Tire oil-gas phase catalytic separation of gasoline and diesel products all meet the national requirements of oil products. New type Thin film evaporator+ fractional distillation refining and regenerating base oil technology of clay, New type Thin film evaporator+ fractional distillation + NMP refining and regenerating base oil technology, Crude oil hydrogenation to produce gasoline and diesel Euro standard, waste engine oil hydrogenation to produce Group II, Group III base oil, Kerosene to produce D Class white spirit solvent oil Etc. the products has reached the international API standards.
The company is committed to Technology First, Quality First principle. Process calculation, equipment calculation and simulation test are carried out for each set of the technology and equipment. The design software used included: Aspen,Pro2,HTRI, HExtran, SW-6, CAD, Plant 3D.
1. Composition of units
The unit is composed of heat exchange part, electric desalting part, initial distillation part, atmospheric distillation part, vacuum distillation part.
Product scheme
Unit product plan is reforming material(naphtha)—Aviation kerosene—diesel—Wax oil hydrocracking/refining program.
The main products are as follows
Naphtha · as a catalytic reforming raw material.
First side oil line of atmospheric column · As a raw material for aviation kerosene hydrogenation.
Second side oil line of atmospheric column · As a raw material for diesel hydrogenation.
Third side oil line of atmospheric column · As a raw material for diesel hydrogenation.
Vacuum column top line oil · As a raw material for diesel hydrogenation.
Vacuum column first line oil · As a raw material for diesel hydrogenation.
Vacuum column second line oil · As wax oil hydrogenation/cracking raw material.
Vacuum column third line oil · As wax oil hydrogenation/cracking raw material
Vacuum column fourth line oil · As wax oil hydrogenation/cracking raw material
Vacuum residual oil · As a raw material of heavy oil catalytic/coking/dissolving/oxidizing asphalt
Second, Raw materials and products
1.Material properties
The raw material is based on the crude oil data sent by the customer and the evaluation made, The basic properties of raw materials are as follows
| Project analysis | Numerical | ASTM |
| API℃ | 35 | CHACT |
| Density, g/cm 3 15℃ | 0.8490 | D-5002 |
| Viscosity, mm 2 /s, 80℉ | 6.864 | D-445 |
| Pour point, ℃ | 27 | D5853 |
| Ash, % | 0.0082 | D-482 |
| acidity, mg KOH/g | ||
| Salt content, PPM NaCl/l | 4.0 | D-3230 |
| sulfur %Mass | 0.574 | D-4294 |
| asphaltene %Mass | 1.75 | D-6560 |
| Hydrogen sulfide, ppm | 7.0 | B. P |
| water %VOL | 0.05 | D-4007 |
| Characterization factor K | ||
| Crude oil category |
Real boiling data
| Test standard | ASTM-D86 |
| Temperature ( ℃ ) | Yield coefficient ( % ) |
| L B P (47) | |
| 50 | 0.1 |
| 75 | 3.8 |
| 100 | 8.5 |
| 125 | 14.5 |
| 150 | 20.0 |
| 175 | 26.0 |
| 200 | 31.5 |
| 225 | 36.5 |
| 250 | 41.0 |
| 275 | 45.0 |
| 300 | 49.0 |
| Total yield | 50 |
| loss | 0.5 |




-
Step 1
Payment and order readiness
Minimum order: 1 Units
Payment terms, specifications, and order details are confirmed before preparation begins.
-
Step 2
Preparation
90 days
-
Step 3
Packaging and dispatch
Ocean freight via Maersk · Approx. shipping fee: $ 0.84 for 1 unit · Transit time: Est. 17-24 days
Final packing, freight, and delivery dates are confirmed before dispatch.
Customer reviews
No reviews yet
Be the first customer to review this product.
Write a review
Request custom sourcing
Can’t find what you’re looking for? Share the requirement and our sourcing team will find the right industrial product.