Electrophilic Mercuration and Thallation of Benzene and Substituted Benzenes in Trifluoroacetic Acid Solution* (Electrophilic Substitution/Selectivity) GEORGE A

Total Page:16

File Type:pdf, Size:1020Kb

Electrophilic Mercuration and Thallation of Benzene and Substituted Benzenes in Trifluoroacetic Acid Solution* (Electrophilic Substitution/Selectivity) GEORGE A Proc. Natl. Acad. Sci. USA Vol. 74, No. 10, pp. 4121-4125, October 1977 Chemistry Electrophilic mercuration and thallation of benzene and substituted benzenes in trifluoroacetic acid solution* (electrophilic substitution/selectivity) GEORGE A. OLAH, IWAO HASHIMOTOt, AND HENRY C. LINtt Institute of Hydrocarbon Chemistry, Department of Chemistry, University of Southern California, Los Angeles, California 90007; and the Department of Chemistry, Case Western Reserve University, Cleveland, Ohio 44101 Contributed by George A. Olah, July 18, 1977 ABSTRACT The mercuration and thallation of benzene and iments at 250 and quenched the mixtures after 5 min, whereas substituted benzenes was studied with mercuric and thallic Brown and Nelson carried out the reaction for 6.5 hr. In sub- trifluoroacetate, respectively, in trifluoroacetic acid. With the in view of the importance of both the mechanistic shortest reaction time (1 sec) at 00, the relative rate of mercu- sequent work, ration of toluene compared to that of benzene was 17.5, with and practical implications of the orientation-rate correlation, the isomer distribution in toluene of: ortho, 17.4%; meta, 5.9%; Brown and McGary (7), carried out a more detailed study of and para, 76.7%. The isomer distribution in toluene varied with the mercuration reaction. They concluded: "A redetermination the reaction time, significantly more at 25° than at 00. The of the isomer distributions and relative rates indicates excellent competitive thallation of benzene and toluene with thallic tri- agreement with the linear relationship of orientation and rel- fluoroacetate in trifluoroacetic acid at 150 showed the relative ative however, that the isomer distri- rate, toluene/benzene, to be 33, with the isomer distribution in rate." They recognized, toluene of: ortho, 9.5%; meta, 5.5%; and para, 85.0%. With butions change with time but still claimed that the corrected increasingly higher reaction temperatures in both mercuration meta isomer distribution in the mercuration of toluene is 9.5 and thallation reactions of aromatics, isomerization (both in- + 0.5% and remarked, "there remains a relatively minor dis- tramolecular and intermolecular) within the relevant ortho- and agreement with the values reported by Klapproth and West- para-metallated intermediate ions and/or of the isomers be- heimer (6% meta) for which we are unable to account." comes more important. Competitive rates and isomer distri- In we have that, regardless of butions of mercuration and thallation of benzene and substi- preceding work (8) suggested tuted benzenes were also determined. The predominant para the substrate selectivity in electrophilic aromatic substitutions substitution in both mercuration and thallation of methylben- (which generally can be most conveniently expressed by kT/kB zenes reflects, besides some steric factors, the strong stabilizing rate ratios), the regioselectivity (positional) of the reactions effect of para methyl groups on the arenium ion intermediates. remains high, with usually predominant ortho-para substitu- Under predominantly kinetically controlled conditions, no tion, the amount of meta isomer being 2-5%. anomalous increase in the amount of meta substitution was We considered it possible that the reported relatively high observed. meta isomer ratio observed in preceding studies of mercuration The mercuration of aromatic hydrocarbons with mercuric of toluene (as well as related alkylbenzenes) was still the result trifluoroacetate in trifluoroacetic acid at 250 has been studied, of ongoing faster isomerization and/or disproportionation of predominantly by Brown and coworkers (1-3). The rate ratio the ortho and para isomers, compared to the more stable meta of toluene to benzene (kT/kB) was