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[ CAS No. 700-57-2 ] {[proInfo.proName]}

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Chemical Structure| 700-57-2
Chemical Structure| 700-57-2
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Product Details of [ 700-57-2 ]

CAS No. :700-57-2 MDL No. :MFCD00074744
Formula : C10H16O Boiling Point : -
Linear Structure Formula :- InChI Key :FOWDOWQYRZXQDP-UHFFFAOYSA-N
M.W : 152.23 Pubchem ID :64149
Synonyms :
Tricyclo[3.3.1.13,7]decan-2-ol

Safety of [ 700-57-2 ]

Signal Word:Warning Class:N/A
Precautionary Statements:P280-P305+P351+P338 UN#:N/A
Hazard Statements:H302 Packing Group:N/A
GHS Pictogram:

Application In Synthesis of [ 700-57-2 ]

* 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 [ 700-57-2 ]
  • Downstream synthetic route of [ 700-57-2 ]

[ 700-57-2 ] Synthesis Path-Upstream   1~13

  • 1
  • [ 700-57-2 ]
  • [ 20098-14-0 ]
Reference: [1] Tetrahedron, 1968, vol. 24, p. 5369 - 5377
  • 2
  • [ 281-23-2 ]
  • [ 122-59-8 ]
  • [ 700-57-2 ]
  • [ 52804-26-9 ]
Reference: [1] Journal of Organic Chemistry USSR (English Translation), 1987, vol. 23, # 9, p. 1672 - 1675[2] Zhurnal Organicheskoi Khimii, 1987, vol. 23, # 9, p. 1882 - 1886
  • 3
  • [ 281-23-2 ]
  • [ 700-58-3 ]
  • [ 768-95-6 ]
  • [ 700-57-2 ]
  • [ 5001-18-3 ]
YieldReaction ConditionsOperation in experiment
31.6% at 120℃; for 6 h; The procedure of Example 1 was repeated, except that the acetic acid serving as a solvent was replaced by propionic acid.
Example 7 The procedure of Example 6 was repeated, except that the amount of the catalyst was changed to 10 μmol.
Example 8 The procedure of Example 6 was repeated, except that the amount of the catalyst was changed to 1.3 μmol.
25.1% at 100℃; for 6 h; The procedure of Example 9 was repeated, except that methanesulfonic acid [CH3SO3H] was added in an amount of 0.004 mL.
23.2% at 100℃; for 6 h; The procedure of Example 9 was repeated, except that europium triflate [Eu(OTf)3] was added in an amount of 10 μmol.
21.7% at 110℃; for 6 h; The procedure of Example 6 was repeated, except that the amount of adamantane employed was changed to 5 mmol, and the catalyst was replaced by Co(acac)2.2H2O.
15.3% at 120℃; for 6 h; The procedure of Example 1 was repeated, except that the catalyst was replaced by a vanadium oxide-TPP complex [VOTPP].
15.5% at 100℃; for 6 h; The procedure of Example 6 was repeated, except that the amount of adamantane employed was changed to 5 mmol, and the reaction temperature was changed to 100° C.

