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1,4-Dimethylbenzene, also known as p-xylene, is an aromatic hydrocarbon based on benzene with two methyl substituents at the 1 and 4 positions. It has the chemical formula C8H10 or C6H4(CH3)2. p-Xylene is a colorless, flammable liquid with a sweet odor and is practically insoluble in water. It is one of the three isomers of dimethylbenzene, collectively known as xylenes.

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  • 106-42-3 Structure
  • Basic information

    1. Product Name: 1,4-Dimethylbenzene
    2. Synonyms: p-Xylene(8CI);1,4-Xylene;4-Methyltoluene;NSC 72419;p-Dimethylbenzene;p-Methyltoluene;p-Phenylenebis(methylene);p-Xylol;1,4-Dimethylbenzene;
    3. CAS NO:106-42-3
    4. Molecular Formula: C8H10
    5. Molecular Weight: 106.1674
    6. EINECS: 203-396-5
    7. Product Categories: Industrial/Fine Chemicals;Analytical Chemistry;Standard Solution of Volatile Organic Compounds for Water & Soil Analysis;Standard Solutions (VOC);Amber Glass Bottles;Analytical Reagents;Analytical/Chromatography;CHROMASOLV for HPLC;Chromatography Reagents &;HPLC &;HPLC Grade Solvents (CHROMASOLV);HPLC/UHPLC Solvents (CHROMASOLV);Solvent Bottles;Solvent by Application;Solvent Packaging Options;Solvents;UHPLC Solvents (CHROMASOLV)
    8. Mol File: 106-42-3.mol
  • Chemical Properties

    1. Melting Point: 13-13℃
    2. Boiling Point: 139.61 °C at 760 mmHg
    3. Flash Point: 27.22 °C
    4. Appearance: colourless liquid
    5. Density: 0.87 g/cm3
    6. Vapor Density: 3.7 (vs air)
    7. Vapor Pressure: 7.943mmHg at 25°C
    8. Refractive Index: n20/D 1.495(lit.)
    9. Storage Temp.: 0-6°C
    10. Solubility: water: soluble0.2g/L
    11. PKA: >15 (Christensen et al., 1975)
    12. Water Solubility: Miscible with alcohol, ether, acetone, benzene and chloroform. Immiscible with water.
    13. Stability: Stable. Incompatible with oxidizing agents. Hygroscopic. Flammable.
    14. Merck: 14,10081
    15. BRN: 1901563
    16. CAS DataBase Reference: 1,4-Dimethylbenzene(CAS DataBase Reference)
    17. NIST Chemistry Reference: 1,4-Dimethylbenzene(106-42-3)
    18. EPA Substance Registry System: 1,4-Dimethylbenzene(106-42-3)
  • Safety Data

    1. Hazard Codes:  Xn:Harmful;
    2. Statements: R10:Flammable.; R20/21:Harmful by inhalation and in contact with skin.; R38:Irritating to skin.;
    3. Safety Statements: S25:Avoid contact with eyes.;
    4. RIDADR: UN 1307 3/PG 3
    5. WGK Germany: 2
    6. RTECS: ZE2625000
    7. TSCA: Yes
    8. HazardClass: 3
    9. PackingGroup: III
    10. Hazardous Substances Data: 106-42-3(Hazardous Substances Data)

106-42-3 Usage

Uses

1. Used in the Chemical Industry:
1,4-Dimethylbenzene is used as a precursor for the production of various chemicals, including benzoic acid, isophthalic acid, and terephthalic acid, which are used in the manufacture of polyester fibers and other plastic and rubber products.
2. Used as a Solvent:
1,4-Dimethylbenzene is used as a solvent in the paint, coatings, and rubber industries due to its ability to dissolve a wide range of substances.
3. Used in the Production of Dyes and Drugs:
p-Xylene is used as a raw material for the production of dyes, drugs, pesticides, and many organic intermediates, such as terephthalic acid and phthalic anhydride.
4. Used in Microscopy:
1,4-Dimethylbenzene is used with Canada balsam as an oil-immersion medium in microscopy and as a clearing agent in microscope techniques.
Physical Properties:
1,4-Dimethylbenzene is a clear, colorless, watery liquid with a sweet odor. It has an odor threshold concentration of 47 ppbv in air. It is less dense than water and has a freezing point of 56°F. The flash point of p-xylene is 27°C, making it dangerously flammable.

References

1.https://en.wikipedia.org/wiki/P-Xylene 2.https://pubchem.ncbi.nlm.nih.gov/compound/p-xylene#section=Top 3.https://www.chemicalsafetyfacts.org/paraxylene/

Synthesis Reference(s)

The Journal of Organic Chemistry, 53, p. 3247, 1988 DOI: 10.1021/jo00249a020Tetrahedron Letters, 26, p. 1935, 1985 DOI: 10.1016/S0040-4039(00)98345-X

Air & Water Reactions

Highly flammable. Insoluble in water.

Reactivity Profile

P-XYLENE may react with oxidizing materials. . Acetic acid forms explosive mixtures with P-XYLENE and air (Shraer, B.I. 1970. Khim. Prom. 46(10):747-750.).

Health Hazard

Vapors cause headache and dizziness. Liquid irritates eyes and skin. If taken into lungs, causes severe coughing, distress, and rapidly developing pulmonary edema. If ingested, causes nausea, vomiting, cramps, headache, and coma. Can be fatal. Kidney and liver damage can occur.

Health Hazard

The toxic properties of xylene isomers aresimilar to toluene or ethylbenzene. The targetorgans are the central nervous system, eyes,gastrointestinal tract, kidneys, liver, blood,and skin, which, however, are affected onlyat high levels of exposure. In humans itsexposure may cause irritation of the eyes,nose, and throat, headache, dizziness, excitement,drowsiness, nausea, vomiting, abdominalpain, and dermatitis. The irritation effectsin humans may be felt at a concentration of200 ppm in air, while exposure to 10,000 ppmfor 6–8 hours may be fatal.The oral toxicity of xylene is low. Ingestionof a high dose, however, can causedepression of the central nervous system,dizziness, nausea, and vomiting and abdominalpain. The oral LD50 values in ratsfor xylene isomers are within the range of5000 mg/kg.The major route of absorption of xyleneis inhalation. Another significant route isskin absorption of the liquid. About 5% ofabsorbed xylene is excreted unchanged inexpired air within a few hours, while less than2% is hydroxylated to xylenols. Over 90% ofabsorbed xylenes are metabolized to o-, m-,and p-isomers of methyl benzoic acid andexcreted in urine as methyl hippuric acids(ACGIH 1986). Small amounts of xylenesmay remain stored in adipose tissue. Repeatedexposures may cause accumulation in theblood.

Fire Hazard

Behavior in Fire: Vapor is heavier than air and may travel considerable distance to a source of ignition and flash back.

Flammability and Explosibility

Flammable

Chemical Reactivity

Reactivity with Water No reaction; Reactivity with Common Materials: No reaction; Stability During Transport: Stable; Neutralizing Agents for Acids and Caustics: Not pertinent; Polymerization: Not pertinent; Inhibitor of Polymerization: Not pertinent.

Safety Profile

Moderately toxic by intraperitoneal route. Mildly toxic by ingestion and inhalation. An experimental teratogen. Experimental reproductive effects. May be narcotic in hgh concentrations. Chronic toxicity not established, but is less toxic than benzene. A very dangerous fire hazard when exposed to heat or flame; can react with oxidzing materials. Explosive in the form of vapor when exposed to heat or flame. To fight fire, use foam, CO2, dry chemical. Potentially explosive reaction with acetic acid + air, 1,3-dichloro-5,5-dimethyl-2,4- imidazolidinhone, nitric acid + pressure. When heated to decomposition it emits acrid smoke and irritating fumes. See also other xylene entries.