found to be 9.89 and the isomer (7) or related rearrangements in the a-complex inter- isomer distribution in toluene was: ortho, 12.2%; meta, 8.6%; mediates of the reactions. These would fully explain the dis- and para, 79.2%. From these results, as well as from their pre- agreements with Klapproth and Westheimer's work. Conse- ceding studies in acetic acid solution with perchloric acid cat- quently, it appeared desirable to reinvestigate in detail the alyst giving kT/kB = 3.6-7, and 12-16% meta isomer, it was mercuration of benzene and substituted benzenes under pre- concluded that the relatively high meta isomer ratio observed dominantly kinetically controlled conditions, minimizing the was due to the high electrophilic reactivity of the mercurating possibility of isomerization and disproportionation affecting agent causing the observed low selectivity substitutions. These the results. results were correlated by the so-called Brown selectivity re- The thallation of benzene and substituted benzenes with lationship (for a review, see ref. 4). thallium trifluoroacetate in trifluoroacetic acid, the mechanism It should be pointed out that, in their original paper on of which was considered to be similar to that of related mer- mercuration of toluene and benzene, Brown and Nelson, (5) curations (9-11), was also studied under similar conditions. extending the claimed quantitative selectivity relationship MATERIALS AND METHODS governing isomer distributions in aromatic substitution, com- mented on the preceding work of Klapproth and Westheimer Materials. Benzene, toluene, and alkylbenzenes were of (6) who found that, in glacial acetic acid with perchloric acid highest available purity. Trifluoroacetic acid (Cationics, Inc.) as catalyst, toluene was mercurated by mercuric acetate at 250 was obtained in sufficient purity to be used without further to give 6% of the meta isomer. Brown and Nelson claimed to purification (boiling point 730). Mercuric and thallium triflu- have observed 12% meta isomer under similar conditions and oroacetate were commercial materials (Aldrich Chemical Co., stated "we are, however, unable to account for the differences Inc.). between the values of the meta isomer." In the former case (6), a precise radiochemical technique was used in establishing Abbreviation: kT/kB, ratio of reaction rates for toluene and ben- orientation, whereas infrared analysis was utilized in the latter. zene. * Paper no. 40 in the series "Aromatic Substitution." Paper no. 39 was Comparison of the experimental sections of Brown and Nelson's Olah, G. A., Pelizza, F. Kobayashi, S. & Olah, J. A. (1976) J. Am. and Klapproth and Westheimer's papers, however, indicates Chem. Soc. 98,296. that the claim of reinvestigation "under similar conditions" is t Visiting Scientist from the Wakayama Technical College, Japan. incorrect. Klapproth and Westheimer carried out their exper- * Senior Research Associate (1974-1975). 4121 Downloaded by guest on October 2, 2021 4122 Chemistry: Olah et al. Proc. Natl. Acad. Sci. USA 74 (1977) r - - -- 1 Table 1. Gas/liquid chromatographic parameters Conditionst of retention Bromo compound Column* Column Time, min E ~G Bromobenzene D I 5.9 Quench o-Bromotoluene D I 10.0 m-Bromotoluene D I 11.0 p -Bromotoluene D I 12.3 FIG. 1. Flow-quenching apparatus for the mercuration of o-Bromoethylbenzene D I 10.3 polymethylbenzenes. Two 50-ml syringes (A and B) are driven by a m-Bromoethylbenzene D I 12.0 syringe pump (C; Sage Instruments, model 351). The separate solu- p-Bromoethylbenzene D I 14.2 tions came together via two flexible Teflon tubes (D and E, inside o-Bromoisovronvlbenzene D I 11.7 diameter 1.4 mm; length, 60 cm), mix at F, react during passage G, and D I 13.8 are quenched at the end of G. p-Bromoisopropylbenzene D I 18.3 o-Bromo-tert- butylbenzene D I 16.2 Competitive Mercuration of Benzene and Substituted m-Bromo-tert- butylbenzene D I 19.3 Benzenes. Mercuric trifluoroacetate (25 ml of 0.2 M solution p-Bromo-tert-butylbenzene D I 22.3 in trifluoroacetic acid) was added rapidly to 25 ml of 1 M so- 4-Bromo-o-xylene C I 2.9 lutions of the aromatics