Method for treating itaconic acid fermentation mother liquor through multistage extraction and steam stripping coupling
A technology of itaconic acid and mother liquor, applied in the separation/purification of carboxylic acid compounds, organic chemistry, etc., can solve the problems of low removal rate, waste of resources, high energy consumption of separation and treatment of itaconic acid fermenting yeast liquid technology, and achieve a solution Higher cost, promoting the effect of promotion and application
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Image
Examples
Embodiment 1
[0028] Feed flow rate is 100kg / h, contains itaconic acid 7%, water 93% (mass fraction) in the feed, the operating pressure of extraction kettle (V1), extraction kettle (V2), extraction kettle (V3) is 0.01atm, The itaconic acid and water mixture enters from the top of the extraction kettle (V1), extraction kettle (V2), and extraction kettle (V3), and the extractant enters from the top of the extraction kettle (V1), extraction kettle (V2), and extraction kettle (V3). Enter, extraction agent is ethyl acetate, and flow rate is 100kg / h (the feed flow mass ratio of extraction agent and phenol-water mixture is 1), extraction kettle (V1), extraction kettle (V2), extraction kettle (V3) The temperature is 30°C. The theoretical plate number of the stripping column (T) is 20, the purity of the itaconic acid after separation is 99.9%, and the yield is 95.1%.
Embodiment 2
[0030] Feed flow rate is 100kg / h, contains itaconic acid 8%, water 92% (mass fraction) in the feed, the operating pressure of extraction kettle (V1), extraction kettle (V2), extraction kettle (V3) is 0.015atm, The itaconic acid and water mixture enters from the top of the extraction kettle (V1), extraction kettle (V2), and extraction kettle (V3), and the extractant enters from the top of the extraction kettle (V1), extraction kettle (V2), and extraction kettle (V3). Enter, extraction agent is ethyl acetate, and flow rate is 200kg / h (the feed flow mass ratio of extraction agent and phenol-water mixture is 2), extraction kettle (V1), extraction kettle (V2), extraction kettle (V3) The temperature is 30°C. The theoretical plate number of the stripping column (T) is 15, the purity of the itaconic acid after separation is 99.96%, and the yield is 95.0%.
Embodiment 3
[0032] Feed flow rate is 100kg / h, contains itaconic acid 9%, water 91% (mass fraction) in the feed, the operating pressure of extraction kettle (V1), extraction kettle (V2), extraction kettle (V3) is 0.02atm, The itaconic acid and water mixture enters from the top of the extraction kettle (V1), extraction kettle (V2), and extraction kettle (V3), and the extractant enters from the top of the extraction kettle (V1), extraction kettle (V2), and extraction kettle (V3). Enter, extraction agent is ethyl acetate, and flow rate is 300kg / h (the feed flow mass ratio of extraction agent and phenol-water mixture is 3), extraction kettle (V1), extraction kettle (V2), extraction kettle (V3) The temperature is 30°C. The theoretical plate number of the stripping tower (T) is 10, the purity of the itaconic acid after separation is 99.98%, and the yield is 95.1%.
PUM
Login to View More Abstract
Description
Claims
Application Information
Login to View More 
