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📍 Operational Castor Oil & Derivatives Plant · North Gujarat · Head Office: Gandhinagar
⚙️ INDUSTRIAL PROCESS ARCHITECTURE · GUJARAT CASTOR BELT

Castor Oil & Derivatives Process Flow

Our integrated plant in North Gujarat is designed for mechanical seed pressing, refining line and hydrogenation and dehydration for derivatives.

Expeller
Seed Pressing
Refining
Refining
Downstream
Hydrogenation & Dehydration
Operational
Active Production
🌿 View Chemical Value Chain: The Castor Chemistry Tree →
Primary Processing · Mechanical Seed Pressing

Castor Seed Pressing & Oil Mill Flow

From certified seed receiving and QC sampling through automated screen cleaning to high-pressure mechanical expelling, yielding unrefined Commercial Castor Oil and expeller castor cake (typically 8–10% residual oil) for organic soil conditioning.

ENGINEERING SCHEMATIC: MECHANICAL SEED PRESSING & OIL RECOVERY
Unit Process Intermediate / Byproduct Commercial Output
RECYCLE SEED INTAKE & QUALITY VERIFICATION Gross/Tare Weighment · Core QC Sampling · Covered Silo Storage MULTI-STAGE SEED CLEANING Vibratory Screeners · Magnetic Separation · Air Aspiration Stones & Foreign Matter Mechanical Separation & Removal Husks & Light Pods Aspirated to Covered Storage THERMAL SEED CONDITIONING Indirect Steam Conditioning for Optimal Pressing Plasticity MECHANICAL SCREW EXPELLING Continuous Solvent-Free Pressing · High-Torque Worm Shafts 100% Pure Mechanical Expression · Zero Chemical Solvents CRUDE CASTOR OIL STREAM Primary Unrefined Extract (Approx. 40% of Seed Mass) DECANTATION & CLARIFICATION Removal of Suspended Meal Foots & Particulates ★ COMMERCIAL OUTPUT COMMERCIAL CASTOR OIL Raw Material for Refining & Industrial Applications Free Fatty Acids < 2.0% · Unrefined Solvent-Free Primary Extract EXPELLER CASTOR CAKE STREAM Expeller Meal Flakes (Approx. 60% of Seed Mass) COOLING & FLAKE SIZING Aeration Cooling to Ambient & Flake Cracking ★ ORGANIC CO-PRODUCT CASTOR CAKE (EXPELLER MEAL) Organic Soil Conditioner & Nutrient Fertilizer Residual Oil: 8–10% · Natural Nitrogen, Phosphorus & Potash Fertilizer

📋 Stage-by-Stage Engineering Breakdown

STAGE 01 Intake & Storage

Seed receiving & QC sampling

Direct farm-gate seed consignments from North Gujarat undergo gross and tare verification and QC sampling. Quality inspectors draw composite core samples for rapid lab analysis of seed moisture, foreign matter, and seed purity.

Castor seeds with green and dried castor capsules
Castor seeds with green and dried castor capsules.
Seed Quality:Selected Hybrid Seed
Seed Moisture:Max. 6.0%
STAGE 02 Zero Waste

Multi-Deck Cleaning & Byproduct Handling

Vibratory screens, rare-earth permanent magnetic drums, and de-stoners remove stems, stones, and iron tramp metal. Light husks and pods are aspirated and conveyed directly to covered storage facilities.

Cleaning Efficiency:> 99.5%
Husks Destination:Covered Storage
STAGE 03 Expelling

Continuous High-Torque Screw Expelling

Cleaned seeds are conditioned and crushed in heavy-duty mechanical screw expellers . Approximately 40% of the seed mass is extracted as unrefined commercial crude castor oil, while the remaining approximately 60% forms expeller cake containing typically 8–10% residual oil.

Mechanical Oil Yield:Approximately 40% of Seed Mass
Cake Residual Oil:Typically 8–10%
STAGE 04 Cake Processing

Expeller Cake Conditioning & Bagging

Hot expeller cake discharged from the press barrels is gently cooled and conditioned into consistent flakes. Containing ~8–10% residual oil and typical 4.0–4.5% organic nitrogen, this cake serves as an organic slow-release fertilizer and soil conditioner.