Source

Detected in distilled water-soluble fractions No. 2 fuel oil (1.11 mg/L), jet fuel A (1.23 mg/L), diesel fuel (0.56 mg/L), and military jet fuel JP-4 (5.48 mg/L) (Potter, 1996); in new and used motor oil at concentrations of 0.26 to 0.29 and 302 to 339 μg/L, respectively (Chen et al., 1994). The average volume percent and estimated mole fraction in American Petroleum Institute PS-6 gasoline are 1.809 and 0.02263, respectively (Poulsen et al., 1992). Diesel fuel obtained from a service station in Schlieren, Switzerland contained m/p-xylene at a concentration of 336 mg/L (Schluep et al., 2001). Thomas and Delfino (1991) equilibrated contaminant-free groundwater collected from Gainesville, FL with individual fractions of three individual petroleum products at 24–25 °C for 24 h. The aqueous phase was analyzed for organic compounds via U.S. EPA approved test method 602. Average m+p-xylene concentrations reported in water-soluble fractions of unleaded gasoline, kerosene, and diesel fuel were 8.611, 0.658, and 0.228 mg/L, respectively. When the authors analyzed the aqueous-phase via U.S. EPA approved test method 610, average m+p-xylene concentrations in water-soluble fractions of unleaded gasoline, kerosene, and diesel fuel were lower, i.e., 6.068, 0.360, and 0.222 mg/L, respectively. Based on laboratory analysis of 7 coal tar samples, m+p-xylene concentrations ranged from ND to 6,000 ppm (EPRI, 1990). Detected in 1-yr aged coal tar film and bulk coal tar at concentrations of 260 and 830 mg/kg, respectively (Nelson et al., 1996). A high-temperature coal tar contained pxylene at an average concentration of 0.03 wt % (McNeil, 1983). Schauer et al. (2001) measured organic compound emission rates for volatile organic compounds, gas-phase semi-volatile organic compounds, and particle-phase organic compounds from the residential (fireplace) combustion of pine, oak, and eucalyptus. The gas-phase emission rate of m-xylene + p-xylene was 60.0 mg/kg of pine burned. Emission rates of both isomers were not measured during the combustion of oak and eucalyptus. Drinking water standard (final): For all xylenes, the MCLG and MCL are both 10 mg/L. In addition, a DWEL of 70 mg/L was recommended (U.S. EPA, 2000).

Environmental fate

Biological. Microbial degradation of p-xylene produced 4-methylbenzyl alcohol, pmethylbenzaldehyde, p-toluic acid, and 4-methylcatechol (quoted, Verschueren, 1983). Dimethylcis, cis-muconic acid, and 2,3-dihydroxy-p-toluic acid were reported to be biooxidation products of p-xylene by Nocardia corallina V-49 using n-hexadecane as the substrate (Keck et al., 1989). Reported biodegradation products of the commercial product containing xylene include α-hydroxy-p-toluic acid, p-methylbenzyl alcohol, benzyl alcohol, 4-methylcatechol, m- and ptoluic acids (Fishbein, 1985). It was reported that p-xylene was cometabolized resulting in the formation of p-toluic and 2,3-dihydroxy-o-toluic acids (Pitter and Chudoba, 1990). In anoxic groundwater near Bemidji, MI, p-xylene anaerobically biodegraded to the intermediate p-toluic acid (Cozzarelli et al., 1990). In gasoline-contaminated groundwater, methylbenzylsuccinic acid was identified as the first intermediate during the anaerobic degradation of xylenes (Reusser and Field, 2002). Photolytic. A n-hexane solution containing m-xylene and spread as a thin film (4 mm) on cold water (10 °C) was irradiated by a mercury medium pressure lamp. In 3 h, 18.5% of the p-xylene photooxidized into p-methylbenzaldehyde, p-benzyl alcohol, p-benzoic acid, and pmethylacetophenone (Moza and Feicht, 1989). Glyoxal and methylglyoxal were produced from the photooxidation of p-xylene by OH radicals in air at 25 °C (Tuazon et al., 1986a). The rate constant for the reaction of p-xylene and OH radicals at room temperature was 1.22 x 10-11 cm3/molecule?sec (Hansen et al., 1975). A rate constant of 7.45 x 10-9 L/molecule?sec was reported for the reaction of p-xylene with OH radicals in the gas phase (Darnall et al., 1976). Similarly, a room temperature rate constant of 1.41 x 10-11 cm3/molecule?sec was reported for the vapor-phase reaction of p-xylene with OH radicals (Atkinson, 1985). At 25 °C, a rate constant of 1.29 x 10-11 cm3/molecule?sec was reported for the same reaction (Ohta and Ohyama, 1985). Chemical/Physical. Under atmospheric conditions, the gas-phase reaction with OH radicals and nitrogen oxides resulted in the formation of p-tolualdehyde (Atkinson, 1990). Kanno et al. (1982) studied the aqueous reaction of p-xylene and other aromatic hydrocarbons (benzene, toluene, oand m-xylene, and naphthalene) with hypochlorous acid in the presence of ammonium ion. They reported that the aromatic ring was not chlorinated as expected but was cleaved by chloramine forming cyanogen chloride. The amount of cyanogen chloride formed increased at lower pHs (Kanno et al., 1982). Products identified from the OH radical-initiated reaction of p-xylene in the presence of nitrogen dioxide were 3-hexene-2,5-dione, p-tolualdehyde, and 2,5-dimethylphenol (Bethel et al., 2000).

Purification Methods

The general purification methods listed for xylene above are applicable. p-Xylene can readily be separated from its isomers by crystallisation from such solvents as MeOH, EtOH, isopropanol, acetone, butanone, toluene, pentane or pentene. It can be further purified by fractional crystallisation by partial freezing, and stored over sodium wire or molecular sieves Linde type 4A. [Stokes & French J Chem Soc, Faraday Trans 1 76 537 1980, Beilstein 5 H 382, 5 I 185, 5 II 296, 5 III 845, 5 IV 951.]

Check Digit Verification of cas no

The CAS Registry Mumber 106-42-3 includes 6 digits separated into 3 groups by hyphens. The first part of the number,starting from the left, has 3 digits, 1,0 and 6 respectively; the second part has 2 digits, 4 and 2 respectively.
Calculate Digit Verification of CAS Registry Number 106-42:
(5*1)+(4*0)+(3*6)+(2*4)+(1*2)=33
33 % 10 = 3
So 106-42-3 is a valid CAS Registry Number.
InChI:InChI:1S/C8H10/c1-7-3-5-8(2)6-4-7/h3-6H,1-2H3