in the same solvent with vigorous stir- 4-Bromo-m-xylene C I 2.7 ring, both precooled and kept at 00. After specific time inter- 2-Bromo-p-xylene C I 3.0 vals, the reaction mixture was quenched with aqueous sodium Bromoesitylene C III 3.2 bromide, maintaining a bromide ion to mercuric ion ratio of 4-Bromo-1,2,3-trimethylben- 3:1. The precipitated arylmercuric bromides were filtered and zene C I 5.1 thoroughly dried under reduced pressure. Then, the mixture 5-Bromo-1,2,4-trimethyl- of arylmercuric bromides was slowly treated with bromine in benzene C I 4.8 chloroform at 00 until a permanent red color developed. Stir- 5-Bromo-1,2,3,4-tetramethyl- ring was continued for 5 hr at 0° and then for an additional hour benzene C II 4.5 at room temperature. Conversion of arylmercuric bromides to 4-Bromo-1,2,3,5-tetramethyl- the corresponding bromoarenes under these conditions was benzene C II 4.5 found to be quantitative for all practical purposes (the slower Bromodurene C III 6.6 conversion of the parent phenylmercuric bromide without Bromopentamethylbenzene C III 17.8 to is not o-Bromofluorobenzene B IV 12.2 raising the temperature ambient always quantitative). m-Bromofluorobenzene B IV 9.8 The reaction mixture was washed with sodium bisulfite solution p-Bromofluorobenzene B IV 10.5 and water and then dried over sodium sulfate. Bromoarenes o-Bromochlorobenzene B V 15.1 were subsequently analyzed by gas/liquid chromatography. m-Bromochlorobenzene B V 13.0 Competitive Mercuration of Polymethylbenzenes. The p-Bromochlorobenzene B V 13.2 rates of mercuration of polymethylbenzenes are so fast that it o-Dibromobenzene B V 25.8 is difficult to carry out the reactions by the usual methods. m-Dibromobenzene B V 21.9 Therefore, a modified flow-quench apparatus (12) was used p-Dibromobenzene B V 22.2 to allow short reaction times (of the order of 1 sec) (Fig. 1). o-Bromoanisole A VI 10.9 Quenching was with aqueous sodium bromide surrounded by m-Bromoanisole A VI 9.6 ice.
Recommended publications
  • Measuring and Predicting Sooting Tendencies of Oxygenates, Alkanes, Alkenes, Cycloalkanes, and Aromatics on a Unified Scale
    Measuring and Predicting Sooting Tendencies of Oxygenates, Alkanes, Alkenes, Cycloalkanes, and Aromatics on a Unified Scale Dhrubajyoti D. Dasa,1, Peter St. Johnb,1, Charles S. McEnallya,∗, Seonah Kimb, Lisa D. Pfefferlea aYale University, Department of Chemical and Environmental Engineering, New Haven CT 06520 bNational Renewable Energy Laboratory, Golden CO 80401 Abstract Soot from internal combustion engines negatively affects health and climate. Soot emissions might be reduced through the expanded usage of appropriate biomass-derived fuels. Databases of sooting indices, based on measuring some aspect of sooting behavior in a standardized combustion environment, are useful in providing information on the comparative sooting tendencies of different fuels or pure compounds. However, newer biofuels have varied chemical structures including both aromatic and oxygenated functional groups, making an accurate measurement or prediction of their sooting tendency difficult. In this work, we propose a unified sooting tendency database for pure compounds, including both regular and oxygenated hydrocarbons, which is based on combining two disparate databases of yield-based sooting tendency measurements in the literature. Unification of the different databases was made possible by leveraging the greater dynamic range of the color ratio pyrometry soot diagnostic. This unified database contains a substantial number of pure compounds (≥ 400 total) from multiple categories of hydrocarbons important in modern fuels and establishes the sooting tendencies of aromatic and oxygenated hydrocarbons on the same numeric scale for the first time. Using this unified sooting tendency database, we have developed a predictive model for sooting behavior applicable to a broad range of hydrocarbons and oxygenated hydrocarbons. The model decomposes each compound into single-carbon fragments and assigns a sooting tendency contribution to each fragment based on regression against the unified database.
