IPC분류정보
국가/구분 |
United States(US) Patent
등록
|
국제특허분류(IPC7판) |
|
출원번호 |
US-0144440
(2008-06-23)
|
등록번호 |
US-8502000
(2013-08-06)
|
발명자
/ 주소 |
- Hassan, Abbas
- Bagherzadeh, Ebrahim
- Anthony, Rayford G.
- Borsinger, Gregory
- Hassan, Aziz
|
출원인 / 주소 |
|
대리인 / 주소 |
|
인용정보 |
피인용 횟수 :
0 인용 특허 :
15 |
초록
▼
Methods and systems for the hydroxylation of olefenic alcohols are described herein. The methods and systems incorporate the novel use of a high shear device to promote mixing and solubility of peroxides with the olefenic alcohol. The high shear device may allow for lower reaction temperatures and p
Methods and systems for the hydroxylation of olefenic alcohols are described herein. The methods and systems incorporate the novel use of a high shear device to promote mixing and solubility of peroxides with the olefenic alcohol. The high shear device may allow for lower reaction temperatures and pressures and may also reduce hydroxylation time with existing catalysts.
대표청구항
▼
1. A method of producing glycerol comprising: a) introducing a peroxide stream into an olefenic alcohol stream to form a reactant stream;b) feeding said reactant stream into a high shear device that subjects said reactant stream to a shear rate of greater than about 20,000s−1, wherein the high shear
1. A method of producing glycerol comprising: a) introducing a peroxide stream into an olefenic alcohol stream to form a reactant stream;b) feeding said reactant stream into a high shear device that subjects said reactant stream to a shear rate of greater than about 20,000s−1, wherein the high shear device comprises a rotor and a stator separated by a shear gap; andc) contacting the reactant stream with a catalyst in a reactor to hydroxylate the olefenic alcohol and produce glycerol. 2. The method of claim 1, wherein the shear gap is in the range of from about 0.02 mm to about 5 mm. 3. The method of claim 1 wherein the peroxide stream comprises hydrogen peroxide, ethylbenzyl hydroperoxide, t-butyl hydroperoxide, t-amyl hydroperoxide, cumene hydroperoxide, 2-methyl-2-hydroperoxy-methyl proprionate, 2-methyl-2-hydroperoxy propanoic acid, pyrrolehydroperoxide, furan hydroperoxide, 2-butylhydroperoxide, cyclohexyl hydroperoxide, and 1-phenyl-ethylhydroperoxide, or combination thereof. 4. The method of claim 1 wherein the olefenic alcohol stream comprises allyl alcohol, methallyl alcohol, cinnamyl alcohol, methyl vinyl carbinol, dimethyl allyl alcohol, oleyl alcohol, methyl vinyl carbinol, crotyl alcohol, methyallyl alcohol, cyclohexenol, or combinations thereof. 5. The method of claim 1, wherein said high shear device operates at a tip speed of at least about 23 m/sec, and wherein each of the rotor and the stator comprise a toothed surface. 6. The method of claim 1, wherein the high shear device operates with an energy expenditure of at least about 1000 W/m3, and wherein the high shear device comprises a second rotor and a second stator separated by a second shear gap. 7. The method of claim 1, further comprising mixing additional catalyst with at least a portion of the reactant stream to form a slurry. 8. The method of claim 1 wherein the catalyst comprises a metal oxide, a tungstic catalyst, an osmium catalyst, formic acid, sulfonic acid, sulfuric acid, or combinations thereof. 9. The method of claim 1, further comprising a second high shear device in fluid communication with the reactor. 10. A method of producing glycerol comprising: introducing a peroxide stream into an olefenic alcohol stream to form a reactant stream;feeding said reactant stream into a high shear device operates with an energy expenditure of at least about 1000 W/m3, wherein the high shear device comprises a rotor and a stator separated by a shear gap; andcontacting the reactant stream with a catalyst in a reactor to hydroxylate the olefenic alcohol and produce glycerol. 11. The method of claim 10, wherein the shear gap is in the range of from about 0.02 mm to about 5 mm. 12. The method of claim 10, wherein, the peroxide stream comprises hydrogen peroxide, ethylbenzyl hydroperoxide, t-butyl hydroperoxide, t-amyl hydroperoxide, cumene hydroperoxide, 2-methyl-2-hydroperoxy-methyl proprionate, 2-methyl-2-hydroperoxy propanoic acid, pyrrolehydroperoxide, furan hydroperoxide, 2-butylhydroperoxide, cyclohexyl hydroperoxide, and 1-phenyl-ethylhydroperoxide, or combination thereof. 13. The method of claim 10, further comprising mixing additional catalyst with at least a portion of the reactant stream to form a slurry. 14. The method of claim 10, wherein the catalyst comprises a metal oxide, a tungstic catalyst, an osmium catalyst, formic acid, sulfonic acid, sulfuric acid, or combinations thereof. 15. A method of producing glycerol comprising: introducing a peroxide stream into an olefenic alcohol stream to form a reactant stream;feeding said reactant stream into a high shear device that subjects said reactant stream to a shear rate greater than about 20,000s−1, wherein the high shear device comprises a rotor and a stator separated by a shear gap, wherein the shear gap is in the range of from about 0.02 mm to about 5 mm; andcontacting the reactant stream with a catalyst in a reactor to hydroxylate the olefenic alcohol and produce glycerol.
※ AI-Helper는 부적절한 답변을 할 수 있습니다.