Base Oil Solvent Extraction Plant

Base Oil Solvent Extraction Plant
Base Oil Solvent Extraction Plant
Base Oil Solvent Extraction Plant
Base Oil Solvent Extraction Plant
Base Oil Solvent Extraction Plant

Base oil extraction equipment primarily utilizes the difference in solubility of different substances in specific solvents to achieve the separation and extraction of base oil. Its working principle is as follows:

 

1. Solvent Selection

Using organic solvents with different solubility characteristics of ideal and non ideal components to purify base oil for better sulfur content, antioxidant

 

2. Mixing and Dissolution

Thoroughly mix the base oil with the solvent. Under certain temperature and pressure conditions,the non-ideal components in the base oil dissolve in the solvent and then.

 

3. Separation Stage

After synchronous high-speed rotation of the mixed liquid and the drum, centrifugal force is generated.The high-density liquid(solvent)approaches the drum wall,while the low-density liquid(base oil) gradually moves towards the center. Finally, the two liquids come out through their  respective channels,achieving liquid separation.

 

4. Solvent Recovery

Treat the solvent phase containing the base oil by changing the temperature and pressure to evaporate or volatilize the solvent, thereby separating the base oil. The recovered solvent can be recycled to reduce costs.

Product Video

Product Presentation

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Product Video

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Product Presentation

Advanced Base Oil Refining Equipment

Base Oil Solvent Extraction Plant

The Base Oil Solvent Extraction Plant is designed for regenerated and refined base oil upgrading through NMP solvent extraction and vacuum solvent recovery. The system removes asphaltenes, gums, sulfur-, nitrogen- and oxidation-related unstable compounds while supporting continuous low-energy and environmentally compliant operation.

Base Oil Refining
NMP Solvent Extraction
Vacuum Recovery
Continuous Operation
Base oil solvent extraction plant overview

Plant Product Highlights

  • Efficient removal of asphaltenes, gums and unstable compounds
  • Integrated extraction and solvent recovery modules
  • Low operating cost with high solvent recovery rate
  • Suitable for regenerated base oil upgrading and pretreatment
0
Hours Continuous Operation
0
Typical Solvent Recovery Rate
0
Typical Extraction Temperature
0
Core Process Modules

Product Highlights

This page presents the Base Oil Solvent Extraction Plant as an industrial equipment product, focusing on solvent refining technology, impurity removal efficiency, solvent recovery performance and application value for base oil upgrading.

Centrifugal extraction technology

Centrifugal Extraction Technology

The system uses NMP centrifugal extraction to improve mass transfer efficiency in a compact structure, helping remove undesirable components more effectively than traditional tower-type processes.

Vacuum solvent recovery system

High Solvent Recovery Efficiency

Vacuum heating and distillation allow efficient solvent separation and recirculation, reducing solvent loss and lowering long-term operating cost.

Refined oil quality improvement

Cleaner & More Stable Base Oil

The process helps improve oil color, oxidation stability, residual carbon level and long-term storage behavior without generating acid sludge or large volumes of solid waste.

Core Process Technology Modules

From extraction to final dried refined oil output, the plant adopts a continuous modular route for impurity removal, solvent recovery and quality upgrading.

1

Extraction

NMP selectively removes non-ideal components from base oil.

2

Recovery

Vacuum separation recovers solvent from raffinate and extract.

3

Stripping

Superheated steam removes residual trace solvent.

4

Drying

Final moisture removal improves product stability.

5

Storage

Finished refined base oil is sent to tank storage for use.

Detailed Process Introduction

A more detailed display of the main process modules, matching product-level technical presentation needs for industrial buyers and investment decision makers.

Solvent extraction unit
01 / Solvent Extraction Unit

The Core Separation Stage of Base Oil Solvent Refining

The preheated base oil and NMP solvent enter the centrifugal extractor under controlled temperature conditions of about 60°C. Through counter-current contact and density difference, undesirable components such as asphaltenes, gums and heteroatomic compounds are transferred into the solvent-rich phase.

  • Selective Separation: removes non-ideal compounds more effectively.
  • Compact Structure: much smaller footprint than tower-type extraction.
  • Efficient Mass Transfer: improves extraction performance.
  • Automated Operation: supports continuous process control.
Solvent recovery unit
02 / Solvent Recovery Unit

Recovering NMP for Cost Control and Process Continuity

After extraction, both the refined oil stream and the extract stream contain solvent. The recovery system uses heating and vacuum distillation to separate volatilized NMP from the oil phases. The condensed solvent is returned to storage for recirculation, helping lower solvent consumption and operating cost.

