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Maleic anhydride (MAN) is an organic compound with the chemical formula C4H2O3. It is the acid anhydride of maleic acid and in its pure state, it is a colorless or white solid with an acrid odor. Possessing two types of chemical functionality, maleic anhydride is a multifunctional chemical intermediate that is uniquely useful in chemical synthesis and applications.

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  • 108-31-6 Structure
  • Basic information

    1. Product Name: Maleic anhydride
    2. Synonyms: TOXILIC ANHYDRIDE;2,5-FURANDIONE;MA;MAN;MALEIC ACID ANHYDRIDE;MALEIC ANHYDRIDE;CIS-BUTENEDIOIC ANHYDRIDE;cis-Butenedioic anhydrides Maleic anhydride
    3. CAS NO:108-31-6
    4. Molecular Formula: C4H2O3
    5. Molecular Weight: 98.05688
    6. EINECS: 203-571-6
    7. Product Categories: Miscellaneous;Organics;Building Blocks;Carbonyl Compounds;Carboxylic Acid Anhydrides;Chemical Synthesis;Organic Building Blocks;Heterocycles;Intermediates & Fine Chemicals;Pharmaceuticals
    8. Mol File: 108-31-6.mol
  • Chemical Properties

    1. Melting Point: 51-56 °C(lit.)
    2. Boiling Point: 200 °C(lit.)
    3. Flash Point: 218 °F
    4. Appearance: White/powder
    5. Density: 1.48
    6. Vapor Density: 3.4 (vs air)
    7. Vapor Pressure: 0.16 mm Hg ( 20 °C)
    8. Refractive Index: 1.4688 (estimate)
    9. Storage Temp.: Store at RT.
    10. Solubility: N/A
    11. PKA: 0[at 20 ℃]
    12. Explosive Limit: 1.4-7.1%(V)
    13. Water Solubility: 79 g/100 mL (25 ºC)
    14. Sensitive: Moisture Sensitive
    15. Stability: Stable. Combustible. Incompatible with water, strong oxidizing agents, alkali metals, strong bases, amines, most common metals,
    16. Merck: 14,5704
    17. BRN: 106909
    18. CAS DataBase Reference: Maleic anhydride(CAS DataBase Reference)
    19. NIST Chemistry Reference: Maleic anhydride(108-31-6)
    20. EPA Substance Registry System: Maleic anhydride(108-31-6)
  • Safety Data

    1. Hazard Codes: C
    2. Statements: 22-34-42/43
    3. Safety Statements: 22-26-36/37/39-45
    4. RIDADR: UN 2215 8/PG 3
    5. WGK Germany: 1
    6. RTECS: ON3675000
    7. F: 21
    8. TSCA: Yes
    9. HazardClass: 8
    10. PackingGroup: III
    11. Hazardous Substances Data: 108-31-6(Hazardous Substances Data)

108-31-6 Usage

Chemical Description

Maleic anhydride is an organic compound used in the production of polyester resins and other chemicals.

Chemical Description

Maleic anhydride is an organic compound with the formula C4H2O3.

Chemical Description

Maleic anhydride is an organic compound with a cyclic anhydride functional group.

