• Patent Dcs System Waste Black Oil Regenerate Base Oil NMP Solvent Refining Machinery
  • Patent Dcs System Waste Black Oil Regenerate Base Oil NMP Solvent Refining Machinery
  • Patent Dcs System Waste Black Oil Regenerate Base Oil NMP Solvent Refining Machinery
  • Patent Dcs System Waste Black Oil Regenerate Base Oil NMP Solvent Refining Machinery
  • Patent Dcs System Waste Black Oil Regenerate Base Oil NMP Solvent Refining Machinery
  • Patent Dcs System Waste Black Oil Regenerate Base Oil NMP Solvent Refining Machinery

Patent Dcs System Waste Black Oil Regenerate Base Oil NMP Solvent Refining Machinery

Certification: CE, SGS
Application: Lubricant Oil, Transformer Oil, Engine Oil
Voltage: 380V
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Currency: US$
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Patent Dcs System Waste Black Oil Regenerate Base Oil NMP Solvent Refining Machinery pictures & photos
Patent Dcs System Waste Black Oil Regenerate Base Oil NMP Solvent Refining Machinery
US $79,000-1,170,000 / Set
Min. Order: 1 Set
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Basic Info.

Model NO.
WR-02
Folw Rate
200 L/min
Function
Waste Oil Refining
Raw Material
Waste Engine Oil
Final Product
Refined Base Oil
Color
Light Yellow
Transport Package
Plastic Thin Film Packing
Specification
as capacity
Trademark
WR
Origin
China
HS Code
84194090
Production Capacity
200 Sets

Packaging & Delivery

Package Size
10000.00cm * 12000.00cm * 26000.00cm
Package Gross Weight
200000.000kg

Product Description

Rectification process
The equipment is composed of pretreatment part, heat exchange part, atmospheric and vacuum part, gas phase directional cracking part, high vacuum film rectification part and vacuum system.
Refining process
Refining consists of two parts: degumming and liquid catalyst.
6. Product program
      The product scheme of the plant is light component oil diesel - vacuum residue scheme.
The main products are as follows:
       Light component oil ---- fuel oil mix
       Diesel ----- Finished diesel       
Vacuum residue waterproof additive or cracking raw material (cracking as fuel oil)
Third. Raw materials and products
     1.Material properties
       The raw material is waste oil provided by the customer. The basic data is as follows:
Rectification process
The equipment consists of pretreatment part, heat exchange part, atmospheric and vacuum part, high vacuum thin film distillation part and vacuum system.
6. Product project
      The plant product project is SN100 and SN250 the main products of the vacuum residue project are as follows:
      SN100-----light base oil or diesel mix
      SN250-----Medium base oil

      Vacuum residue oil-wasterproof additive or cracking material(cracking for fuel oil)
Third.Raw materials and products
  1. Material properties
       The raw material is waste oil provided by the customer.
The basic data is as follows:
Item Test value Standard
appearance Dark black Visual inspection
smell Gasoline, diesel and burnt smell Smelling method
Density(20ºC)/kg*m-3 880.70 GB/T 1884--92
viscosity(40ºC)/mm2*s-1 67.28 GB/T 265--88
viscosity(100ºC)/mm2*s-1 14.23 GB/T 265--88
Acid value/mg*g-1 1.61 GB/T 7304--83
Residual carbon mass fraction/% 1.76 GB/T 268--87
Ash mass fraction/% 0.78 GB/T 508--85
Pour point/mg*g-1 -24 GB/T 3535--83
Opening flash point/ºC 192 GB/T 3536--88
Moisture mass fraction/% 0.10 GB/T 260--88
Mechanical impurity mass fraction/% 0.23 GB/T 511--88
Sulphur content/mg*kg-1 4040 GB/T 387--90
Nitrogen content/mg*kg-1 1692 GB/T 9170--88
Pentane insoluble mass fraction 14.1 Gb/T8926A
Waste oil composition:
Saturated hydrocarbon/% Mononuclear aromatics/% Bicyclic aromatic hydrocarbon /% Polycyclic aromatic hydrocarbons - polar compounds/%
75-79 13 3.5 6.5

Saturated hydrocarbon classification:
alkane/% cycloalkane
1 cycle/% 2 cycle/% 3 cycle/% 4 cycle/%
27 27 18.5 12 15

The physical composition of waste lubricating oil is complex, and it has the properties of high temperature coking and heat sensitivity.
   2. Product and by-product summary
     The main products of this project are base oil, and the product results are as follows:
Product distribution:
Item Yield
Non-condeansable gas 2%
SN100 25%
SN250 50%
Residual oil 21%(cracking material)
moisture 2%
Residual oil cracking product:
Item Yield
Fuel oil 30%
Base oil material 45%
residue 20%
Non-condensable gas 5%



Forth.production method and production process
 1. Production method
   In this project, the base oil is treated into the base oil by the production method of combining thin film evaporation and distillation tower under the condition of high vacuum.
   
