Нефтяной кокс

Core Equipment

Delayed Coking Heating FurnaceRapidly heats to 485–510°C to ensure the oil reaches reaction temperature in a short time. Coke DrumsLarge vertical pressure vessels; two drums operate alternately for coking and decoking, serving as the key equipment for forming the sponge coke structure. Fractionating TowerSeparates coking oil and gas, stabilizes reaction conditions, and ensures uniform coke quality. High-Pressure Hydraulic Decoking SystemIncludes high-pressure water pumps, coke cutters and drilling machines, using 20–30 MPa high-pressure water for cutting and discharging coke. Crushing & Screening EquipmentJaw crushers and vibrating screens to produce export-grade particle sizes (0–10mm, 10–30mm, etc.). Calcining KilnsRotary kilns or vertical retort furnaces for producing calcined sponge coke.

Core Technologies

Delayed Coking TechnologyControls temperature, pressure and recycle ratio to ensure stable production of sponge coke. Sponge Coke Structure Control TechnologyRegulates pore structure by adjusting feedstock properties, reaction temperature and residence time. Low Sulfur & Low Metal Control TechnologyAdapted to high-end metallurgical and aluminum electrolysis markets in Russia and the Middle East. High-Pressure Water Non-Damaging Decoking TechnologyEnsures intact coke lump structure and reduces fine coke powder. Continuous Crushing & Screening TechnologyProduces uniform particle size to meet export and marine transportation standards. Calcining Upgrading TechnologyReduces volatile matter, increases fixed carbon content and enhances export added value.

Product Introduction

Product Introduction

Sponge coke is the type of petroleum coke with the largest output, widest application and highest export volume. It gets its name from its loose, porous structure similar to sponge.Produced from vacuum residue via the delayed coking process, it is mainly used in prebaked anodes, graphite products, carburizers, silicon carbide, electrode pastes, metallurgical fuels and other fields.

Types and Characteristics of Equipment

Type

Fuel Grade Petroleum Coke Calcined Petroleum Coke Green Petroleum Coke Low Sulfur Petroleum Coke High Sulfur Petroleum Coke

Features

Appearance: Black porous lumps with loose structure and moderate hardnessHigh fixed carbon: 85%–92% (over 98.5% after calcination)Adjustable sulfur content: low sulfur <1.5%, medium sulfur 1.5%–3%, high sulfur >3%Low impurity content: low ash, vanadium and nickel contents, suitable for metallurgy and aluminum electrolysisGood reaction activity: easy graphitization and sintering, ideal for anode materialsGood processability: easy to crush and screen, with uniform and stable particle sizeCost-effective: the most common basic carbon raw material in the global carbon industry

Basic Principles and System Composition

Basic Working Principle

Using vacuum residue as raw material, the process is carried out in a delayed coking unit: High-temperature cracking: Macromolecular hydrocarbons are broken down into small molecular oil and gas.Condensation polymerization: Aromatic hydrocarbons are gradually dehydrogenated and condensed to form solid carbonaceous material.Delayed reaction: The feedstock is rapidly heated in a furnace, and coking is "delayed" in the coke drum to prevent coking in the furnace tubes. This finally forms petroleum coke with a spongy porous structure, known as sponge coke.

Overall System Composition

Raw Material System

Vacuum residue, heat exchange heating, dehydration and impurity removal

Heating Reaction System

Heating furnace, coke drum, fractionating tower

Oil-Gas Separation System

Separation and recovery of dry gas, gasoline, diesel oil and wax oil

Decoking System

Steam purging, water cooling, high-pressure hydraulic decoking

Post-treatment System

Crushing, sieving, conveying, storage and packaging

Utilities

High-pressure water system, steam system, nitrogen system, wastewater treatment

Basic Principles and System Composition

Raw Material PreheatingVacuum residue enters the unit and is heated through heat exchange with hot oil from the fractionating tower. Heating Furnace HeatingThe residue is fed into the heating furnace and rapidly heated to 485–510°C. Coking Reaction in Coke DrumsHigh-temperature oil enters the coke drums, where cracking and condensation reactions occur for approximately 24–36 hours, gradually forming sponge coke. Oil-Gas SeparationOverhead oil and gas enter the fractionating tower and are separated into dry gas, gasoline, diesel oil, and wax oil. Drum Switching, Purging and CoolingWhen one drum is full of coke, production switches to the other drum.Steam purging → water cooling to a safe temperature. High-Pressure Hydraulic DecokingTop and bottom heads are opened.High-pressure water first drills a central hole → then cuts the coke.Sponge coke is discharged from the bottom of the drum. Post-Treatment (Export Grade)Coarse crushing → fine crushing → screening → classification → conveying → silo storage.For calcined coke: fed into a rotary kiln for calcination at 1200–1350°C. Packaging and ShipmentTon bag packaging / bulk shipment.

Многоязычная поддержка

Многоязычная профессиональная поддержка в сфере внешней торговли 

Комплексные логистические услуги

Полный спектр логистических услуг, включая таможенное оформление и организацию доставки.

Полный комплект экспортной документации

Полный комплект экспортной документации: протоколы инспекции и т.д.

Превосходная своевременная доставка

Гарантированная своевременная доставка благодаря эффективному управлению производством и логистикой.

Послепродажное обслуживание и техническая поддержка

Своевременное послепродажное и техническое обслуживание зарубежных клиентов.