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Type | HazMat fee for 500 gram (Estimated) |
Excepted Quantity | USD 0.00 |
Limited Quantity | USD 15-60 |
Inaccessible (Haz class 6.1), Domestic | USD 80+ |
Inaccessible (Haz class 6.1), International | USD 150+ |
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Accessible (Haz class 3, 4, 5 or 8), International | USD 200+ |
Structure of 617-55-0
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Search for reports by entering the product batch number.
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Search for reports by entering the product batch number.
Batch number can be found on the product's label following the word 'Batch'.
Search for reports by entering the product batch number.
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CAS No. : | 617-55-0 |
Formula : | C6H10O5 |
M.W : | 162.14 |
SMILES Code : | C([C@@H](O)CC(=O)OC)(=O)OC |
MDL No. : | MFCD00066215 |
InChI Key : | YSEKNCXYRGKTBJ-BYPYZUCNSA-N |
Pubchem ID : | 10285815 |
GHS Pictogram: |
![]() ![]() ![]() |
Signal Word: | Danger |
Hazard Statements: | H226-H317-H318 |
Precautionary Statements: | P210-P233-P240-P241-P242-P243-P261-P272-P280-P303+P361+P353-P305+P351+P338+P310-P333+P313-P370+P378-P403+P235-P501 |
Class: | 3 |
UN#: | 1993 |
Packing Group: | Ⅲ |
Num. heavy atoms | 11 |
Num. arom. heavy atoms | 0 |
Fraction Csp3 | 0.67 |
Num. rotatable bonds | 5 |
Num. H-bond acceptors | 5.0 |
Num. H-bond donors | 1.0 |
Molar Refractivity | 34.69 |
TPSA ? Topological Polar Surface Area: Calculated from |
72.83 ?2 |
Log Po/w (iLOGP)? iLOGP: in-house physics-based method implemented from |
1.3 |
Log Po/w (XLOGP3)? XLOGP3: Atomistic and knowledge-based method calculated by |
-0.68 |
Log Po/w (WLOGP)? WLOGP: Atomistic method implemented from |
-0.92 |
Log Po/w (MLOGP)? MLOGP: Topological method implemented from |
-0.58 |
Log Po/w (SILICOS-IT)? SILICOS-IT: Hybrid fragmental/topological method calculated by |
-0.29 |
Consensus Log Po/w? Consensus Log Po/w: Average of all five predictions |
-0.24 |
Log S (ESOL):? ESOL: Topological method implemented from |
-0.09 |
Solubility | 133.0 mg/ml ; 0.819 mol/l |
Class? Solubility class: Log S scale |
Very soluble |
Log S (Ali)? Ali: Topological method implemented from |
-0.37 |
Solubility | 68.4 mg/ml ; 0.422 mol/l |
Class? Solubility class: Log S scale |
Very soluble |
Log S (SILICOS-IT)? SILICOS-IT: Fragmental method calculated by |
0.1 |
Solubility | 204.0 mg/ml ; 1.26 mol/l |
Class? Solubility class: Log S scale |
Soluble |
GI absorption? Gatrointestinal absorption: according to the white of the BOILED-Egg |
High |
BBB permeant? BBB permeation: according to the yolk of the BOILED-Egg |
No |
P-gp substrate? P-glycoprotein substrate: SVM model built on 1033 molecules (training set) |
No |
CYP1A2 inhibitor? Cytochrome P450 1A2 inhibitor: SVM model built on 9145 molecules (training set) |
No |
CYP2C19 inhibitor? Cytochrome P450 2C19 inhibitor: SVM model built on 9272 molecules (training set) |
No |
CYP2C9 inhibitor? Cytochrome P450 2C9 inhibitor: SVM model built on 5940 molecules (training set) |
No |
CYP2D6 inhibitor? Cytochrome P450 2D6 inhibitor: SVM model built on 3664 molecules (training set) |
No |
CYP3A4 inhibitor? Cytochrome P450 3A4 inhibitor: SVM model built on 7518 molecules (training set) |
No |
Log Kp (skin permeation)? Skin permeation: QSPR model implemented from |
-7.77 cm/s |
Lipinski? Lipinski (Pfizer) filter: implemented from |
0.0 |
Ghose? Ghose filter: implemented from |
None |
Veber? Veber (GSK) filter: implemented from |
0.0 |
Egan? Egan (Pharmacia) filter: implemented from |
0.0 |
Muegge? Muegge (Bayer) filter: implemented from |
1.0 |
Bioavailability Score? Abbott Bioavailability Score: Probability of F > 10% in rat |
0.55 |
PAINS? Pan Assay Interference Structures: implemented from |
0.0 alert |
Brenk? Structural Alert: implemented from |
1.0 alert: heavy_metal |
Leadlikeness? Leadlikeness: implemented from |
No; 1 violation:MW<1.0 |
Synthetic accessibility? Synthetic accessibility score: from 1 (very easy) to 10 (very difficult) |
2.57 |
* 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.