Reference: [1] Chemical Communications, 2018, vol. 54, # 50, p. 6772 - 6775
[2] Patent: US2006/235245, 2006, A1, . Location in patent: Page/Page column 5-7
[3] Patent: US2006/235245, 2006, A1, . Location in patent: Page/Page column 6-7
[4] Patent: US2006/235245, 2006, A1, . Location in patent: Page/Page column 6-7
[5] Patent: US2006/235245, 2006, A1, . Location in patent: Page/Page column 6-7
[6] Patent: US2006/235245, 2006, A1, . Location in patent: Page/Page column 5-7
[7] Patent: US2006/235245, 2006, A1, . Location in patent: Page/Page column 6-7
[8] Tetrahedron Letters, 1995, vol. 36, # 44, p. 8059 - 8062
[9] Journal of Catalysis, 2005, vol. 233, # 1, p. 81 - 89
[10] Chemistry Letters, 2005, vol. 34, # 11, p. 1486 - 1487
  • 4
  • [ 281-23-2 ]
  • [ 64-19-7 ]
  • [ 700-58-3 ]
  • [ 19066-22-9 ]
  • [ 768-95-6 ]
  • [ 700-57-2 ]
  • [ 5001-18-3 ]
  • [ 22635-62-7 ]
  • [ 56137-59-8 ]
  • [ 29817-47-8 ]
YieldReaction ConditionsOperation in experiment
22.3% at 120℃; for 6 h; The procedure of Example 1 was repeated, except that the catalyst was replaced by acetylacetonatovanadium [V(acac)3].
18% at 120℃; for 6 h; Adamantane (10 mmol, 1.36 g) and acetylacetonatovanadyl [VO(acac)2] (5 μmol, 1.3 mg) serving as a catalyst were dissolved in acetic acid (10 mL) placed in a three-neck flask, and oxygen (1 atm) was continuously blown into the flask at a flow rate of 10 mL/min under stirring with a stirrer, to thereby allow partial oxidation of adamantane (ADM) to proceed for six hours at 120° C. The resultant product was subjected to quantitative analysis by means of a gas chromatograph, and as a result, the product was found to contain 1-adamantanol (1-AdOH), 2-adamantanol (2-AdOH), 1,3-adamantanediol (1,3-(AdOH)2), acetic acid esters of them, and 2-adamantanone (2-Ad=O). In the case of this product, adamantane conversion, total yield, and turnover number (TON) were found to be 37.0percent, 25.8percent, and 517, respectively. The results are shown in Table 1. Table 1 also shows analysis results for the cases of the below-described Examples and Referential Examples. As used herein, the turnover number is obtained by use of the following equation: [amount (mol) of adamantane consumed through reaction/amount (mol) of active metal (e.g., vanadium or cobalt) contained in the employed catalyst]. The greater the turnover number, the higher the reaction rate.
Example 2 The procedure of Example 1 was repeated, except that the amount of adamantane employed was changed to 5 mmol.
10.1% at 120℃; for 6 h; The procedure of Example 1 was repeated, except that the catalyst was replaced by ammonium metavanadate [NH4VO3].
Reference: [1] Patent: US2006/235245, 2006, A1, . Location in patent: Page/Page column 5-7
[2] Patent: US2006/235245, 2006, A1, . Location in patent: Page/Page column 5-7
[3] Patent: US2006/235245, 2006, A1, . Location in patent: Page/Page column 5-7
  • 5
  • [ 281-23-2 ]
  • [ 700-57-2 ]
  • [ 5001-18-3 ]
Reference: [1] Tetrahedron Letters, 2009, vol. 50, # 15, p. 1677 - 1680
  • 6
  • [ 281-23-2 ]
  • [ 75-05-8 ]
  • [ 700-58-3 ]
  • [ 768-95-6 ]
  • [ 700-57-2 ]
  • [ 5001-18-3 ]
  • [ 880-52-4 ]
Reference: [1] Applied Catalysis A: General, 2018, vol. 560, p. 171 - 184
  • 7
  • [ 281-23-2 ]
  • [ 768-95-6 ]
  • [ 700-57-2 ]
  • [ 5001-18-3 ]
Reference: [1] Catalysis Today, 2012, vol. 185, # 1, p. 157 - 161
[2] Chemistry - A European Journal, 2013, vol. 19, # 43, p. 14697 - 14701
  • 8
  • [ 281-23-2 ]
  • [ 74087-85-7 ]
  • [ 700-58-3 ]
  • [ 768-95-6 ]
  • [ 700-57-2 ]
  • [ 5001-18-3 ]
  • [ 22635-62-7 ]
Reference: [1] Tetrahedron Letters, 1996, vol. 37, # 2, p. 249 - 252
  • 9
  • [ 281-23-2 ]
  • [ 768-95-6 ]
  • [ 5001-18-3 ]
  • [ 700-57-2 ]
  • [ 20098-16-2 ]
Reference: [1] Journal of the Chemical Society, Perkin Transactions 2: Physical Organic Chemistry (1972-1999), 1996, # 9, p. 1811 - 1820
  • 10
  • [ 700-58-3 ]
  • [ 925-90-6 ]
  • [ 700-57-2 ]
  • [ 14648-57-8 ]
Reference: [1] Chemical Communications, 2010, vol. 46, # 15, p. 2674 - 2676
[2] Chemical Communications, 2010, vol. 46, # 15, p. 2674 - 2676
  • 11
  • [ 10467-10-4 ]
  • [ 700-58-3 ]
  • [ 75-03-6 ]
  • [ 700-57-2 ]
  • [ 14648-57-8 ]
Reference: [1] Patent: US2003/120106, 2003, A1,
  • 12
  • [ 281-23-2 ]
  • [ 103-84-4 ]
  • [ 700-57-2 ]
  • [ 1459-50-3 ]
Reference: [1] Journal of Organic Chemistry USSR (English Translation), 1987, vol. 23, # 9, p. 1672 - 1675[2] Zhurnal Organicheskoi Khimii, 1987, vol. 23, # 9, p. 1882 - 1886
  • 13
  • [ 700-57-2 ]
  • [ 20098-17-3 ]
Reference: [1] Petroleum Chemistry, 2004, vol. 44, # 2, p. 126 - 133
[2] Tetrahedron, 1968, vol. 24, p. 5369 - 5377
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