Process for producing dioctyl terephthalate by semi-continuous method
A dioctyl phthalate, semi-continuous technology, applied in the field of chemical production, can solve the problems of low equipment use efficiency, low equipment utilization rate, low product stability, etc., and achieves low raw material and energy consumption, improved automation, The effect of stable product quality
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Examples
Embodiment 1
[0027] A semi-continuous process for producing dioctyl terephthalate, using terephthalic acid and isooctyl alcohol as raw materials, and tetrabutyl titanate as a catalyst, adopts a semi-continuous process to synthesize dioctyl terephthalate, The specific steps are as follows:
[0028] Batch production: raise the temperature of the preheated first esterification tank to 180°C, add terephthalic acid (PTA) and isooctyl alcohol in batches, the molar ratio of acid to alcohol is 1:3, the catalyst tetrabutyl titanate The amount of ester addition is 0.2% of the total mass of the raw materials, and it is slowly stirred for 3 hours. The mixture in the first esterification kettle is added in batches to the second esterification kettle, and the catalyst tetrabutyl titanate is added at the same time. The catalyst addition amount is 0.1% of the total mass of the raw material, continue to stir, and raise the temperature to 220°C, and react for 2h.
[0029] Continuous production: After the e...
Embodiment 2
[0032] The difference between this example and Example 1 is that it is batch production: the preheated first esterification tank is heated to 185°C, and terephthalic acid (PTA) and isooctyl alcohol, acid alcohol are added in batches The molar ratio of the catalyst is 1:3.5, the amount of catalyst tetrabutyl titanate is 0.25% of the total mass of the raw material, slowly stirred for 3.5h, and the mixture in the first esterification tank is added in batches to the second esterification tank At the same time, the catalyst tetrabutyl titanate was added, the amount of the catalyst added was 0.15% of the total mass of the raw materials, the stirring was continued, and the temperature was raised to 225° C., and the reaction was carried out for 2.5 hours.
[0033] Continuous production: After the esterification reaction is completed, the mixture enters the neutralizer, the temperature is controlled at 50°C, and the acidity value of the solution is measured. At the same time, 4% sodium ...
Embodiment 3
[0036] The difference between this example and Example 2 lies in the batch production: the preheated first esterification tank is heated to 190°C, and terephthalic acid (PTA) and isooctyl alcohol, acid alcohol are added in batches The molar ratio of the catalyst is 1:4.5, and the amount of catalyst tetrabutyl titanate added is 0.3% of the total mass of the raw material, slowly stirred for 4h, and the mixture in the first esterification tank is added in batches to the second esterification tank, At the same time, the catalyst tetrabutyl titanate was added, and the amount of catalyst added was 0.2% of the total mass of the raw materials. Stirring was continued, and the temperature was raised to 230° C. for 3 hours of reaction.
[0037] Continuous production: After the esterification reaction is completed, the mixture enters the neutralizer, the temperature is controlled at 55°C, the acidity value of the solution is measured, and at the same time, 4% sodium carbonate aqueous solut...
PUM

Abstract
Description
Claims
Application Information

- Generate Ideas
- Intellectual Property
- Life Sciences
- Materials
- Tech Scout
- Unparalleled Data Quality
- Higher Quality Content
- 60% Fewer Hallucinations
Browse by: Latest US Patents, China's latest patents, Technical Efficacy Thesaurus, Application Domain, Technology Topic, Popular Technical Reports.
© 2025 PatSnap. All rights reserved.Legal|Privacy policy|Modern Slavery Act Transparency Statement|Sitemap|About US| Contact US: help@patsnap.com