Production technology of bi-tribydroxy methyl propane and/or trihydroxy methyl propane methylal
A technology of trimethylolpropane formal and ditrimethylolpropane, which is applied in the field of producing high-purity ditrimethylolpropane and trimethylolpropane formal, can solve low, only 80- 90%, high energy consumption, and yield less than 2%, to achieve the effect of simple separation, low energy consumption, and high yield
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Embodiment 1
[0041] Step 1: Take 15 mol of formaldehyde with a mass percentage concentration of 10%, 1 mol of n-butyraldehyde with a mass percentage concentration of 85%, and 0.8 mol of NaOH solution with a mass percentage concentration of 55% and add it to an atmospheric chemical reaction kettle with a stirrer The temperature is controlled at 35°C, and the reaction time is controlled at 7 hours. First, trimethylolpropane is generated through Toulon reaction and Connizzaro reaction, and then trimethylolpropane is converted into the main component through etherification and disproportionation. It is the condensation liquid of ditrimethylolpropane and trimethylolpropane methylal, and simultaneously generates by-products and impurities such as trimeric trimethylolpropane and acetal substances, sodium formate, light fractions, Bis-TMP, etc.
[0042] Step 2: Evaporation and dehydration. A two-effect evaporation process is used to remove water from the condensation liquid obtained in step 1, the...
Embodiment 3
[0047] Step 1: get 9 mol of formaldehyde with a mass percentage concentration of 50%, 1 mol of n-butyraldehyde with a mass percentage concentration of 85%, 0.5 mol of potassium hydroxide (KOH) solution with a mass percentage concentration of 85%, formaldehyde, potassium hydroxide The solution is used as the bottom water, and the feeding method of n-butyraldehyde is continuously added into a 0.4mpa pressure reactor with a stirrer for stirring. The temperature is controlled at 20°C, and the reaction time is controlled at 5 hours. The Zara reaction produces trimethylolpropane, and then trimethylolpropane undergoes etherification and disproportionation reactions to generate a condensation liquid whose main components are ditrimethylolpropane and trimethylolpropane formal, while generating by-products and impurities Such as trimeric trimethylolpropane and acetal substances, potassium formate, light fractions, Bis-TMP, etc.
[0048] Step 2: Evaporation and dehydration. A 4-effect e...
Embodiment 4
[0053] Step 1: getting mass percentage concentration is 70% formaldehyde 6mol, getting mass percentage concentration is 50% n-butyraldehyde 1mol, getting mass percentage concentration is 10% sodium carbonate (Na 2 CO 3 ) solution 1.8mol, sodium carbonate solution, n-butyraldehyde as bottom water, formaldehyde is added in batches into a reactor with a pressure of 0.3mpa for stirring, the temperature is controlled at 50°C, and the reaction time is controlled at 3 Hours, first through the Toulon reaction and Connizzaro reaction to generate trimethylolpropane, and then trimethylolpropane undergoes etherification and disproportionation reactions to generate ditrimethylolpropane and trimethylolpropane as the main components Aldehyde condensation liquid, while generating by-products and impurities such as trimeric trimethylolpropane and acetals, sodium formate, light fractions, Bis-TMP, etc.
[0054] Step 2: Evaporation and dehydration. A 5-effect evaporation process is used to rem...
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