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Diisopropylbenzene

    • Product Name Diisopropylbenzene
    • Alias DIPB
    • Einecs 202-746-9
    • Mininmum Order 1 g
    • Factory Site Tengfei Creation Center,55 Jiangjun Avenue, Jiangning District,Nanjing
    • Price Inquiry admin@sinochem-nanjing.com
    • Manufacturer Sinochem Nanjing Corporation
    • CONTACT NOW
    VTB
    Specifications

    HS Code

    855848

    Cas Number 25321-09-9
    Molecular Formula C12H18
    Molar Mass 162.27 g/mol
    Appearance Colorless liquid
    Density 0.86 g/cm3
    Melting Point -60 °C
    Boiling Point 230-235 °C
    Solubility In Water Insoluble
    Odor Aromatic
    Flash Point 90 °C
    Refractive Index 1.490
    Vapor Pressure 0.25 mmHg at 25 °C

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

    Packing & Storage
    Packing Diisopropylbenzene is packaged in a 500 mL amber glass bottle with a secure screw cap, labeled with hazard warnings.
    Shipping Diisopropylbenzene is shipped as a liquid in tightly sealed drums or containers, compliant with applicable transport regulations. It is classified as a combustible liquid and should be protected from heat, sparks, and open flames. Proper labeling, ventilation, and secondary containment are essential during shipping to prevent leaks, spills, or exposure.
    Storage Diisopropylbenzene should be stored in a cool, dry, well-ventilated area, away from heat, ignition sources, and incompatible materials like strong oxidizers. Keep the chemical in tightly closed, properly labeled containers made of materials compatible with aromatic hydrocarbons. Avoid prolonged exposure to air and light, and store at ambient temperature, protecting from direct sunlight and humidity to prevent degradation or hazardous reactions.
    Application of Diisopropylbenzene

    Applications of Diisopropylbenzene in Industrial Manufacturing

    As a direct manufacturer of diisopropylbenzene, we supply material optimized for several key industrial segments where performance, compliance, and consistent quality are mandatory. The applications below reflect direct, large-scale downstream integration based on established sector regulations and customer-specific process controls.

    1. Hydroperoxide Intermediate for Phenol and Acetone Production

    Major phenol plants employ diisopropylbenzene as a crucial step in the Hock process, where it serves as an intermediate during hydroperoxidation. Routine feedstock adjustments depend on purity and oxidative stability, and the material undergoes conversion via air oxidation followed by cleavage under acidic conditions, ultimately yielding phenol and acetone. Downstream integration is contingent on meeting strict impurity profiles and stability parameters to safeguard process yield and end-product quality.

    Industry compliance standards

    • ISO 9001:2015 quality management systems
    • REACH Regulation (EC) No 1907/2006 registration for EU operators
    • US EPA TSCA (Toxic Substances Control Act)
    • Purity and traceability standards as per leading phenol plant requirements

    Typical usage ratio

    • Feedstock charge typically 10–16% (w/w) relative to acetone and other charge materials; specific ratio managed via process analytics depending on required phenol output and reaction conversion rates

    Downstream process integration

    • Hydroperoxidation step: introduced after isopropylation stage, air oxidized with metal catalyst, then directed to downstream acid-cleavage reactors and phase separation units

    Final product types

    • Technical-grade phenol
    • Acetone
    • Cumene byproducts (for solvent and fuel additive applications)

    2. Precursor in Tetramethylbenzidine (TMB) Synthesis for Analytical Reagents

    Laboratories and fine chemical manufacturers select diisopropylbenzene as a key raw intermediate in the synthesis of tetramethylbenzidine, which is widely used as a chromogenic substrate in peroxidase-based diagnostics and environmental testing kits. Reaction control calls for precise incorporation at the alkylation and oxidation steps, with stringent batch-to-batch monitoring for metal residues and aromatic purity to ensure downstream reagent consistency and shelf-life stability.

