JPH08217723A - Production of polyglycerol fatty acid ester - Google Patents

Abstract

PURPOSE: To obtain the subject compound having high substitution degree, uniform appearance and excellent storage stability and surfactant action and useful as various detergents, emulsifiers, etc., by reacting a polyglycerol with a fatty acid in the presence of a specific amount of an alkali catalyst. CONSTITUTION: The objective compound having an esterification degree of >=40%. an OH value of <=170mgKOH/g and a high substitution degree is produced by reacting (A) a polyglycerol having an average polymerization degree of 7-18 with (B) a fatty acid such as lauric acid or stearic acid in the presence of (C) 0.06-0.25mol%, especially 0.07-0.22mol% (based on the component B) of an alkali catalyst (e.g. potassium hydroxide or sodium hydroxide). Preferably, the reaction is carried out at >=180 deg.C and the temperature is further raised by 10-80 deg.C when the conversion of the component B reaches >=70mol%.

Description

Detailed Description of the Invention

[0001]

BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing polyglycerin fatty acid ester, and more particularly to a method for producing highly substituted polyglycerin fatty acid ester.

[0002]

2. Description of the Related Art Polyglycerin fatty acid ester (hereinafter referred to as
Sometimes called PoGE. ) Is known as a surfactant approved as a food additive, and is mainly used as an emulsifying agent and a solubilizing agent for foods, and is also attempted to be used as cosmetics, pharmaceuticals and detergents.
As a method for producing PoGE, glycerin is first subjected to polycondensation at a high temperature of 200 ° C. or higher in the presence of an alkali catalyst, and then desalted,
By performing purification such as decolorization, polyglycerin (hereinafter,
Sometimes referred to as PoG. Is obtained, and then PoG is esterified with a fatty acid to obtain PoGE (JP-A-62-45513, JP-A-5-45513).
8-185537, JP-A-63-23837, JP-A-6-
3-68541, etc.). This esterification reaction has good reactivity, and is carried out in the presence of an alkali catalyst while removing produced water from the outside of the system in some cases.

In the production of such PoGE, in order to control the HLB of the produced PoGE, a method of controlling the charging ratio of the fatty acid and PoG which are the reaction raw materials to control the degree of esterification has been adopted. However, in the production of such PoGE, especially in the production of highly substituted PoGE having a relatively high degree of esterification,
There have been problems that the reaction products are non-uniform and separation occurs over time. In addition, there is a problem that the function of the produced PoGE as an emulsifier is lowered.

[0004]

The object of the present invention is to obtain a high degree of substitution PoG obtained by reacting PoGE having an average degree of polymerization of 7 or more and 18 or less with a fatty acid in the presence of an alkali catalyst.
Another object of the present invention is to provide a method for producing a high degree of substitution PoGE which is excellent in the action as an emulsifier by preventing the reaction product of E from becoming nonuniform and separating.

[0005]

The present invention has been made to solve the above-mentioned problems, and its gist is to provide a polyglycerol having an average degree of polymerization of 7 or more and 18 or less and a fatty acid in the presence of an alkali catalyst. And the degree of esterification is 40
When producing a highly substituted polyglycerin fatty acid ester having a mol value of not less than 170 [mgKOH / g] and a hydroxyl value of not more than 170 [mgKOH / g], the amount of alkali catalyst is 0.06 to 0.2 with respect to the fatty acid.
It exists in the manufacturing method of polyglycerin fatty acid ester characterized by being 5 mol%. Hereinafter, the present invention will be described in detail.

As PoG, those having an average degree of polymerization of 7 or more and 18 or less and a hydroxyl value of 850 to 1100 are used. P
When the degree of polymerization of oG is increased, the viscosity becomes high and it becomes difficult to proceed the reaction. As the upper limit of the average degree of polymerization of PoG,
It is preferably 15, particularly preferably 12. PoG is generally a mixture of PoG having different degrees of polymerization, and if the content of PoG having a high degree of polymerization is too high, the appearance uniformity of the resulting PoGE may deteriorate.

