NADH Purification via Reverse-Phase Chromatography

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Solution Overview

Problem

Conventional methods for purifying reduced form of β-nicotinamide adenine dinucleotide result in low purity and yield, limiting production capability and failing to meet market demand.

Innovation Solution

A method involving sequential microfiltration and nanofiltration of a reaction solution, followed by gradient elution using a reverse-phase chromatographic column with an ion pair reagent, cation exchange resin for sodium ion conversion, and final freeze drying, enhancing purity and yield through specific membrane and reagent choices.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Manufacturing precision

If ion exchange chromatography is used for purifying NADH, then the purification process can be performed, but the purity is only about 90% and the yield is only 60%

Engineering Contradiction:
ImprovepurityVSAvoidyield
Core Design Contradiction:
Manufacturing precisionVSProductivity

Solution Approach 1:

The purification process is divided into multiple sequential steps: microfiltration, nanofiltration, reverse-phase chromatography with gradient elution, cation exchange, and freeze drying. Each step targets specific impurities or optimization goals, allowing simultaneous achievement of high purity (98%) and high yield (90%+) through cumulative refinement rather than relying on a single chromatography step.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

Microfiltration and nanofiltration are performed before chromatography to remove particulate matter and concentrate the NADH solution. This preliminary concentration and clarification reduces the load on subsequent chromatography steps, improving both purity and yield by preventing column fouling and optimizing separation efficiency.

Inventive Principle:
Principle #10Preliminary action

2Productivity

If conventional purification methods are used, then the process can be maintained simply, but the production capability is greatly limited

Engineering Contradiction:
Improveproduction capabilityVSAvoidprocess complexity
Core Design Contradiction:
ProductivityVSDevice complexity

Solution Approach 1:

The production process is segmented into distinct operational modules (filtration, chromatography, ion exchange, drying) that can be independently optimized and scaled. This modular approach enables increased production capability while maintaining manageable complexity through standardized, repeatable unit operations.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

Gradient elution is employed in reverse-phase chromatography, where the mobile phase composition changes continuously during the separation process. This dynamic parameter change optimizes resolution and recovery across different compounds, enhancing both purity and yield without requiring excessively complex equipment.

Inventive Principle:
Principle #35Parameter changes

3Manufacturing precision

If ion exchange chromatography is used, then the purification can be performed, but the yield is only 60% and production capability is limited

Engineering Contradiction:
ImprovepurityVSAvoidyield
Core Design Contradiction:
Manufacturing precisionVSLoss of substance

Solution Approach 1:

Nanofiltration is performed before chromatography to concentrate the NADH solution to 30-40 g/L. This preliminary concentration reduces the volume requiring chromatographic processing, minimizes adsorption losses on the column, and improves overall yield while maintaining high purity through the subsequent purification steps.

Inventive Principle:
Principle #10Preliminary action

Solution Approach 2:

The conventional ion exchange chromatography mechanism is replaced with reverse-phase chromatography using hydrophobic interactions. This substitution, combined with gradient elution, provides better recovery characteristics and reduces substance loss, achieving yield of 90% or more while maintaining purity of 98%.

Inventive Principle:
Principle #28Mechanics substitution (Replace mechanical system)

Applied Scientific Principles

This section explains which scientific principles are used to turn an abstract innovation direction into a practical engineering solution.

Function Achieved in This Case

The method achieves a purity of up to 98% and a yield of 90% or more, significantly improving production efficiency and reducing costs, thus meeting market requirements.

Implementation Method 1

a. sequentially microfiltrating and nanofiltrating a reaction solution obtained after an enzymatic reaction, to collect a concentrate for use; In the method for purifying reduced form of β-nicotinamide adenine dinucleotide, the nanofiltration membrane used for nanofiltration in Step a is a hollow fiber membrane with a 200 molecular weight cut-off.

Methodology Applied
Scientific EffectNanofiltration: Semipermeable Membrane

Implementation Method 2

b. then adding an ion pair reagent to the concentrate, and purifying by gradient elution using a reverse-phase chromatographic column as a stationary phase, a buffer solution as a phase A, and ethanol as a phase B;

Methodology Applied
Scientific EffectReverse-phase chromatography: Chromatography

Implementation Method 3

c. changing the cations in the purified filtrate into sodium ions by using a cation exchange resin;

Methodology Applied
Scientific EffectCation exchange: Ion Exchange

Implementation Method 4

d. nanofiltrating the filtrate obtained in Step c, and finally freeze drying it in a vacuum freeze drier.

Methodology Applied
Scientific EffectFreeze drying: Freeze Drying

Data Source

PatentUS10214556B2Method for purifying reduced form of β-nicotinamide adenine dinucleotide
Publication Date: 2019.02.26 BONTAC BIO ENG (SHENZHEN) CO LTD

AI summary

A method for purifying a salt of reduced form of β-nicotinamide adenine dinucleotide (NADH) includes: sequentially microfiltrating and nanofiltrating a reaction solution obtained after an enzymatic reaction, collecting a concentrate for use; adding an ion pair reagent to the concentrate, and purifying by gradient elution to obtain a purified filtrate using a reverse-phase chromatographic column as a stationary phase, a buffer solution as a phase A, and ethanol as a phase B; changing the cations in the purified filtrate into sodium ions to obtain a filtrate by using a cation exchange resin; and nanofiltrating the filtrate, and freeze drying in a vacuum freeze drier. The method results in an excellent purity and yield of a salt of NADH that meets requirements in industry.