106-42-3 Well-known Company Product Price

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  • Alfa Aesar

  • (A10534)  p-Xylene, 99%   

  • 106-42-3

  • 100ml

  • 129.0CNY

  • Detail
  • Alfa Aesar

  • (A10534)  p-Xylene, 99%   

  • 106-42-3

  • 500ml

  • 186.0CNY

  • Detail
  • Alfa Aesar

  • (A10534)  p-Xylene, 99%   

  • 106-42-3

  • 2500ml

  • 711.0CNY

  • Detail
  • Sigma-Aldrich

  • (PHR1314)    pharmaceutical secondary standard; traceable to USP

  • 106-42-3

  • PHR1314-1G

  • 732.19CNY

  • Detail
  • Sigma-Aldrich

  • (296333)  p-Xylene  anhydrous, ≥99%

  • 106-42-3

  • 296333-100ML

  • 745.29CNY

  • Detail
  • Sigma-Aldrich

  • (296333)  p-Xylene  anhydrous, ≥99%

  • 106-42-3

  • 296333-1L

  • 1,315.08CNY

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  • Sigma-Aldrich

  • (134449)  p-Xylene  ReagentPlus®, 99%

  • 106-42-3

  • 134449-500ML

  • 210.60CNY

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  • Sigma-Aldrich

  • (134449)  p-Xylene  ReagentPlus®, 99%

  • 106-42-3

  • 134449-2.5L

  • 524.16CNY

  • Detail
  • Sigma-Aldrich

  • (134449)  p-Xylene  ReagentPlus®, 99%

  • 106-42-3

  • 134449-20L

  • 9,874.80CNY

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  • Sigma-Aldrich

  • (317195)  p-Xylene  for HPLC, ≥99%

  • 106-42-3

  • 317195-100ML

  • 728.91CNY

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  • Sigma-Aldrich

  • (317195)  p-Xylene  for HPLC, ≥99%

  • 106-42-3

  • 317195-1L

  • 1,315.08CNY

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  • Sigma-Aldrich

  • (95682)  p-Xylene  puriss. p.a., ≥99.0% (GC)

  • 106-42-3

  • 95682-1L

  • 1,469.52CNY

  • Detail

106-42-3SDS

SAFETY DATA SHEETS

According to Globally Harmonized System of Classification and Labelling of Chemicals (GHS) - Sixth revised edition

Version: 1.0

Creation Date: Aug 12, 2017

Revision Date: Aug 12, 2017

1.Identification

1.1 GHS Product identifier

Product name p-Xylene

1.2 Other means of identification

Product number -
Other names 4-methyltoluene

1.3 Recommended use of the chemical and restrictions on use

Identified uses For industry use only. Intermediates,Processing aids, not otherwise listed
Uses advised against no data available

1.4 Supplier's details

1.5 Emergency phone number

Emergency phone number -
Service hours Monday to Friday, 9am-5pm (Standard time zone: UTC/GMT +8 hours).

More Details:106-42-3 SDS

106-42-3Synthetic route

4-methyl-benzaldehyde
104-87-0

4-methyl-benzaldehyde

para-xylene
106-42-3

para-xylene

Conditions
ConditionsYield
With hydrogen In water; ethyl acetate at 50℃; under 15001.5 Torr; for 5h;99%
With hydrogen In water at 25℃; for 1h;99%
With hydrogen at 350℃; under 760.051 Torr;95%
ethene
74-85-1

ethene

2,5-hexanedione
110-13-4

2,5-hexanedione

para-xylene
106-42-3

para-xylene

Conditions
ConditionsYield
With solid acid catalyst tin phosphate In n-heptane at 300℃; under 15001.5 Torr; for 12h; Reagent/catalyst; Solvent; Pressure; Temperature;90%
With copper(II) bis(trifluoromethanesulfonate) at 250 - 270℃; under 26892.4 - 82745.9 Torr; for 5h; Inert atmosphere;44%
2,5-dimethylfuran
625-86-5

2,5-dimethylfuran

ethene
74-85-1

ethene

para-xylene
106-42-3

para-xylene

Conditions
ConditionsYield
With P-containing zeolite Beta In n-heptane at 250℃; under 46504.7 Torr; Reagent/catalyst; Diels-Alder Cycloaddition;97%
With benzoic acid anhydride In acetic acid at 280℃; under 63006.3 Torr; for 8h; Pressure; Reagent/catalyst; Solvent; Temperature; Time;92.3%
With copper(II) bis(trifluoromethanesulfonate) In tetrahydrofuran at 270℃; under 26892.4 - 82745.9 Torr; for 5h; Catalytic behavior; Reagent/catalyst; Solvent; Inert atmosphere;91%
2,5-dimethylfuran
625-86-5

2,5-dimethylfuran

ethene
74-85-1

ethene

A

para-xylene
106-42-3

para-xylene

B

2,5-hexanedione
110-13-4

2,5-hexanedione

Conditions
ConditionsYield
In n-heptane at 249.84℃; under 37503.8 Torr; for 24h; Reagent/catalyst; Autoclave; Inert atmosphere;A 75%
B n/a
In acetic acid at 280℃; under 63006.3 Torr; for 4h; Pressure; Reagent/catalyst; Solvent; Temperature; Time;A 68.5%
B 12.1%
With Sn-BEA In n-heptane at 250℃; under 46504.7 Torr; for 24h; Catalytic behavior; Kinetics; Diels-Alder Cycloaddition; Autoclave; Inert atmosphere; chemoselective reaction;A 43%
B n/a
methanol
67-56-1

methanol

toluene
108-88-3

toluene

A

o-xylene
95-47-6

o-xylene

B

para-xylene
106-42-3

para-xylene

C

m-xylene
108-38-3

m-xylene

Conditions
ConditionsYield
With hydrogen; P-modified ZSM-5 In water at 480 - 485℃; under 1794.37 Torr; for 23.53h; Product distribution / selectivity;A n/a
B 15.54%
C n/a
H-ZSM-5(73) at 400℃; Product distribution; further catalysts (alumosilicates, modified zeolites);
Na(+)x(Mg3)(Si(4-x)Alx)O10(OH)2 at 349.9℃; for 1h; Product distribution; various pillared clays and zeolites as catalysts;
methanol
67-56-1

methanol

toluene
108-88-3

toluene

para-xylene
106-42-3

para-xylene

Conditions
ConditionsYield
With hydrogen In water at 400℃; under 3750.38 Torr; Reagent/catalyst; Pressure; Temperature; Concentration; Inert atmosphere;29.3%
With hydrogen at 250℃; Kinetics; Thermodynamic data; Further Variations:; pH-values;
silica bound HZSM-5 zeolite at 600℃; under 3620.13 - 4137.29 Torr; for 3.25 - 7.5h; Conversion of starting material;
4-Methylbenzyl alcohol
589-18-4

4-Methylbenzyl alcohol

benzamide
55-21-0

benzamide

A

para-xylene
106-42-3

para-xylene

B

N-(p-methylbenzyl)benzamide
65608-94-8

N-(p-methylbenzyl)benzamide

Conditions
ConditionsYield
With barium trifluoromethanesulfonate In toluene at 150℃; for 18h; Reagent/catalyst; Glovebox; Inert atmosphere;A 29%
B 72%
o-xylene
95-47-6

o-xylene

m-xylene
108-38-3

m-xylene

para-xylene
106-42-3

para-xylene

Conditions
ConditionsYield
With hydrogen; silicate ITQ-13, aluminium form at 360℃; under 10343.2 Torr; Product distribution / selectivity; fixed-bed downflow reactor;23.5%
MTW-zeolite/Al2O3 (Catalyst B) at 280℃; under 26618.1 Torr; Conversion of starting material; Liquid phase;
Ga-MFI zeolite/ZrO2/Al2O3 (Catalyst C) at 300℃; under 26618.1 Torr; Conversion of starting material; Liquid phase;
2,5-dimethylfuran
625-86-5

2,5-dimethylfuran

ethene
74-85-1

ethene

A

para-xylene
106-42-3

para-xylene

B

3,6-dimethylcyclohex-2-enone
15329-10-9

3,6-dimethylcyclohex-2-enone

C

2,5-hexanedione
110-13-4

2,5-hexanedione

Conditions
ConditionsYield
With H-BEA-25 In 1,4-dioxane at 249.84℃; under 15001.5 Torr; for 4h; Diels-Alder Cycloaddition; Autoclave; chemoselective reaction;
1,4-dimethylcyclohex-1-ene
2808-79-9

