# P-Xylene

**P-Xylene** (para-xylene; 1,4-dimethylbenzene) is an aromatic hydrocarbon in which two methyl groups occupy the 1 and 4 positions of a benzene ring, giving the formula C₈H₁₀ or C₆H₄(CH₃)₂<sup>[1](https://pubchem.ncbi.nlm.nih.gov/compound/7809)</sup>. It is one of the three xylene isomers, alongside o-xylene (1,2-dimethylbenzene) and m-xylene (1,3-dimethylbenzene)<sup>[2](https://cdn.who.int/media/docs/default-source/wash-documents/wash-chemicals/xylenes.pdf)</sup>. Its principal industrial role is as the feedstock for terephthalic acid, the raw material of polyester fiber<sup>[3](https://www.epa.gov/sites/default/files/2020-10/documents/c06s11.pdf)</sup>.

| Key fact | Detail |
|---|---|
| Identity | CAS 106-42-3; formula C₈H₁₀; molecular weight 106.16 g/mol<sup>[1](https://pubchem.ncbi.nlm.nih.gov/compound/7809)</sup> |
| Physical state | Colorless liquid with an aromatic odor; solid below 56 °F (13.2 °C)<sup>[4](https://www.cdc.gov/niosh/npg/npgd0670.html)</sup> |
| Boiling point / density | 138.4–138.5 °C; density 0.861 g/cm³ at 20 °C<sup>[5](https://www.osha.gov/sites/default/files/methods/osha-1002.pdf)</sup> |
| Water solubility | 198 mg/liter at 25 °C; log octanol–water partition coefficient 3.15<sup>[2](https://cdn.who.int/media/docs/default-source/wash-documents/wash-chemicals/xylenes.pdf)</sup> |
| Flammability | Class IC flammable liquid; flash point 81 °F; explosive limits 1.1–7.0% in air<sup>[4](https://www.cdc.gov/niosh/npg/npgd0670.html)</sup> |
| Exposure limits | NIOSH REL and OSHA PEL both TWA 100 ppm (435 mg/m³); NIOSH short-term limit 150 ppm; IDLH 900 ppm<sup>[4](https://www.cdc.gov/niosh/npg/npgd0670.html)</sup> |
| Main use | Air oxidation to terephthalic acid (TPA) for polyester manufacture<sup>[3](https://www.epa.gov/sites/default/files/2020-10/documents/c06s11.pdf)</sup> |

## Physical properties

P-Xylene is a colorless, watery liquid with a sweet odor, less dense than water and insoluble in water in practical terms<sup>[1](https://pubchem.ncbi.nlm.nih.gov/compound/7809)</sup>. Its melting point of 13.2 °C is unusually high for the family: o-xylene melts at −25 °C and m-xylene at −47.4 °C, so p-xylene is the only isomer that freezes near room temperature<sup>[5](https://www.osha.gov/sites/default/files/methods/osha-1002.pdf)</sup><sup> • </sup><sup>[6](https://www.dcceew.gov.au/environment/protection/npi/substances/xylenes-individual-or-mixed-isomers)</sup>. Boiling points, by contrast, are close together: 138.4 °C for p-xylene, 139.0 °C for m-xylene, and 144.4 °C for o-xylene<sup>[2](https://cdn.who.int/media/docs/default-source/wash-documents/wash-chemicals/xylenes.pdf)</sup>. [Vapor pressure](https://www.edgepedia.org/vapor-pressure) at 25 °C is 1.17 kPa, and the conversion factor in air is 1 ppm = 4.41 mg/m³<sup>[2](https://cdn.who.int/media/docs/default-source/wash-documents/wash-chemicals/xylenes.pdf)</sup>.

The high freezing point relative to the other isomers, combined with the closeness of the boiling points, shapes how the compound is purified. Simple fractional distillation cannot resolve the isomers; separation instead exploits the freezing-point difference through crystallization, or uses selective adsorption<sup>[7](https://egon.cheme.cmu.edu/Papers/rlima_grossmann_aichej.pdf)</sup>.

## Separation from mixed xylenes

Petrochemical streams contain the C₈ aromatics as a mixture of the three xylenes plus ethylbenzene, and p-xylene must be extracted at high purity for downstream use<sup>[7](https://egon.cheme.cmu.edu/Papers/rlima_grossmann_aichej.pdf)</sup>. Three process families are used: crystallization, adsorption, and hybrid crystallization/adsorption schemes<sup>[7](https://egon.cheme.cmu.edu/Papers/rlima_grossmann_aichej.pdf)</sup>.

