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Method and system using one-step method for continuous production of alkyl glycoside

A technology of alkyl glycosides and one-step method is applied in the field of continuous production of alkyl glycosides and systems by one-step method, which can solve the problems of expensive metal borohydride, reduced bleaching efficiency and high production cost, and achieves improved oxidation effect and continuous glycosidation. The effect of response and improvement of utilization

Active Publication Date: 2015-03-18
HEBEI UNIVERSITY OF SCIENCE AND TECHNOLOGY
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0011] But this kind of bleaching method causes the utilization rate of hydrogen peroxide to be low because the decomposition of hydrogen peroxide itself, can make the aqueous solution of alkyl glycoside produce stable foam simultaneously and make bleaching process be difficult to carry out (hydrogen peroxide decomposes and produces oxygen, and oxygen emerges from solution and makes solution form a large amount Bubbles), in addition, there is an excessive amount of undecomposed hydrogen peroxide in the bleached product, resulting in unstable color, and the product is easy to turn yellow during storage
U.S. Patent (US6166189) proposed to use lithium borohydride, or sodium borohydride, potassium borohydride to treat the bleached alkyl glycoside aqueous solution to remove excess hydrogen peroxide and make the product stable, but the metal borohydride is expensive and the production cost is high. Not suitable for industrial production
At the same time, there are almost no relevant patent records about the equipment used in the bleaching process of the alkyl glucoside aqueous solution. The conventional method is to directly add hydrogen peroxide into the bleaching kettle containing the alkyl glucoside. The oxygen produced by the decomposition causes the aqueous solution of alkyl glycosides to generate a large amount of foam, which often requires a large space for bubble breaking or an effective breaking method, which greatly reduces the bleaching efficiency, and is also a technical problem that is difficult for relevant practitioners in this industry to solve

Method used

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  • Method and system using one-step method for continuous production of alkyl glycoside
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  • Method and system using one-step method for continuous production of alkyl glycoside

Examples

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specific Embodiment 1

[0096] Specific Example 1: Mix C8-C10 mixed fatty alcohols (each accounting for about 50%) and anhydrous glucose in a mass ratio of 1:1 in a stirred tank and stir evenly, and mix the uniformly mixed mixture in a 0.5m 3 The flow rate per hour is sent to the colloid mill for grinding, the liquid from the colloid mill is sent to the hydrocyclone particle size separator, and the discharge speed of the light phase control valve and the heavy phase control valve is adjusted to make the hydrocyclone The mass ratio of the inner light phase to the heavy phase is 1:7, and the quasi-colloidal light phase is obtained. Observing the light phase with a microscope, it is found that the particle diameter in the light phase is up to 2.5 microns, and the average particle diameter in the field of view is about 1 micron. Put it in a graduated cylinder and observe that the sedimentation distance is less than 3.5 cm in 30 minutes. Add mixed alcohol to the light phase to make the alcohol-sugar ratio ...

specific Embodiment 2

[0099] Specific embodiment 2: after getting decyl alcohol and glucose and mix by the ratio of 2:1, put into stirring tank 1 and mix evenly, with 0.5m per hour 3 The flow rate is sent to the colloid mill 2 for grinding, and the liquid from the colloid mill 2 is sent to the hydrocyclone particle separator 3, and the discharge speed of the valve 5 and valve 4 is adjusted to make the liquid in the hydrocyclone particle separator 3 The mass ratio of the light phase to the heavy phase is 1:10 (the mass ratio of 1:10 is the mass inside the particle size separator), and the quasi-colloidal light phase is obtained. Observe with a microscope, the diameter of the particles in the light phase is less than 2.5 microns, and the average particle diameter in the field of view is about 0.8 microns. Put it in a graduated cylinder for observation, and the sedimentation distance in 30 minutes is less than 3.5 cm. The light phase material coming out from the top or central discharge port of the li...

specific Embodiment 3

[0100] Specific embodiment 3: get decyl alcohol and glucose and mix by the ratio of 0.5:1 and put into stirring tank 1 and mix evenly, with 0.5m per hour 3 The flow rate is sent to the colloid mill 2 for grinding, and the liquid from the colloid mill 2 is sent to the hydrocyclone particle separator 3, and the discharge speed of the valve 5 and valve 4 is adjusted to make the liquid in the hydrocyclone particle separator 3 The mass ratio of the light phase to the heavy phase is 1:1, and the quasi-colloidal light phase is obtained. Observe with a microscope, the particle diameter in the light phase is up to 1 micron, and the average particle diameter in the field of view is about 0.5 micron. Put it in a graduated cylinder for observation, and the sedimentation distance is less than 2 cm in 30 minutes. Add decyl alcohol to the light phase material coming out of the top outlet of the liquid cyclone particle size separator 3 to make the mass ratio of alcohol to sugar reach 5:1, the...

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Abstract

The invention discloses a method and system using one-step method for continuous production of alkyl glycoside, the system comprises pretreatment equipment, glycosidation reaction equipment and bleaching equipment, the pretreatment equipment comprises a mixing kettle, a colloid mill and a particle fraction separator, the glycosidation reaction equipment is provided with multistage independent reaction units, the bleaching equipment is provided with an overflow wall and a reaction chamber, the method is mainly as follows: before the glycosidation reaction, reactants are mixed by the mixing tank, and ground by the colloid mill for quasi solation treatment to make the glucose particle size not more than 10 mu m to form a stable and uniform sol phase, the stable and uniform sol phase enters into the particle fraction separator for separation of a light phase, the light phase is sent into the a glycosidation reactor for multistage glycosidation reaction for continuous production of an alkyl glycoside crude product, after neutralization and dealcoholization, the alkyl glycoside crude product through the overflow wall overflows into the reaction chamber for the formation of a liquid film, and a finished product is prepared by bleaching after oxidizing gas / liquid film contact. The method can realize the continuous production of the alkyl glycoside by one-step method, and the product quality is stable and uniform.

Description

technical field [0001] The invention relates to a method for continuously producing alkyl glycosides in one step and a production system suitable for the method. Background technique [0002] Alkyl glycoside (APG) is a new type of nonionic surfactant that has appeared since the 1990s. It is generally composed of natural renewable resources fatty alcohols and sugar compounds (mostly glucose, but also other monosaccharides or Hydrolyzed into monosaccharide compounds), formed by dehydration under an acidic catalyst. Because APG has many characteristics of nonionic surfactant and anionic surfactant, it can be well compounded with any surfactant, and it is highly efficient, non-toxic, non-irritating to the skin, fully biodegradable, synergistic Effect is obvious and so on, so it is widely used in various fields of people's life. [0003] In the current industry, there are mainly two methods for the industrial production of alkyl glycosides. One is the "two-step method" used in ...

Claims

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Application Information

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IPC IPC(8): C07H15/04C07H1/00B01J19/18
CPCC07H1/00C07H15/04
Inventor 郑学明尚会建刘红梅
Owner HEBEI UNIVERSITY OF SCIENCE AND TECHNOLOGY
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