1,4-dimethylcyclohex-1-ene

para-xylene
106-42-3

para-xylene

Conditions
ConditionsYield
With palladium on activated charcoal In toluene at 130℃; under 7500.75 - 30003 Torr; for 3h; Autoclave;
1,4-dimethyl-7-oxa-bicyclo[2.2.1]heptane-2,3-dicarboxylic acid anhydride
111957-97-2

1,4-dimethyl-7-oxa-bicyclo[2.2.1]heptane-2,3-dicarboxylic acid anhydride

A

3,6-dimethyl phthalic anhydride
5463-50-3

3,6-dimethyl phthalic anhydride

B

para-xylene
106-42-3

para-xylene

Conditions
ConditionsYield
With zeolite Y with a silica-alumina at 200℃; for 2h; Temperature; Inert atmosphere;A 72%
B 17%
With 1 wtpercent Pd/C loaded on zeolite H-Y with a silica-alumina ratio of 40 In toluene at 200℃; under 750.075 Torr; for 4h; Inert atmosphere;
4-Methylbenzyl alcohol
589-18-4

4-Methylbenzyl alcohol

benzamide
55-21-0

benzamide

A

para-xylene
106-42-3

para-xylene

B

N-(p-methylbenzyl)benzamide
65608-94-8

N-(p-methylbenzyl)benzamide

C

N,N′‑(4‑methylbenzylidene)bisbenzamide
40891-10-9

N,N′‑(4‑methylbenzylidene)bisbenzamide

Conditions
ConditionsYield
With indium sulfate In toluene at 150℃; for 18h; Glovebox; Inert atmosphere;A 60%
B 14%
C 40%
With zinc(II) sulfate In toluene at 150℃; for 18h; Glovebox; Inert atmosphere;A 41%
B 58%
C 6%
With zinc(II) chloride In toluene at 150℃; for 18h; Glovebox; Inert atmosphere;A 47%
B 42%
C 21%
ethylbenzene
100-41-4

ethylbenzene

para-xylene
106-42-3

para-xylene

Conditions
ConditionsYield
With hydrogen at 480℃; under 8826.09 Torr; Leiten ueber Platin/Aluminiumoxid-Siliciumdioxid;
With hydrogen; 0.3 wtpercent Pt/0.1 wtpercent S/100 wtpercent MTW-zeolite (Catatalyst C) at 370 - 375℃; under 4650.47 Torr; Conversion of starting material;
With hydrogen; 0.3 wtpercent Pt/0.1 wtpercent S/50 wtpercent MTW/50 wtpercent mordenite (Catalyst F) at 370 - 375℃; under 4650.47 Torr; Conversion of starting material;
methanol
67-56-1

methanol

toluene
108-88-3

toluene

benzene
71-43-2

benzene

A

o-xylene
95-47-6

o-xylene

B

para-xylene
106-42-3

para-xylene

C

m-xylene
108-38-3

m-xylene

Conditions
ConditionsYield
With hydrogen; 1/16 inch extrudates which contained 65 weight percent H-ZSM-5 and 35 weight percent silica binder at 371.101℃; under 3309.83 Torr;
With hydrogen; 1/16 inch extrudates which contained 65 wt. percent H-ZSM-23 having a silica to alumina mole ratio of 110:1 and 35 wt. percent of alumina binder at 499.99℃; under 7757.43 Torr;
With hydrogen; SAPO-11 at 499.99℃; under 7757.43 Torr;
methanol
67-56-1

methanol

toluene
108-88-3

toluene

benzene
71-43-2

benzene

para-xylene
106-42-3

para-xylene

Conditions
ConditionsYield
With hydrogen; silica selectivated ZSM-5 at 371.101℃; under 10343.2 Torr;
4-methyl-benzaldehyde
104-87-0

4-methyl-benzaldehyde

A

4-Methylbenzyl alcohol
589-18-4

4-Methylbenzyl alcohol

B

para-xylene
106-42-3

para-xylene

Conditions
ConditionsYield
With triethylsilane; palladium dichloride In ethanol for 0.5h; Inert atmosphere;A 10.0 %Chromat.
B 88.5 %Chromat.
With palladium on silica; hydrogen In dodecane at 190℃; under 22502.3 Torr; for 5h;
With palladium on activated charcoal; hydrogen In water at 100℃; for 10h; chemoselective reaction;A 40 %Chromat.
B 60 %Chromat.
m-xylene
108-38-3

m-xylene

A

o-xylene
95-47-6

o-xylene

B

para-xylene
106-42-3

para-xylene

Conditions
ConditionsYield
With parent microporous ZSM-5 zeolite at 250℃; for 0.25h; Reagent/catalyst;A 27%
B 10%
With hydrogen; H-ZSM-5 at 349.9℃; under 15001.2 Torr; Product distribution; further catalysts, variation of temperature;
CVD boria-alumina at 450℃; Product distribution; dependence of conversion on B2O3 content of catalyst;
para-chlorotoluene
106-43-4

para-chlorotoluene

bis{μ-[2-(dimethylamino)ethanolato-N,O:O]}tetramethyldialuminum

bis{μ-[2-(dimethylamino)ethanolato-N,O:O]}tetramethyldialuminum

para-xylene
106-42-3

para-xylene

Conditions
ConditionsYield
With tri-tert-butyl phosphine; {MoPdcp[μ-(CO)2][μ3-(CO)](PPh3)}2 In benzene at 120℃; for 15h;98%
toluene
108-88-3

toluene

A

para-xylene
106-42-3

para-xylene

B

benzene
71-43-2

benzene

Conditions
ConditionsYield
With hydrogen; platinum-containing ZSM-5 molecular sieve catalyst at 420℃; under 11251.1 Torr;
With hydrogen; alumina-phosphate-bound MFI catalyst at 560℃; under 18376.8 Torr; Gas phase;
With hydrogen; alumina-phosphate-bound MFI catalyst at 560℃; under 18376.8 Torr; Gas phase;
4-Methylbenzyl alcohol
589-18-4

4-Methylbenzyl alcohol

benzamide
55-21-0

benzamide

A

para-xylene
106-42-3

para-xylene

B

N-(p-methylbenzyl)benzamide
65608-94-8

N-(p-methylbenzyl)benzamide

C

bis(4-methylbenzyl) ether
38460-98-9

bis(4-methylbenzyl) ether

Conditions
ConditionsYield
With tin(II) trifluoromethanesulfonate In toluene at 150℃; for 18h; Glovebox; Inert atmosphere;A 8%
B 33%
C 50%
With zinc trifluoromethanesulfonate In toluene at 150℃; for 18h; Reagent/catalyst; Glovebox; Inert atmosphere;A 33%
B 22%
C 21%
2,5-dimethylfuran
625-86-5

2,5-dimethylfuran

ethene
74-85-1

ethene

A

para-xylene
106-42-3

para-xylene

B

p-n-propyltoluene
1074-55-1

p-n-propyltoluene

C

2-ethyl-p-xylene
1758-88-9

2-ethyl-p-xylene

Conditions
ConditionsYield
With palladium-decorated gold nanoparticles anchored on amphoteric zirconia In n-heptane at 300℃; under 30402 Torr; for 6h;
2,5-dimethylfuran
625-86-5