    [Show full text]
  • Mechanistic Study of Methylbenzene Dealkylation in Methanol-To-Olefins
    Journal of Catalysis 369 (2019) 86–94 Contents lists available at ScienceDirect Journal of Catalysis journal homepage: www.elsevier.com/locate/jcat Mechanistic study of methylbenzene dealkylation in methanol-to-olefins catalysis on HSAPO-34 ⇑ Andrew Hwang, Blake A. Johnson, Aditya Bhan Department of Chemical Engineering and Materials Science, University of Minnesota, Minneapolis, MN 55455, USA article info abstract Article history: Methylbenzenes entrained within the cavities of silicoaluminophosphate zeotype HSAPO-34 react with Received 14 June 2018 methanol in H+-mediated dealkylation to give ethylene and propylene in methanol-to-olefins catalysis. Revised 1 August 2018 Methylbenzenes dealkylation on solid acids is proposed to occur either via the side-chain mechanism, Accepted 14 October 2018 where an exocyclic C@C undergoes successive methylation prior to CAC cleavage for olefin elimination, or the paring mechanism, where ring contraction to a bicyclohexenyl cation precedes CAC cleavage for olefin elimination. Distinct dealkylation mechanisms prescribe distinct combinations of C atoms—from Keywords: aromatic methyl, aromatic ring, and methanol/dimethyl ether—to comprise the olefin product. Site- Methanol-to-olefins specific isotope tracing that distinguishes between isotope labels in aromatic methyl and aromatic ring Methylbenzenes dealkylation Isotope tracing positions for each methylbenzene shows that tetramethylbenzene gives ethylene via the side-chain Site-specific mechanism and penta- and hexamethylbenzene give propylene via the paring mechanism. The ratio of Quantitative 13C NMR propylene selectivity to ethylene selectivity increases in methanol reactions on HSAPO-34 entrained with HSAPO-34 a distribution of methylbenzenes deliberately manipulated towards increasing fractions of penta- and Methylbenzene flash chromatography hexamethylbenzene, corroborating the conclusion that aromatic precursors and dealkylation mecha- nisms for ethylene diverge from those for propylene.
    [Show full text]
  • Chapter 21 Practice Problems 1
    Chapter 21 Practice Problems 1. Name the following: A) isopropane B) methylpentane C) methylbutane D) n-pentane E) dodecane 2. Name the following: A) n-heptane B) 2-methyl-2-ethylbutane C) 3,3-dimethylpentane D) 2,2-diethylpropane 3. Name the following: A) 2,4-diethylpentane B) 3,5-dimethylheptane C) secondary ethylpentane D) 2,3-dimethyl-2,3-diethylpropane E) none of these 4. In lecture, a professor named a molecule 2-ethyl-4-tert-butylpentane. A student pointed out that the name was incorrect. What is the correct systematic name for the molecule? A) 2-t-butyl-5-methylhexane B) 2-ethyl-4,5,5-trimethylhexane C) 3,5,6,6-tetramethylheptane D) 2,2,3,5-tetramethylheptane E) undecane 5. Structural isomers have A) different molecular formulas and different structures. B) different molecular formulas but the same structure. C) the same molecular formula and the same structure. D) the same molecular formula but different structures. E) none of these 6. How many structural isomers does propane have? A) 3 B) 2 C) 1 D) 5 E) 4 7. The product of ethane undergoing dehydrogenation is called A) propene. B) methene. C) ethene. D) propane. E) none of these 8. Which of the following, upon reacting with oxygen, would form the greatest amount of carbon dioxide? A) n-pentane B) isopentane C) neopentane D) Two of these would form equal amounts. E) All of these would form equal amounts. 9. Which of the following has the lowest boiling point? A) methane B) butane C) ethane D) propane E) All of these have the same boiling point.
