Cracked C4 Raffinate Oil

    • Product Name: Cracked C4 Raffinate Oil
    • Chemical Name (IUPAC): Cracked C4 Raffinate Oil does not have a single IUPAC chemical name because it is a complex mixture of hydrocarbons, not a pure compound.
    • CAS No.: 68512-11-2
    • Chemical Formula: C5H10
    • Form/Physical State: Liquid
    • Factroy Site: Jiangbei New District,Nanjing City
    • Price Inquiry: sales4@ascent-chem.com
    • Manufacturer: Sinopec Yangzi Petrochemical
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    Specifications

    HS Code

    893880

    Product Name Cracked C4 Raffinate Oil
    Appearance Colorless to pale yellow liquid
    Odor Hydrocarbon-like
    Boiling Point Range Celsius 10-30
    Density Kg Per M3 575-630
    Flash Point Celsius -20
    Main Components C4 hydrocarbons (butenes, butanes, butadiene traces)
    Solubility In Water Insoluble
    Vapor Pressure Kpa 200-260 at 20°C
    Autoignition Temperature Celsius 280
    Refractive Index N20d 1.37-1.39

    As an accredited Cracked C4 Raffinate Oil factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Cracked C4 Raffinate Oil is packaged in 200-liter steel drums, securely sealed and clearly labeled for industrial use and safety.
    Container Loading (20′ FCL) Container Loading (20′ FCL) for Cracked C4 Raffinate Oil: Typically loaded in ISO tanks or drums, max capacity around 21-22 metric tons.
    Shipping Cracked C4 Raffinate Oil should be shipped in tightly sealed, corrosion-resistant containers, typically by tank truck, railcar, or approved bulk vessels. Ensure compliance with relevant hazardous material transport regulations. Keep away from sources of ignition and store in a cool, well-ventilated area. Proper labeling and documentation are required during transit.
    Storage Cracked C4 Raffinate Oil should be stored in tightly closed, properly labeled metal tanks or drums in a cool, well-ventilated, and dry area, away from sources of ignition and incompatible materials such as strong oxidizers. Storage areas must have appropriate spill containment measures and be equipped with fire suppression systems. Personnel should follow all safety and environmental regulations during storage and handling.
    Shelf Life Cracked C4 Raffinate Oil typically has a shelf life of 6-12 months when stored in cool, dry, and sealed conditions.
    Application of Cracked C4 Raffinate Oil

    Applications of Cracked C4 Raffinate Oil in Industrial Manufacturing

    Cracked C4 raffinate oil, produced and refined in our own integrated facilities, serves as a critical raw material across multiple petrochemical value chains. Its consistent composition, controlled olefin content, and low aromatic impurities enable a range of industry-specific applications, each governed by distinct process requirements and regulatory standards. Below we outline the most significant downstream manufacturing scenarios based on tangible market demand and proven industrial practice.

    1. Synthetic Rubber Feedstock for Butadiene Extraction

    Major elastomer producers use our raffinate oil as a primary feed in extractive distillation units targeting butadiene separation. The precise hydrocarbon profile supports high yield extraction economics, with strict adherence to emissions and operator safety protocols during fractionation. This addresses demand for synthetic rubbers in tire, hose, and sealing applications, where product consistency originates at the feedstock selection stage.

    Industry compliance standards

    • ISO 9001:2015 Quality Management Systems
    • REACH (EC) No 1907/2006 Registration, Evaluation, Authorisation and Restriction of Chemicals (Europe)
    • U.S. EPA Clean Air Act Section 112(g) for hazardous air pollutants in butadiene units
    • SHE (Safety, Health and Environment) protocols for petrochemical handling

    Typical usage ratio

    • Batch formulation: 82-97% volumetric input relative to the total feedstock charge, adjusted based on the target butadiene recovery and residue composition analysis.

    Downstream process integration

    • Direct charge into extractive distillation or solvent extraction columns immediately after pre-treatment to remove C5/C6 impurities.

    Final product types

    • High-purity butadiene monomer
    • Styrene-butadiene rubber (SBR)
    • Polybutadiene rubber (PBR)
    • Acrylonitrile butadiene styrene (ABS) precursors

    2. Maleic Anhydride Production via C4 Oxidation

    Industrial manufacturers operating fixed-bed oxidation reactors use the raffinate oil as a controlled C4 hydrocarbon source. Its defined isobutene/1-butene ratio enables reliable reactor performance and selectivity, substantially reducing undesired byproducts. Strict process monitoring ensures compliance with environmental and cross-contamination controls during catalytic conversion of inputs sourced exclusively from certified producers.