  • High Recovery Efficiency: reduces solvent loss.
  • Vacuum Operation: supports effective separation at controlled conditions.
  • Closed-Loop Recycling: improves economic performance.
  • Low Energy Design: supports industrial cost control.
Post-extraction base oil recovery
03 / Stripping & Final Solvent Removal

Deep Removal of Residual Solvent for Better Base Oil Quality

Even after vacuum recovery, trace NMP remains dissolved in the refined oil. The stripping stage uses superheated steam and counter-current mass transfer to remove most residual solvent, further optimizing refined base oil purity and market value.

  • Lower Residual Solvent: improves final product acceptability.
  • Better Product Quality: supports premium refined oil targets.
  • Continuous Operation: suitable for industrial throughput.
  • Integrated Utility Design: supports stable plant operation.
Refined base oil drying
04 / Refined Base Oil Drying

Final Moisture Removal Before Product Storage

The refined base oil enters the drying column after heating, where trace moisture is vaporized and removed. This final step improves product stability, handling quality and storage readiness before the oil is pumped to the tank farm.

  • Reduced Moisture Content: supports better storage stability.
  • Improved Appearance: helps achieve cleaner finished oil.
  • Safer Downstream Use: lowers water-related quality risks.
  • Stable Final Output: prepares oil for commercial application.

Refined Base Oil Quality Improvement

A business-grade data presentation for product upgrading effect, impurity removal, solvent recovery performance and refined oil marketability.

≈70
CNY/Ton Operating Cost Benchmark
≥99.9%
Solvent Recovery Potential
~60°C
Typical Extraction Temperature
24h
PLC Controlled Operation
Impurity Removal Structure
 
Indicative distribution of removed non-ideal components and retained refined oil fraction.
Solvent Recovery Efficiency Curve
 
Typical cumulative solvent recovery trend across staged treatment.
Quality Improvement by Process Stage
 
Indicative reduction of color index and residual solvent through extraction, recovery, stripping and drying.
Refined Base Oil Performance Radar
 
A visual overview of refined base oil performance across clarity, stability and usability indicators.

Model Selection Guide

Choose the right Base Oil Solvent Extraction Plant based on your feedstock type, target product grade, utility conditions, investment budget and long-term return strategy.

Model Type Capacity Recommended Application Investment Level Key Advantage
Pilot Unit 5–10 L / Batch Lab verification, solvent ratio trial and process validation Low Suitable for technology testing before commercial scale deployment
Compact Plant 5 – 15 T / Day Small recyclers, lubricant workshops and entry-level upgrading projects Low–Moderate Compact footprint and lower startup threshold
Large Scale Plant 30 – 60 T / Day Industrial re-refining bases and large regional regeneration projects High Higher throughput usually brings stronger long-term profitability and market competitiveness

Pilot Unit

Testing
Capacity5–10 L / Batch
ApplicationLab testing & technical validation
InvestmentLow
AdvantageFeasibility verification before scaling up

Compact Plant

Entry
Capacity5 – 15 T / Day
ApplicationSmall upgrading projects
InvestmentLow–Moderate
AdvantageCompact layout and lower startup threshold

Large Scale Plant

Industrial
Capacity30 – 60 T / Day
ApplicationLarge industrial re-refining deployment
InvestmentHigh
AdvantageHigher throughput generally supports higher total profit
Recommended Choice: The 20–30 T / Day Standard Plant is suitable for most commercial customers because it offers a practical balance between investment level, product quality improvement, continuous operation and solvent recovery performance.

Balanced Investment

The 20–30 T / Day configuration fits customers looking for controllable capital input and stable upgrading performance.

Stable Product Upgrading

This model range is widely suitable for continuous refined base oil production with improved clarity and oxidation stability.

Scalable Profit Potential

For customers with stable feedstock and stronger market demand, larger-capacity plants can offer stronger overall profitability.

Technical Specifications

Typical reference data and process indicators for the Base Oil Solvent Extraction Plant and refined oil quality improvement.

Parameter Typical Value / Range Performance Impact
Extraction Solvent N-Methyl-2-pyrrolidone (NMP) Selective removal of non-ideal oil components
Extraction Temperature About 60°C Supports efficient mass transfer and stable separation
Solvent Recovery Rate ≥ 99.9% Reduces solvent loss and operating cost
Operation Mode 24h PLC Controlled Supports continuous industrial production
Equipment Footprint Compact centrifugal layout Smaller than traditional tower extraction systems
Pollution Profile No acid sludge / low solid waste Improves environmental compliance
Target Improvement Color, residual carbon, odor, oxidation stability Supports higher-grade refined base oil output
Utility Integration Vacuum, heating, stripping and drying Enables closed-loop continuous refining operation

Extraction Solvent

Value N-Methyl-2-pyrrolidone (NMP)
Selective removal of non-ideal oil components.