    [Show full text]
  • Δ13c of Aromatic Compounds in Sediments, Oils And
    1 δ13C of aromatic compounds in sediments, oils and 2 atmospheric emissions: a review 3 Alex I. Holman a, Kliti Grice a* 4 5 a Western Australia Organic and Isotope Geochemistry Centre, The Institute for 6 Geoscience Research, School of Earth and Planetary Sciences, Curtin University, 7 GPO Box U1987, Perth, WA 6845, Australia 8 9 * Corresponding author 10 Alex Holman: Tel.: +61(0) 8 9266 9723. E-mail address: [email protected] 11 Kliti Grice: Tel.: +61(0) 8 9266 2474. E-mail address: [email protected] 12 13 14 15 16 17 18 19 Abstract 20 This review discusses major applications of stable carbon isotopic 21 measurements of aromatic compounds, along with some specific technical aspects 22 including purification of aromatic fractions for baseline separation. δ13C 23 measurements of organic matter (OM) in sediments and oils are routine in all 24 fields of organic geochemistry, but they are predominantly done on saturated 25 compounds. Aromatic compounds are important contributors to sedimentary 26 organic matter, and provide indication of diagenetic processes, OM source, and 27 thermal maturity. Studies have found evidence for a small 13C-enrichment during 28 diagenetic aromatisation of approximately 1 to 2 ‰, but the formation of polycyclic 29 aromatic hydrocarbons (PAHs) from combustion and hydrothermal processes 30 seems to produce no effect. Likewise, maturation and biodegradation also produce 31 only small isotopic effects. An early application of δ13C of aromatic compounds was 32 in the classification of oil families by source. Bulk measurements have had some 33 success in differentiating marine and terrigenous oils, but were not accurate in all 34 settings.
    [Show full text]
  • Effects of Sulfide Minerals on Aromatic Maturity Parameters
    Organic Geochemistry 76 (2014) 270–277 Contents lists available at ScienceDirect Organic Geochemistry journal homepage: www.elsevier.com/locate/orggeochem Effects of sulfide minerals on aromatic maturity parameters: Laboratory investigation using micro-scale sealed vessel pyrolysis ⇑ ⇑ Alex I. Holman a, , Paul F. Greenwood a,b,c, Jochen J. Brocks d, Kliti Grice a, a Western Australia Organic and Isotope Geochemistry Centre, Department of Chemistry, The Institute for Geoscience Research, Curtin University, GPO Box U1987, Perth, WA 6845, Australia b Centre for Exploration Targeting, University of Western Australia, Crawley, WA 6009, Australia c WA Biogeochemistry Centre, University of Western Australia, Crawley, WA 6009, Australia d Research School of Earth Sciences, The Australian National University, Canberra, ACT 0200, Australia article info abstract Article history: Sedimentary organic matter from the Here’s Your Chance (HYC) Pb–Zn–Ag deposit (McArthur Basin, Received 19 December 2013 Northern Territory, Australia) displays increased thermal maturity compared to nearby non-mineralised Received in revised form 28 August 2014 sediments. Micro-scale sealed vessel pyrolysis (MSSVpy) of an immature, organic rich sediment from the Accepted 2 September 2014 host Barney Creek Formation (BCF) was used to simulate the thermal maturation of OM from the HYC Available online 16 September 2014 deposit, and to assess the effect of sulfide minerals on organic maturation processes. MSSVpy at increas- ing temperatures (300, 330 and 360 °C) resulted in increased methylphenanthrene maturity ratios which Keywords: were within the range reported for bitumen extracted from HYC sediments. The methylphenanthrene Micro-scale sealed vessel pyrolysis index ratio from MSSVpy of the BCF sample was lower than in HYC, due to a reduced proportion of meth- Polycyclic aromatic hydrocarbon Thermal maturity ylated phenanthrenes.