Cake Nitrogen (N):4.0% – 4.5% (typical)
Residual Oil:8.0% – 10.0% (typical)

Extraction Mass Balance (1,000 kg Cleaned Seed Basis)

Theoretical & Plant Operating Metrics
Stream / Component Type Mass Balance (kg) Composition & Purity Primary Industrial Destination
Cleaned Castor Seed Feed INPUT 1,000 kg Farmgate Seed Feed (Cleaned) Direct Farmer Sourcing from North Gujarat's castor belt (Banaskantha and Vav-Tharad region)
Primary Crude Castor Oil PRODUCT 400 kg (40%) Unrefined, FFA 1.5%–2.0% Sent to Clarification, Decantation & Refining
Castor Cake (Expeller Cake) PRODUCT 590 kg (59%) Residual Oil ~8%–10%, Nitrogen 4.0%–4.5% (typical) Organic Soil Conditioner & Natural N-P-K Manure
Husks & Solid Debris BYPRODUCT 10 kg (1%) Fibrous Biomass & Inert Dust Covered Storage / Biomass Coproduct (Zero Fossil Emission)
Secondary Processing · Adsorption & Bleaching

Castor Oil Chemical Refining Flow

Advanced degumming, foots sedimentation, high-vacuum thermal moisture stripping, Activated Bleaching Earth & Carbon adsorption, and hermetic vertical pressure leaf filtration producing FSG/BSS, PPG, and British Pharmacopoeia (Castor Oil BP) grades.

ENGINEERING SCHEMATIC: THERMAL ADSORPTION REFINING
Unit Process Filter Aid (Hyflow) Bleaching Earth (Tonsil) Certified Product
CRUDE CASTOR OIL INFLOW Primary Feedstock from Oil Mill Crushing Line GRAVIMETRIC DECANTATION Gravimetric Settling of Mucilaginous Gums & Meal Foots Foots Recycled Returned to Expeller Mill (Zero Loss) CLARIFIED OIL BUFFER TANK Pre-Conditioned Buffer Feed for Adsorption Bleaching Filter Aid (Hyflow) Diatomaceous Pre-Coat Matrix Bleaching Earth (Tonsil) Natural Adsorbent Clay Activated Carbon Decolorization & Odor Stripping HIGH-VACUUM BLEACHER Thermal Adsorption Vessel · Closed Vacuum System Thermal Adsorption of Pigments & Oxidation Compounds PRESSURE LEAF FILTRATION (VPLF) Hermetic Closed Vertical Filtration · Stainless Wire Mesh Leaves Spent Earth Cake Automated Dry Discharge SECURITY POLISH FILTRATION High-Retention Guard Filtration Imparting Optical Clarity ★ INDUSTRIAL STANDARD REFINED FSG / BSS First Special Grade (British Standard) Low Color · Low Free Fatty Acids Polyurethanes · Resins · Coatings · Lubricants ★ ULTRA-PALE SPECIALTY PALE PRESSED GRADE (PPG) High Dielectric Stability & Purity Ultra-Low Acidity · High Lubricity Dielectric Transformer Fluids · Specialized Greases ★ COMPENDIAL GRADE CASTOR OIL BP / PH. EUR. Conforms to BP & Ph. Eur. Monograph Tested Purity · Heavy Metals < 10 ppm Pharma Excipients · Formulations · Cosmetics

📋 Refining Operation & Quality Parameters

STAGE 01 Recycle Loop

Decantation & Foots Recycle

Crude oil settles in continuous conical decanters where heavy mucilaginous gums and solid meal fines gravimetrically separate. Clarified supernatant moves forward to bleaching, while settled foots are continuously recycled back to the expellers for closed-loop recycled oil recovery.

Foots Separation:Gravimetric Settling
Oil Loss:0.0% (Recycled)
STAGE 02 Triple Dosing

Controlled Adsorption Chemical Dosing

Clarified oil is treated in an automated slurry dosing reactor with Hyflow filter aid (0.1%–0.3%) for leaf pre-coat, Tonsil / Galleon acid-activated bleaching earth (1.0%–1.5%) for chlorophyll/carotene removal, and Activated Carbon (0.75%–1.0%) for deep polyaromatic odor stripping.

Bleaching Earth:1.0% – 1.5% Tonsil
Activated Carbon:0.75% – 1.0%
STAGE 03 Thermal Vacuum

High-Vacuum Thermal Bleacher

The oil slurry enters an agitated vacuum reactor operated at 95°C to 110°C under vacuum. Controlled agitation strips trace moisture to <0.25% while maximizing adsorptive interaction between clay active sites and coloring bodies.