    Industry compliance standards

    • ISO 14001:2015 Environmental Management in chemical oxidation processes
    • RoHS (Restriction of Hazardous Substances) when used in resin production for downstream electronics
    • Technical Regulation of the Eurasian Economic Union TR CU 041/2017 “On safety of chemical products” (for Eurasian market)
    • OECD Guidelines on the Testing of Chemicals for catalyst wear and emissions

    Typical usage ratio

    • Feed gas blend: 40-70% by volume of processed stream, varied according to catalyst age and conversion efficiency. Detailed flow adjustments respond to byproduct composition measured onsite.

    Downstream process integration

    • Introduced at the feedstock blend stage directly before vaporization and oxygen enrichment, then routed into tubular or fluid-bed oxidizers equipped for C4 chemistry.

    Final product types

    • Refined maleic anhydride
    • Unsaturated polyester resins (UPR)
    • Alkyd resins
    • Plasticizers for PVC and other polymers

    3. Intermediate for C4 Olefin Alkylation in Gasoline Refining

    Refinery alkylation units blend the raffinate oil with isobutane and acid catalysts to manufacture high-octane alkylate. The material’s controlled impurity profile and optimized butene content directly influence yields and regulatory compliance related to finished fuel quality. Regular testing ensures that each delivered lot meets batch-to-batch reproducibility and supports seamless feed integration into alkylation reactors with tight sulfur and diolefin content limitations.

    Industry compliance standards

    • EN 228:2012 Automotive Fuels – Unleaded Petrol (Europe)
    • ASTM D4814 Standard Specification for Automotive Spark-Ignition Engine Fuel (USA)
    • API Standard 941 for Process Equipment
    • Clean Fuels Regulations (cf. EPA Tier 3 Gasoline Sulfur Rule)

    Typical usage ratio

    • 20-45% of total alkylation unit hydrocarbon input, adjusted to seasonal volatility and market octane demand specifications. Formulation changes respond to isomer ratio analysis and sulfur tests per shipment.

    Downstream process integration

    • Pumped into feedstock blend tanks upstream of acid-catalyzed alkylation reactors, with inline quality monitoring before isobutane co-processing.

    Final product types

    • Pilot alkylate
    • Premium-grade gasoline blending components
    • Low-sulfur high-octane fuels
    • Specialty aviation gasoline stocks

    4. Linear Alpha Olefin Precursor for Plasticizer Synthesis

    Downstream chemical manufacturers transform the raffinate oil through catalytic dehydrogenation and oligomerization steps to generate linear alpha olefins, essential intermediates in plasticizer and lubricant base oil production. Tight control over feedstock purity and composition ensures batch reproducibility and process uptime, crucial for manufacturers operating under third-party audits and customer-driven specification controls.

    Industry compliance standards

    • OECD Good Manufacturing Practice (GMP) for chemical intermediates (applicable for lubricants/plasticizers used in food-contact materials)
    • EU Regulation (EC) No 1935/2004 for food-contact substances (when relevant)
    • ISO 21469:2006 for lubricant base oils safety
    • National chemical inventory registrations (e.g., TSCA, IECSC, PICCS)

    Typical usage ratio

    • 50-100% of the total olefin precursor batch, depending on targeted chain lengths in linear alpha olefin product slate and customer application requirements. Operators adjust input ratios according to catalyst selectivity and in-process GC-MS analysis.

    Downstream process integration

    • Dispatched to dehydrogenation reactors for conversion to mixed butenes, followed by separation and oligomerization reactors configured for alpha olefin formation.

    Final product types

    • Dioctyl phthalate (DOP) and other phthalate/non-phthalate plasticizers
    • Lubricant base stocks
    • Alpha olefin sulfonates
    • Synthetic fatty alcohols for detergents

    5. Fuel Component for Industrial Heating Oil and Marine Bunkers

    Energy sector operators utilize this refinery stream as a blending component in formulating industrial heating oils and select marine fuel types. The high calorific value, controlled sulfur residue, and streamlined compatibility with typical refinery blending infrastructure allow for predictable combustion characteristics. Our product enters these systems only after verification of its molar mass distribution and contaminants, in accordance with sector-specific global standards and port authority regulations.

    Industry compliance standards

    • ISO 8217:2017 Specifications of marine fuels
    • IMO MARPOL Annex VI for sulfur emissions (marine applications)
    • DIN 51603-1 for fuel oils (Germany, industrial use)
    • REACH registration for chemical substances traded in Europe

    Typical usage ratio

    • 5-30% volumetric addition to base thermal oil or bunker fuel blend, variable by seasonal shipping routes, customer engine tolerance, and sulfur blending targets. Ratio finalized after viscosity and flash point testing in end-user labs.

    Downstream process integration

    • Blended at tank farm or terminal post-distillation, ahead of cargo transfer or fuel delivery to bulk end-users. Inline monitoring and tank sampling confirm compliance before final shipment.