Uses

Used in Chemical Synthesis:
Maleic anhydride is used as a dienophile in Diels-Alder syntheses, a widely employed method in organic chemistry for creating six-membered rings.
Used in Manufacturing Alkyd Resins:
Maleic anhydride is used in the production of alkyd-type resins, which are important in the formulation of coatings, inks, and adhesives.
Used in Dyestuff Industry:
It serves as a dye intermediate, contributing to the manufacturing process of various dyes.
Used in Pharmaceutical Industry:
Maleic anhydride is used in the production of pharmaceuticals, given its role as a key intermediate in the synthesis of several drugs.
Used in Agricultural Chemicals:
It is a precursor for the synthesis of agricultural chemicals such as maleic hydrazide and malathion, which are used in the production of herbicides and insecticides.
Used in Copolymerization Reactions:
Maleic anhydride is utilized in copolymerization reactions to produce a variety of polymers with specific properties.
Used in Unsaturated Polyester Resins (UPR) Production:
As a major end-use feedstock, maleic anhydride is used in the manufacture of unsaturated polyester resins, which have applications in construction, marine, and automobile industries.
Used in Synthetic Tensides, Insecticides, Herbicides, and Fungicides:
Maleic anhydride is employed in the synthesis of these substances for use in various industries.
Used in the Production of 1,4-Butanediol (BDO), Gamma-Butyrolactone, and Tetrahydrofuran (THF):
These chemicals are derived from maleic anhydride and have a wide range of applications, with BDO being one of the world's fastest-growing chemicals.
Physical Properties:
Maleic anhydride is a white, hydroscopic crystalline substance, often shipped as briquettes. It has an odor threshold concentration of 0.32 ppm and melts at 113°F. It is shipped both as a solid and in the molten state, and its vapors, fumes, and dusts can be strong irritants to the eyes, skin, and mucous membranes.
Chemical Properties:
In its pure form, maleic anhydride appears as colorless needles, white lumps, or pellets. It has an irritating, choking odor and dissolves in water to produce maleic acid. It also dissolves in ethanol and can produce esters.

Production Methods

Maleic anhydride was traditionally manufactured by the oxidation of benzene or other aromatic compounds. As of 2006, only a few smaller plants continue to use benzene; due to rising benzene prices, most maleic anhydride plants now use n-butane as a feedstock. In both cases, benzene and butane are fed into a stream of hot air, and the mixture is passed through a catalyst bed at high temperature. The ratio of air to hydrocarbon is controlled to prevent the mixture from catching on fire. Vanadium pentoxide and molybdenum trioxide are the catalysts used for the benzene route, whereas vanadium and phosphorus oxides are used for the butane route. 2 CH3CH2CH2CH3 + 7 O2 → 2 C2H2(CO)2O + 8 H2O.

Preparation

To a flask equipped with a Dean-Stark trap, condenser, and mechanical stirrer is added 116 gm (1.0 mole) of maleic acid and 120 ml of tetrachloroethane. The contents are heated, the water (18 ml, 1.0 mole) distilled off as the azeotrope, and the residue distilled under reduced pressure to afford 87.7 gm (89.5%) of the anhydride, b.p. 82-84°C (15 mm), m.p. 53°C. The residue remaining in the flask consists of about 10 gm of fumaric acid, m.p. 287°C. Fumaric and maleic acids both give maleic anhydride on heating. Fumaric acid must first be heated to a higher temperature to effect its conversion to maleic acid prior to its dehydration.

Reactions

The chemistry of maleic anhydride is very rich, reflecting its ready availability and bifunctional reactivity. It hydrolyzes, producing maleic acid, cis-HOOC–CH=CH–COOH. With alcohols, the halfester is generated, e.g., cis-HOOC–CH=CH–COOCH3. Maleic anhydride is a potent dienophile in Diels-Alder reactions. It is also a ligand for low-valent metal complexes, examples being Pt(PPh3)2(MA) and Fe(CO)4(MA). Maleic anhydride dimerizes in a photochemical reaction to form cyclo butane tetra carboxylic dianhydride (CBTA). This compound is used in the production of polyimides and as an alignment film for liquid crystal displays.

Synthesis Reference(s)

The Journal of Organic Chemistry, 60, p. 6676, 1995 DOI: 10.1021/jo00126a013

Air & Water Reactions

Soluble in water. Reacts slowly with water to form maleic acid and heat.