2,5-dimethylfuran

ethene
74-85-1

ethene

A

4,4-dimethylcyclohexenone
1073-13-8

4,4-dimethylcyclohexenone

B

para-xylene
106-42-3

para-xylene

C

3,6-dimethylcyclohex-2-enone
15329-10-9

3,6-dimethylcyclohex-2-enone

Conditions
ConditionsYield
With Sn-BEA In n-heptane at 275℃; under 30402 Torr; for 1h;
triplal
854432-99-8

triplal

A

para-xylene
106-42-3

para-xylene

B

1,2,4-Trimethylbenzene
95-63-6

1,2,4-Trimethylbenzene

Conditions
ConditionsYield
With palladium/alumina; hydrogen In hexane at 325℃; Flow reactor; Green chemistry;A 84.8%
B 6.5%
With hydrogen In hexane at 325℃; Flow reactor; Green chemistry;A 19.5%
B 73.2%
4-Methylbenzyl chloride
104-82-5

4-Methylbenzyl chloride

A

para-xylene
106-42-3

para-xylene

B

1,2-di-p-tolylethane
538-39-6

1,2-di-p-tolylethane

Conditions
ConditionsYield
With copper nickel; pyrographite In 1,2-dimethoxyethane at 85℃; for 20h;A 10%
B 90%
With nickel In 1,2-dimethoxyethane for 2h; Ambient temperature;A 20%
B 76%
With magnesium at 600℃;A 23%
B 60%
With water; naphthalen-1-yl-lithium In tetrahydrofuran; diethyl ether; Petroleum ether at -95℃; for 0.75h; Title compound not separated from byproducts;A 64 % Chromat.
B 36 % Chromat.
methanol
67-56-1

methanol

toluene
108-88-3

toluene

A

para-xylene
106-42-3

para-xylene

B

m-xylene
108-38-3

m-xylene

Conditions
ConditionsYield
With Ga2O3 zeolite; silica gel In gas at 400℃; Product distribution; var. catalyst, var. temp.;
With hydrogen; Catalyst G (prepared from NH4-ZSM-5 and H3PO4) at 200 - 500℃; under 1034.32 Torr; Product distribution / selectivity;
With hydrogen; Catalyst H (prepared from NH4-ZSM-5 and H3PO4) at 200 - 500℃; under 1034.32 Torr; Product distribution / selectivity;
carbon monoxide
201230-82-2

carbon monoxide

p-xylylene glycol
589-29-7

p-xylylene glycol

A

para-xylene
106-42-3

para-xylene

B

1,4-phenylenediacetic acid
7325-46-4

1,4-phenylenediacetic acid

C

4-tolylacetic acid
622-47-9

4-tolylacetic acid

Conditions
ConditionsYield
With hydrogen iodide; tetrakis(triphenylphosphine) palladium(0) In acetone at 90℃; under 68400 Torr; for 42h; Carbonylation; reduction;A n/a
B 48%
C 16%
methanol
67-56-1

methanol

toluene
108-88-3

toluene

benzene
71-43-2

benzene

A

o-xylene
95-47-6

o-xylene

B

para-xylene
106-42-3

para-xylene

C

ethylbenzene
100-41-4

ethylbenzene

D

m-xylene
108-38-3

m-xylene

Conditions
ConditionsYield
With hydrogen; silicon-selectivated H-ZSM-5/silica bound at 371.101℃; under 10343.2 Torr;
With hydrogen; zeolite bound zeolite at 371.101℃; under 10343.2 Torr;
o-xylene
95-47-6

o-xylene

ethylbenzene
100-41-4

ethylbenzene

m-xylene
108-38-3

m-xylene

para-xylene
106-42-3

para-xylene

Conditions
ConditionsYield
catalyst contained 15.0percentw EU-1 zeolite in H form, 84.7percentw Al2O3, 0.3percentw Pt and treated with dimethyldisulphide at 390℃; under 11251.1 Torr; Product distribution / selectivity;
catalyst contained 15.0percentw NU-87 zeolite in H form, 84.7percentw Al2O3, 0.3percentw Pt and treated with dimethyldisulphide at 390℃; under 11251.1 Torr; Product distribution / selectivity;
catalyst contained 8.0percentw EU-1 zeolite in H form, 7.0percentw NU-87 zeolite in H form, 84.7percentw Al2O3, 0.15percentw Pt, 0.15percentw Re and treated with dimethyldisulphide at 390℃; under 11251.1 Torr; Product distribution / selectivity;
4-Methylbenzyl alcohol
589-18-4

4-Methylbenzyl alcohol

para-xylene
106-42-3

para-xylene

Conditions
ConditionsYield
With palladium dichloride In methanol at 40℃; for 18h; Inert atmosphere; Green chemistry; chemoselective reaction;99%
Multi-step reaction with 2 steps
1: hydrogen; / 350 °C / 760.05 Torr
2: hydrogen; / 350 °C / 760.05 Torr
View Scheme
With formic acid; methanesulfonic acid; 1,2-bis((di-tert-butylphosphoryl)methyl)benzene; palladium(II) acetylacetonate; 1,2-bis[di(t-butyl)phosphinomethyl]benzene In 1,2-dichloro-ethane at 100℃; for 18h; Schlenk technique; Sealed tube; Inert atmosphere;93 %Chromat.
With 2,4,6-trimethyl-pyridine; 4,4'-dimethoxyphenyl disulfide; iridium(lll) bis[2-(2,4-difluorophenyl)-5-methylpyridine-N,C20]-4,40-di-tert-butyl-2,20-bipyridine hexafluorophosphate; triphenylphosphine In toluene for 24h; Irradiation;63 %Chromat.
carbon monoxide
201230-82-2

carbon monoxide

toluene
108-88-3

toluene

A

o-xylene
95-47-6

o-xylene

B

para-xylene
106-42-3

para-xylene

C

m-xylene
108-38-3

m-xylene

Conditions
ConditionsYield
With hydrogen at 400℃; under 24549.5 Torr; Temperature; Flow reactor; Inert atmosphere;
para-xylene
106-42-3

para-xylene

4-bromo-m-xylene
553-94-6

4-bromo-m-xylene

Conditions
ConditionsYield
With potassium bromide; sodium nitrite In water; trifluoroacetic acid at 20℃; for 0.16h; Product distribution; under argon;100%
With oxygen; potassium bromide; sodium nitrite In water; trifluoroacetic acid at 20℃; for 5h; Product distribution;96%
With sulfuric acid; dihydrogen peroxide; sodium bromide In water at 49.84℃;94%
para-xylene
106-42-3

para-xylene

mononitro-p-xylene
89-58-7

mononitro-p-xylene

Conditions
ConditionsYield
With zeolite ZSM-5-60; Nitrogen dioxide100%
With nitric acid; sulfuric acid In dichloromethane at 25℃; for 0.7h;100%
With nitric acid In toluene at 60℃; for 2h;98%
para-xylene
106-42-3

para-xylene

4-methyl-benzaldehyde
104-87-0

4-methyl-benzaldehyde

Conditions
ConditionsYield
With oxygen; 10-methyl-9-phenylacridin-10-ium perchlorate In chloroform at 24.84℃; for 10h; Oxidation; Pyrolysis; visible light;100%
With sulfuric acid; 9-mesityl-2,7,10-trimethylacridinium perchlorate; water; oxygen In acetonitrile at 24.84℃; for 1.33333h; Quantum yield; Reagent/catalyst; Irradiation;100%
With N-hydroxyphthalimide; oxygen; cobalt(II) acetate; acetic acid at 20℃; under 760.051 Torr; chemoselective reaction;100%
para-xylene
106-42-3