**Crystallization** exploits the large freezing-point difference between p-xylene and the other isomers. In an industrial suspension process, p-xylene particles crystallize on the wall of a scraped crystallizer, are circulated to a growth vessel where they enlarge, and are then recovered by driving the slurry through a wash column<sup>[8](https://pubs.acs.org/doi/full/10.1021/acsomega.3c00069)</sup>. Older crystallization plants recovered only about two-thirds of the p-xylene present, producing roughly 0.1–0.15 kg of p-xylene per kg of mixed xylenes containing 12 to 22% p-xylene<sup>[9](https://nepis.epa.gov/Exe/ZyPURL.cgi?Dockey=910169OJ.TXT)</sup>.

**Adsorption** uses a shape-selective zeolite adsorbent selective to the para structure. In the Parex process, p-xylene is adsorbed from a C₈ aromatic mixture in a fixed bed and desorbed by washing with a hydrocarbon of different boiling point, with a multiport rotary valve simulating countercurrent flow of adsorbent and liquid; reported recovery efficiencies are 95 to 99%, at adsorption temperatures of 120 to 150 °C<sup>[9](https://nepis.epa.gov/Exe/ZyPURL.cgi?Dockey=910169OJ.TXT)</sup><sup> • </sup><sup>[10](https://www.sciencedirect.com/science/article/pii/S0255270106000997)</sup>. Adsorption was the preferred option before the 2000s<sup>[8](https://pubs.acs.org/doi/full/10.1021/acsomega.3c00069)</sup>.

**Isomerization** complements both routes. Because m-xylene is the naturally most abundant isomer, isomerization converts it to the more useful ortho- and para- forms<sup>[9](https://nepis.epa.gov/Exe/ZyPURL.cgi?Dockey=910169OJ.TXT)</sup>. With modern isomerization catalysts, the p-xylene fraction in the effluent from isomerization reactors exceeds 65 wt%, and this enrichment has made continuous crystallization widely adopted in newly built plants<sup>[8](https://pubs.acs.org/doi/full/10.1021/acsomega.3c00069)</sup>. Integrated schemes also exist in which pressure swing adsorption first separates p-xylene and ethylbenzene from the C₈ aromatics, followed by crystallization to product-grade purity<sup>[11](https://patents.google.com/patent/US6600083B2/en)</sup>.

## Oxidation to terephthalic acid

The dominant use of p-xylene is its oxidation to terephthalic acid (TPA), which requires purification before use in polyester fiber manufacture<sup>[3](https://www.epa.gov/sites/default/files/2020-10/documents/c06s11.pdf)</sup>. The most widespread technology is the Mid-Century process, also known as the AMOCO process: direct liquid-phase catalytic oxidation of p-xylene with air, usually in a homogeneous reaction medium with a transition-metal catalyst<sup>[12](https://pmc.ncbi.nlm.nih.gov/articles/PMC9961377/)</sup>. In the classical flowsheet, p-xylene, fresh and recovered acetic acid, and a catalyst system such as manganese or cobalt acetate with sodium bromide are fed to a reactor; air compressed to about 2000 kPa (290 psi) is the oxidant, and the exothermic reaction is held at about 200 °C (392 °F) by controlling the pressure at which the mixture boils<sup>[3](https://www.epa.gov/sites/default/files/2020-10/documents/c06s11.pdf)</sup>. Patent literature describes the same chemistry over a temperature window of 180 to 230 °C with cobalt, manganese, and bromine catalysts in acetic acid solvent<sup>[13](https://patents.google.com/patent/EP0135341A1/en)</sup>.

The crude TPA is recovered by crystallization: partially oxidized impurities such as p-toluic acid and p-formylbenzoic acid remain more soluble in acetic acid while TPA crystallizes out, and the wet cake is dried to free-flowing crystals<sup>[3](https://www.epa.gov/sites/default/files/2020-10/documents/c06s11.pdf)</sup>. TPA itself is extremely insoluble in water and most common organic solvents and does not melt; it sublimes<sup>[3](https://www.epa.gov/sites/default/files/2020-10/documents/c06s11.pdf)</sup>. Process variants include the use of pure or nearly pure oxygen as the oxidant to maximize liquid-phase oxygen concentration<sup>[14](https://patents.google.com/patent/US5696285A/en)</sup>, and spray-reactor concepts aimed at high-purity TPA<sup>[15](https://www.sciencedirect.com/science/article/pii/S0009250913006179)</sup>.

## Health and safety

P-Xylene is a Class IC flammable liquid, with a flash point of 81 °F and lower and upper explosive limits of 1.1% and 7.0% in air; it is incompatible with strong oxidizers and strong acids<sup>[4](https://www.cdc.gov/niosh/npg/npgd0670.html)</sup>. Occupational exposure occurs by inhalation, skin absorption, ingestion, and skin or eye contact<sup>[4](https://www.cdc.gov/niosh/npg/npgd0670.html)</sup>.

