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Method for separating adenosine cyclic 3',5'-(hydrogen phosphate) from catalytic liquid through macroporous adsorptive resins

A cyclic adenosine monophosphate, pore adsorption technology, applied in chemical instruments and methods, organic chemistry, preparation of sugar derivatives, etc., can solve incomplete elution of cyclic adenosine monophosphate, poor adsorption selectivity, high concentration of pigments and impurities, etc. problems, achieve the effect of shortening the process cycle, shortening the time and improving the purity

Inactive Publication Date: 2019-06-07
江苏集萃工业生物技术研究所有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The disadvantage of this method is that the adsorption selectivity of activated carbon to cyclic adenosine monophosphate is poor, and a large amount of pigment and other impurities in the solution will be adsorbed at the same time, and the adsorption affinity with cyclic adenosine monophosphate is strong, resulting in poor elution of cyclic adenosine monophosphate. Completely, the concentration of pigment and impurities in the eluate is high, so the yield and purity of cyclic adenosine monophosphate in the eluate obtained by this method are low
[0005] In addition, in the fermentation liquid (catalyst liquid) of cyclic adenosine monophosphate, there are a large amount of inorganic salts, mainly including magnesium chloride, potassium dihydrogen phosphate, sodium chloride, etc., which must be removed before concentrated crystallization, otherwise during the dissolution and crystallization process It will be precipitated, which will affect the quality of the final cyclic adenosine monophosphate product

Method used

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  • Method for separating adenosine cyclic 3',5'-(hydrogen phosphate) from catalytic liquid through macroporous adsorptive resins
  • Method for separating adenosine cyclic 3',5'-(hydrogen phosphate) from catalytic liquid through macroporous adsorptive resins

Examples

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Embodiment 1

[0035] The small test of embodiment 1 cyclic adenosine monophosphate separation

[0036] Take 50mL of cyclic adenosine monophosphate catalytic solution, in which the concentration of cAMP is about 5.0g / L, ATP 7g / L, pyruvate 8g / L, MgCl 2 5.6g / L, potassium dihydrogen phosphate 4g / L. The pH of the solution was first adjusted to 2.8, and then centrifuged at 4000 rpm for 15 minutes to collect 35 mL of supernatant. Then the column separation was performed on a glass chromatography column equipped with HP-20 resin, and pure water was used for elution. The loading capacity of the resin in the chromatography column is 235g, the porosity of the bed is 0.33, and the total volume of the bed is about 350mL. The flow rates of loading and elution are both 1BV / h. Then the eluate is collected in sections, and the concentration of cyclic adenosine monophosphate, ATP, and magnesium ions is measured, and the concentration of each component in the effluent is as described in the patent figur...

Embodiment 2

[0037] Embodiment 2 Scale-up of separation of cyclic adenosine monophosphate

[0038] Take 1L of cyclic adenosine monophosphate catalytic solution, in which the concentration of cAMP is about 6g / L, ATP 3g / L, pyruvate 7g / L, MgCl 2 6g / L, potassium dihydrogen phosphate 2g / L, first adjust the pH of the solution to 3.0, then centrifuge at 4000 rpm for 15 minutes, and collect 920mL of supernatant. Then the column separation was performed on a glass chromatography column equipped with HP-20 resin, and pure water was used for elution. The loading capacity of the resin in the chromatography column is 2000g, the porosity of the bed is 0.33, and the total volume of the bed is about 3L. The flow rates of loading and elution are both 1BV / h. Then the eluate was collected in sections, and the concentrations of cyclic adenosine monophosphate, ATP and magnesium ions were determined. The cAMP eluate collected has a volume of 9200 mL, a concentration of 0.6 g / L, a purity of 96%, and a yield of...

Embodiment 3

[0039] Chromatographic separation and crystallization of embodiment 3 cyclic adenosine monophosphate

[0040] Take 3L cyclic adenosine monophosphate catalytic solution, wherein the concentration of cAMP is about 6.7g / L, ATP 2g / L, pyruvate (6g / L, MgCl 2 5.2g / L, potassium dihydrogen phosphate 3g / L, first adjust the pH of the solution to 2.9, then centrifuge at 5000 rpm for 12 minutes, and collect 2790mL of supernatant. Then, it was separated on a glass chromatography column equipped with HP-20 resin, and eluted with pure water. The loading capacity of the resin in the chromatography column is 6000g, the porosity of the bed is 0.33, and the total volume of the bed is about 9L. The flow rates of loading and elution are both 1BV / h. Then the eluate was collected in sections, and the concentrations of cyclic adenosine monophosphate, ATP and magnesium ions were determined. The cAMP eluate collected has a volume of 28.5 L, a concentration of 0.59 g / L, a purity of 97.2%, and a yield...

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Abstract

The invention provides a method for separating adenosine cyclic 3',5'-(hydrogen phosphate) from catalytic liquid through macroporous adsorptive resins. The method comprises the following steps of (1)performing solid-liquid separation on catalytic liquid containing adenosine cyclic 3', 5'-(hydrogen phosphate), and taking clear liquid; (2) performing adsorption on the clear liquid through an adsorption column loaded with macroporous adsorptive resins, and performing eluting with water, or alkali liquid or ethanol water to obtain eluent containing adenosine cyclic 3', 5'-(hydrogen phosphate); and (3) concentrating the eluent containing adenosine cyclic 3', 5'-(hydrogen phosphate), performing crystallization, and performing drying so as to obtain the adenosine cyclic 3', 5'-(hydrogen phosphate). According to the method disclosed by the invention, the adenosine cyclic 3', 5'-(hydrogen phosphate) is separated by hydrophobic macroporous adsorptive resins under the acid condition, compared with a method using ion exchange resins and activated carbon, the method has the advantages that the adenosine cyclic 3', 5'-(hydrogen phosphate) can be eluted with pure water, a subsequent desalinatingprocess can be reduced, separation degree with other impurity components is high, product yield and purity are high, besides, the resins are easy to regenerate, water consumption can be saved by about 70% or above, and the method has definite industrialization application prospects.

Description

technical field [0001] The invention relates to a method for separating cyclic adenosine monophosphate from an enzyme catalysis solution, belonging to the technical field of separation and purification in biochemical industry. Background technique [0002] Cyclic adenosine monophosphate, chemical name adenosine-3', 5'-cyclic phosphate (Adenosine cyclic 3', 5'-(hydrogenphosphate)), molecular formula is C 10 h 12 N 5 o 6 P, with a molecular weight of 329.21 and a melting point of 260°C, is a protein kinase activator and is a nucleotide derivative. It is an important substance with physiological activity that widely exists in the human body. It is produced by adenosine triphosphate under the catalysis of adenylyl cyclase and can regulate various functional activities of cells. As the second messenger of hormones, hormones regulate physiological functions and substance metabolism in cells, can change the function of cell membranes, and promote calcium ions in the reticulum s...

Claims

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Application Information

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IPC IPC(8): C07H19/213C07H1/06
Inventor 应汉杰周精卫顾炜炜吴菁岚陈勇
Owner 江苏集萃工业生物技术研究所有限公司