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Method for removing chlorhydric acid and ferrous chloride from hydrolysed biomass glyc solution by diluted acid

A technology of dilute acid hydrolysis and ferrous chloride, applied in chemical instruments and methods, sugar derivatives, sugar derivatives, etc., can solve the problems of reducing yeast fermentation efficiency, high solubility, harmfulness, etc., and achieves easy operation and high salt concentration. The effect of reduction and low processing cost

Inactive Publication Date: 2007-08-15
上海洁申实业有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

But NaCl and CaCl 2 The solubility of the yeast is very large and cannot be removed by precipitation, which will cause harmful effects to the subsequent fermentation process and reduce the fermentation efficiency of the yeast

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0026] 100ml fresh anion exchange resin D315 is packed in the first anion column, 100ml fresh anion exchange resin D315 is packed in the second anion column, and 100ml fresh cation exchange resin 732 is packed in the cation column.

[0027] All resins were provided by Huachang Polymer Co., Ltd., East China University of Science and Technology. Resin volumes mentioned here and below are apparent volumes.

[0028] Take 500ml containing 2% HCl, 2% FeCl 2 And a solution of 3% glucose, make it pass through the first anion column, the cation column and the second anion column successively at normal pressure and 20°C. It takes 10 minutes to pass through the first anion column, 10 minutes to pass through the cation column, and 10 minutes to pass through the second anion column.

[0029] The acidity of the solution that goes out of the first anion exchange column is pH=2

[0030] Measure the pH of the final solution to 5.0, FeCl 2 The concentration is 0.00364kmol / m 3 .

Embodiment 2

[0032] The first anion column, the resin type and loading amount packed in the second anion column and cation column are all equal to embodiment 1.

[0033] Take 500ml containing 2% HCl, 0.5% FeCl 2 And a solution of 3% glucose, make it pass through the first anion column, the cation column and the second anion column successively at normal pressure and 20°C. It takes 10 minutes to pass through the first anion column, 5 minutes to pass through the cation column, and 10 minutes to pass through the second anion column.

[0034] The acidity of the solution that goes out of the first anion exchange column is pH=2

[0035] The pH of the final solution was determined to be 5.6, FeCl 2 The concentration is 0.00187kmol / m 3 .

Embodiment 3

[0037] The first anion column, the resin type and loading amount packed in the second anion column and cation column are all equal to embodiment 1. However, the anion resins packed in the first anion column and the second anion column are regenerated after saturation, and the resin containing 1kmol / m is used for regeneration. 3 NaOH and 3kmol / m 3 Sodium chloride solution. The cation resin packed in the cation exchange column is saturated with 1kmol / m 3 hydrochloric acid solution regeneration.

[0038] Take 500ml containing 2% HCl, 0.5% FeCl 2 And a solution of 3% glucose, make it pass through the first anion column, the cation column and the second anion column successively at normal pressure and 20°C. It takes 10 minutes to pass through the first anion column, 5 minutes to pass through the cation column, and 10 minutes to pass through the second anion column.

[0039] The acidity of the solution that goes out of the first anion exchange column is controlled at pH=2

[0...

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Abstract

The process of eliminating hydrochloric acid and ferrous chloride from saccharide solution obtained via hydrolyzing biomass with dilute acid includes the following steps: making the saccharide solution pass through the first anionic exchange column, the cationic exchange column and the second anionic exchange column successively to eliminate hydrochloric acid and ferrous chloride. The present invention has simple operation, low processing cost and probability of recovering and reusing ferrous chloride. The present invention has ultimate solution pH 5.6 and ferrous chloride concentration lower than 0.00194 kmol / cu m.

Description

technical field [0001] The present invention relates to a kind of from containing HCl and FeCl 2 A method for removing these two substances in a solution, especially a method for removing HCl and FeCl from the sugar solution obtained after dilute acid hydrolysis of biomass by using a series ion exchange column method 2 Methods. technical background [0002] With the gradual depletion of non-renewable fossil energy and the continuous rise of international crude oil prices, the development and utilization of biomass energy, which is rich in resources and does not cause environmental pollution, has important strategic significance. [0003] Biomass is not only abundant, but also the only renewable resource that can be converted into liquid fuels. It absorbs CO from the atmosphere during its growth 2 , can reduce the environmental problems and greenhouse effect caused by the use of fossil fuels. In this context, the development of biomass waste to liquid fuel technology has ...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C07H1/06B01J47/02B01J47/028
Inventor 朱龙德李庭琛任冠明华建锋李军杰
Owner 上海洁申实业有限公司