Yield | Reaction Conditions | Operation in experiment |
---|---|---|
With hydrogen; In Dimethyl ether; at 56 - 110℃; under 120012.0 Torr; for 0.5 - 2h;Product distribution / selectivity; | HYDROGENATION OF DIMETHYL MALATE:; The following conditions were used Hydrogen pressure 0,1, 10 and 30 bar Substrate 0,4 and 1,5 mol% Catalyst CuMn AI203, particle size 90-180 um Samples are taken at regular intervals after the substrate feed is started. Experiment 1: This was performed according to the procedure described above in Materials, Equipment and Activation Procedure. The reaction temperature was 56C, Hydrogen pressure was 10bar, DME pressure was 150bar, substrate concentration in solution was 0.4 mol%, and 10G of catalyst were used. The following results were obtained: Time on DM L DE BT HGB H-THF HGB equiv Selectivity stream area% area% 5 67.5 0.22 15.16 0.14 15.86 0.1 31.02 95.4% 13 58.4 0.09 21.45 0.27 18.29 0.07 39.74 95.5% 20 63.1 0.15 19.8 0.37 15.6 0.07 35.4 95.9% 30 67.8 0.07 18.2 0.58 12.39 0.06 30.59 95.0% 60 76.5 0.04 15 0.48 7.22 0.04 22.22 94.6% DM = dimethyl malate L = 2 (5H)-Furanone DE = 3,4-dihydroxy methyl butyrate ester BT = butanetriol HGB = 3-hydroxy-gammabutyrolactone (produced by in-situ cyclisation of 3,4-dihydroxy methyl butyrate ester) H-THF = hydroxy-THF Notes: HGB EQUIVALENT = area%"HGB"+ area%"Dihydroxy ester" (as hydroxy ester can be cyclise to HGB) SELECTIVITY DEFINED AS (AREA% USEFUL PRODUCTS) / (AREA % OF ALL PRODUCTS) HGB (S) was obtained in 97.9% ee Experiment 2: This was performed according to the procedure described above in Materials, Equipment and Activation Procedure. The reaction temperature was 110C, Hydrogen pressure was 10bar, DME pressure was 150bar, substrate concentration in solution was 1.5 mol%, and 5.9g of catalyst were used. The following results were obtained : Time on DM L DE BT HGB H-THF HGB equiv Selectivity stream area% area% 5 64.1 0.55 18.22 1.6 15.3 33.52 93.4% 15 72.6 0.24 15.38 0.9 10 0.1 25.38 92.6% 30 77.6 0.16 13.3 0.5 7.8 0.1 21.1 94.2% Note: HGB (S) obtained in 98.8% ee Conclusion: These experiments illustrate high selectivity for HGB in the hydrogenation of dimethyl malate EXPERIMENT-MEOH removal and the effect on the conversion of LDMM to HGB Experiment 3: This was performed according to the procedure described above in Materials, Equipment and Activation Procedure. The reaction temperature was 80C, Hydrogen pressure was 10bar, DME pressure was 150bar, substrate concentration in solution was 0.4 mol%, and 87g of catalyst were used. After 2 hours on stream, the product was found to contain 39.8 area% starting material and 51.5 area% HGB-EQUIVALENT (as defined in Example 1). The product was formed with 85.5% selectivity. The collected product from this experiment, after depressurisation and removal of Methanol, was used as the feed for another hydrogenation, under otherwise identical conditions. The following results were obtained. Time on DM area% L DE BT HGB HGB Selectivity stream equiv area% 50 14.7 5.3 15.2 8 47.4 62.6 73.4% 60 18. 8 4.4 14. 8 11.7 45.5 60.3 74.3% 75 21.15 3.7 21.1 11.5 43.2 64. 3 81.5% 90 13. 4 7. 1 5.5 59.1 66.2 76.4% 105 26.7 3.4 17.5 8.7 40.6 58. 1 79.3% 120 25.6 2.3 17.7 9.5 42 59.7 80. 2% Conclusions : When the reaction products from one incomplete hydrogenation are depressurised and Methanol removed by evaporation, then re-hydrogenated the conversion is increased FROM-50% TO-60%, and the selectivity remains approximately constant. |
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