CN116675701A - Medium-length/short-chain isosorbide-based structured fat plasticizer and preparation method thereof - Google Patents

Medium-length/short-chain isosorbide-based structured fat plasticizer and preparation method thereof Download PDF

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Publication number
CN116675701A
CN116675701A CN202310658917.XA CN202310658917A CN116675701A CN 116675701 A CN116675701 A CN 116675701A CN 202310658917 A CN202310658917 A CN 202310658917A CN 116675701 A CN116675701 A CN 116675701A
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fatty acid
isosorbide
acid
chain fatty
medium
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楚喆
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Henan Zhengtong Food Technology Co ltd
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Henan Zhengtong Food Technology Co ltd
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    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07DHETEROCYCLIC COMPOUNDS
    • C07D493/00Heterocyclic compounds containing oxygen atoms as the only ring hetero atoms in the condensed system
    • C07D493/02Heterocyclic compounds containing oxygen atoms as the only ring hetero atoms in the condensed system in which the condensed system contains two hetero rings
    • C07D493/04Ortho-condensed systems
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K5/00Use of organic ingredients
    • C08K5/04Oxygen-containing compounds
    • C08K5/15Heterocyclic compounds having oxygen in the ring
    • C08K5/151Heterocyclic compounds having oxygen in the ring having one oxygen atom in the ring
    • C08K5/1535Five-membered rings
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07BGENERAL METHODS OF ORGANIC CHEMISTRY; APPARATUS THEREFOR
    • C07B2200/00Indexing scheme relating to specific properties of organic compounds
    • C07B2200/07Optical isomers
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W90/00Enabling technologies or technologies with a potential or indirect contribution to greenhouse gas [GHG] emissions mitigation
    • Y02W90/10Bio-packaging, e.g. packing containers made from renewable resources or bio-plastics

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Heterocyclic Carbon Compounds Containing A Hetero Ring Having Oxygen Or Sulfur (AREA)

Abstract

The invention discloses a medium-length/short-chain isosorbide-based structured fat plasticizer and a preparation method thereof, belonging to the field of plastic additives. The invention adopts isosorbide with aromatic structure, medium-long chain fatty acid and short chain fatty acid to carry out esterification reaction and acylation reaction to prepare the medium-long chain/short chain fatty acid isosorbide structural fat. The modified polyester fiber has the chemical structure and physical and chemical properties similar to those of phthalate plasticizers, and has the characteristics of being renewable, green, nontoxic, biodegradable and the like. The structure is as follows:n=6‑16;m=0‑5。