para-xylene

4-Methylbenzyl bromide
104-81-4

4-Methylbenzyl bromide

Conditions
ConditionsYield
With bromine In tetrachloromethane Solvent;100%
With 2,4,4,6-Tetrabromo-2,5-cyclohexadien-1-one; silica gel for 4.5h; UV-irradiation;84%
With bromine In tetrachloromethane for 1.5h; Ambient temperature;83%
para-xylene
106-42-3

para-xylene

1,4 dimethylcyclohexane
589-90-2

1,4 dimethylcyclohexane

Conditions
ConditionsYield
With hydrogen; [(norbornadiene)rhodium(I)chloride]2; phosphinated polydiacetylene In n-heptane at 30℃; under 60800 Torr; for 1.5h;100%
With Ti8O8(14+)*6C8H4O4(2-)*4O(2-)*3.3Li(1+)*0.7Co(2+)*0.7C4H8O*0.7H(1-); hydrogen In neat (no solvent) at 120℃; under 37503.8 Torr; for 18h;100%
With hydrogen at 150℃; under 2280.15 Torr; for 0.5h; Kinetics; Reagent/catalyst; Temperature;100%
para-xylene
106-42-3

para-xylene

benzoyl chloride
98-88-4

benzoyl chloride

2,5-dimethylbenzophenone
4044-60-4

2,5-dimethylbenzophenone

Conditions
ConditionsYield
With tris(fluorosulphonyl)methane at 138℃; for 3h;100%
Hf[N(SO2C8F17)2]4 In various solvent(s) at 120℃; for 3h;98%
With C4F9SO3H at 138℃; for 5h;91%
[Cp*Ru(CH3CN)3]OTf
113860-02-9

[Cp*Ru(CH3CN)3]OTf

para-xylene
106-42-3

para-xylene

{C5(CH3)5}Ru{C6H4(CH3)2}(1+)*CF3SO3(1-)={(C5(CH3)5)Ru(C6H4(CH3)2)}(CF3SO3)

{C5(CH3)5}Ru{C6H4(CH3)2}(1+)*CF3SO3(1-)={(C5(CH3)5)Ru(C6H4(CH3)2)}(CF3SO3)

Conditions
ConditionsYield
In tetrahydrofuran byproducts: CH3CN; under N2; addn. of Ru-complex to p-xylene and THF (benzene-free), mixt. stirred (30°C); addn. of hexane, solid filtered, washed twice (hexane), dried (vac.), elem. anal.;100%
para-xylene
106-42-3

para-xylene

3-nitro-benzaldehyde
99-61-6

3-nitro-benzaldehyde

allyl-trimethyl-silane
762-72-1

allyl-trimethyl-silane

tetrahydro-4-(2,5-dimethylphenyl)-2,6-bis(3-nitrophenyl)-2H-pyran
1157865-90-1

tetrahydro-4-(2,5-dimethylphenyl)-2,6-bis(3-nitrophenyl)-2H-pyran

Conditions
ConditionsYield
With boron trifluoride diethyl etherate at 0 - 20℃; for 2h; Sakurai-Hosomi-Prins-Friedel-Crafts reaction; stereoselective reaction;100%
para-xylene
106-42-3

para-xylene

C6H6*C33H30N12S3
1280197-89-8

C6H6*C33H30N12S3

0.25C8H10*C33H30N12S3

0.25C8H10*C33H30N12S3

Conditions
ConditionsYield
at 40℃; for 480h; Gas phase;100%
4-tert-Butylbenzyl alcohol
877-65-6

4-tert-Butylbenzyl alcohol

para-xylene
106-42-3

para-xylene

2-(4-(tert-butyl)benzyl)-1,4-dimethylbenzene

2-(4-(tert-butyl)benzyl)-1,4-dimethylbenzene

Conditions
ConditionsYield
With (diethylamino)difluorosulfonium tetrafluoroborate In dichloromethane at 20℃; for 4h; Inert atmosphere;100%
para-xylene
106-42-3

para-xylene

(6-bromo-2-methylimidazo[1,2-a]pyridin-3-yl)methanol

(6-bromo-2-methylimidazo[1,2-a]pyridin-3-yl)methanol

6-bromo-3-[(2,5-dimethylphenyl)methyl]-2-methylimidazo[1,2-a]pyridine

6-bromo-3-[(2,5-dimethylphenyl)methyl]-2-methylimidazo[1,2-a]pyridine

Conditions
ConditionsYield
With methanesulfonic acid at 100℃; for 1h;100%
para-xylene
106-42-3

para-xylene

2-bromo-5-chlorobenzyl bromide
66192-24-3

2-bromo-5-chlorobenzyl bromide

2-(2-bromo-5-chlorobenzyl)-1,4-dimethylbenzene

2-(2-bromo-5-chlorobenzyl)-1,4-dimethylbenzene

Conditions
ConditionsYield
With indium(III) bromide In dichloromethane for 6h; Schlenk technique; Inert atmosphere; Molecular sieve;100%
para-xylene
106-42-3

para-xylene

terephthalic acid
100-21-0

terephthalic acid

Conditions
ConditionsYield
With ammonium acetate; water; hydrogen bromide; oxygen; manganese(II) acetate; cobalt(II) diacetate tetrahydrate; 1-n-butyl-3-methylimidazolim bromide; acetic acid at 200℃; under 30753.1 Torr; for 10h; Time; Temperature; Reagent/catalyst; Concentration; Inert atmosphere;99.9%
With oxovanadium(IV) sulfate; hydrogen bromide; oxygen; acetic acid In water at 100℃; under 750.075 Torr; for 20h;98%
With oxygen; acetic acid; hydrogen bromide; cobalt(II) acetate; manganese(II) acetate In water at 200℃; under 22502.3 Torr; for 0.05h; Product distribution / selectivity; Inert atmosphere;98.3%
para-xylene
106-42-3

para-xylene

p-Xylylene dichloride
623-25-6

p-Xylylene dichloride

Conditions
ConditionsYield
With chlorine; 3-butyl-1,2-dimethylimidazolium chloride In perfluoroheptane at 84℃; for 3h; Temperature; Solvent;99.11%
With chlorine; 3-butyl-1,2-dimethylimidazolium chloride at 120℃; for 3h; Reagent/catalyst; Temperature; Ionic liquid; Irradiation;99.1%
durch Chlorieren;
para-xylene
106-42-3

para-xylene

p-benzylchloride

p-benzylchloride

Conditions
ConditionsYield
Stage #1: para-xylene With 1-dodecyl-3-methylimidazol-1-ium chloride at 110℃; Irradiation;
Stage #2: With chlorine at 90 - 120℃; Reagent/catalyst; Temperature; Reflux;
99.11%
1,1-Diphenylmethanol
91-01-0

