Home Cart 0 Sign in  

[ CAS No. 32360-05-7 ] {[proInfo.proName]}

,{[proInfo.pro_purity]}
Cat. No.: {[proInfo.prAm]}
Chemical Structure| 32360-05-7
Chemical Structure| 32360-05-7
Structure of 32360-05-7 * Storage: {[proInfo.prStorage]}
Cart0 Add to My Favorites Add to My Favorites Bulk Inquiry Inquiry Add To Cart

Quality Control of [ 32360-05-7 ]

Related Doc. of [ 32360-05-7 ]

Alternatived Products of [ 32360-05-7 ]

Product Details of [ 32360-05-7 ]

CAS No. :32360-05-7 MDL No. :MFCD00026683
Formula : C22H42O2 Boiling Point : -
Linear Structure Formula :- InChI Key :HMZGPNHSPWNGEP-UHFFFAOYSA-N
M.W : 338.57 Pubchem ID :122600
Synonyms :

Safety of [ 32360-05-7 ]

Signal Word:Warning Class:N/A
Precautionary Statements:P261-P305+P351+P338 UN#:N/A
Hazard Statements:H315-H319-H335 Packing Group:N/A
GHS Pictogram:

Application In Synthesis of [ 32360-05-7 ]

* 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.

  • Upstream synthesis route of [ 32360-05-7 ]
  • Downstream synthetic route of [ 32360-05-7 ]

[ 32360-05-7 ] Synthesis Path-Upstream   1~4

  • 1
  • [ 112-89-0 ]
  • [ 920-46-7 ]
  • [ 32360-05-7 ]
YieldReaction ConditionsOperation in experiment
76% for 5 h; 1) 20 g of octabromohydrin was added to a 1000 ml single-necked flask, 250 ml of dichloropropane and 17.7 g of triethylamine were added, and 16.65 g of methacryloyl chloride was added dropwise with stirring. After completion of the dropwise addition, stirring was continued for 5 hours. After completion of the reaction, the system was washed with water and saturated sodium carbonate and saturated brine, respectively. The organic phase was dried over anhydrous sodium sulfate, concentrated, and chromatographed. 18.4 g of octadecyl methacrylate was obtained in a yield of 76percent.
Reference: [1] Patent: CN105906664, 2016, A, . Location in patent: Paragraph 0041; 0042
  • 2
  • [ 112-92-5 ]
  • [ 80-62-6 ]
  • [ 32360-05-7 ]
YieldReaction ConditionsOperation in experiment
99.3 %Chromat.
Stage #1: for 1 h; Heating / reflux
Stage #2: at 111 - 129℃; for 4 h;
Example 2; The same reaction apparatus as used in Example 1 was used. First, the reactor was charged with 750.9 9 (7.5 mol) of methyl methacrylate, 676.3 g (2.5 mol) of stearyl alcohol and 0.042 g of 4-acetylamino-2,2,6,6-tetramethylpiperidine-N-oxyl, and the mixture was then heated to conduct dehydration in the reaction system over a period of 1 hour under the total reflux. Then, the reactor was cooled and charged with 1.23 g (0.005 mol) of tetramethyl titanate (purity: 70percent), and heating was begun again. And thereafter, the ester-exchange reaction was carried out in the same manner as in Example 1. At the beginning of the reaction, the operation was conducted under the total reflux, and the removal of an azeotropic mixture of methanol/methyl methacrylate from the reaction system was started at the time when the temperature of the uppermost stage in the distillation column reached 64.5° C., the temperature of the middle stage 74° C., and the temperature of the lowest stage 98.8° C. (the conversion of 4percent at this time). Thereafter, until the conversion reached 97percent, the reaction was carried out while controlling the reflux ratio within the range of 5 to 50, so as to maintain the temperature of the uppermost stage in the distillation column at 64 to 65° C., the temperature of the middle stage at 70 to 80° C., and the temperature of the lowest stage at 99 to 100° C. After 4 hours from the beginning of the reaction, the conversion reached 98percent and the temperature of the middle stage in the distillation column rose to 93° C. Thereafter, in order to completely remove, from the reaction system, methanol contained in the liquid refluxed from the uppermost stage in the distillation column to the uppermost stage in the distillation column again through the condenser and the reflux line, the reflux ratio was set to zero, and thereby all the liquid in the reflux line was distilled off until the temperature of the uppermost stage in the distillation column was stably maintained at 98° C. or higher. Thus, the reaction was terminated. The reaction time was 4.5 hours. During this time, the temperature of the uppermost stage in the distillation column was maintained at 95° C. or higher, and the temperatures of the middle stage and the lowest stage in the distillation column were maintained at 99° C. or higher. The amount of the azeotropic mixture of methanol/methyl methacrylate removed was 124.5 g, and the content of methanol was 62.8percent (78.2 g) and the content of methyl methacrylate was 37.2percent (46.3 g). When 1297.7 g of the resulting reaction solution in the reactor was analyzed by gas chromatography, it contained 35.0percent of methyl methacrylate, 0percent of stearyl alcohol and 64.8percent of stearyl methacrylate, and the yield was 99.3percent.
Reference: [1] Patent: US2006/84823, 2006, A1, . Location in patent: Page/Page column 5-6
[2] Patent: US2129662, 1934, ,
  • 3
  • [ 112-92-5 ]
  • [ 920-46-7 ]
  • [ 32360-05-7 ]
Reference: [1] Macromolecules, 2014, vol. 47, # 2, p. 589 - 600
[2] Organic Process Research and Development, 2004, vol. 8, # 3, p. 461 - 468
  • 4
  • [ 112-92-5 ]
  • [ 79-41-4 ]
  • [ 32360-05-7 ]
Reference: [1] Journal of Polymer Science, 1959, vol. 38, p. 209,210-212[2] Chem.Abstr., 1960, # 9347,
Same Skeleton Products
Historical Records