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Chemical Structure| 109-08-0 Chemical Structure| 109-08-0
Chemical Structure| 109-08-0

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Product Details of 2-Methylpyrazine

CAS No. :109-08-0
Formula : C5H6N2
M.W : 94.11
SMILES Code : CC1=CN=CC=N1
MDL No. :MFCD00006142
InChI Key :CAWHJQAVHZEVTJ-UHFFFAOYSA-N
Pubchem ID :7976

Safety of 2-Methylpyrazine

GHS Pictogram:
Signal Word:Danger
Hazard Statements:H225-H302-H315-H319-H335
Precautionary Statements:P261-P305+P351+P338
Class:3
UN#:1993
Packing Group:

Application In Synthesis of 2-Methylpyrazine

* All experimental methods are cited from the reference, please refer to the original source for details. We do not guarantee the accuracy of the content in the reference.

  • Downstream synthetic route of [ 109-08-0 ]

[ 109-08-0 ] Synthesis Path-Downstream   1~37

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YieldReaction ConditionsOperation in experiment
39% 2-Methoxybenzonitrile (3.0 g, 22.5 mmol) and 2-methylpyrazine (2.2 g, 23.0 mmol) were dissolved in an ice-water bathIn dry tetrahydrofuran (50 mL) and stirred under nitrogen for 1.5 hours.under this conditionLithium diisopropylamide (23 mL, 45.06 mmol, tetrahydrofuran solution) was slowly added, and the addition was complete and the temperature was raised to 40C and stirring was continued for 3 hours.The reaction solution was cooled to ambient temperature, quenched with ammonium chloride solution, extracted with ethyl acetate (50 mL × 3), dried over anhydrous sodium sulfate, and filtered.The organic layer was concentrated under reduced pressure and the residue was purified by flash column chromatography (petroleum ether/ethyl acetate = 1/1) to give compound 5.1 as a yellow solid.Body (2.2 g, yield: 39%).
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  • L-lysyl-L-phenylalanine [ No CAS ]
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YieldReaction ConditionsOperation in experiment
In water; at 375℃; under 760.051 Torr; for 6h;Inert atmosphere; Flow reactor; The dehydrocyclization activities of Zn?Cr?Ocatalysts calcined at different temperatures were performedat 375°C and atmospheric pressure in a fixedbedvertical quartz reactor (i.d = 8 mm, length =450 mm) placed in a two zone furnace operated in adown flow mode. In the first zone maintained at300°C the reaction mixture was preheated whereas inthe second zone containing the catalyst bed the reactortemperature was set at 375°C. Temperatures in theboth zones were monitored by a temperature controller-cum-programmer using a K-type thermocouple.Glycerol (Fluka) and EDA (SDFCL, India) wereused. Nitrogen (IOLAR-I grade, BOC, India) wasused as a carrier gas. The catalytic activities were measured using ?18/+23 sieved (BSS) particles. The carbonmass balance was done based on the inlet and outletconcentration of the organic moiety. Prior to thereaction, the calcined catalyst (about 0.2 g) wasreduced in a flow of 5percent H2 and 95percent Ar (30 mL min?1)at 400°C for 5 h. The catalytic activities were measuredunder strict kinetic control. An aqueous glycerol solution(20 wtpercent in H2O) was used with a glycerol to EDAmole ratio of 1 :1 , at a flow rate of 5 mL h?1 (10 mmolglycerol + 10 mmol EDA + 200 mmol H2O), alongwith N2 as a carrier gas at a flow rate of 1800 mL h?1.The feed mixture mole ratio is glycerol : EDA : H2O :N2= 1 : 1 : 20 : 8. The product mixture was analyzed bygas chromatograph (Shimadzu, GC-17A) via a flameionization detector (FID) using a ZB-5 capillary columnat a ramping rate of 10°C min?1 from 60 to280°C. The mass balance for all the measurements was>95percent. The samples were analyzed by GC-MS(QP5050A Shimadzu) using a ZB-5 capillary columnwith EI mode.
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  • (E)-N,N-dimethyl-5-(2-(pyrazin-2-yl)vinyl)thiophen-2-amine [ No CAS ]
 

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