Reactivity Profile

Maleic anhydride react vigorously on contact with oxidizing materials. Reacts exothermically with water or steam. Undergoes violent exothermic decomposition reactions, producing carbon dioxide, in the presence of strong bases (sodium hydroxide, potassium hydroxide, calcium hydroxide), alkali metals (lithium, sodium, potassium), aliphatic amines (dimethylamine, trimethylamine), aromatic amines (pyridine, quinoline) at temperatures above 150° C [Vogler, C. A. et al., J. Chem. Eng. Data, 1963, 8, p. 620]. A 0.1% solution of pyridine (or other tertiary amine) in Maleic anhydride at 185°C gives an exothermic decomposition with rapid evolution of gas [Chem Eng. News 42(8); 41 1964]. Maleic anhydride is known as an excellent dienophile in the Diels-Alder reaction to produce phthalate ester derivatives. These reactions can be extremely violent, as in the case of 1-methylsilacyclopentadiene [J. Organomet., Chem., 1979, 179, c19]. Maleic anhydride undergoes a potentially explosive exothermic Diels-Alder reaction with 1-methylsilacyclopenta-2,4-diene at 150C [Barton, T. J., J. Organomet. Chem., 1979, 179, C19], and is considered an excellent dieneophile for Diels-alder reactions [Felthouse, Timothy R. et al. "Maleic anhydride , Maleic Acid, and Fumaric Acid." Kirk-Othmer Encyclopedia of Chemical Technology. John Wiley & Sons, Inc. 2005].

Hazard

Irritant to tissue. Dermal and respiratory sensitization. Questionable carcinogen.

Health Hazard

Inhalation causes coughing, sneezing, throat irritation. Skin contact causes irritation and redness. Vapors cause severe eye irritation; photophobia and double vision may occur.

Fire Hazard

Behavior in Fire: When heated above 300°F in the presence of various materials may generate heat and carbon dioxide. Will explode if confined.

Flammability and Explosibility

Nonflammable

Safety Profile

Poison by ingestion and intraperitoneal routes. Moderately toxic by skin contact. A corrosive irritant to eyes, skin, and mucous membranes. Can cause pulmonary edema. Questionable carcinogen with experimental tumorigenic data. Mutation data reported. A pesticide. Combustible when exposed to heat or flame; can react vigorously on contact with oxidizing materials. Explosive in the form of vapor when exposed to heat or flame. Reacts with water or steam to produce heat. Violent reaction with bases (e.g., sodmm hydroxide, potassium hydroxide, calcium hydroxide), dkah metals (e.g., sodium, potassium), amines (e.g., dimethylamine, triethylamine), lithium, pyridine. To fight fire, use alcohol foam. Incompatible with cations. When heated to decomposition (above 150℃) it emits acrid smoke and irritating fumes. See also ANHYDRIDES.

Potential Exposure

Maleic anhydride is used in unsaturated polyester resins; Agricultural chemical, and lubricating additives; in the manufacture of unsaturated polyester resins; in the manufacture of fumaric acid; in alkyd resin manufacture; in the manufacture of pesticides e.g., malathion, maleic hydrazide, and captan).

Shipping

UN2215 Maleic anhydride, Hazard class: 8; Labels: 8-Corrosive material. Maleic Anhydride is commercialized and transported in the solid and molten forms. The molten Maleic Anhydride is transported at temperatures ranging from 60 to 80°C in well-insulated tank containers or road tankers provided with heating devices. In the solid form, it can be transported as pastilles, which are usually packed in polyethylene bags of 25 kg and transported either by rail tanker or by truck.

Purification Methods

Crystallise it from *benzene, CHCl3, CH2Cl2 or CCl4. Sublime it under reduced pressure. [Skell et al. J Am Chem Soc 108 6300 1986, Beilstein 17 III/IV 5897, 17/11 V 55.]

Toxicity evaluation

Maleic anhydride was described as having anticarcinogenic properties, and some of the maleic copolymers can have biologic activity by themselves, especially antitumor activity. Information related to this compound is contradictory. Chromosomal aberrations in cultured hamster cells but no mutagenicity in in vitro tests in bacteria have been reported. No effects on cholinesterase activity have been described after exposure to maleic anhydride.

