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llms.txt · MCP 가이드개인정보처리방침 · 이용약관 · 지원v1.8.0
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Phosphoric Acid → L-Lysinol

HRID 589145
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HRID 589145 반응식
[NH2:1][C@H:2]([C:8](O)=[O:9])[CH2:3][CH2:4][CH2:5][CH2:6][NH2:7].S(=O)(=O)(O)O.P(=O)(O)(O)O.[H][H].[OH-].[Na+]>O.[Pt].[Re].[Ru].[Pt].[Ru].[Re]>[NH2:1][C@H:2]([CH2:8][OH:9])[CH2:3][CH2:4][CH2:5][CH2:6][NH2:7]
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참가 물질

11

반응물 5

HCID 1004Phosphoric AcidHCID 1118Sulfuric AcidHCID 5962L-Lysine5회HCID 14798Sodium HydroxideHCID 178418361HCID 178418361, 화합물2회

생성물 1

HCID 11607920L-Lysinol

시약·촉매·용매 5

HCID 23939
Platinum
촉매
2회
HCID 23950Ruthenium촉매
HCID 57449507HCID 57449507, 화합물촉매
HCID 60209655HCID 60209655, 화합물촉매
HCID 962Water용매

실험 절차

In particular, the process comprises charging a high pressure reactor with a solution of lysine in water, acid, and a hydrogenation catalyst. The high pressure reactor may be a batch, continuous, or semi-continuous reactor. The acid including, but not limited to sulfuric acid or phosphoric acid, is present in an amount of at least 0.5 molar equivalent of lysine or 1 molar equivalent or of lysine or 2 molar equivalent of lysine. Alternatively, the pH of the aqueous lysine solution can be adjusted with an acid to a pH in the range of 1-5 or 1.5-4 or 2-3. The catalyst is present in an amount in the range of 0.2-50% or 0.5-10% or 1-5% by weight of the total reaction mass. The hydrogenation catalyst can be chosen from those known in the art, for example ruthenium supported on carbon, platinum supported on carbon, platinum supported on titanium dioxide, or supported rhenium-ruthenium or rhenium-platinum catalysts. The process further comprises filling the reactor with hydrogen up to a pressure in the range of 0.7-14 MPa or 1.5-11 MPa or 2-9 MPa at a temperature in the range of 50-220° C. or 100-200° C. or 120-180° C. The process also comprises maintaining the pressure until ceasing of hydrogen uptake. The process further comprises cooling the reactor to room temperature and adding sodium hydroxide until pH is greater than 12. The process also comprises removing water and extracting the resulting residue, a mixture of lysinol and salt, with a solvent that will dissolve lysinol but not the salts and then removing the solvent to obtain lysinol in the form of a colorless oil. In an embodiment, the lysinol is enantioenriched (S)-lysinol. In another embodiment, the ratio of (S)-lysinol to (R)-lysinol is in the range of 99.9:0.1 to 51:49 or 98:2 to 70:30 or 95:5 to 80:20.

후처리

  1. customin the range of 50-220° C. or 100-200° C. or 120-180° C
  2. customThe process also comprises removing water
  3. extractionextracting the resulting residue
  4. additiona mixture of lysinol and salt
  5. dissolutionwith a solvent that will dissolve lysinol
  6. customnot the salts and then removing the solvent

출처 및 근거

ORD 기록
ord-0ede03ce02ce4832a6e74ecb4e8bbc43
출처 데이터셋
uspto-grants-2016_01
DOI
10.6084/m9.figshare.5104873.v1
특허 번호
US09228056B2

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