    Industry compliance standards

    • ISO 13485:2016 for medical device and diagnostic reagent manufacturers
    • European Pharmacopoeia (Ph. Eur.) standards for chemical starting materials
    • USP <1043> Ancillary Materials for Cell, Gene, and Tissue-Engineered Products (for certain diagnostic applications)

    Typical usage ratio

    • Charge levels typically 8–12% (w/w) of total alkylation mix; ratio is fine-tuned based on oxidant strength and desired TMB output; excessive levels avoided to prevent chromophore impurities

    Downstream process integration

    • Added during stepwise alkylation of benzene derivatives, followed by controlled oxidation with specific metal catalysts and subsequent TMB isolation, washing, and purification

    Final product types

    • Diagnostic assay substrates (ELISA kits, immunoassay reagents)
    • Colorimetric water and food safety test kits
    • Laboratory-grade chromogenic agents

    3. Chain Transfer Agent in Specialty Polymer Production

    Polymer manufacturers use diisopropylbenzene as a chain transfer agent or additive to mediate molecular weight distribution during emulsion and solution polymerization of styrene- and acrylate-based systems. The compound’s aromatic structure provides controlled chain termination and adjustment of final mechanical properties. Industrial compounding demands exacting raw material qualification, since variation can alter key product attributes such as melt flow, glass transition, and tensile strength.

    Industry compliance standards

    • Good Manufacturing Practice (GMP) for plastics and polymer additives (EU No 2023/2006)
    • FDA 21 CFR §177.2600 for rubber articles intended for repeated use
    • ISO 9001:2015 for process consistency and Quality Control monitoring

    Typical usage ratio

    • 0.2–2.5% (w/w) relative to total monomer mass; dependent on polymer backbone design, desired molecular distribution, and targeted end-use mechanical profile

    Downstream process integration

    • Introduced simultaneous with monomer addition in batch/continuous reactors; rate of feed adjusted to align with chain length targets and polymerization kinetics

    Final product types

    • Impact-modified polystyrenes (HIPS, ABS copolymers)
    • Specialty acrylic elastomers
    • Functional block copolymers and engineering plastics

    4. Solvent and Carrier for Fine Chemical Reactions

    In fine chemical synthesis, manufacturers use diisopropylbenzene as a high-boiling, low-reactivity reaction solvent or carrier, particularly in alkylation, Friedel–Crafts, and Grignard-scale organic synthesis processes. Material qualification requires low halogen, sulfur, and peroxide content to minimize side reactions and guarantee conformity in downstream synthesis. Solvent recovery systems often integrate this raw material for cost and environmental management.

    Industry compliance standards

    • GMP guidelines for starting materials used in API synthesis (ICH Q7)
    • EPA NESHAP standards for Hazardous Air Pollutants (HAP) from chemical manufacturing (for solvent handling/recovery)
    • ISO 14001:2015 for Environmental Management Systems relating to solvent use

    Typical usage ratio

    • 10–30% (w/w) of total reaction mass as solvent or carrier; ratio based on solute solubility profile and targeted yield; the upper range applies to multi-stage batch synthesis, while continuous systems may run lower concentrations with in-line recovery

    Downstream process integration

    • Charged to reactor prior to primary active ingredients; serves as primary or co-solvent through heating, reflux, and extraction cycles, then purified and recycled for subsequent batches

    Final product types

    • Niche intermediates for crop protection chemicals
    • Pharmaceutical starting materials (non-active ingredient)
    • Electronic-grade fine chemicals and solvents

    5. Precursor in High-Purity Antioxidant Additive Manufacturing

    Producers of high-purity phenolic antioxidant additives rely on diisopropylbenzene as a key feedstock for synthesizing certain high-value hindered phenol antioxidants, including those designed for polyolefin and lubricant stabilization applications. Feedstock selection directly influences downstream antioxidant purity and color stability, with rigorous analytical verification required at the sourcing and post-synthesis QC stages.

    Industry compliance standards

    • China GB 9685-2016 for food contact additives
    • EU Regulation (EU) No 10/2011 on plastic materials intended to come into contact with food
    • ASTM D4676 (Standard Classification for Polyolefin Additives)

    Typical usage ratio

    • Feedstock load ranges from 6–14% (w/w) of antioxidant reaction batch, adjusted based on target molecular functionality and downstream stabilization requirements specific to resin or oil type

    Downstream process integration

    • Reacted with phenolic or alkyl substituents in controlled batch reactors; precise temperature and catalyst selection optimize antioxidant structure for targeted polymer compatibility and dispersibility

    Final product types

    • Hindered phenol antioxidants for high-performance polymers
    • Stabilizer blends for lubricating base oils
    • Food packaging and masterbatch additive concentrates
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