    Final product types

    • Intermediate and heavy marine bunkers (IFO, MGO)
    • Industrial heating oil
    • Thermal process oils for boilers and power plants
    • Auxiliary refinery fuels

    Free Quote

    Competitive Cracked C4 Raffinate Oil prices that fit your budget—flexible terms and customized quotes for every order.

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    Certification & Compliance
    More Introduction

    Cracked C4 Raffinate Oil: Engineered for Reliability and Performance

    Understanding Cracked C4 Raffinate Oil – Its Purpose and Position in the Chemical Industry

    Drawing from decades on the production floor and in process optimization meetings, we have seen how every refinery byproduct carves out a unique place in industrial value chains. Cracked C4 Raffinate Oil arises as a result of C4 hydrocarbon stream processing, primarily during steam cracking. By separating butadiene and isobutylene from the C4 fraction, the remaining stream, known as C4 Raffinate, still holds significant utility across downstream applications when managed with technical discipline.

    Many customers ask what sets our Cracked C4 Raffinate Oil apart. This isn’t a general-purpose hydrocarbon solvent or a byproduct that just gets swept into the lowest-value use. Instead, our engineers design the process parameters—reactor temperature, fractional distillation cut points, and selective hydrogenation settings—specifically to achieve a balanced composition. The result: a chemical feedstock that consistently delivers known behaviors in end-use applications, especially rubber modifiers, adhesives, and fuel blending.

    Model and Manufacturing Process: What Goes Into Reliable C4 Raffinate Oil

    Through the lens of a manufacturer who depends on reliable production schedules, I’ve experienced firsthand how minor shifts in feedstock purity, cracking severity, or column conditions cause broad swings in raffinate quality. This fuelled our team’s decision to standardize our flagship C4 Raffinate Oil model based on fixed carbon number distribution and seamless interface between cracking and downstream purification. We target a cut with a dominant C4 backbone, limiting C5 and higher hydrocarbons, and tightly monitor unsaturate content.

    Continuous process verification minimizes unwanted polymerizable species and ensures that residue levels fall within a tight operational envelope. Our batch logs and automated analyzers have prevented costly surprises in later-use applications—whether the raffinate stream enters a synthetic rubber plant or a custom solvent operation. Each tank release reflects compounded experience from every previous run and real commitment to process feedback from end-users.

    Specifications: Physical and Chemical Features from Our Plant to Yours

    Unlike speculative traders, we focus on what shows up in the customer’s tank, not just what’s reported on a datasheet. The color, odor threshold, and density tell as much about upstream controls as any one purity number. We observe our finished Cracked C4 Raffinate Oil for:

    Rarely do customers see analyses drift, and when they do, we trace back through analyzer logs and manually sampled points to correct the issue at source, not after a complaint. These plant-proven controls take priority over chasing after theoretical specification improvements that don’t deliver results in end-use.

    End Uses: The Critical Role Cracked C4 Raffinate Oil Plays in Manufacturing

    Many downstream processors prize C4 Raffinate Oil for its role as a hydrocarbon feed, often in alkylation, rubber manufacture, or as a precursor for high-octane blending components. In our experience, operators of hydrocarbon resin and synthetic rubber units require predictable stream chemistry with repeatable volatility and minimized color development. When sampled by their QC team, our product enters polymerizations and blending systems with no unplanned shutdowns, which speaks to the quiet reliability that gets overlooked in marketing brochures.

    In alkylation units, cracked raffinate serves as an isobutene source after additional separation steps. Reliable butene composition supports stable alkylate yields in refineries producing reformulated gasoline. For synthetic rubber production, especially when targeting styrene butadiene or polybutadiene materials, our oil simplifies recipe adjustments and keeps Mooney viscosity readings inside target zones. Adhesive manufacturers benefit from stable boiling components and minimum peroxides, creating clean, clear products.

    From this vantage as a chemical producer, we see how seemingly small variances ripple downstream: a spike in diolefins leads to polymer fouling; trace hydrogensulfide causes off-odor in sealant resins; excessive heavies gum up vaporizer lines. Each of these headaches is preventable by listening to plant instrumentation and not cutting corners on column upkeep.

    Distinctions Between Cracked C4 Raffinate Oil and Related Streams

    Operators often ask how cracked C4 Raffinate Oil performs against other C4 stream products. While n-butane, isobutane, and crude C4 each fill roles in processing, the raffinate cut is more selective. The main differences we achieve through distillation and hydrotreatment are:

    Our teams have handled every grade over the years—crude C4 for mixed dehydrogenation, pure isobutene grades for chemical synthesis, and highly refined 1-butene cuts for polymerization. Few streams offer the same versatility as Cracked C4 Raffinate Oil when engineered and managed with end-use knowledge.

