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Method for separating natural phytol from chlorophyll unsaponifiable matters

A technology for saponification and phytol, applied in the field of separation of natural phytol, can solve the problems of only reaching 15kPa-20kPa, high requirements for heating equipment, and difficulty in obtaining high purity, and achieves reduction of equipment investment, improvement of competitiveness, Energy saving effect

Active Publication Date: 2014-03-19
四川通世达生物科技有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] 1. High energy consumption
Since the boiling point of phytol is as high as 203-204°C (1.33kPa), the vacuum degree of traditional vacuum distillation can only reach 15kPa-20kPa, and the distillation temperature is >300°C. Repeated vacuum distillation requires high heating equipment and energy consumption also very high;
[0005] 2. Poor quality
Therefore, it is still difficult to guarantee the quality and obtain high purity despite repeated distillation, and the separation cost is too high

Method used

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  • Method for separating natural phytol from chlorophyll unsaponifiable matters

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0024] Such as figure 1 Shown, a kind of method for separating natural phytol from chlorophyll unsaponifiable matter, comprises the following steps:

[0025] A, carry out saponification separation to pasty chlorophyll;

[0026] B, chromatographic purification;

[0027] C. Scraper film evaporation;

[0028] D. Short-range molecular distillation.

[0029] In step A, first take the pasty chlorophyll, add 500L of 45% NaOH solution and heat up to 50°C to make it pH=12-14, then stir it at a speed of 80r / min for 75 minutes to undergo saponification reaction, and then Add 2500L acetone to the solution and keep the temperature at 40°C, stir for 30 minutes to promote its dissolution, then let it stand for 30 minutes, the saponified crystals will precipitate and sink to the bottom of the tank, and the saponified crystals will be filtered out by filtration, so as to obtain no Saponified acetone solution.

[0030] After carrying out step A, the acetone solution of 800L of acetone is a...

Embodiment 2

[0035] The difference between this example and Example 1 is that in step A, first take the pasty chlorophyll, add 500L of 40% NaOH solution and heat up to 60°C to make its pH=12-14, and then add 120r / Stir at a speed of min for 60 minutes for saponification reaction, then add 3000L acetone to the solution and keep the temperature at 50°C, stir for 20 minutes at the same time to promote its dissolution, then let it stand for 30 minutes, the saponified product crystallizes and sinks to the bottom of the tank , The saponifiable crystals are filtered out by filtration to obtain an unsaponifiable acetone solution.

[0036] After carrying out step A, add the acetone of 500L to rinse again after the saponifiable crystal obtained after filtering, and repeat the process of filtering and washing 4 times, and finally combine the unsaponifiable acetone solution obtained after the washing with the step The unsaponifiable acetone solutions in A were combined.

[0037] In step B, the unsapo...

Embodiment 3

[0041] The difference between this example and examples 1 and 2 is that in step A, first take the pasty chlorophyll, add 500L of 50% NaOH solution and heat up to 40°C to make its pH=12-14, and then add 60r Stir at a speed of 1 / min for 90 minutes for saponification reaction, then add 2000L acetone to the solution and keep the temperature at 30°C, stir for 40 minutes at the same time to promote its dissolution, then let it stand for 30 minutes, the saponified product crystallizes and settles in the tank At the bottom, the saponifiable crystals were filtered out by filtration to obtain an unsaponifiable acetone solution.

[0042] After carrying out step A, add the acetone of 1000L of acetone again to rinse the saponifiable matter crystal obtained after filtering out, and repeat the process of filtering out and washing for 2 times, and finally combine the unsaponifiable matter acetone solution obtained after the washing with step The unsaponifiable acetone solutions in A were comb...

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Abstract

The invention discloses a method for separating natural phytol from chlorophyll unsaponifiable matters. The method comprises the following steps of A, saponification separating the paste chlorophyll; B, chromatographically purifying; C, evaporating through a scraper film; D, carrying out molecular distilling in a short-range manner. The method for separating the natural phytol from the chlorophyll unsaponifiable matter is simple and convenient to operate, less in energy consumption, high in product purity, low in application cost, high in enterprise economic benefit, capable of promoting the industrial development and capable of better protecting the environment.

Description

technical field [0001] The invention relates to the fields of food and biochemical industry, in particular to a method for separating natural phytol from chlorophyll unsaponifiable matter. Background technique [0002] Domestic manufacturers of sodium copper chlorophyllin almost always use pasty chlorophyll as raw material, and saponify the pasty chlorophyll by adding NaOH. After saponification, the saponified product is separated to prepare sodium copper chlorophyllin, while the unsaponifiable product is often discarded. , which is not only easy to cause environmental pollution, but also contains about 20-30% of natural phytol is wasted. Phytol, also known as phytoalcohol, is a component of chlorophyll, molecular formula C 20 h 40 O, molecular weight 296.5, boiling point 203-204°C (1.33kPa), is the raw material for the synthesis of vitamin K1 and vitamin E. Natural phytol is listed as a natural flavor in the "Hygienic Standards for the Use of Food Additives" (GB2760-2007)...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07C33/03C07C29/80
CPCC07C29/74C07C29/88C07C33/03
Inventor 樊平原周定志朱万岭
Owner 四川通世达生物科技有限公司