As the fatty acid, a linear or branched saturated or unsaturated fatty acid having 12 to 24 carbon atoms is used. Examples of such fatty acid raw materials include lauric acid, myristic acid, palmitic acid, stearic acid, oleic acid, erucic acid, ricinoleic acid, and behenic acid. The fatty acids may be used alone or in combination of two or more at an arbitrary ratio. Therefore, mixed fatty acids obtained from natural products can be used as they are.

As the alkali catalyst, any one such as alkali metal or alkaline earth hydroxide can be used.
Potassium hydroxide and sodium hydroxide are preferred from the viewpoint of easy handling and availability. The amount of the alkali catalyst is 0.06 to 0.25 mol%, preferably 0.07 to 0.25 mol% based on the fatty acid when using PoG having an average degree of polymerization of 7 or more and 18 or less.
The content is 0.22 mol%, particularly preferably 0.07 to 0.15 mol%. When the amount of the alkali catalyst is less than the above range, a large amount of unreacted PoG remains in the reaction product, and hydrophilic PoG and hydrophobic high substitution degree PoGE are mixed, so that the system tends to become non-uniform. . In addition, unreacted Po
If a large amount of G remains, PoG having a higher degree of polymerization may be obtained in the reaction system, and it becomes difficult to obtain the esterification rate of the produced PoGE from the raw material charging ratio. Conversely, if the amount of alkali catalyst is too large, the production of fatty acid alkali salts will increase
The emulsifying power of GE tends to decrease.

PoGE is produced by reacting PoG with a fatty acid in the presence of the above-mentioned specific amount of alkali catalyst. The reaction temperature is 180 to 270 ° C, preferably 20
It is 0 to 270 ° C., and the reaction time is 1 to 5 hours. P
When reacting oG with a fatty acid, the reaction is first carried out at 180 to 270 ° C, and after the fatty acid conversion reaches 70%, the reaction temperature is further raised by 10 to 80 ° C to carry out the reaction.
It is preferable because the oG can be reduced. The highly substituted PoGE obtained by the present invention is a PoGE having an esterification degree of 40 mol% or more and a hydroxyl value of 170 [mgKOH / g] or less.
Is. The reaction product of PoG and fatty acid has a degree of esterification of less than 40 mol% or a hydroxyl value of more than 170 P.
With oGE, it is difficult to obtain a reaction product having a uniform appearance. The reaction product is subjected to purification steps such as decolorization and deodorization as necessary, and then commercialized according to a conventional method. For example, a liquid or paste at room temperature may be filled as it is into a shipping container, or water may be added to add 2
You may fill a shipping container as 0-60 weight% aqueous solution. Those that are solid at room temperature are crushed by, for example, a flaker or the like to give a product in the form of granules.

[0010]

EXAMPLES The present invention will be described in more detail with reference to examples below, but the present invention is not limited to the following examples unless it exceeds the gist thereof. The fatty acids used as raw materials are erucic acid (85% or higher purity manufactured by Tokyo Kasei), oleic acid (80% purity manufactured by NOF Corporation), lauric acid (90% purity manufactured by Lion).
%) And stearic acid (purity 70%, manufactured by Kao Corporation) were used.

Example 1 Fatty acids and PoG shown in Table 1
(Decapolyglycerin = 750, average degree of polymerization 10, hydroxyl value 888 mgKOH / g: manufactured by Sakamoto Yakuhin) were used in a predetermined amount and charged into a stirring reactor equipped with a heating jacket.
After the temperature was raised to 40 ° C., a 10 wt% sodium hydroxide aqueous solution was added in the amount shown in Table 1, and the esterification reaction was carried out at this temperature for 4 hours. The fatty acid conversion rate at this point was 90%. The reaction mixture was heated to 260 ° C. and kept for 4 hours, and the fatty acid conversion was 98.2%. The transmittance of the obtained PoGE and the appearance are observed and evaluated,
The results are shown in Table-2. The PoG having a degree of polymerization of 7 or more in the used PoG was 39% by weight.

