PSI Tubes (@ 600°F)
• single pass shell and tube

Tanks

212802

• 6,200 Gallon, CS, vertical storage tank, mounted on a skirt.
• Manufactured by National Tank Co.
• Rated for 644 psi at 460 degrees F, 6'6" diameter x 23' long, Welded dish heads.
• Wall thickness= 1.625"  Skirt height 5'.

212803

• 6,200 Gallon, CS, vertical storage tank, mounted on a skirt.
• Manufactured by Nooter.
• Rated for 644 psi at 460 degrees F, 6'6" diameter x 23' long, Welded dish heads.
• Wall thickness= 1.625"  Skirt height 5'.

212804

• 9,000 Gallon, CS,  vertical pressure tank.
• Manufactured by Delta Southwestern.
• Rated for 405 psi at 875 degrees F.13' diameter x 5' straight side with welded hemi heads.
• Wall thickness =2.9".  Eight lug supports.

212805

• 5,700 Gallon, CS, vertical pressure tank
• Manufactured by National Tank.
• Rated for 430 psi at 800 degrees F. 10'6" diameter x 7' straight side with welded hemi heads.
• Wall thickness is 1.6".  Support by lugs.

212806

• 6,200 Gallon, CS, vertical storage tank, mounted on a skirt.
• Manufactured by National Tank.
• Rated for 644 psi at 460 degrees F, 6'6" diameter x 23' long, Welded dish heads.
• Wall thickness= 1.625"  Skirt height 5'.

212807

• 6,200 Gallon, CS, vertical storage tank, mounted on a skirt.
• Manufactured by National Tank.
• Rated for 644 psi at 460 degrees F, 6'6" diameter x 23' long, Welded dish heads.
• Wall thickness= 1.625"  Skirt height 5'.

Furnace

212800

• 15.00 mm/btu, vertical furnace(SU heater) manufactured by Econo-Therm.
• Rated for 2750 psi at 950 degrees F.
• 6 burners, with stack.
• Overall height 111', stack section is 33'3" high, furnace section is 10'6" high.  Length is 111' long. 10'6" width with refractory lining.

• Finished sorbitan ester manufacturing capacity is approximately 9,500 metric tons/year.  This ester plant was constructed in the 1980's and shut down in 2009.

• There are no technology licensing issues.

• Esterification process control systems and programming are completely up-to-date and are for sale with the facility.  They are Siemens PCS7 and Fisher-Provox systems.

• Some spare parts for critical equipment are available with the sale.

• Documentation is available and is primarily electronic.

  Click Here to View a Brief Overview on the Sorbitan Plant

• This is the largest unit in a highly integrated facility that sits on 57 acres of land, two-thirds of which are undeveloped.  The facility produces Methyl Amines for use in Higher Amines and Amine Derivatives.

• The Methyl Amines plant has a capacity of 46,000 metric tons per year mixed amines production.

The following products are produced from the reaction of methanol and ammonia:

• Monomethylamine (MMA)

• Dimethylamine (DMA)

• Trimethylamine (TMA)

Ethylbenzene (EB) Plant

The EB-plant converts Ethylene and Benzene into Ethylbenzene through a catalytic reaction (Badger vapor phase technology). The nameplate capacity is 610 kt/yr. EB production.

Styrene Monomer (SM) Plant

The Styrene plant consists of 2 sections; a Cracking section (EB is in two catalyst filled reactors converted with steam in to Styrene Monomer and Hydrogen (Dehydrogenation). The process operated at high temperatures.

The second unit (Finishing section) purifies the SM an recycles unused EB to the feed of the cracking section.

The nameplate capacity of 530 kt/yr. SM production

1.5 M liters capacity, located just outside of a river, the site is on 10 leased acres within a production facility

Major Equipment:

• 10-150,000 liter 304 SS fermenters with 400 HP agit. & 3,000 scfm air input
• 1- 150,000 liter 304 SS batch sterilization tank with 400 HP agitator
• 3-  7,000 liter seed tanks
• 2- Komline Sanderson Rotary Vac. Filters 10 ft diameter and 12 ft long
• 1- Komline Sanderson 125 cu ft agitated & jacketed paddle dryer
• 1- Wyssmont S40 Turbo Tray Dryer
• 28,000 cfm of process air capacity
• 3,500 ton of chiller capacity
• Cooling towers

Site Services:

• Steam, process water, emergency services, and waste water treatment

Process Description

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.

Capacity:  550 short tons per day

Pressure:  Single Medium Pressure 65-70 psig

% of Nitric:  61%

Spare Parts: spare 8000hp motor / Spare compressor rotating assembly /Blade carrier and various compressor spare parts on site.

(3) Plastic Recycle Systems Available

• Materials: PET, PS, LDPE, LLDPE, HDPE, PP, Other Polymers
• Feedstock Forms: Flake, Regrind, Shredded Film, Densified Forms
• Process:
  • Shredding
  • Grinding
  • Washing
  • Drying
  • Extrusion
  • Pelletization
• Power Supply:
  • 380 VAC/3PH/50Hz
  • 480 VAC/3PH/60Hz

(2) 8" lines consisting of:

• 8” Single Screw Extruder
• 10 Inch Slide Plate Screen Changer,
• Two (2) High Force Compactor Densifier Extruders,
• Underwater Pelletizer And
• Recycle, Cleaning, Washing & Drying System

Estimated Rate for the (2) Lines: 1,000 - 5,000 lbs/hour (material dependent)

(1) 10" line consisting of:

• 10” Single Screw Extruder1 2 Inch Slide Plate Screen Changer,
• Two (2) High Force Compactor Densifier Extruder,
• Underwater Pelletizer and
• Recycle, Cleaning, Washing & Drying System

Estimated Rate for the line: 1,000 - 7,000 lbs/hour (material dependent)

(1) 160mm Compounding Line Also Available

• Estimated rate: 1,000-5,000 kgs/hr
• All Necessary Feedstock Forms
• Materials: PA, PS, PE, PP, PET and other materials
• Process: Extrusion - Devolitilizing - Pelletizing
• Available Power Supply: 480 VAC/3PH/60Hz
• 160mm Twin Screw
• High Capacity Devolatilizing Extruder
• Three Zone Vacuum Relief Sections
• 44:1 L/D With 2000 HP AC Drive
• 450MM Dual Bolt Screen Changer
• Underwater Pelletizer

1,240 liter, 304SS, batch Hydrogenation reactor system.

Complete system, includes:

• 1,240 liter High Pressure Jacketed Reactor

• 4 m3/h High Pressure Magnetic Pump

• 0.25-45 m3/h Liquids Injection Pump

• 6.5 m2 Horizontal Heat Exchanger

• 1.3 m2 Fundabac Filter

• 2.5 m2 Horizontal Heat Excahnger

• 250 liter Vertical CS Compressed Air Tank

• 0.3 m3/h Washing Water, Exhaust Air Scrubber

• Siemens S7 Controls

• Instruments

• The hydrogen plant was only installed in 2007 and is based on Foster Wheeler technology. The plant produces 25,000 Nm³/hr of 99.99% pure H2. The Plant was shutdown in 2011.

• The H2 from the PSA plant is partially recycled to mix with the methane feed with the rest sent to the site H2 system at 99.99%.

• The exit temperature from the shift reactor is 412°C. The H2and CO2 passes through a series of shell and tube steam generators, heat exchangers and an air fin fan cooler which drops the gas temperature down to 60°C. Any remaining water is separated in the cold condensate drum which is then heated to feed the deaerator. Heat exchangers are stainless steel.

• Expected documentation was observed during the inspection, such as PFDs, P&IDs, procedures, and equipment files.