1000 litre per hour Agro Diesel output CCC Cold Convertion reactor

SKU: 364215376135191
€1,800,000.00Price
Color: Green
Machinery description
    	
  • Entry of the mixture in a horizontal reactor with stirrer (0.5 - 4.0 rpm)
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  • Process temperatures <400 ° C
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  • Residence time 5-15 minutes
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  • Without pressure processing
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  • Independently controlled heating zones 2-4
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  • Gas calming zone in the discharge of the reactor for the separation of the produced gas and the solid components (catalyst, coal dust).

  • Process characteristics

    • catalytic oiling 
    • Pressure-free pulping process 
    • Relatively low temperatures (<400 ° C) 
    • Continuous process, not a batch furnace 
    • Material entry up to 1000 kg / h 
    • Production: 400-800 liters per ton of material entry, depending on the type (rubber, plastic) and quality of the input material and the catalyst. 

  • Material storage and dosage

     

    • Dry storage of material to be entered 
    • Feedstock from shredder Material Size 0-20mm 
    • Feedstock Moisture <10%, better <5%. 
    • Hopper with agitator to prevent bridging 
    • Discharge with exposed screw conveyor and gravimetric dosing unit 
    • Transport for the pretreatment means of conveyor belts 
    • Metal cutter 

  • Machinery description

     

    • Entry of the mixture in a horizontal reactor with stirrer (0.5 - 4.0 rpm)
    • Process temperatures <400 ° C
    • Residence time 5-15 minutes
    • Without pressure processing
    • Independently controlled heating zones 2-4
    • Gas calming zone in the discharge of the reactor for the separation of the produced gas and the solid components (catalyst, coal dust).

  • Maintenance

    • Every year overhaul (20 AT). 
    • Cutting blade extruder.
    • Interior reactor (bearing agitator and wear)
    • Cleaning the condenser.
    • Review of all moving parts.

  • Condensation

     

    • Atmospheric condensing of oil vapor.
    • No fractionation.
    • Standing tube condenser
    • water-cooled
    • Mixture of Nafta, kerosene, diesel, light fuel oil
    • Permanent gas are fed to the CHP (methane, butane, propane, heating value of about 3500 MJ / kg)

  • Water separation

     

    • For the separation of oil and water
    • Up to 10% water, depending on the material moisture when introduced into the reactor.
    • Before de-watering, the oil is filtered.
    • Before the product will be used in the CHP unit, a further filtering is necessary to minimize any possible constipation of the injectors.

  • Heat and electricity

     

    • CHP 500 kW (for a the single Reactor)
    • Fuel consumption (without addition of gas) about 60-70 l / h at 1000 kg / h material entry. By using the permanent gas 20-40% less.
    • Fuel for CHP its own oil and gas production.
    • Use of waste heat after return from the reactor for the drying of the feed stock, heating, hot water production, refrigeration

  • Pretreatment

     

    • Entry into a twin-screw extruder for densification of the material and expulsion of air.
    • Compacting of about 0.4-0.6 t / m3 at 1-1.2 t / m3
    • Pre-eating of the material.
    • After the extruder, the compacted material is milled again.

  • Catalyst addition

     

    • Powdered aluminum oxide 99% alpha-alumina
    • gravimetric dosing
    • Entry in 1-5% weight fraction based on material entry
    • Alternative catalysts constantly tested (zeolites, nickel / molybdenum and others)
    • It can be mixed with recycled Kat material and thus supplied to the process