Operating Temp:95°C – 110°C
Vacuum Level:28" Hg Deep Vacuum
STAGE 04 Hermetic Leaf

Pressure Leaf & Security Polish Filtration

Bleached oil is pumped through vertical pressure leaf filters (VPLF) operating under pressure leaf filtration. Spent bleaching earth forms an impermeable cake and is vibrated dry. The crystal-clear oil passes through 5-micron security guard cartridges to ensure complete optical brilliance.

Filtration Media:VPLF + 5µ Polish
Colour Lovibond:Max 20Y + 2R (FSG)

Refining Mass Balance (1,000 kg Crude Oil Basis)

Adsorption Reagent Ratios & Finished Yields
Process Stream Type Mass (kg) / Dosage Analytical Specification Industrial Utilization
Crude Castor Oil Feedstock FEED 1,000 kg FFA 1.5%–2.0%, Moisture <0.50% From Oil Mill Continuous Expelling
Tonsil Bleaching Earth & Carbon REAGENT 17.5 kg – 25.0 kg High-surface active montmorillonite + Carbon Adsorption of carotenoids & phosphatides
Refined Castor Oil (FSG / BSS) PRODUCT 960 kg (96%) FFA <1.0%, Lovibond 20Y+2R, IV 82–90 High-Grade Resins, Lubricants & Derivatives
Spent Bleaching Earth Cake BYPRODUCT 22 kg (2.2%) Dry spent clay with adsorbed pigments Safe industrial solid recovery / cement blending
Foots Recycle Stream RECYCLE 25 kg (Circular) Suspended meal fines & heavy triglycerides Recycled into Expellers (100% Oil Recovery)
Tertiary Processing · Catalytic Synthesis

Castor Oil Derivatives & Co-Products Manufacturing

Controlled catalytic hydrogenation, alkaline hydrolysis, sulphuric acidulation, and spent lye vacuum distillation synthesizing Hydrogenated Castor Oil (HCO), Ricinoleic Acid, 12-Hydroxystearic Acid (12-HSA), and Refined Glycerin.

ENGINEERING SCHEMATIC: DERIVATIVES SYNTHESIS & CO-PRODUCT RECOVERY
Catalytic Unit Hydrogen (H₂) / Acid Alkaline Caustic Commercial Output
REFINED CASTOR OIL FEEDSTOCK Refined Bleached Castor Oil for Value-Added Derivatives + Hydrogen (H₂) Gas Catalytic Hydrogenation Reagent CATALYTIC HYDROGENATION Selective Double-Bond Saturation · Pressure Autoclave System ★ COMMERCIAL PRODUCT & INTERMEDIATE HYDROGENATED CASTOR OIL (HCO / WAX) High-Melting Castor Wax (Flakes & Powder) for Greases & Polymers + Caustic Soda Solution Continuous Alkaline Hydrolysis Agent CONTINUOUS ALKALINE HYDROLYSIS Cleavage into Soap Phase & Free Glycerol + Acid & Water Wash Acidulation Phase Splitting Agent ACIDULATION & PHASE SPLITTING Separation into Organic Fatty Acid Layer & Aqueous Spent Lye WATER WASHING & DRYING Multi-Stage Washing to Neutral pH & Moisture Removal CHILLING, FLAKING & PULVERIZING Rotary Drum Solidification & Controlled Particle Sizing ★ DERIVATIVE OUTPUT 12-HYDROXYSTEARIC ACID (12-HSA) Free-Flowing Flakes & Micronized Powder Primary Thickener for Automotive & Industrial Lithium Greases Specialty Polymers · Resins · Cosmetic Wax Formulations SPENT LYE CO-PRODUCT RECOVERY STREAM Aqueous Solution of Glycerin & Salt Co-Products Evaporation & Desalting Concentration & Vacuum Distillation ★ CO-PRODUCT OUTPUT REFINED GLYCERIN Refined 99.5% Glycerol Grade Technical & Formulation Quality Personal Care · Resins · Polyols Direct Fat Splitting Hydrolysis & Vacuum Distillation ★ SPECIALTY ACID RICINOLEIC ACID Pure Hydroxy Fatty Acid Polyamide-11 Monomer Feedstock Bio-Surfactants · Esters · Fluids

📋 Reaction Stoichiometry & Operating Conditions

STAGE 01 Hydrogenation

Catalytic Hydrogenation to HCO Wax

1,000 kg of Refined FSG Castor Oil is reacted with technical hydrogen gas in the presence of supported Nickel catalyst at 140°C–180°C. Double bonds are selectively saturated, yielding hard white HCO wax.