Incompatibilities

Reacts slowly with water (hydrolyzes) to form maleic acid, a medium-strong acid. Dust may form explosive mixture with air. Reacts with strong oxidizers, oil, water, alkali metals; strong acids; strong bases. Violent reaction with alkali metals and amines above 66C. Dangerous reaction with oxidizers, amines, alkali metals, and hydroxides. Compounds of the carboxyl group react with all bases, both inorganic and organic (i.e., amines) releasing substantial heat, water and a salt that may be harmful. Incompatible with arsenic compounds (releases hydrogen cyanide gas), diazo compounds, dithiocarbamates, isocyanates, mercaptans, nitrides, and sulfides (releasing heat, toxic, and possibly flammable gases), thiosulfates and dithionites (releasing hydrogen sulfate and oxides of sulfur)

Waste Disposal

Consult with environmental regulatory agencies for guidance on acceptable disposal practices. Generators of waste containing this contaminant (≥100 kg/mo) must conform to EPA regulations governing storage, transportation, treatment, and waste disposal. Controlled incineration: care must be taken that complete oxidation to nontoxic products occurs.

Check Digit Verification of cas no

The CAS Registry Mumber 108-31-6 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 8 respectively; the second part has 2 digits, 3 and 1 respectively.
Calculate Digit Verification of CAS Registry Number 108-31:
(5*1)+(4*0)+(3*8)+(2*3)+(1*1)=36
36 % 10 = 6
So 108-31-6 is a valid CAS Registry Number.
InChI:InChI=1S/C4H2O3/c5-3-1-2-4(6)7-3/h1-2H

108-31-6 Well-known Company Product Price

  • Brand
  • (Code)Product description
  • CAS number
  • Packaging
  • Price
  • Detail
  • TCI America

  • (M0005)  Maleic Anhydride  >99.0%(GC)(T)

  • 108-31-6

  • 25g

  • 105.00CNY

  • Detail
  • TCI America

  • (M0005)  Maleic Anhydride  >99.0%(GC)(T)

  • 108-31-6

  • 500g

  • 150.00CNY

  • Detail
  • Alfa Aesar

  • (A12178)  Maleic anhydride, 98+%   

  • 108-31-6

  • 250g

  • 183.0CNY

  • Detail
  • Alfa Aesar

  • (A12178)  Maleic anhydride, 98+%   

  • 108-31-6

  • 1000g

  • 234.0CNY

  • Detail
  • Alfa Aesar

  • (A12178)  Maleic anhydride, 98+%   

  • 108-31-6

  • 5000g

  • 756.0CNY

  • Detail
  • Aldrich

  • (M188)  Maleicanhydride  99%

  • 108-31-6

  • M188-25G-A

  • 441.09CNY

  • Detail
  • Aldrich

  • (M188)  Maleicanhydride  99%

  • 108-31-6

  • M188-1KG-A

  • 637.65CNY

  • Detail
  • Aldrich

  • (M188)  Maleicanhydride  99%

  • 108-31-6

  • M188-5KG-A

  • 848.25CNY

  • Detail
  • Aldrich

  • (M188)  Maleicanhydride  99%

  • 108-31-6

  • M188-25KG-A

  • 3,940.56CNY

  • Detail
  • Aldrich

  • (M625)  Maleicanhydride  powder, 95%

  • 108-31-6

  • M625-25G

  • 138.06CNY

  • Detail
  • Aldrich

  • (M625)  Maleicanhydride  powder, 95%

  • 108-31-6

  • M625-1KG

  • 1,478.88CNY

  • Detail
  • Sigma-Aldrich

  • (63200)  Maleicanhydride  puriss., ≥99.0% (NT)

  • 108-31-6

  • 63200-100G-F

  • 375.57CNY

  • Detail

108-31-6SDS

SAFETY DATA SHEETS

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

Version: 1.0

Creation Date: Aug 10, 2017

Revision Date: Aug 10, 2017

1.Identification

1.1 GHS Product identifier

Product name maleic anhydride

1.2 Other means of identification

Product number -
Other names Toxilic anhydride

1.3 Recommended use of the chemical and restrictions on use

Identified uses For industry use only. Maleic anhydride is used primarily in the formation of unsaturated polyester resins for use in boats, autos, trucks, buildings, piping, and electrical goods. Lube oil adhesives synthesized from maleic anhydride are used to prolong oil-change intervals and improve engine efficiency. Maleic anhydride is also used to make copolymers, pesticides, and other organic compounds, and in Diels-Alder syntheses.
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:108-31-6 SDS