Extraction Temperature

Value About 60°C
Supports efficient mass transfer and stable separation.

Solvent Recovery Rate

Value ≥ 99.9%
Reduces solvent loss and operating cost.

Operation Mode

Value 24h PLC Controlled
Supports continuous industrial production.

Equipment Footprint

Value Compact centrifugal layout
Smaller than traditional tower extraction systems.

Pollution Profile

Value No acid sludge / low solid waste
Improves environmental compliance.

Target Improvement

Value Color, residual carbon, odor, oxidation stability
Supports higher-grade refined base oil output.

Utility Integration

Value Vacuum, heating, stripping and drying
Enables closed-loop continuous refining operation.

Third-Party Verification

Refined base oil upgrading effect can be supported by laboratory testing to strengthen market trust and technical credibility.

Third-party oil test report

Independently Verified Quality Improvement

The refined oil produced by the plant can be tested by recognized laboratories to verify appearance improvement, solvent removal effect, oxidation stability and residual impurity reduction.

  • Verified color improvement
  • Confirmed lower residual impurities
  • Supports stability evaluation
  • Strengthens commercial sales credibility
Download Test Report

Applications & Feedstocks

The plant is designed for re-refining companies, lubricant recovery facilities and industrial oil regeneration projects handling various base-oil-related streams.

A

Regenerated Base Oil

Upgrading recycled base oil quality for higher-value applications.

B

Lubricant Pretreatment

Removes gums and oxidation residues before blending or finishing.

C

Re-Refining Projects

Suitable for industrial waste oil regeneration and base oil recovery plants.

D

Energy Recycling

Supports closed-loop reuse and resource recovery projects.

E

Waste Lubricating Oil

Used lubricating oils requiring impurity removal and upgrading.

F

Vacuum Distilled Base Oil

Further upgrading after front-end distillation process.

G

Industrial Oil Streams

Selected industrial oil fractions with upgrading value.

H

Refined Oil Improvement

Processes targeting better color, stability and market grade.

Project Cases

Representative project references showing actual upgrading effect, operating advantages and business value.

Base oil project case

Vietnam Re-Refined Base Oil Project

Capacity: 30 T / Day

Feedstock: Re-Refined Base Oil Stream

Process: NMP Solvent Extraction

Result: Upgraded Product Quality

After replacing traditional acid-clay treatment, the project improved product quality, reduced refining cost and achieved environmentally compliant continuous operation.

Reference Benefit: Lower Operating Cost & Better Product Grade
Before extraction oil

Before Extraction Condition

Status: Untreated Oil Sample

Color: Dark Brown

Impurity: High

Stability: Poor

Untreated oil typically shows darker color, higher residual carbon and weaker oxidation stability, limiting its direct market value.

Upgrade Value: Strong Quality Improvement Potential
After extraction oil

After Extraction Result

Status: Refined Oil Sample

Color: Pale Yellow

Residual Carbon: Lower

Stability: Improved

After extraction, the oil becomes cleaner, lighter in appearance and more suitable for higher-grade regenerated base oil applications.

Commercial Value: Better Market Acceptance & Higher Selling Potential
Swipe naturally by scrolling down — each project case is displayed in a mobile-friendly stacked format for easier reading.

Frequently Asked Questions

Common questions from customers evaluating this Base Oil Solvent Extraction Plant as a product purchase.

The plant is designed to upgrade refined or regenerated base oil by removing asphaltenes, gums, sulfur-containing compounds and other unstable impurities through NMP solvent extraction and solvent recovery.

The system uses N-Methyl-2-pyrrolidone (NMP), a selective solvent suitable for separating undesirable components from base oil streams.

Yes. Standard configurations are designed for PLC-controlled 24-hour continuous operation under industrial production conditions.

The process can improve oil color, reduce residual carbon and impurities, lower odor and enhance oxidation stability, depending on feedstock condition and process configuration.

Compared with traditional acid-clay refining, this process avoids acid sludge generation, reduces solid waste and supports cleaner industrial operation.

Need a Base Oil Solvent Extraction Plant?

Send us your feedstock type, daily capacity target, current oil condition and expected refined product grade. We will recommend a suitable plant configuration and equipment layout for your project.

Get My Plant Proposal

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