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Process for preparing furfural by using agricultural by-products of high and crude fiber plants

A technology for agricultural and sideline products and crude fiber, applied in chemical instruments and methods, carbon compounds, inorganic chemistry, etc., can solve the problems of reduced production efficiency, high impurities such as soil, and non-combustibility, so as to reduce the generation of sulfur oxides, Less residual sulfuric acid and strong adsorption capacity

Inactive Publication Date: 2012-09-12
北京博能康成科技有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The commonly used method nowadays is to use the waste residue as boiler fuel, but the acid content in the waste residue is high, the calorific value is low, it is not easy to burn, and the sulfur-containing compounds produced during the combustion process are also very easy to cause the boiler to be corroded and damaged.
Due to the high carbon content of furfural residue, which is more than 40% (mass fraction), it is a good raw material for preparing activated carbon. In recent years, the industry has tried to use chemical methods to make furfural residue into activated carbon, but due to the following factors, The quality of the activated carbon produced does not meet the industrial requirements: 1) furfural waste residue is the acid hydrolysis product of corn cob, and the cellulose structure of corn cob is severely damaged during the hydrolysis process, which makes the chemical activator harmful to the cellulose in corn cob The swelling and erosion effects of the corn cob are reduced, which affects the post-activation pore-forming process; 2) The corn cob is decomposed into particles of different sizes during the hydrolysis process, and the particle size varies greatly. Uniformly promulgated in the material, if screening and grading will greatly reduce the production efficiency and the process is complicated, the wet sticky and acidic furfural residue is difficult to break, even if it is broken, the cost is unacceptable for industrial production; 3) corn is Plants with high silicon content, coupled with lax raw material sources and high impurities such as soil, lead to the presence of high silicon, which has a significant impact on the quality of activated carbon; 4) A large amount of residual sulfuric acid will release sulfur when furfural slag is activated at high temperature oxides, causing pollution
Therefore, the processing method of existing furfural waste residue needs to be improved

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0036] 1) Raw material pretreatment: use dried corn cob as raw material, first remove dust and other impurities, and then use 1m 3 Crush at a speed of / min, and screen particles below 1mm.

[0037] 2) Preparation of acid catalyst: mix 3% phosphoric acid and 9% sulfuric acid in a ratio of 2:1.

[0038] 3) Hydrolysis: Put the corncob pellet raw materials into the hydrolysis tank, and pass the acid catalyst into the hydrolysis tank according to the amount of 45kg acid catalyst per cubic meter of corncob, mix and stir, at the same time, turn on the ultrasonic device in the hydrolysis tank ,hydrolysis.

[0039] 4) Introduce 180℃ high-temperature steam into the hydrolysis tank to heat the hydrolysis tank to strip the hydrolysis product furfural.

[0040] 5) The gas stripped furfural enters the furfural phase separator to obtain crude furfural and furfural residue. The productivity of crude furfural is 10%.

[0041]

Embodiment 2

[0043] 1) Raw material pretreatment: use dried corn cobs, corn stalks, wheat stalks, cotton stalks as raw materials to remove dust and other impurities, and then use 1m 3 Smash at a speed of / min, and screen particles below 20mm.

[0044] 2) Preparation of acid catalyst: mix 3% phosphoric acid and 9% sulfuric acid in a ratio of 2:1.

[0045] 3) Hydrolysis: Put the raw material particles into the hydrolysis tank, and pass the acid catalyst into the hydrolysis tank according to the amount of 45kg acid catalyst per cubic meter of corncob, mix and stir, and at the same time, turn on the ultrasonic device in the hydrolysis tank. hydrolysis.

[0046] 4) Introduce 200 ℃ high temperature steam into the hydrolysis tank to heat the hydrolysis tank to strip the hydrolysis product furfural.

[0047] 5) The gas stripped furfural enters the furfural phase separator to obtain crude furfural and furfural residue.

[0048] 6) The obtained crude furfural solution is further purified by distillation in t...

Embodiment 3

[0051] 1) Raw material pretreatment: use dried corn cobs, peanut husks, rice husks as raw materials to remove dust and other impurities, and then use 1m 3 Smash at a speed of / min, and screen particles below 10mm.

[0052] 2) Preparation of acidic catalyst: mix 3% phosphoric acid and 12% sulfuric acid in a ratio of 2:1.

[0053] 3) Hydrolysis: Put the corncob pellet raw materials into the hydrolysis tank, and pass the acid catalyst into the hydrolysis tank according to the amount of 45kg acid catalyst per cubic meter of corncob, mix and stir, at the same time, turn on the ultrasonic device in the hydrolysis tank ,hydrolysis.

[0054] 4) Introduce the high temperature steam of 150℃ into the hydrolysis tank to heat the hydrolysis tank to strip the hydrolyzed product furfural.

[0055] 5) The gas stripped furfural enters the furfural phase separator to obtain crude furfural and furfural residue. The productivity of crude furfural is 10%.

[0056] 6) The obtained crude furfural solution is...

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Abstract

The invention discloses a process for preparing furfural by using agricultural by-products of high and crude fiber plants. The process includes the steps of 1) conducting pretreatment of raw materials; 2) hydrolyzing pretreated raw materials in a hydrolyzing tank, and using an acid catalyst formed by mixing sulfuric acid and phosphoric acid during the hydrolytic process; 3) introducing high-temperature steam into the hydrolyzing tank, heating up the hydrolyzing tank, and conducting gap stripping for hydrolysis products of furfural; and 4) feeding gas stripped furfural to into a furfural phase splitter to obtain coarse furfural and furfural residues. According to the process, the acid catalyst combining the sulfuric acid and the phosphoric acid is used for hydrolyzing the raw materials, and the hydrolytic process is assisted by ultrasonic treatment simultaneously, so that the productivity of the furfural is improved, the residue amount of the sulfuric acid is a little, the production of sulfur oxides in the subsequent activating process of furfural residues is reduced, and the environmental pollution is reduced. Besides, the invention also provides a process for producing activated carbon adsorbents by using the furfural residues. The process includes the steps of drying the furfural residues, screening, roasting, hardening activating and steam curing, the obtained activated carbon specific surface is large, the iodine value is high and the adsorption capacity is high.

Description

[0001] Technical field [0002] The invention relates to the technical field of furfural preparation, in particular to a method for preparing furfural and activated carbon from high-crude fiber plant agricultural and sideline products. [0003] Background technique [0004] Furfural is an important organic compound made from agricultural and sideline products. It has a wide range of uses, such as rubber, plastics, synthetic fibers, pesticides, medicines, coatings, chemical reagents, etc. [0005] At present, most of furfural is obtained by hydrolyzing polypentose from crops containing polypentane bran. Many crops’ stems, barks and seed husks contain polypentose, which can be used as raw materials for furfural production, such as corn cobs, cottonseed husks, rice husks and bagasse. Among them, corn cobs have a higher aldehyde yield. , The theoretical aldehyde rate is 19%. Therefore, acid hydrolysis of corncobs or other agricultural by-products is currently used to produce furfural. ...

Claims

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Application Information

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IPC IPC(8): C07D307/50C01B31/08C01B32/324C01B32/336
Inventor 肖天存宋亚军刘婕纵秋云黄瑜陈浩逸
Owner 北京博能康成科技有限公司
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