108-31-6Relevant articles and documents

Surface dynamics of a vanadyl pyrophosphate catalyst for n-butane oxidation to maleic anhydride: An in situ Raman and reactivity study of the effect of the P/V atomic ratio

Cavani, Fabrizio,Luciani, Silvia,Esposti, Elisa Degli,Cortelli, Carlotta,Leanza, Roberto

, p. 1646 - 1655 (2010)

This work focused on investigating the effect of the P/V atomic ratio in vanadyl pyrophosphate, catalyst for n-butane oxidation to maleic anhydride, on the nature of the catalytically active phase. Structural transformations occurring on the catalyst surface were investigated by means of in situ Raman spectroscopy in a non-reactive atmosphere, as well as by means of steady-state and non-steady-state reactivity tests, in response to changes in the reaction temperature. It was found that the nature of the catalyst surface is affected by the P/V atomic ratio even in the case of small changes in this parameter. With the catalyst having P/V equal to the stoichiometric value, a surface layer made of α-VOPO4 developed in the temperature interval 340400°C in the presence of air; this catalyst gave a very low selectivity to maleic anhydride in the intermediate T range (340-400°C). However, at 400440°C δ-VOPO4 overlayers formed; at these conditions, the catalyst was moderately active but selective to maleic anhydride. With the catalyst containing a slight excess of P, the ratio offering the optimal catalytic performance, δVOPO4 was the prevailing species over the entire temperature range investigated (340-440°C). Analogies and differences between the two samples were also confirmed by reactivity tests carried out after in situ removal and reintegration of P. These facts explain why the industrial catalyst for n-butane oxidation holds a slight excess of P; they also explain discrepancies registered in the literature about the nature of the active layer in vanadyl pyrophosphate.

Structure Sensitivity of the Catalytic Oxidation of n-Butane to Maleic Anhydride

Cavani, Fabrizio,Centi, Gabriele,Trifiro, Ferruccio

, p. 492 - 494 (1985)

Disorder along the (020) cleavage plane of the (VO)2P2O7 catalyst considerably enhances the activity of the selective oxidation of n-butane to maleic anhydride.

ΑII-(V1-xWx)OPO4 catalysts for the selective oxidation of n-butane to maleic anhydride

Schulz,Roy,Wittich,d'Alnoncourt, R. Naumann,Linke,Strempel,Frank,Glaum,Rosowski

, p. 113 - 119 (2019)

The vanadyl pyrophosphate (VPP) based catalyst is unique in converting n-butane selectively (60–70%) into maleic anhydride (MAN), whereas a MAN selectivity of 20% may be regarded as high for structurally different catalyst systems. We present novel vanadium phosphorus oxides and mixed metal phosphate solid solutions tested for n-butane oxidation to MAN with a selectivity of >30%. The majority of the catalysts were prepared by solution combustion synthesis. (V1-xWx)OPO4 with αII structure was found to be more active and selective in the oxidation of n-butane compared to β-VOPO4. By adjusting the tungsten content the oxidation state of vanadium in (V1-xWx)OPO4 can be tuned between 4.74 and 4.99, which is regarded as a key factor for MAN production. All catalysts were structurally stable, but the specific surface area increased during the reaction, as detected by X-ray diffraction and N2 physisorption, respectively. (V1-xMox)OPO4 was also stable, but the MAN selectivity was lower compared to β-VOPO4. Low conversions result from the low surface area of the screening samples, however, could be overcome by advanced synthesis protocols.

In Situ FTIR Spectroscopy of 1-Butene and 1,3-Butadiene Selective Oxidation to Maleic Anhydride on V-P-O Catalysts

Wenig, Robert W.,Schrader, Glenn L.

