Method for preparing reducing sugar by supercritical hydrolysis of plant fibers and semi-continuous reactor thereof

A plant fiber and reaction device technology, which is applied in chemical/physical/physical-chemical stationary reactors, sugar production, monosaccharide, etc. problem, to achieve the effect of accurate monitoring

Inactive Publication Date: 2010-12-01
SOUTH CHINA UNIV OF TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The problem caused by the operation of this intermittent device is that the heating process needs to go through a process other than the supercritical state to reach the supercritical state, and the material has already started to react before reaching the supercritical state, and the heating time is too long, etc., which will cause low temperature. Polysaccharides and glucose continue to be decomposed into by-products such as furfural and ketones, resulting in low yields of reducing sugars, and by-products can strongly inhibit fermentation, thereby affecting the ethanol production rate of the entire fermentation; and it takes time to cool after the reaction, during the cooling process The materials in the medium are still reacting, which will directly affect the accuracy of the test results

Method used

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  • Method for preparing reducing sugar by supercritical hydrolysis of plant fibers and semi-continuous reactor thereof
  • Method for preparing reducing sugar by supercritical hydrolysis of plant fibers and semi-continuous reactor thereof
  • Method for preparing reducing sugar by supercritical hydrolysis of plant fibers and semi-continuous reactor thereof

Examples

Experimental program
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Effect test

Embodiment 1

[0023] Unload the 8 nuts on the cover 3 of the reactor body with a wrench, shake the lifting hand wheel 19 on the lifting screw 25 counterclockwise, the reactor body 1 will descend with the lifting screw 25, and when the reactor body 1 falls to the bottom, Add pure water more than 3 times the volume of the material into the reactor body with a measuring cylinder, then shake the lifting handwheel 19 on the lifting screw 25 clockwise, and the reactor body 1 rises with the lifting screw 25 until it reaches the level of the kettle cover. 3 When matching, put 8 nuts on the bolts of the kettle cover 3 and tighten them diagonally, open the nitrogen cylinder, the valve on the reactor body pipeline, use nitrogen to drive away the air in the kettle, and close the valve at the bottom of the storage tank 6. The spherical valve 22 is connected to the electric heating furnace 2 on the reaction kettle body 1, and the condensed water pipeline is opened to condense the rotor to avoid degaussing...

Embodiment 2

[0032] In order to illustrate that the present invention has a shorter reaction time than the batch reaction device, plant fiber waste corrugated carton (OCC) is selected as raw material, and the process conditions are: temperature 390 ° C, pressure 23-24MPa, the volume of water in the reactor body 150mL, The plant fiber slurry solid-liquid ratio (g / g) 1: 65 that adds in the storage tank, reaction time 10-90s, rotating speed 100rpm, its result is as follows table 3

[0033] Table 3: Hydrolyzed reducing sugar yield of OCC at 390°C, 23-24Mpa

[0034]

[0035]

[0036] It can be seen from Table 3 that at a temperature of 390°C, a pressure of 23Mpa, and a volume of water in the reactor body of 150mL, when the solid-liquid ratio (g / g) of the added plant fiber slurry is 1:65, the reaction time only needs 10s, and the reducing sugar yield It is 51.39%, and the traditional batch reaction device needs several minutes or even dozens of minutes for the light temperature raising pro...

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Abstract

The invention discloses a method for preparing reducing sugar by the supercritical hydrolysis of plant fibers and a semi-continuous reactor thereof. According to the method, supercritical hydrolysis is realized by high-pressure feeding and high-pressure sampling. The reaction conditions of a reactor are that: the temperature is between 380 and 400 DEG C; the pressure is 24 to 30MPa; the volume ofwater in a kettle is 150 to 200mL; solid-liquid ratio (g / g) of added plant fiber slurry is 1:30-1:65; and reaction time is 5s to 5min. The reactor comprises a feeding part, a reactor body and a product collecting part, wherein the feeding part presses materials into the reactor by the high pressure stored in a material storage tank; and the sampling part presses a reaction product into a sample receiving bottle through a sampling tube by the high pressure in the reactor. Because the volume of the supercritical water is much more than that of the materials, the materials can smoothly exchange heat in an instant to reach the set condition. The process is considered not to be subjected to other reactions beyond the supercritical condition. The yield of the reducing sugar prepared by the method can be over 50 percent.

Description

technical field [0001] The invention relates to a technology for preparing reducing sugars by hydrolysis of plant fibers, in particular to a semi-continuous reaction device and a method for preparing reducing sugars by supercritical hydrolysis of plant fibers. Background technique [0002] With the rapid development of the global economy in today's world, the demand and consumption of energy has increased, and the development and utilization of non-renewable resources such as coal, oil and natural gas has been increased. The increasing depletion of coal, oil, etc. and the use of them have brought a series of environmental pollution problems such as greenhouse effect and water pollution, forcing the world's energy structure to urgently change from a model dominated by petrochemical energy to one dominated by renewable energy. mode conversion. Therefore, finding new energy sources to replace fossil fuels such as petroleum and coal is an urgent task of scientific research. ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C13K1/02C07H3/02B01J19/18
CPCY02P20/54
Inventor 王艳万金泉张晶晶马邕文
Owner SOUTH CHINA UNIV OF TECH
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