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

Inactive Publication Date: 2012-06-27
YIBIN TIANYUAN GRP CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0006] The second is that the gas contains a small amount of carbon dioxide, which generates sodium carbonate when the gas and caustic soda are synthesized, and the caustic soda contains a small amount of sodium carbonate and sodium chloride. These impurities follow the sodium formate synthesis liquid into the sodium formate evaporation stage, because they are not easy to separate. Therefore, entering the product restricts the purity of the sodium formate product
[0007] The third is that sodium formate evaporation and drying technology generally adopts single-effect or double-effect intermittent evaporation technology for production, and airflow drying technology is used for drying after centrifugation. Since sodium formate is a supersaturated solution, the saturated solution of sodium formate crystallizes during the intermittent production process, causing serious blockage Due to the uncontrollable drying time of air-flow drying, the pipeline and equipment are often blocked when the drying is not complete; at the same time, the moisture content of sodium formate after air-flow drying is unstable, which makes packaging difficult and easy to handle. In short, the output and quality of sodium formate are seriously affected and the operating cost is high

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  • Method for producing sodium formate by using coal gas
  • Method for producing sodium formate by using coal gas

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Experimental program
Comparison scheme
Effect test

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...

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Abstract

The invention discloses a method for producing sodium formate by using coal gas. The method comprises the steps that: a production raw material liquid is prepared; coal gas is added to the raw material liquid, and a synthesis reaction is carried out, such that a reaction product liquid is obtained; and sodium formate in the reaction product liquid is evaporated, crystallized, separated, dried, and packaged. According to the invention, a limitation of a low concentration of produced sodium formate is broken. Under a condition that current raw material concentration, reaction temperature and reaction pressure are not changed, the concentration of sodium formate in the reaction product liquid is no lower than 500g / L, such that vapor consumption is saved. Also, with a method that formic acid is added, the purity of sodium formate is higher than 99.5%. Also, evaporation, crystallization, drying and packaging manners are changed, such that sodium formate is prevented from moisture absorbing and caking. With the method provided by the invention, apparatus productivity is greatly improved, vapor consumption is reduced, system operation stability is improved, continuous production is realized, and product quality is improved. Therefore, economic, environmental and social benefits are ensured.

Description

technical field [0001] The present invention relates to a kind of method of producing sodium formate, particularly a kind of method of synthetic method producing sodium formate. Background technique [0002] Sodium formate, molecular formula: HCOONa, molecular weight: 68.01, white granular or crystalline powder. Slight formic acid smell, hygroscopic. At high temperature, it decomposes into sodium oxalate and hydrogen, and then generates sodium carbonate. Soluble in about 1.3 parts of water, soluble in glycerin, slightly soluble in ethanol, its aqueous solution is neutral, pH is 7, relative density is 1.92. The melting point is 253°C. irritating. Commodities often contain 2 molecules of crystal water. Uses: leather industry, camouflage acid in chrome tanning process; used as catalyst and stable synthetic agent; reducing agent in printing and dyeing industry; used in the production of hydrosulfite, oxalic acid and formic acid. [0003] Synthetic method is a common method...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07C53/06C07C51/10C07C51/43
Inventor 王政强谭金和黄泽厚罗传元
Owner YIBIN TIANYUAN GRP CO LTD
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