, p. 1911 - 1918 (1987)

The selective oxidation of 1-butene and 1,3-butadiene was studied by transmission infrared spectroscopy.Vanadium-phosphorous-oxygen catalysts prepared by the reaction of V2O5 with H3PO4 in alcohol solution were used.Infrared spectra were collected in situ during the flow of 75 cm3 of 1.5percent hydrocarbon-in-air mixtures over catalysts having P-to-V ratios of 0.9, 1.0, and 1.1.Reaction temperatures from 300 to 400 deg C were investigated with 1-butene feeds, whereas the highly reactive 1,3-butadiene was studied only at 300 deg C.An adsorbed butadiene species, maleic acid, maleic anhydride were observed during both olefin partial oxidation studies.Evidence was obtained for a second olefin species which had been previously observed for in situ n-butane selective oxidation studies.Concentrations of adsorbed species were found to vary with catalyst phosphorous loading, reaction temperature, and time of exposure to reaction conditions.

Activity and Selectivity in Catalytic Reactions of Buta-1,3-diene and But-1-ene on Supported Vanadium Oxides

Mori, Kenji,Miyamoto, Akira,Murakami, Yuichi

, p. 13 - 34 (1986)

The activity and selectivity in the oxidation of buta-1,3-diene, and oxidation and isomerization of but-1-ene on unsupported and supported V2O5 catalysts have been investigated in terms of the catalyst structure.The rate of oxidation is mainly determined by the number of surface V=O species on the catalyst for both buta-1,3-diene and but-1-ene.The roughness of the V2O5 surface affected the activity for buta-1,3-diene, but not for but-1-ene oxidation.It was also found that TiO2 support increases the activity of the surface V=O for but-1-ene oxidation.The selectivity to maleic anhydride was determined by the number of V2O5 layers on the support for both reactions.When the number of V2O5 layers was 1 or 2, the selectivity was low, while it increased markedly with an increase in the number of V2O5 layers to 5, and attained a constant value above 5 layers.Both V2O5 and support were active for the isomerization of but-1-ene to cis- and trans-but-2-ene.On V2O5, the cis/trans ratio was low, while it was as high as 3 for the Al2O3 support.The rate and selectivity of the isomerization on supported catalysts were explained in terms of the structure of V2O5 on the support.Difference in the structure-activity/selectivity correlation between oxidation and isomerization and that between but-1-ene oxidation and buta-1,3-diene oxidation were also discussed.

Effects of cobalt additive on amorphous vanadium phosphate catalysts prepared using precipitation with supercritical co2 as an antisolvent

Lopez-Sanchez, J. Antonio,Bartley, Jonathan K.,Burrows, Andrew,Kiely, Christopher J.,Haevecker, Michael,Schloegl, Robert,Volta, Jean Claude,Poliakoff, Martin,Hutchings, Graham J.

, p. 1811 - 1816 (2002)

The effect of addition of cobalt to an amorphous vanadium phosphate for the selective oxidation of n-butane to maleic anhydride is described and discussed. Cobalt is a well known promoter for crystalline vanadium phosphate catalysts and is most effective at a concentration of 1 atom % relative to vanadium. In contrast, for amorphous vanadium phosphate materials, prepared by precipitation using supercritical CO2 as an antisolvent, cobalt appears to act as a catalyst poison, decreasing both the catalyst activity and selectivity for maleic anhydride. Detailed analysis by transmission electron microscopy, 31P spin echo mapping NMR spectroscopy and X-ray absorption spectroscopy is described, which highlight differences with the unmodified catalyst. It is concluded that the addition of cobalt affects the morphology of the material and the oxidation state of vanadium, and that these changes deleteriously affect the catalytic performance.

