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  • 2111067-88-8 Structure
  • Basic information

    1. Product Name: C12H9F2NO2
    2. Synonyms:
    3. CAS NO:2111067-88-8
    4. Molecular Formula:
    5. Molecular Weight: 237.206
    6. EINECS: N/A
    7. Product Categories: N/A
    8. Mol File: 2111067-88-8.mol
  • Chemical Properties

    1. Melting Point: N/A
    2. Boiling Point: N/A
    3. Flash Point: N/A
    4. Appearance: N/A
    5. Density: N/A
    6. Refractive Index: N/A
    7. Storage Temp.: N/A
    8. Solubility: N/A
    9. CAS DataBase Reference: C12H9F2NO2(CAS DataBase Reference)
    10. NIST Chemistry Reference: C12H9F2NO2(2111067-88-8)
    11. EPA Substance Registry System: C12H9F2NO2(2111067-88-8)
  • Safety Data

    1. Hazard Codes: N/A
    2. Statements: N/A
    3. Safety Statements: N/A
    4. WGK Germany:
    5. RTECS:
    6. HazardClass: N/A
    7. PackingGroup: N/A
    8. Hazardous Substances Data: 2111067-88-8(Hazardous Substances Data)

2111067-88-8 Usage

Check Digit Verification of cas no

The CAS Registry Mumber 2111067-88-8 includes 10 digits separated into 3 groups by hyphens. The first part of the number,starting from the left, has 7 digits, 2,1,1,1,0,6 and 7 respectively; the second part has 2 digits, 8 and 8 respectively.
Calculate Digit Verification of CAS Registry Number 2111067-88:
(9*2)+(8*1)+(7*1)+(6*1)+(5*0)+(4*6)+(3*7)+(2*8)+(1*8)=108
108 % 10 = 8
So 2111067-88-8 is a valid CAS Registry Number.

2111067-88-8Downstream Products

2111067-88-8Relevant articles and documents

Pyrrolecarboxylic acid derivative synthesis method

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Paragraph 0116; 0120-0121; 0123, (2019/11/04)

The invention discloses a pyrrolecarboxylic acid derivative synthesis method, which comprises: obtaining a group substituted formylacetone derivative by using a group substituted acetyl derivative andethyl acetate as raw materials; carrying out cyclization with diethyl aminomalonate hydrochloride to generate a pyrrolecarboxylic acid derivative ethyl ester; and carrying out a hydrolysis reaction to obtain the target product pyrrolecarboxylic acid derivative. According to the present invention, the method has characteristics of mild reaction conditions, simple purification, high yield and highproduct purity, and is suitable for process amplification and mass production.

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