H₂ Gas Consumption:92 Nm³ / MT Oil
Iodine Value Drop:82–90 → < 4.0 Units
Melting Point:84.0°C – 88.0°C
STAGE 02 Hydrolysis

Alkaline Hydrolysis

1,000 kg molten HCO is continuously fed into the hydrolysis reactor and reacted with 150 kg of 30% caustic soda (NaOH) solution. The triglyceride ester linkages are cleaved, producing sodium 12-hydroxystearate soap and releasing free glycerin in an aqueous medium.

NaOH (30%) Dosing:150 kg / MT HCO
Reaction Type:Triglyceride Hydrolysis
STAGE 03 Acidulation

Acidulation & 12-HSA Flaking

The soap is acidulated with 190 kg of 60% sulphuric acid (H₂SO₄) and washed with 400 kg demineralized water. The mixture separates cleanly into an organic fatty acid layer (940 kg 12-HSA chilled and flaked on rotary drums) and an aqueous spent lye layer containing glycerin and sodium sulphate.

12-HSA Yield:940 kg (Losses: 19 kg)
Acid Value:Min. 175 mg KOH/g
Melting Point:Min. 74.0°C
STAGE 04 Co-Products

Spent Lye Evaporation & Salt Recovery

The spent lye aqueous phase (92 kg Glycerin + 250 kg Na₂SO₄ + 850 kg H₂O) is treated and concentrated in multi-effect evaporators. Centrifugal crystallization separates 250 kg of Sodium Sulphate Anhydrous (under development), while the concentrated glycerin is distilled to produce 69 kg of Refined Glycerin (under development).

Refined Glycerin:69 kg (99.5% Min)
Sodium Sulphate:250 kg (99.40% Min)

Derivatives Stoichiometric Mass Balance (1,000 kg FSG Basis)

Full Chemical Input / Output Material Accounting
Material Component Stream Type Quantity / Consumption Stoichiometric Specification Industrial Output / Application
Refined FSG Castor Oil Feed RAW FEED 1,000 kg Iodine Value: 82 – 90 units Feedstock for Catalytic Hydrogenation
Technical Hydrogen Gas (H₂) REAGENT 92 Nm³ (approx. 8.2 kg) Purity > 99.9% H₂ gas Selective double-bond saturation
Supported Nickel Catalyst CATALYST 1.2 kg / MT Active reduced Nickel Heterogeneous hydrogenation catalyst
Hydrogenated Castor Oil (HCO) INTERMEDIATE 1,000 kg (100%) Iodine Value < 4.0, MP 84°C–88°C Commercial Castor Wax / Feed for Hydrolysis
Caustic Soda (NaOH 30% Sol.) REAGENT 150 kg 30% Aqueous Sodium Hydroxide Alkaline ester bond hydrolysis
Sulphuric Acid (H₂SO₄ 60%) REAGENT 190 kg 60% Technical Sulphuric Acid Acidulation of sodium ricinoleate soap
Demineralized Wash Water UTILITY 400 kg Conductivity < 10 µS/cm Removal of trace salt and free acid
12-Hydroxystearic Acid (12-HSA) PRIMARY PRODUCT 940 kg (94.0%) Melting Point Min. 74°C, Acid > 175 Multipurpose Lithium Complex Greases & Polymers
Handling / Moisture Losses PROCESS LOSS 19 kg (1.9%) Evaporative moisture & filter wash Process evaporation and scrubber venting
Refined Glycerin (USP / Tech) CO-PRODUCT 69 kg (6.9%) Purity Min. 99.5%, Colour APHA < 20 Pharmaceutical, Alkyd Resins & Cosmetics
Sodium Sulphate Anhydrous CO-PRODUCT 250 kg (25.0%) Purity Min. 99.40% Na₂SO₄, White Crystal Detergents, Glass & Textile Dyeing
Interactive Oleochemical Pathways

Explore the Castor Chemistry Tree

View our molecular reaction taxonomy mapping 4 stages of value addition from crude castor oil and expeller cake to ricinoleic acid, sebacic acid, bio-polyols, and specialty metallic stearates.

Launch Interactive Chemistry Tree →