     
     
     
     
     
     
     
     
     
     
     
     
     
     
     
Waste oil composition:
Saturated hydrocarbon/% Mononuclear aromatics/% Bicyclic aromatic hydrocarbon /% Polycyclic aromatic hydrocarbons - polar compounds /%
75-79 13 3.5 6.5

Saturated hydrocarbon classification:
alkane/% cycloakane
1cycle/% 2 cycle/% 3 cycle/% 4 cycle/%
27 27 18.5 12 15

The physical composition of waste lubricating oil is complex, and it has the properties of high temperature coking and heat sensitivity.
   2.Product and by-product summary
     The main products of this project are diesel, and the product results are as follows:
Product distribution:
No. Item Oil yield Usage
1 Diesel 85% * Gas station blending
* Diesel car are used
2 Residual oil 12% * Cracking materials
* Water-proof material
3 Non-condensable oil 3% * It can be used as fuel by gas spray gun.
* Excess waste gas can be stored through a storage system.

12% Overview of residue decracking products:
Item Yield
Cracking oil materials 75%
Residual 20%
Non-condensable gas 5%

3. Product feature
Diesel:(Different regional raw materials, the results will be different)
Item Unit Data
Density(20ºC) Kg/m3 830.6
Flash point ºC 55-60
Acid value mgKOH/ml 0.07
Viscosity mm2/s mm2/s 4.6
Cetane number   >55
Moisture   no
Mechanical impurities   no
sulphur(mass fraction) mg/mg 0.03%
  
Gas phase pyrolysis distillation data:
 
Distillate mass/% Detection of distillation temperature of gas phase cracking oil /ºC
Initial boiling point 84
5 156
10 170
50 289
90 326
95 335
Dry point of distillation 342

Forth.Production method and production process
 1. Production method
   This project adopts the production method of combining thin film evaporation and distillation tower under high vacuum condition to deweight waste oil into gross oil. In the gas phase oriented cracking tower, the gross oil is cracked to produce diesel oil through a series of later refining, and qualified diesel products are produced to meet the use standards.
Patent Dcs System Waste Black Oil Regenerate Base Oil NMP Solvent Refining MachineryPatent Dcs System Waste Black Oil Regenerate Base Oil NMP Solvent Refining MachineryPatent Dcs System Waste Black Oil Regenerate Base Oil NMP Solvent Refining MachineryPatent Dcs System Waste Black Oil Regenerate Base Oil NMP Solvent Refining MachineryPatent Dcs System Waste Black Oil Regenerate Base Oil NMP Solvent Refining MachineryPatent Dcs System Waste Black Oil Regenerate Base Oil NMP Solvent Refining MachineryPatent Dcs System Waste Black Oil Regenerate Base Oil NMP Solvent Refining MachineryPatent Dcs System Waste Black Oil Regenerate Base Oil NMP Solvent Refining MachineryPatent Dcs System Waste Black Oil Regenerate Base Oil NMP Solvent Refining MachineryPatent Dcs System Waste Black Oil Regenerate Base Oil NMP Solvent Refining MachineryPatent Dcs System Waste Black Oil Regenerate Base Oil NMP Solvent Refining MachineryPatent Dcs System Waste Black Oil Regenerate Base Oil NMP Solvent Refining Machinery

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From payment to delivery, we protect your trading.
Patent Dcs System Waste Black Oil Regenerate Base Oil NMP Solvent Refining Machinery pictures & photos
Patent Dcs System Waste Black Oil Regenerate Base Oil NMP Solvent Refining Machinery
US $79,000-1,170,000 / Set
Min. Order: 1 Set
Gold Member Since 2023

Suppliers with verified business licenses

Secured Trading Service
Trading Company
Registered Capital
739010.91 USD