Surface Acidity of Vanadyl Pyrophosphate, Active Phase in n-Butane Selective Oxidation

Busca, Guido,Centi, Gabriele,Trifiro, Ferruccio,Lorenzelli, Vincenzo

, p. 1337 - 1344 (1986)

The surface acidity of two (VO)2P2O7catalysts with similar specific activities per square meter of surface area in 1-butene selective oxidation, but different specific activities in n-butane selective oxidation, was studied by ammonia, pyridine, acetonitrile, CO, and CO2 adsorption, by ammonia temperature-programmed desorption, and by 2-propanol oxidation.The results for both catalysts indicate the presence of strong Broensted sites attributed to surface P-OH groups and of medium strong Lewis sites attributed to V(IV) coordinatively unsaturated ions exposed on the surface.The presence of these centers was related to the (VO)2P2O7 structure itself and is fairly independent of the (VO)2P2O7 preparation method.However, in the (VO)2P2O7 prepared in an organic medium and to a lesser extent in the (VO)2P2O7 prepared in an aqueous medium, the presence of very strong Lewis sites also was observed.The enhancement of the rate of n-butane activation in the (VO)2P2O7 prepared in an organic medium was attributed to the presence of these sites.The role of the preparation method in the formation of such very strong Lewis sites also is discussed.

Preparation and characterization of vanadyl hydrogen phosphate hydrates; VO(HPO4)*1.5 H2O and VO(HPO4)*0.5 H2O

Matsuura, Ikuya,Ishimura, Tomohiro,Kimura, Naomasa

, p. 769 - 770 (1995)

A new phase of vanadyl(IV) hydrogen phosphate sesquihydrate, VO(HPO4)*1.5 H2O, has been obtained by the reduction of VOPO4*2H2O with 1-butanol.The unit cell is the orthorhombic system with lattice constants a=7.43 Angstroem, b=9.62 Angstroem, and c=7.97 Angstroem in space group Pmmn.

X-Ray Study of a Vanadium-Phosphorus Mixed Oxide Catalyst for Selective Butane Oxidation to Maleic Anhydride

Bergeret, G.,Broyer, J. P.,David, M.,Gallezot, P.,Volta, J. C.,Hecquet, G.

, p. 825 - 826 (1986)

The radical electron distribution obtained from X-ray patterns has been used to study the structure of a poorly-crystalline vanadium-phosphorus mixed oxide (VPO) catalyst after selective oxidation of n-butane; the effective catalyst consists of a mixture of a crystallized (VO)2P2O7 phase (V(4+)) and an amorphorus VPO phase (V(5+)) showing many corner-sharing VO6 octahedra.

Effects of Consecutive Oxidation on the Production of Maleic Anhydride in Butane Oxidation over Four Kinds of Well-Characterized Vanadyl Pyrophosphates

Igarashi, Hiroshi,Tsuji, Katsuyuki,Okuhara, Toshio,Misono, Makoto

, p. 7065 - 7071 (1993)

Factors determining the selectivity of butane oxidation at high conversion levels have been examined by using four kinds of well-characterized vanadyl pyrophosphate catalysts (C-1 - C-4) in kinetic experiments.The catalysts were carefully characterized by scanning electron microscopy, X-ray powder diffraction, X-ray photoelectron spectroscopy, and infrared spectroscopy and were made of a single crystalline phase of vanadyl pyrophosphate, (VO)2P2O7.C-1 was prepared by reduction with NH2OH*HCl and consisted of large particles (5 μm) and small particles (0.2 μm).The particles of C-2 obtained from V2O4 had a size of 2 μm.C-3, which was obtained by an organic solvent method, showed a rose-like structure.C-4 from VOPO4*2H2O had a large plate-like structure (5 μm).While all of the catalysts exhibited similar selectivities for the formation of maleic anhydride (63-72 percent) at low conversion levels, the extend of selecticity decreases with an increase in the conversion and strongly depends on the catalysts.It also correlates oppositely with the catalytic activity for the oxidation of maleic anhydride, measured separately.This indicates that the consecutive oxidation of product maleic anhydride is a crucial factor for the selectivity at high conversions.A simulation using a model that includes the consecutive oxidation of maleic anhydride, in which the experimental rate constants for the oxidation of butane and maleic anhydride have been used, reproduced the selectivity-conversion curves experimentally observed.

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