Method for co-production of dimethyl decynediol and methyl hexynol
A technology of dimethyl decyne diol and methyl hexynol, which is applied in the field of co-production of dimethyl decyne diol and methyl hexynol, can solve the problems of high temperature, long reaction time and large molecular structure steric hindrance. and other problems, to achieve the effect of improving production efficiency, low reaction temperature, and inhibiting side reactions
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Examples
Embodiment 1
[0038] (1) Put 1750g of ethyl butyl ether as solvent and 250g of potassium tert-butoxide (industrial grade, purity 98%) into the grinder in order to grind it into a slurry, transfer it to the reaction kettle, start stirring, and heat to 70℃~ Keep at 80°C for 1 hour, then lower the temperature to 15°C to 20°C for control. Feed acetylene gas, keep the acetylene pressure in the range of 0.1MPa-0.12MPa, and react for 1.5 hours.
[0039] (2) Add 360g of 2-pentanone (industrial grade, purity 99.5%) into the reactor from the overhead tank evenly and slowly, and control the addition within 80-100 minutes, while keeping the acetylene pressure in the range of 01MPa-0.12MPa for reaction. After adding 2-pentanone, gradually raise the reaction temperature to 33°C to 35°C at a rate of 1°C to 2°C every about 10 minutes and keep it there. After the reaction lasted for about 3.5 hours, the residual 5-methyl-2-hexanone in the reaction material was sampled and detected to be less than 8%, and t...
Embodiment 2
[0048] The operation was carried out according to the operation method of Example 1, wherein: the feeding material in the operation step (1) was 2000 g of solvent n-butyl ether, and the catalyst was 140 g of potassium hydroxide (industrial grade, purity 94%). The pressure of acetylene is 0.1MPa~0.12MPa.
[0049] The feeding material in operation step (2) is 370 g of 2-pentanone (industrial grade, purity 99.5%), which is equivalent to 2-pentanone: potassium hydroxide (pure) = 1.1:1 (molar ratio). The pressure of acetylene is 0.12MPa~0.14MPa.
[0050] In the operation step (3), the feeding material is 2-pentanone (industrial grade, purity 99.5%) 268g, the total amount of 2-pentanone added twice: potassium hydroxide (pure) = 1.9:1 (molar ratio) . Control the entry temperature of the water medium at 78°C to 80°C; control the residence time of the reaction materials in the reaction tube for 1 to 1.5 minutes. The total amount of clear water used to terminate the reaction is about...
Embodiment 3
[0053] The operation was carried out according to the operation method of Example 1, wherein: the feed in the operation step (1) was 1800 g of solvent xylene, and the catalyst was 260 g of potassium isobutoxide (self-made, purity 97.5%). The pressure of acetylene is 0.1MPa~0.12MPa.
[0054] The feeding material in operation step (2) is 390 g of 2-pentanone (industrial grade, purity 99.5%), which is equivalent to 2-pentanone:potassium isobutoxide (purity)=1.21:1 (molar ratio). The pressure of acetylene is 0.08MPa~0.1MPa.
[0055] In the operation step (3), the feeding material is 2-pentanone (industrial grade, purity 99.5%) 208g, the total amount of 2-pentanone added twice: potassium isobutoxide (pure) = 1.85:1 (molar ratio ). Control the entry temperature of the water medium at 62°C to 64°C; control the residence time of the reaction materials in the reaction tube for 2.5 to 3 minutes. The total amount of clear water used to terminate the reaction is about 550g.
[0056] F...
PUM
Abstract
Description
Claims
Application Information
- R&D Engineer
- R&D Manager
- IP Professional
- Industry Leading Data Capabilities
- Powerful AI technology
- Patent DNA Extraction
Browse by: Latest US Patents, China's latest patents, Technical Efficacy Thesaurus, Application Domain, Technology Topic, Popular Technical Reports.
© 2024 PatSnap. All rights reserved.Legal|Privacy policy|Modern Slavery Act Transparency Statement|Sitemap|About US| Contact US: help@patsnap.com