    [Show full text]
  • Supporting Information
    Electronic Supplementary Material (ESI) for ChemComm. This journal is © The Royal Society of Chemistry 2015 Electronic Supplementary Information for Anodic aromatic C,C cross-coupling reaction using parallel laminar flow mode in a flow microreactor Toshihiro Arai, Hiroyuki Tateno, Koji Nakabayashi, Tsuneo Kashiwagi, and Mahito Atobe Department of Environment and System Sciences, Yokohama National University, 79-7 Tokiwadai, Hodogaya-ku, Yokohama 2408501, Japan. *To whom the correspondence should be addressed. E-mail: [email protected] This PDF file includes: Instrumentation Materials Experimental procedure Spectroscopic data S1 1. Instrumentation Nuclear magnetic resonance (1H NMR) spectra were measured on BRUKER DRX 300 1 1 spectrometer operating at 300 MHz ( H NMR) in CDCl3. All H NMR chemical shifts were reported in ppm relative to internal references of TMS at 0.00. Preparative electrolyses were carried out with a HOKUTO DENKO HABF-501A Potentiostat/Galvanostat. GCMS analyses were performed with a Shimadzu gas chromatograph mass spectrometer GCMS-QP2010. 2. Materials Acetonitrile, acetic acid, and naphthalene (1) were purchased from Kanto Chemical and used as received. Pentamethylbenzene (2), isodurene (5), mesitylene (6), 2-bromonaphthalene (8), and tetrabutylammonium tetrafluoroborate (Bu4NBF4) were purchased from Tokyo Chemical Industry and used as received. 3. Flow Microreactor Figure S1 shows construction procedure for the electrochemical two-inlet flow microreactor. The reactor was constructed from glass plates and two platinum (Pt) plates (3 cm width, 3 cm length each) (Step 1 of Figure S1). A spacer (20 m thickness double faced adhesive tape) was used to leave a rectangular channel exposed, and the two electrodes were simply sandwiched together (area of the two electrodes: 1 × 3 cm2).
    [Show full text]
  • 1,2,4-Trimethylbenzene Transformation Reaction Compared with Its Transalkylation Reaction with Toluene Over USY-Zeolite Catalyst
    1,2,4-Trimethylbenzene Transformation Reaction Compared with its Transalkylation Reaction with Toluene over USY-Zeolite Catalyst Sulaiman Al-Khattaf*, Nasir M. Tukur, and Adnan Al-Amer Chemical Engineering Department, King Fahd University of Petroleum & Minerals Dhahran 31261, Saudi Arabia Abstract 1,2,4-Trimethyl benzene (TMB) transalkylation with toluene has been studied over USY-zeolite type catalyst using a riser simulator that mimics the operation of a fluidized-bed reactor. 50:50 wt% reaction mixtures of TMB and toluene were used for the transalkylation reaction. The range of temperature investigated was 400-500 oC and time on stream ranging from 3 to 15 seconds. The effect of reaction conditions on the variation of p-xylene to o-xylene products ratio (P/O), distribution of trimethylbenzene (TMB) isomers (1,3,5-to-1,2,3-) and values of xylene/tetramethylbenzenes (X/TeMB) ratios are reported. Comparisons are made between the results of the transalkylation reaction with the results of pure 1,2,4-TMB and toluene reactions earlier reported. Toluene that was found almost inactive, became reactive upon blending with 1,2,4-TMB. This shows that toluene would rather accept a methyl group to transform to xylene than to loose a methyl group to form benzene under the present experimental condition with pressures around ambient. The experimental results were modeled using quasi-steady state approximation. Kinetic parameters for the 1,2,4-TMB disappearance during the transalkylation reaction, and in its conversion into isomerization and disproportionation products were calculated using the catalyst activity decay function based on time on stream (TOS).
    [Show full text]
  • Referee's Comment in Italic Font; Author's Response in Blue Without
    Referee’s Comment in Italic Font; Author’s response in Blue without Italic Font. 1-page 31153, In title and in many places throughout article it would be more accurate to say “monocyclic aromatic hydrocarbons” instead of the more general “aromatic hydrocarbons” to make clear that the focus of this study was benzene and substituted benzene compounds. Agree. We will change all “aromatic hydrocarbons” to “monocyclic aromatic hydrocarbons”. 2-page 31154, line 2, The wording “determines the SOA formation” is unclear. Does it refer to SOA yield? composition? Both? The “SOA formation” means both the SOA yield and SOA chemical composition. We will insert “(SOA yield and chemical composition)” after “determines the SOA formation”. 3-page 31154, line 16, Unclear what is meant by “less oxidized per mass/carbon.” “less oxidized per mass/carbon” corresponds to two parameters which are used to compare the SOA formation difference in different aromatic hydrocarbons in this paper. “oxidized per mass” refers to SOA yield which determines SOA formation potential on a mass basis.“oxidized per carbon” refers to SOA chemical composition (e.g. OSc, O/C and H/C) which determines SOA formation potential on a mole or carbon number basis. To clarify the meaning of “less oxidized per mass/carbon”, we will add “on a basis of SOA yield or chemical composition” after “less oxidized per mass/carbon”. 4-page 31155, line 13, Define what is meant by “methyl group branching” Good point. We will replace “methyl group branching ratio” with “the increase of branched structure”. 5-page 31158, line 14, How are the yield values found in this study different from those in previous studies? Higher or lower? The differences in absolute values of SOA yield in previous studies and this studies depend on the photooxidation conditions.