1,1-Diphenylmethanol

para-xylene
106-42-3

para-xylene

((2,5-dimethylphenyl)methylene)dibenzene
7249-83-4

((2,5-dimethylphenyl)methylene)dibenzene

Conditions
ConditionsYield
With silica gel supported sodium hydrogen sulfate at 80℃; for 0.5h; Friedel-Crafts type alkylation;99%
With H5CoW12O40 supported on rice husk ash extracted nano silica at 60℃; for 0.666667h; Reagent/catalyst; Green chemistry;98%
With Fe3O4/FeO at 60℃; for 0.333333h; Green chemistry;92%
para-xylene
106-42-3

para-xylene

p-Toluic acid
99-94-5

p-Toluic acid

Conditions
ConditionsYield
With tert.-butylhydroperoxide; water at 20℃; for 10h; Inert atmosphere;99%
With N-hydroxy-tetrahydrophthalimide; oxygen; nitric acid at 50℃; under 750.075 - 1500.15 Torr; for 25h; Autoclave; Green chemistry;91.16%
With MoO(O2)(8-quinolinolate)2; dihydrogen peroxide In acetonitrile for 6h; Oxidation; Heating;88%
para-xylene
106-42-3

para-xylene

acetyl chloride
75-36-5

acetyl chloride

1-(2,5-dimethylphenyl)-1-ethanone
2142-73-6

1-(2,5-dimethylphenyl)-1-ethanone

Conditions
ConditionsYield
With aluminum (III) chloride In chloroform at 0 - 20℃; Inert atmosphere;99%
With aluminum (III) chloride In carbon disulfide at 0 - 20℃; Friedel Crafts acylation; Inert atmosphere;95%
Friedel-Crafts alkylation;90%
para-xylene
106-42-3

para-xylene

benzoic acid anhydride
93-97-0

benzoic acid anhydride

2,5-dimethylbenzophenone
4044-60-4

2,5-dimethylbenzophenone

Conditions
ConditionsYield
sulfated zirconia at 100℃; for 2h; Product distribution; Further Variations:; Catalysts; Friedel-Crafts acylation;99%
With C4F9SO3H at 138℃; for 5h;93%
para-xylene
106-42-3

para-xylene

1-bromomethyl-4-bromobenzene
589-15-1

1-bromomethyl-4-bromobenzene

1,4-dimethyl-2-(4-bromobenzyl)benzene

1,4-dimethyl-2-(4-bromobenzyl)benzene

Conditions
ConditionsYield
With indium(III) chloride; 4 A molecular sieve In dichloromethane at 20℃; for 16h; Friedel-Crafts alkylation;99%
With potassium cyanide; aluminum oxide at 50℃; for 5h;83 % Chromat.

106-42-3Related news

Structural analysis of liquid 1,4-Dimethylbenzene (cas 106-42-3) at 293 K08/19/2019

Structural analysis of liquid 1,4-dimethylbenzene C6H4(CH3)2 by X-ray monochromatic radiation scattering method was performed. The X-ray measurements were made at room temperature for the scattering angle range Θ varying from 3 to 60°. The most probable parameters of 1,4-dimethylbenzene molecu...detailed

106-42-3Relevant articles and documents

Boosting the synthesis of value-added aromatics directly from syngasviaa Cr2O3and Ga doped zeolite capsule catalyst

Gao, Weizhe,Gao, Xinhua,Ma, Qingxiang,Tsubaki, Noritatsu,Wang, Kangzhou,Wang, Yang,Wu, Mingbo,Yang, Guohui,Zhang, Baizhang,Zhang, Peipei,Zhao, Heng

, p. 7786 - 7792 (2021)

Even though the transformation of syngas into aromatics has been realizedviaa methanol-mediated tandem process, the low product yield is still the bottleneck, limiting the industrial application of this technology. Herein, a tailor-made zeolite capsule catalyst with Ga doping and SiO2coating was combined with the methanol synthesis catalyst Cr2O3to boost the synthesis of value-added aromatics, especiallypara-xylene, from syngas. Multiple characterization studies, control experiments, and density functional theory (DFT) calculation results clarified that Ga doped zeolites with strong CO adsorption capability facilitated the transformation of the reaction intermediate methanol by optimizing the first C-C coupling step under a high-pressure CO atmosphere, thereby driving the reaction forward for aromatics synthesis. This work not only reveals the synergistic catalytic network in the tandem process but also sheds new light on principles for the rational design of a catalyst in terms of oriented conversion of syngas.

A Facile Solid-Phase Route to Renewable Aromatic Chemicals from Biobased Furanics

Thiyagarajan, Shanmugam,Genuino, Homer C.,Van Der Waal, Jan C.,De Jong, Ed,Weckhuysen, Bert M.,Van Haveren, Jacco,Bruijnincx, Pieter C. A.,Van Es, Daan S.

, p. 1368 - 1371 (2016)

Renewable aromatics can be conveniently synthesized from furanics by introducing an intermediate hydrogenation step in the Diels-Alder (DA) aromatization route, to effectively block retro-DA activity. Aromatization of the hydrogenated DA adducts requires tandem catalysis, using a metal-based dehydrogenation catalyst and solid acid dehydration catalyst in toluene. Herein it is demonstrated that the hydrogenated DA adducts can instead be conveniently converted into renewable aromatics with up to 80 % selectivity in a solid-phase reaction with shorter reaction times using only an acidic zeolite, that is, without solvent or dehydrogenation catalyst. Hydrogenated adducts from diene/dienophile combinations of (methylated) furans with maleic anhydride are efficiently converted into renewable aromatics with this new route. The zeolite H-Y was found to perform the best and can be easily reused after calcination. Just heat and tumble: Furanics-derived hydrogenated Diels-Alder adducts can be conveniently converted, over acidic zeolites, into renewable aromatics using a solid-phase conversion strategy. The zeolite H-Y was found to perform the best and can be easily reused after calcination.

Vapor phase alkylation of toluene using various alcohols over H 3PO4/MCM-41 catalyst: Influence of reaction parameters on selectivity and conversion

Abbaspourrad, Alireza,Kalbasi, Roozbeh Javad,Zamani, Farzad

, p. 875 - 885 (2010)

A mesoporous MCM-41 molecular sieve material with a molar ratio of SiO 2/Al2 O3 = 70 and loaded with H3 PO4 was used as a catalyst for the alkylation of toluene, using various alcohols, namely methanol, iso-propanol, and tert-butanol, as alkylating agents. Para-alkylated toluene was the predominant product, formation of which was enhanced by moderate temperature, low amounts of the alkylating agents in the feed, and high carrier gas flow rate. Time on stream was found to exert a profound effect on the selectivity and conversion to the different products. TUeBITAK.

Continuous process for the production of aromatic hydrocarbons from n-hexane and C5+ natural gas liquid over Pd-loaded ZSM-5 zeolite

Suwanprasop, Somsaluay,Khamnuansiri, Pharkpoom,Nhujak, Thumnoon,Roengsumran, Sophon,Petsom, Amorn

, p. 577 - 582 (2003)

A continuous process for the production of aromatic hydrocarbons from n-hexane and C5+ natural gas liquid (C5+ NGL) over Pd-loaded ZSM-5 zeolite in a tubular reactor was developed. The optimal conditions for continuous aromatization of n-hexane and C5+ NGL were found at 400°C reaction temperature and 0.4 cm3/min reactant feeding rate, employing ZSM-5 (0.5% Pd content) as a catalyst; under these conditions, n-hexane conversion and aromatic contents in reaction product were found to be 99.7% and 92.3%, respectively. GC and GC/MS analysis revealed that this continuous process for n-hexane aromatization yielded both benzene derivatives and naphthalene derivatives, including benzene (5.7%), toluene (23.6%), xylenes (25.0%), 4-ethyltoluene (3.5%), 1,3,5-trimethylbenzene (4.9%), 1-methylnaphthalene (4.3%), and 1,5-dimethylnaphthalene (3.6%). Under the same reaction conditions, C5+ NGL gave 94.3% conversion and 92.6% aromatic contents in reaction product. The composition of product included benzene (8.1%), toluene (23.3%), xylenes (22.8%), 4-ethyltoluene (4.3%), 1,3,5-trimethylbenzene (3.7%), 1-methylnaphthalene (4.1%), and 1,5-dimethylnaphthalene (2.9%).

