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6-(Acetylamino)hexanoic acid

Detailed Information

  • Product Name:6-(Acetylamino)hexanoic acid
  • CasNo.:57-08-9
  • MF:C8H15 N O3
  • MW:173.212

pd_nature

  • Purity:99%
  • pd_boiling:102-106 ºC
  • Packing:White.
  • Throughput:

Product Details;

CasNo: 57-08-9

MF: C8H15 N O3

Appearance: White.

Chinese Manufacturer Supply 6-(Acetylamino)hexanoic acid 57-08-9 On Stock with Competitive Price

  • Molecular Formula:C8H15 N O3
  • Molecular Weight:173.212
  • Appearance/Colour:White. 
  • Vapor Pressure:1.12E-07mmHg at 25°C 
  • Melting Point:102-106 ºC 
  • Refractive Index:1.4590 (estimate) 
  • Boiling Point:404.5°Cat760mmHg 
  • PKA:4.75±0.10(Predicted) 
  • Flash Point:198.4°C 
  • PSA:66.40000 
  • Density:1.074g/cm3 
  • LogP:1.15840 

6-Acetamidohexanoic acid(Cas 57-08-9) Usage

Manufacturing Process

400 L of demineralized water, 5.0 kg of calcium hydroxide, and 155.0 kg (1000 moles) of acetyl-caprolactame are introduced under stirring and at a temperature of about 25°C into a 1000 L stainless double walled reactor. The temperature is raised to 30°C. 75.0 kg of calcium hydroxide are introduced stepwise in the form of successive amounts of 2.0 kg each in the medium, under stirring and at a temperature adjusted and maintained 25°- 30°C through external cooling, in a manner such that the time required to introduce into the reactor the whole amount of calcium hydroxide approximates 1.5 h. When the stirring is stopped, the pH is about 7.5-7.8. The obtained mixture is stirred continuously at a temperature of 30°C during 14 h. At the end of this operation the pH is again adjusted at a value 7.5-7.8. The hydrolysate is filtered on a 60 x 60 pressfilter comprising 6 compartments and equipped with fabrics of the polyester known under the designation TERGAL which have been previously coated with a suspension of a cellulose commercialized under the trademark SOLKA FLOX BW20. The duration of filtration is of 1.5 h. 580 L of the filtrate are recovered and subjected to a concentration under reduced pressure in an evaporator the volume of which is of 750 L, at a distillation temperature ranging from 45°-50°C under a reduced pressure of 10-15 Torr. The operation is ran until concentration of the solution to 280 L, the concentrated solution being then left standing. The crystallisation is already considerable 2 h after the end of the operation of concentration. Crystallisation is ended after 16-24 h. The crystals are centrifuged at a speed of 700 revolutions/minute. The centrifuged crystals of calcium acexamate are washed twice on the centrifuge with 20 l of acetone. 107.0 kg of crystals are obtained, which are dried under vacuum at 40°C. The 96.0 kg of dry calcium acexamate obtained are ground and sifted. Acexamic acid may be produced by treatment of the calcium acexamate with HCl.

Therapeutic Function

Antifibrinolytic

InChI:InChI=1/C8H15NO3/c1-7(10)9-6-4-2-3-5-8(11)12/h2-6H2,1H3,(H,9,10)(H,11,12)/p-1

57-08-9 Relevant articles

Examination of the Aspirin Acetylation Site of Human Serum Albumin by 13C NMR Spectroscopy

Gerig, J. T.,Katz, K. E.,Reinheimer, J. D.,Sullivan, Glenn R.,Roberts, John D.

, p. 158 - 161 (1981)

Human serum albumin has been specificall...

Ferrocene-biotin conjugates targeting cancer cells: Synthesis, interaction with avidin, cytotoxic properties and the crystal structure of the complex of avidin with a biotin-linker-ferrocene conjugate

Plaziuk, Damian,Zakrzewski, Janusz,Salmain, Michele,Blauzi, Andrzej,Rychlik, Blaziej,Strzelczyk, Pawel,Bujacz, Anna,Bujacz, Grzegorz

, p. 5774 - 5783 (2013)

Friedel-Crafts acylation of ferrocene wi...

CXCR4-TARGETED DIAGNOSTIC AND THERAPEUTIC AGENTS WITH REDUCED SPECIES SELECTIVITY

-

Page/Page column 64, (2020/05/07)

The present disclosure relates to imagin...

Generation of amine dehydrogenases with increased catalytic performance and substrate scope from ε-deaminating L-Lysine dehydrogenase

Tseliou, Vasilis,Knaus, Tanja,Masman, Marcelo F.,Corrado, Maria L.,Mutti, Francesco G.

, (2019/08/22)

Amine dehydrogenases (AmDHs) catalyse th...

Method for synthesizing hexanediamine by taking caprolactam as raw material

-

Paragraph 0030; 0033; 0034; 0048; 0051; 0052, (2019/11/21)

The invention discloses a method for syn...

Energetic contribution to both acidity and conformational stability in peptide models

Kubyshkin, Vladimir,Durkin, Patrick,Budisa, Nediljko

supporting information, p. 5209 - 5220 (2016/07/06)

The acidity of N-acyl amino acids is dep...

57-08-9 Process route

N-acetylcaprolactam
1888-91-1

N-acetylcaprolactam

caprolactam
105-60-2,9012-16-2

caprolactam

6-(acetylamino)hexanoic acid
57-08-9

6-(acetylamino)hexanoic acid

6-aminohexanoic acid
60-32-2,93208-38-9

6-aminohexanoic acid

Conditions
Conditions Yield
With water; at 100 ℃; Product distribution; different time of hydrolysis;
acetic anhydride
108-24-7

acetic anhydride

6-aminohexanoic acid
60-32-2,93208-38-9

6-aminohexanoic acid

6-(acetylamino)hexanoic acid
57-08-9

6-(acetylamino)hexanoic acid

Conditions
Conditions Yield
With N-ethyl-N,N-diisopropylamine; In N,N-dimethyl-formamide; at 0 - 20 ℃;
79%
With pyridine; In benzene;
In dichloromethane; for 0.5h;
With dmap; at 20 ℃; for 0.5h;

57-08-9 Upstream products

  • 1888-91-1
    1888-91-1

    N-acetylcaprolactam

  • 108-24-7
    108-24-7

    acetic anhydride

  • 60-32-2
    60-32-2

    6-aminohexanoic acid

  • 64-19-7
    64-19-7

    acetic acid

57-08-9 Downstream products

  • 3338-03-2
    3338-03-2

    2-methyl-4,5,6,7-tetrahydro-3H-azepine

  • 105-60-2
    105-60-2

    caprolactam

  • 60-32-2
    60-32-2

    6-aminohexanoic acid

  • 124-09-4
    124-09-4

    1,6-Hexanediamine

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