[Examples 2 to 10, Comparative Examples 1 to 10] Table-
Using the fatty acids shown in 1 and PoG in predetermined amounts, and
The reaction was performed in the same manner as in Example 1 except that a predetermined amount of 10 wt% sodium hydroxide aqueous solution shown in 1 was used. Obtained P
The oGE was evaluated and the results are shown in Table-2. In addition, each evaluation method was performed as follows.

[Measurement Method of Transmittance] Using a quartz glass having a cell width of 1 cm × 1 cm, an absorption spectrometer (UV-12 manufactured by Shimadzu Corporation)
00), the transmittance was measured at a wavelength of 650 nm. The results are shown in Table-2. [Observation of reaction liquid appearance] After completion of the reaction, the reaction liquid was transferred to a 225 ml transparent glass container and allowed to stand overnight at 25 ° C. From the appearance of the sample, the presence or absence of precipitation and the presence of turbidity were observed and evaluated. The results are shown in Table-2. Criteria for evaluation-Presence or absence of precipitation ○ ... None × ... Presence of existence / absence of separation of liquid system ○ ... Liquid system is transparent and uniform △ ... Transparent immediately after completion of reaction, and separated product after standing at 25 ° C for 12 hours. ×: Separated substance was generated immediately after the reaction.

[Measurement of degree of esterification] With respect to PoGE obtained by the reaction of PoG with fatty acid, its hydroxyl group value (OHV), saponification value (SV) and acid value (AV) are used as standard oil and fat physical property test methods (Nippon Oil Chemical (Established by the association)
The average esterification rate is obtained by dividing the number of esterified hydroxyl groups by the total number of hydroxyl groups in the sample containing esterified hydroxyl groups, and was calculated by the following formula. The results are shown in Table-2.

[0015]

[Equation 1]

[Polymerization Degree Analysis of PoG] Polymerization degree of hydroxyl group was analyzed by the method shown below to analyze the degree of polymerization of PoG. Apparatus Waters 410 column MCI-GEL (CK-06-SH; 8
× 300 mm) Carrier 0.1% phosphoric acid aqueous solution 0.5 ml / min Sample Synthesized polyglycerin fatty acid ester 2
40 g of 0.5 N potassium hydroxide alcohol solution
The mixture was heated under reflux at 93 ° C. for 1.5 hours to separate into an oil phase portion and an aqueous phase portion, the aqueous phase portion was diluted to 2% with a 0.1% phosphoric acid aqueous solution, and 10 μl was injected into the apparatus.

[Water-in-oil type emulsion test] Po obtained in Examples 1 and 3 and Comparative Examples 1 to 4 in rapeseed oil (manufactured by Kanegafuchi Chemical Industry)
Each GE was dissolved in 2.4% by weight of the total amount of rapeseed oil, and then demineralized water was added so that the weight ratio of water / oil was 20/80, and the mixture was used in a thermostatic chamber at 30 ° C for 5 minutes using a Yayoi shaker. (200 times / min) Shake emulsification. The results are shown in Table-3.

[0018]

[Table 1]

[0019]

[Table 2]

[0020]

[Table 3]

[0021]

The highly substituted polyglycerin fatty acid ester obtained by the method of the present invention has a uniform appearance, excellent storage stability, and excellent action as a surfactant. Is useful as

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Claims (3)

[Claims] 1. A polyglycerin having an average degree of polymerization of 7 or more and 18 or less is reacted with a fatty acid in the presence of an alkali catalyst to give an esterification degree of 40 mol% or more and a hydroxyl value of 170.
When producing a highly substituted polyglycerin fatty acid ester of [mgKOH / g] or less, the amount of alkali catalyst is 0.06 to 0.25 mol% with respect to the fatty acid, and the method for producing a polyglycerin fatty acid ester. . 2. The reaction is carried out by further increasing the reaction temperature by 10 to 80 ° C. after polyglycerin is reacted with fatty acid at 180 ° C. or higher to reach a reaction rate of fatty acid of at least 70%. The manufacturing method described in. 3. The amount of alkali catalyst is 0.07 with respect to fatty acid.
It is-0.22 mol%, The manufacturing method of Claim 1 or 2.