Post-synthesis modification of TUN zeolite: Textural, acidic and catalytic properties

Kub, Martin,?ilková, Nadě?da,?ejka, Ji?í

, p. 63 - 70 (2011)

Dealumination, desilication and silylation of TUN zeolite was investigated and related to the catalytic behavior in toluene disproportionation and its alkylation with isopropyl alcohol. Only negligible concentration of acid sites was identified on the "external" surface of parent TUN zeolite and this concentration increased with increasing desilication. Silylation resulted in channel narrowing and probably some plugging. As a result, significant increase in the para-selectivity in toluene disproportionation and its alkylation with isopropyl alcohol was achieved. No changes in toluene conversion were observed for all parent and modified samples in toluene alkylation confirming diffusion and transport of products as the rate determining step in 10-ring zeolites. Selectivity to cymenes and p-cymene decreased with dealumination as well as desilication. In contrast, silylation increased both cymene (80%) and p-cymene (90%) selectivity in toluene alkylation.

Destruction of halogenated hydrocarbons with solvated electrons in the presence of water

Sun, Guang-Ri,He, Jin-Bao,Pittman Jr., Charles U.

, p. 907 - 916 (2000)

Model halogenated aromatic and aliphatic hydrocarbons and halogenated phenols were dehalogenated in seconds by solvated electrons generated from sodium in both anhydrous liquid ammonia and ammonia/water solutions. The minimum sodium required to completely dehalogenate these model compounds was determined by increasing the Na/substrate ratio until halogen loss was complete. Minimum sodium consumptions were determined in both anhydrous liquid ammonia and with a (5, 20, 50-fold molar excess of water per mole of halide). While more Na was consumed in the presence of water, these dehalogenations were still efficient when a 50-fold water excess was present. Dehalogenation is faster than competiting reactions with water. CCl4 and CH3CCl3 in the presence of a stoichiometric deficiency of sodium produced only CH4 and CH3CH3 and recovered CCl44 or CH3CCl3, respectively. No partially dechlorinated products were detected, indicating dechlorination was diffusion controlled. Na consumption per chlorine removed (as NaCl) was lower than that of Li, K or Ca and this advantage increased in the presence of water. Na consumption was lower using Na chunks instead of a thin Na mirror. Chloroaromatic compounds gave the parent aromatic hydrocarbon and aminated products in anhydrous ammonia but aminated products did not form when water was present. (C) 2000 Elsevier Science Ltd.

Pyrolysis of 3-carene: Experiment, Theory and Modeling

Sharath,Chakravarty,Reddy,Barhai,Arunan

, p. 2119 - 2135 (2015)

Thermal decomposition studies of 3-carene, a bio-fuel, have been carried out behind the reflected shock wave in a single pulse shock tube for temperature ranging from 920 K to 1220 K. The observed products in thermal decomposition of 3-carene are acetylene, allene, butadiene, isoprene, cyclopentadiene, hexatriene, benzene, toluene and p-xylene. The overall rate constant for 3-carene decomposition was found to be k / s-1 = 10(9.95 ± 0.54) exp (- 40.88 ± 2.71 kcal mol-1/RT). Ab-initio theoretical calculations were carried out to find the minimum energy pathway that could explain the formation of the observed products in the thermal decomposition experiments. These calculations were carried out at B3LYP/6-311 + G(d,p) and G3 level of theories. A kinetic mechanism explaining the observed products in the thermal decomposition experiments has been derived. It is concluded that the linear hydrocarbons are the primary products in the pyrolysis of 3-carene.

A facile strategy to prepare shaped ZSM-5 catalysts with enhanced para-xylene selectivity and stability for toluene methylation: The effect of in situ modification by attapulgite

Wang, Yiren,Chang, Yang,Liu, Min,Zhang, Anfeng,Guo, Xinwen

, (2019)

A general strategy for preparing shaped toluene methylation catalysts with enhanced para-selectivity and stability is developed by extruding ZSM-5 zeolite with attapulgite as a binder. The novel attapulgite/ZSM-5 extrudate exhibited significantly higher para-selectivity and stability in comparison to the conventional alumina-bound ZSM-5 extrudate. The catalyst samples have been characterized by in situ X-ray diffraction, scanning electron microscope (SEM), NH3 temperature programmed desorption (TPD), thermogravimetric analysis (TGA) as well as n-hexane/cyclohexane physical adsorption. The enhanced catalytic performance of attapulgite/ZSM-5 extrudate is correlated with the in-situ modification of acid sites in the catalyst by mobile alkaline species, which is introduced via extrusion with attapulgite. Moreover, a higher para-selectivity was obtained over attapulgite-bound modified ZSM-5 extrudate. Such facile and universal strategy of extruding ZSM-5 catalysts with attapulgite as binder could pave a way for preparation of shaped zeolite-base catalyst with enhanced catalytic performance.

Renewable p-Xylene from 2,5-Dimethylfuran and Ethylene Using Phosphorus-Containing Zeolite Catalysts

Cho, Hong Je,Ren, Limin,Vattipalli, Vivek,Yeh, Yu-Hao,Gould, Nicholas,Xu, Bingjun,Gorte, Raymond J.,Lobo, Raul,Dauenhauer, Paul J.,Tsapatsis, Michael,Fan, Wei

, p. 398 - 402 (2017)

p-Xylene is a major commodity chemical used for the production of polyethylene terephthalate, a polymer with applications in polyester fibers, films, and bottles. The Diels–Alder cycloaddition of 2,5-dimethylfuran and ethylene and the subsequent dehydration of the cycloadduct intermediate is an attractive reaction pathway to produce renewable p-xylene from biomass feedstocks. However, the highest yields reported previously do not exceed 75 %. We report that P-containing zeolite Beta is an active, stable, and selective catalyst for this reaction with an unprecedented p-xylene yield of 97 %. It can catalyze the dehydration reaction selectively from the furan-ethylene cycloadduct to p-xylene without the production of alkylated and oligomerized products. This behavior is distinct from that of Al-containing zeolites and other solid phosphoric acid catalysts and establishes a commercially attractive process for renewable p-xylene production.

Diels-Alder and dehydration reactions of furan derivatives with ethylene catalyzed by liquid Br?nsted acids and Lewis acids

Song, Song,Wu, Guangjun,Dai, Weili,Guan, Naijia,Li, Landong

, p. 134 - 141 (2016)

The tandem Diels-Alder and dehydration reactions of furan derivatives with ethylene represent a promising approach for the production of renewable aromatics. Herein, a series of haloacetic acids and rare-earth metal triflates are employed as liquid Br?nsted and Lewis acid catalysts, respectively, in the Diels-Alder and dehydration reactions of 2,5-dimethylfuran with ethylene to get an insight of this type of acid-catalyzed reaction. With the carefully selected catalysts and solvent, a quasi-homogeneous reaction system can be formed, where accurate kinetic studies could be performed. Haloacetic acids exhibit considerable activity in the Diels-Alder and dehydration reactions with a similar apparent activity energy value of ~8.4 kcal/mol, and CF2ClCOOH with a proper Br?nsted acidity is optimized for the reaction. Rare-earth metal triflates also exhibit considerable activity in the Diels-Alder and dehydration reactions with a similar apparent activity energy value of ~13.0 kcal/mol, and Sc(OTf)3 with the highest Lewis acidity is optimized. On the basis of kinetic analysis results, the impacts of acidity on the performance of catalysts are discussed in detail and the reaction network is proposed. Besides, the substrate scope of furan derivatives for the Diels-Alder and dehydration reactions with ethylene is investigated using CF2ClCOOH and Sc(OTf)3 as catalysts for possible extensions of the reaction.

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