The exposure limits are set at a TWA of 100 ppm (435 mg/m³) by both NIOSH and OSHA, with a NIOSH short-term exposure limit of 150 ppm (655 mg/m³); concentrations up to 900 ppm, the immediately dangerous to life or health (IDLH) value, are assigned respirator protection ranging from organic-vapor cartridge respirators to self-contained breathing apparatus<sup>[4](https://www.cdc.gov/niosh/npg/npgd0670.html)</sup>. Vapor exposure above the recommended limit can irritate the eyes, nose, and throat and cause chest tightening and an abnormal gait<sup>[1](https://pubchem.ncbi.nlm.nih.gov/compound/7809)</sup>. Overexposure can produce headache, fatigue, dizziness, listlessness, confusion, irritability, nausea and loss of appetite, and flushing of the face<sup>[1](https://pubchem.ncbi.nlm.nih.gov/compound/7809)</sup>. Target organs listed by NIOSH include the eyes, skin, respiratory system, central nervous system, gastrointestinal tract, blood, liver, and kidneys<sup>[4](https://www.cdc.gov/niosh/npg/npgd0670.html)</sup>.

## Environmental behavior

Releases of xylene go largely to air because of volatility; the calculated environmental distribution is 99.1% air, 0.7% water, 0.1% soil, and 0.1% sediment<sup>[2](https://cdn.who.int/media/docs/default-source/wash-documents/wash-chemicals/xylenes.pdf)</sup>. Xylene degrades in air with a half-life of a few days and is readily biodegraded in soils and surface waters; in aerobic groundwater, reported half-lives range from 24 to over 161 days, while under anaerobic groundwater conditions no biotransformation is expected<sup>[2](https://cdn.who.int/media/docs/default-source/wash-documents/wash-chemicals/xylenes.pdf)</sup>. The odor threshold for xylene isomers in water is 0.02–1.8 mg/liter, and concentrations of 0.3–1.0 mg/liter produce a detectable taste and odor<sup>[2](https://cdn.who.int/media/docs/default-source/wash-documents/wash-chemicals/xylenes.pdf)</sup>.

## References

1. [P-Xylene, CID 7809, PubChem](https://pubchem.ncbi.nlm.nih.gov/compound/7809)
2. [Xylenes in Drinking-water, WHO/SDE/WSH/03.04/25](https://cdn.who.int/media/docs/default-source/wash-documents/wash-chemicals/xylenes.pdf)
3. [AP-42, Chapter 6.11: Terephthalic Acid, U.S. EPA](https://www.epa.gov/sites/default/files/2020-10/documents/c06s11.pdf)
4. [p-Xylene, NIOSH Pocket Guide to Chemical Hazards, CDC](https://www.cdc.gov/niosh/npg/npgd0670.html)
5. [Xylenes (o-, m-, p-isomers), OSHA Method 1002](https://www.osha.gov/sites/default/files/methods/osha-1002.pdf)
6. [Xylenes (individual or mixed isomers), Australian DCCEEW National Pollutant Inventory](https://www.dcceew.gov.au/environment/protection/npi/substances/xylenes-individual-or-mixed-isomers)
7. [Optimal synthesis of p-xylene separation processes, Lima & Grossmann, AIChE Journal](https://egon.cheme.cmu.edu/Papers/rlima_grossmann_aichej.pdf)
8. [Process Optimization of Para-xylene Crystallization Separation Process, ACS Omega](https://pubs.acs.org/doi/full/10.1021/acsomega.3c00069)
9. [Industrial Process Profiles for Environmental Use: Chapter 5, Basic Petrochemical Industry, U.S. EPA](https://nepis.epa.gov/Exe/ZyPURL.cgi?Dockey=910169OJ.TXT)
10. [Separation of para-xylene from xylene mixture via crystallization, Chemical Engineering and Processing](https://www.sciencedirect.com/science/article/pii/S0255270106000997)
11. [US6600083B2, Para-xylene production process integrating pressure swing adsorption and crystallization](https://patents.google.com/patent/US6600083B2/en)
12. [p-Xylene Oxidation to Terephthalic Acid: New Trends, PMC](https://pmc.ncbi.nlm.nih.gov/articles/PMC9961377/)
13. [EP0135341A1, Process for preparing terephthalic acid from para-xylene](https://patents.google.com/patent/EP0135341A1/en)
14. [US5696285A, Production of terephthalic acid using pure or nearly pure oxygen as oxidant](https://patents.google.com/patent/US5696285A/en)
15. [A spray reactor concept for catalytic oxidation of p-xylene to produce high-purity terephthalic acid, Chemical Engineering Science](https://www.sciencedirect.com/science/article/pii/S0009250913006179)

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*Topic: Encyclopedia › Physical world and mathematics › Chemistry › Organic substances › Organic reactions, structure and reference › Stereochemistry and isomerism › Isomerism and structural isomers › Positional (regio) isomerism*

*Initially written Sep 17, 2026 · Reviewed: Oct 15, 2026 · Edited: Oct 15, 2026 · Last review: Oct 15, 2026*

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License: Edgepedia Community License 1.0, https://www.edgepedia.org/edgepedia/license