High-yield manna sugar preparation process

A preparation process, the technology of mannitol, applied in the field of preparation of organic compounds, can solve the problems of high production cost, high heat source, power consumption, high steam consumption, etc., and achieve the effect of increasing the yield

Inactive Publication Date: 2004-09-15
南宁市化工研究设计院
View PDF0 Cites 13 Cited by
  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] (1) Kelp extraction method: Dried kelp contains 5-10% mannitol, which can be extracted by physical crystallization after concentration. The quality of mannitol produced by this method is poor, difficult to filter, high heat source, and not suitable for medical use. , and this method consumes a lot of steam, energy and manpower, and the production cost is high
[0005] (2) Electrolytic reduction method: glucose (or invert sugar) can be reduced to a mixture of mannitol and sorbitol under electrolytic conditions, and then extracted by crystallization to obtain mannitol. This method has long reaction time, low efficiency, and high power consumption. Alcohol yield is low (only up to 15%), has long been eliminated
[0010] Some of the various mannitol production methods mentioned above cannot be industrialized at all, such as the method using fructose or mannose as raw materials; Electrolytic reduction method and kelp extraction method; although some are industrially produced and operated, the yield of mannitol is low, such as the yield of sucrose hydrolysis process hydrogenation method is only 19-20%, glucose epimerization and enzyme isomerization The yield of the hydrogenation process is only 35%, and the remaining by-products are low-value and poor-quality sorbitol liquid products, and the economic benefits need to be improved

Method used

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
View more

Image

Smart Image Click on the blue labels to locate them in the text.
Viewing Examples
Smart Image
  • High-yield manna sugar preparation process
  • High-yield manna sugar preparation process

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0028] 1100 grams of oral crystalline glucose (containing 1 crystal water molecule, the actual glucose dry matter is 1000 grams) is dissolved in 900ml deionized water, is mixed with Bx50.30% glucose aqueous solution, adds 1.5 grams of sodium molybdate, after stirring and dissolving, use The pH value of the sugar solution was adjusted to 3.85 with hydrochloric acid, and then heated and maintained at 100° C. for 2 hours with stirring. After removing ionic impurities with cation and anion exchange resins, the sugar solution after isomerization is obtained, and the composition is as follows: mannose 30.4%, glucose 69.6%.

[0029] Mannose-glucose separation is carried out using a simulated moving bed device, the separation temperature is 58°C, calcium-type cation exchange resin is used as the adsorbent, and water is used as the eluent to continuously obtain mannose-rich components and glucose-rich components. The epimerization reaction is carried out by repeated circulation of the ...

Embodiment 2

[0032]5320 grams of isomerized sugar solution obtained after epimerization reaction, the concentration is 50%, and its chemical composition is as follows: 310 grams of mannose, accounting for 30.45%, and 1850 grams of glucose, accounting for 69.55%. Separation of mannose-glucose using a simulated moving bed device, with a feed concentration of 50%, at a separation temperature of 57°C, using calcium-type cation exchange resin as an adsorbent, water as an eluent, and passing through a 12-column simulated moving bed After the device is separated, 2900 grams of mannose-rich components are obtained, with a concentration of 32.07%, including 700 grams of mannose and 230 grams of glucose, and the content of mannose is 75.27%, which can be hydrogenated to produce mannitol; the glucose-rich component 7680 grams, concentration is 22.53%, wherein mannose 110 grams, glucose 1620 grams, mannose content is 6.36%.

[0033] Add 1020 grams of oral glucose to the above-mentioned 7680 grams of g...

Embodiment 3

[0035] After the isomerized sugar solution is separated by 24-column simulated moving bed, the mannose content in the obtained mannose-rich component is 88.8%, and the concentration is 33.66%, which is mixed with a part of the epimerized sugar solution and adjusted to The mannose content of the mixed sugar solution is 75.63%, and hydrogenation reaction is carried out after separation to produce mannitol.

[0036] material

[0037] When the mannose content in the mannose-rich component obtained after the simulated moving bed separation is too high, the mannose-rich component can be mixed with a part of the isomerized sugar solution as in Example 3 to obtain the mixed sugar The mannose content of the liquid is 75.63%, which can guarantee the hydrogenation requirement.

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to view more

PUM

No PUM Login to view more

Abstract

The invention is a high-yield mannitol preparing method using glucose as raw material, on acidic condition, making the glucose through epimerization reaction to obtain the mixture mannitose-glucose, separate mannitose-glucose by simulated moving bed at 40-85 deg.C, using calcium cation exchange resin as sorbent and water as eluent to continuously obtain glucose-rich component and mannitose-rich component, where the former can repeatedly make epimerization reaction, the latter can generate manitol when added with hydrogen and the mannitol content in the mixed alcohol added with hydrogen is up to above 75%, then crystallizing, centrifuging and drying to obtain the mannitol product, where mannitol productivity is 70% of dry glucose charging capacity.

Description

Technical field: [0001] The invention belongs to the field of preparation of organic compounds. Especially a kind of technology that uses glucose as raw material to prepare mannitol. Background technique: [0002] Mannitol is a commonly used diuretic and dehydrating drug, and it is also one of the widely used pharmaceutical preparations and infusion drugs. It can also be used in the manufacture of sugar-free chewing gum, polyether, explosives, etc. in industry. [0003] The preparation method of industrial mannitol has following several ways: [0004] (1) Kelp extraction method: Dried kelp contains 5-10% mannitol, which can be extracted by physical crystallization after concentration. The quality of mannitol produced by this method is poor, difficult to filter, high heat source, and not suitable for medical use. , and this method consumes a large amount of steam, energy and manpower, and the production cost is high. [0005] (2) Electrolytic reduction method: glucose (or ...

Claims

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to view more

Application Information

Patent Timeline
no application Login to view more
Patent Type & Authority Applications(China)
IPC IPC(8): C07C29/56C07C31/26
Inventor 章朝晖王建平刘极健冯巧嫦李志宇刘勇波曾志文
Owner 南宁市化工研究设计院
Who we serve
  • R&D Engineer
  • R&D Manager
  • IP Professional
Why Eureka
  • Industry Leading Data Capabilities
  • Powerful AI technology
  • Patent DNA Extraction
Social media
Try Eureka
PatSnap group products