    [Show full text]
  • United States Patent [19] [11] Patent Number: 6,147,270 Pazzucconi Et Al
    US006147270A United States Patent [19] [11] Patent Number: 6,147,270 Pazzucconi et al. [45] Date of Patent: Nov. 14, 2000 [54] PROCESS FOR THE PREPARATION OF 5,670,704 9/1997 Hagen et al. ......................... .. 585/471 2,6-DIMETHYLNAPHTHALENE USING A 5,672,799 9/1997 Perego et al. ......................... .. 585/467 MTW ZEOLITIC CATALYST FOREIGN PATENT DOCUMENTS [75] Inventors: Giannino Pazzucconi, Broni; Carlo 2 246 788 2/1992 United Kingdom . Perego, Carnate; Roberto Millini, WO 90/03960 4/1990 WIPO. Cerro al Lambro; Francesco Frigerio, OTHER PUBLICATIONS Torre d’lsola; Riccardo Mansani, Sassari; Daniele Rancati, Porto Torres, “MTW”; internet search record, Dec. 1999. all of Italy Primary Examiner—Marian C. Knode [73] Assignee: Enichem S.p.A., S. Donato Milanese, Assistant Examiner—Thuan D. Dang Italy Attorney, Agent, or Firm—Oblon, Spivak, McClelland, Maier & Neustadt, PC. [21] Appl. No.: 09/281,961 [57] ABSTRACT [22] Filed: Mar. 31, 1999 A highly selective process is described for preparing 2,6 dimethylnaphthalene Which comprises reacting a naphtha [30] Foreign Application Priority Data lene hydrocarbon selected from naphthalene, Apr. 17, 1998 [IT] Italy ............................... .. MI98A0809 methylnaphthalenes, dimethylnaphthalenes, trimethylnaphthalenes, polymethylnaphthalenes or their [51] Int. Cl.7 ................................................... .. C07C 15/12 mixtures With one or more benzene hydrocarbons selected [52] US. Cl. ........................................... .. 585/475; 585/471 from benzene, toluene, Xylenes, trimethylbenZenes, [58] Field of Search ................................... .. 585/475, 471, tetramethylbenZenes, pentamethylbenZene and/or 585/470 heXamethylbenZene, under at least partially liquid phase conditions, in the presence of a Zeolite belonging to the [56] References Cited structural type MTW and optionally in the presence of a U.S.
    [Show full text]
  • A Process for Separating Ethylbenzene from Feedstream Containing Meta-Xylene Using a Zeolite Adsorbent
    Europâisches Patentamt 0105 698 ® European Patent Office @ Publication number: B1 Office européen des brevets © EUROPEAN PATENT SPECIFICATION (§) Dateof publication of patent spécification: 18.03.87 (D Intel.4: C 07 C 15/073, C 07 C 7/13 (D Application number: 83305799.5 (§) Date offiling: 28.09.83 (§) A process for separating ethylbenzene from feedstream containing meta-xylene using a zeolite adsorbent. (§) Priority: 28.09.82 US 426242 ® Proprietor: Exxon Research and Engineering Company P.O. Box 390 180 Park Avenue Date of publication of application: Florham Park New Jersey 07932 (US) 18.04.84 Bulletin 84/16 ® Inventor: Barthomeuf, Denise Marie (S) Publication of the grant of the patent: 217 Prospect Avenue 18.03.87 Bulletin 87/12 Cranford New Jersey 07016 (US) Inventor: Hulme, Roger 1017 Clark Street (S) Designated Contracting States: Linden New Jersey 07036 (US) BE CH DE FR GB IT Ll LU NL SE @) Représentative: Somers, Harold Arnold et al (§) Références cited: ESSO Engineering (Europe) Ltd. Patents & GB-A-1 307264 Licences Apex Tower High Street GB-A-1 488 616 New Malden Surrey KT3 4DJ (GB) GB-A-1 550 391 US-A-3734 974 OÙ US-A-3 795711 US-A-3 864416 00 CHEMICAL ABSTRACTS, vol. 88, no. 3, January <0 16, 1978, page 584, abstract no. 22327f COLUMBUS,OHIO (US) 10 O Note: Within nine months from the publication of the mention of the grant of the European patent, any person may give notice to the European Patent Office of opposition to the European patent granted. Notice of opposition shall CL be filed in a written reasoned statement.
