Method for producing sodium formate by using coal gas
A production method, sodium formate technology, applied in the field of synthetic method to produce sodium formate, can solve the problems of packaging difficulty, quality impact, high operating cost, etc., achieve the effect of continuous production, increase device capacity, and improve product quality
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Image
Examples
Embodiment 1
[0033] Such as figure 1 As shown, the sodium formate solution generated from the synthesis reactor is added to the alkali mixing tank. The sodium hydroxide content in the prepared alkali solution is 200g / L, and the sodium formate content is 101g / L. The synthesis reaction occurs under the condition of MPa. The sodium formate produced in the sodium formate synthesizer is 440g / L. The sodium formate solution is transported to the first-effect evaporation to initially concentrate to 750g / L, and is continuously transported to the DTB crystallizer for further concentration and continuous formation of crystals. , the vacuum degree in the DTB crystallizer is controlled at -0.071MPa, and the operating temperature is 83°C. During the operation, the formic acid with a mass concentration of 20% is accurately added to the DTB crystallizer through a metering pump, and the amount of formic acid added is combined with the crystallizer. The pH value and sodium carbonate content are determined. ...
Embodiment 2
[0039] Add the sodium formate solution generated from the synthesis reactor into the alkali mixing tank. The sodium hydroxide content in the prepared alkali solution is 230g / L, and the sodium formate content is 151g / L. The temperature is 180°C and the pressure is 2.1MPa. The synthesis reaction occurs under the following conditions. The sodium formate produced in the sodium formate synthesizer is 560g / L. The sodium formate solution is transported to the first-effect evaporation to initially concentrate to 780g / L, and is continuously transported to the DTB type crystallizer for further concentration and continuous formation of crystals. DTB type The vacuum degree in the crystallizer is controlled at -0.077MPa, and the operating temperature is 91°C. During the operation, formic acid with a mass concentration of 70% is accurately added to the DTB type crystallizer through a metering pump. The amount of formic acid added is combined with the pH in the crystallizer. The value and sod...
Embodiment 3
[0045] Add the sodium formate solution generated in the synthesis reactor into the alkali mixing tank. The sodium hydroxide content in the prepared alkali solution is 250g / L, and the sodium formate content is 182g / L. The temperature is 187°C and the pressure is 2.0MPa. The synthesis reaction occurs under the following conditions. The sodium formate produced in the sodium formate synthesizer is 602g / L. The sodium formate solution is transported to the first-effect evaporation and initially concentrated to 810g / L, and is continuously transported to the DTB type crystallizer for further concentration and continuous formation of crystals. DTB type The vacuum degree in the crystallizer is controlled at -0.066MPa, and the operating temperature is 94°C. During the operation, formic acid with a mass concentration of 70% is accurately added to the DTB type crystallizer through a metering pump. The amount of formic acid added is combined with the pH value in the crystallizer. The content...
PUM
Property | Measurement | Unit |
---|---|---|
melting point | aaaaa | aaaaa |
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