    Challenges in Production and Application

    Seasoned operators see production challenges not listed in textbooks—catalyst life shortened by trace poisons, shipping line upsets traced to missed drying cycles, and complexity in balancing plant throughput with API gravity targets. On more than one occasion, we have adjusted fractionation cut-points in real time to respond to unexpected compositions in the upstream cracker.

    Certain customers, especially in fuel blending, feel the effects of small departures from expectation most acutely. Shifts in volatility or unreacted butadiene can force mid-run changes or risk batch rejections. Our focus has always stayed with closed-loop feedback: keeping open lines with end-users, encouraging direct complaints, and inviting periodic plant visits for collaboration on new process needs. We have designed trial runs for clients who need variations—for instance, producing lower-unsaturate raffinate for minimal odor applications or developing packages with precise pour points for cold-weather regions.

    To us, solutions come through plant investment and experience sharing—not just tightening specs for the sake of marketing differentiation. Plant upgrades, analyzer recalibrations, and operator cross-training have proven more effective than chasing incremental refinements that never address the daily production realities. We pass down that lesson to every new generation of shift leads and process engineers.

    Commitment to Sustainability and Responsible Handling

    The chemical industry faces growing expectations on environmental stewardship and operational transparency. Our C4 Raffinate Oil production setup embodies the shift toward energy-efficient fractionation, closed-loop effluent treatment, and vapor recovery, which now form a core part of our process design.

    We install continuous air monitoring around storage tanks and integrate real-time emissions tracking with local regulatory bodies. Routine waste minimization audits seek out solvent recovery opportunities and flare gas reduction. For customers operating in regions with stringent VOC limits or special permitting, this track record translates to fewer supply disruptions and easier audits.

    Beyond regulatory compliance, the move to more sustainable operations pays off by improving process stability—tight leak control and reliable emissions capture lead to fewer plant trips, protecting both personnel safety and product quality. This is no abstract notion: each ton of raffinate shipped reliably means fewer costly surprises for all partners in the chain.

    Lessons Learned: Product Value Shaped by Long-Term Experience

    Reflecting on years of C4 fraction work, the most valuable lesson remains that each shipment tells a story—from the cracker’s heater outlet to final customer feedback. Each batch not only reflects technical engineering, but also the relationships built through open communication and knowledge of real-world process needs.

    Feedback loops—whether weekly trend reviews or rapid response teams for off-spec discoveries—have prevented more lost production than any tweak to a spec sheet. Listening to downstream users has reshaped how we control feedstock purity, invest in analyzer technology, and train our operators. For example, consistent trace analysis ahead of final shipment catches high sulfur that would otherwise impact catalyst performance in customer alkylation units. Addressing these practical operating truths builds trust and strengthens partnerships.

    Growing adoption of digital monitoring and inline sample verification means that real-time adjustments, whether for batch homogeneity or impurity removal, create a more reliable supply for all links in the supply chain. This technical convergence aligns with our deep-rooted operating knowledge—discipline acquired shift after shift and confirmed through user feedback.

    Moving Forward: Innovation and Adaptation

    Demands for improved sustainability, higher process uptime, and evolving customer needs mean that no chemical product stays static. We regularly revisit C4 Raffinate Oil production, adjusting separation steps and upgrading decontamination technology to keep pace with permitted emissions caps and shifting market applications.

    A strong partnership mindset serves best: sharing learnings and process data with collaborators, co-developing customized feedstocks for new downstream uses, and leveraging operating experience to introduce incremental process improvements. The most successful developments come from the field, not corporate boardrooms or theoretical whitepapers.

    We support customer experiments in new blending recipes, work hand-in-hand with operators trialing novel antioxidant packages, and adapt our product cut ranges when regional or regulatory requirements change. The value of these efforts shows up in stable order volumes, positive feedback, and technical partnerships that outlast commodity price cycles.

    Conclusion: Delivering Quality and Consistency from Producer Experience

    Cracked C4 Raffinate Oil does not thrive on the margins of refinery production—it stands as a product forged through years of process improvements, investment in plant reliability, and close communication with end-users. By focusing on stable impurity profiles, repeatable volatility, and minimum contaminants, we have shaped a product that addresses the real working constraints in chemical manufacturing, rubber compounds, and blending operations.

    We draw confidence from careful attention to technical detail and from a willingness to invest in plant and people. Direct knowledge from production teams, coupled with lessons from partner plants and customer sites, guide every incremental advance. This pragmatic approach has built our reputation for reliability—a value that delivers day after day to the operators who depend on every shipment of Cracked C4 Raffinate Oil.