Repository logo
Communities & Collections
Research Outputs
Fundings & Projects
People
Statistics
New user? Click here to register.Have you forgotten your password?
  1. Home
  2. KMITL
  3. Publication
  4. Concentrated lactic acid production from invert sugar in alkaline solution
Loading...
Thumbnail Image

Concentrated lactic acid production from invert sugar in alkaline solution

Author(s)
Sirisangsawang, Rinlada
Kitchaiya, Prakob
Date Issued
January 1, 2019
Type
Article
DOI
10.3303/CET1975103
Abstract
High concentration of lactic acid production is not practical in industry, which is currently produced by fermentation. This work investigated lactic acid synthesis derived from invert sugar in an alkaline solution at low temperature under atmospheric pressure. 30 % invert sugar was continuously added into 3.5 - 8.5 M concentrated sodium hydroxide solutions in a semi-batch reactor at 30 – 80 °C. The central composited design (CCD) was used for design experiments and three variables such as reaction temperature, initial concentration of sodium hydroxide (NaOH) and feed time being investigated. The reaction temperature and initial concentration of NaOH were more pronounced on the yield. At 70 °C, 8.5 M NaOH, and feed time of 6 h. 76 % lactic acid yield was achieved. An independent study at 70 % invert sugar and 15 M NaOH solution caused runaway in a batch reactor, while the yield in a semi-batch reactor was 62 %.
Citation
Chemical Engineering Transactions, 75, 613-618, 2019
Metrics
Get Involved!
  • Source Code
  • Documentation
  • Slack Channel
Make it your own

DSpace-CRIS can be extensively configured to meet your needs. Decide which information need to be collected and available with fine-grained security. Start updating the theme to match your Institution's web identity.

Need professional help?

The original creators of DSpace-CRIS at 4Science can take your project to the next level, get in touch!

Built with DSpace-CRIS software - Extension maintained and optimized by 4Science

  • Accessibility settings
  • Privacy policy
  • End User Agreement
  • Send Feedback