    [Show full text]
  • Disproportionation of 1,2,4-Trimethylbenzene Over Zeolite NU-87
    Korean J. Chem. Eng., 17(2), 198-204 (2000) Disproportionation of 1,2,4-Trimethylbenzene over Zeolite NU-87 Se-Ho Park, Jong-Hyung Lee and Hyun-Ku Rhee† School of Chemical Engineering and Institute of Chemical Processes, Seoul National University, Kwanak-ku, Seoul 151-742, Korea (Received 27 September 1999 • accepted 30 December 1999) Abstract−The catalytic properties of zeolite NU-87 were investigated with respect to the disproportionation of 1, 2,4-trimethylbenzene and the results were compared to those obtained over H-beta and H-mordenite with 12-mem- bered ring channel system. In the conversion of 1,2,4-trimethylbenzene, the disproportionation to xylene and tetra- methylbenzene is preferred to the isomerization into 1,2,3- and 1,3,5-isomers over all the three zeolites, but this trend is much more pronounced over HNU-87 owing to its peculiar pore structure. Disproportionation reaction is found to proceed within the micropores of HNU-87, whereas isomerization occurs mainly on the external surface. The high selectivity to disproportionation gives more xylenes and tetramethylbenzenes over HNU-87. The detailed descrip- tions for the product distribution are also reported. Key words: NU-87, 1,2,4-Trimethylbenzene, Disproportionation, Isomerization INTRODUCTION EXPERIMENTAL Disproportionation of trimethylbenzene (TMB) to xylene and 1. Catalysts Preparation = tetramethylbenzene (TeMB) is an important process for the indus- H-mordenite (Engelhard, SiO2/Al2O3 45) and H-beta (PQ Corp., = try, mainly due to the increasing demand for p-xylene to be used SiO2/Al2O3 22) used in this study were taken from commercial for the production of polyester resins.
    [Show full text]
  • Working with Hazardous Chemicals
    A Publication of Reliable Methods for the Preparation of Organic Compounds Working with Hazardous Chemicals The procedures in Organic Syntheses are intended for use only by persons with proper training in experimental organic chemistry. All hazardous materials should be handled using the standard procedures for work with chemicals described in references such as "Prudent Practices in the Laboratory" (The National Academies Press, Washington, D.C., 2011; the full text can be accessed free of charge at http://www.nap.edu/catalog.php?record_id=12654). All chemical waste should be disposed of in accordance with local regulations. For general guidelines for the management of chemical waste, see Chapter 8 of Prudent Practices. In some articles in Organic Syntheses, chemical-specific hazards are highlighted in red “Caution Notes” within a procedure. It is important to recognize that the absence of a caution note does not imply that no significant hazards are associated with the chemicals involved in that procedure. Prior to performing a reaction, a thorough risk assessment should be carried out that includes a review of the potential hazards associated with each chemical and experimental operation on the scale that is planned for the procedure. Guidelines for carrying out a risk assessment and for analyzing the hazards associated with chemicals can be found in Chapter 4 of Prudent Practices. The procedures described in Organic Syntheses are provided as published and are conducted at one's own risk. Organic Syntheses, Inc., its Editors, and its Board of Directors do not warrant or guarantee the safety of individuals using these procedures and hereby disclaim any liability for any injuries or damages claimed to have resulted from or related in any way to the procedures herein.
    [Show full text]