2005Unpublished venueRequires access

A Continuous Operation for Electroreduction of Oxalic Acid to Glyoxylic Acid

Jun Li, Qingbiao Li

Open publisher page 1 citations

Abstract

A simulative-continuous-operation approach was proposed to study the continuous operation for electroreduction of oxalic acid to gloxylic acid using a packed bed reactor and a parallel reactor with cooled cathode in order to solve the low productivity problem in current state by using traditional reactor.The effects of the concentration of oxalic acid and temperature on this process were also studied.Results showed that,after 30min of the reaction(residence time),the mass fraction of the produced glyoxylic acid in the catholic solution could reach 3.76% and 3.66% with respect to a saturated oxalic acid method and a step-temperature decreasing method.From this study,we conclude that it is feasible to produce glyoxylic acid through the three-dimensional electrode reactor under a continuous operation.

About this research paper

What this paper is about

A simulative-continuous-operation approach was proposed to study the continuous operation for electroreduction of oxalic acid to gloxylic acid using a packed bed reactor and a parallel reactor with cooled cathode in order to solve the low productivity problem in current state by using traditional reactor.The effects of the concentration of oxalic acid and temperature on this process were also studied.Results showed that,after 30min of the reaction(residence time),the mass fraction of the produced glyoxylic acid in the catholic solution could reach 3.76% and 3.66% with respect to a saturated oxalic acid method and a step-temperature decreasing method.From this study,we conclude that it is feasible to produce glyoxylic acid through the three-dimensional electrode reactor under a continuous operation.

Why it matters

OpenAlex reports 1 citations for this work. Citation counts describe recorded attention and do not establish research quality.

Key contribution

A contribution statement is not available in the OpenAlex record.

Method / approach

Method details are not available in the OpenAlex metadata.

Main findings

Findings are not separately available in the OpenAlex metadata.

Limitations

Limitations are not available in the OpenAlex metadata.

Applications

Application details are not available in the OpenAlex metadata.

Available abstract

A simulative-continuous-operation approach was proposed to study the continuous operation for electroreduction of oxalic acid to gloxylic acid using a packed bed reactor and a parallel reactor with cooled cathode in order to solve the low productivity problem in current state by using traditional reactor.The effects of the concentration of oxalic acid and temperature on this process were also studied.Results showed that,after 30min of the reaction(residence time),the mass fraction of the produced glyoxylic acid in the catholic solution could reach 3.76% and 3.66% with respect to a saturated oxalic acid method and a step-temperature decreasing method.From this study,we conclude that it is feasible to produce glyoxylic acid through the three-dimensional electrode reactor under a continuous operation.

Key concepts: Glyoxylic acid, Oxalic acid, Chemistry, Residence time (fluid dynamics), Nuclear chemistry, Inorganic chemistry, Continuous stirred-tank reactor, Phosphoric acid

Related papers

Back to paper searchBrowse research topicsOriginal source
A Continuous Operation for Electroreduction of Oxalic Acid to Glyoxylic Acid — Research Paper | ScholarLens