Description

Medium-length/short-chain isosorbide-based structured fat plasticizer and preparation method thereof
Technical Field
The invention relates to a medium-long/short-chain isosorbide-based structured fat plasticizer and a preparation method thereof, belonging to the field of plastic additives.
Background
Under the large background of carbon-to-peak carbon neutralization, the replacement of petroleum-based plasticizers by bio-based plasticizers is a trend. Phthalate plasticizers have potential toxicity and carcinogenicity and pose a great threat to human health and ecological environment. The biomass-derived bio-based plasticizer has green, nontoxic and biodegradable properties, and has a wide development prospect.
The medium-length/short-chain fatty acid isosorbide structured fat plasticizer is derived from cellulose, glucose and fat, and has the characteristics of being renewable, green, nontoxic, biodegradable and the like. In contrast, the modified polyamide has a chemical structure and physical and chemical properties similar to those of phthalic plasticizers. Meanwhile, the PVC/PLA composite material has the advantages of designability, good compatibility of PVC and PLA, good mechanical property, low glass transition temperature, good thermal stability, low volatility, low migration, extraction resistance and the like. Therefore, the development of the plasticizer has good practical application value. Li Wenbo, arbitrary, tao Zijun and the like have studied the preparation of isosorbide-based plasticizers and the properties of plasticized PVC (2021 year 4 of engineering plastics application), which are modified by synthesizing isosorbide and pelargonic acid into a novel bio-based plasticizer, namely isosorbide di-n-pelargonate (SDN), and studied the plasticizing effect of green plasticizers and the influence on the properties of blends, but SDN has no designability, cannot meet the different formulation requirements of PVC, and has poor compatibility and migration to PLA. No report is currently available on the medium-long/short chain fatty acid isosorbide structured lipid plasticizers.
Disclosure of Invention
The invention aims to provide a medium-long/short chain fatty acid isosorbide structured fat plasticizer.
In order to achieve the purpose of the invention, the technical scheme is as follows:
the medium-long/short chain fatty acid isosorbide structured lipid plasticizer has the following structure:n=6-16;m=0-5。
it is prepared by the following steps:
(1) Adding isosorbide and medium-long chain fatty acid into a reaction kettle, adding a catalyst, and heating under vacuum to perform esterification reaction. And after the reaction is finished, cooling, and determining that the acid value is less than 3 and reaches the end point to obtain the isosorbide mono fatty acid ester. The molar ratio of isosorbide to medium-long chain fatty acid is preferably 1:1. The reaction temperature is preferably 160-190 ℃.
(2) Gradually adding short-chain fatty anhydride into the isosorbide fatty acid ester, adding a catalyst, heating to 120-140 ℃ under vacuum to perform acylation reaction, cooling after the reaction is finished, and determining that the acid value is less than 3 as an end point. Filtering, washing, distilling and refining the obtained crude product. The molar ratio of isosorbide monofatty acid ester to short chain fatty acid anhydride is preferably 1:1; the reaction temperature is preferably 130 ℃.
The catalyst is one or more of tetrabutyl phthalate, benzenesulfonic acid, phosphoric acid, phosphotungstates and the like.
The medium-long chain fatty acid is C8-18 saturated fatty acid, preferably: octanoic acid, isooctanoic acid, decanoic acid, lauric acid, palmitic acid, epoxidized oleic acid, stearic acid, and the like.
The short-chain fatty acid anhydride is C2-7 saturated fatty acid anhydride, preferably acetic anhydride, butyric anhydride, valeric anhydride or heptanoic anhydride, etc.
The invention has the advantages that: the plasticizer is derived from biomass, and has the characteristics of being renewable, green, nontoxic, biodegradable and the like. Has similar chemical structure and physical and chemical properties as phthalate plasticizer.
Drawings
FIG. 1 is a graph showing the decomposition temperature of PVC test pieces incorporating different plasticizers;
FIG. 2 shows the migration of plasticizers in 95% ethanol by mass for various PVC test pieces;
FIG. 3 is a bar graph showing the volatilization loss rate of different plasticizers in PVC test pieces as a function of time;
fig. 4 shows the migration of plasticizers in 95% ethanol by mass in different PLA test strips:
FIG. 5 is a bar graph of the rate of volatilization loss of various plasticizers in PLA test strips versus time.
Detailed Description
For a better illustration of the invention, the following are given by way of example:
example 1
(1) Adding isosorbide and octanoic acid into a reaction kettle in a molar ratio of 1:1, adding a phosphotungstate catalyst, and heating to 160 ℃ under vacuum to perform esterification reaction. After 4-5h of reaction, cooling to 60 ℃, and determining that the acid value is less than 3 and reaches the end point to obtain the isosorbide mono-fatty acid ester.
(2) Acetic anhydride is gradually added into the isosorbide mono-fatty acid ester according to the molar ratio of 1:1, meanwhile, a phosphotungstic acid salt catalyst is added, the mixture is heated to 130 ℃ under vacuum to carry out acylation reaction for 2 hours, the temperature is reduced to 60 ℃ after the reaction is finished, and the acid value is measured to be less than 3. Filtering, washing, distilling and refining the obtained crude product.
Example 2
(1) Adding isosorbide and lauric acid into a reaction kettle in a molar ratio of 1:1, adding a benzenesulfonic acid catalyst, and heating to 180 ℃ under vacuum to perform esterification reaction. After 4-5h of reaction, cooling to 60 ℃, and determining that the acid value is less than 3 and reaches the end point to obtain the isosorbide mono-fatty acid ester.
(2) And gradually adding the butyric anhydride into the isosorbide mono-fatty acid ester according to the molar ratio of 1:1, adding a benzenesulfonic acid catalyst, heating to 130 ℃ under vacuum for acylation reaction for 2 hours, cooling to 60 ℃ after the reaction is finished, and determining that the acid value is less than 3 as an end point. Filtering, washing, distilling and refining the obtained crude product.
Example 3
(1) Adding isosorbide and epoxidized oleic acid into a reaction kettle in a molar ratio of 1:1, adding a benzenesulfonic acid catalyst, and heating to 170 ℃ under vacuum to perform esterification reaction. After 4-5h of reaction, cooling to 60 ℃, and determining that the acid value is less than 3 and reaches the end point to obtain the isosorbide mono-fatty acid ester.
(2) And gradually adding heptanoic anhydride into the isosorbide mono-fatty acid ester according to the molar ratio of 1:1, adding a benzenesulfonic acid catalyst, heating to 130 ℃ under vacuum for acylation reaction for 2 hours, cooling to 60 ℃ after the reaction is finished, and determining that the acid value is less than 3 as an end point. Filtering, washing, distilling and refining the obtained crude product.
Application example 1
The plasticizer prepared in the above example is abbreviated as ISP, and is applied to PVC, and the performance test is as follows:
1. ISP decomposition temperature is highest compared with DOP, DOTP, TBC, ATBC, etc., and has good thermal stability, as shown in figure 1 and table 1.
The decomposition temperatures of the PVC test pieces to which the different plasticizers were added are shown in the following table:
TABLE 1
2. According to EU food grade test rule food (EU) No1020116112, the mobility test of PVC test pieces added with different plasticizers (ISP, DOP, DOTP TBC, ATBC) shows that: in the 95% ethanol solution by mass, ISP has smaller mobility than DOP, DOTP, TBC, ATBC, etc., as shown in figure 2.
3. The volatilization loss rate of the PVC test pieces added with different plasticizers (ISP, DOP, TBC, ATBC) is tested according to the activated carbon method in HG/T4458-2012, and the volatilization loss rate of the ISP test pieces is obviously lower than that of the test pieces of other products, as shown in figure 3.
4. Mechanical strength test of PVC test pieces with different plasticizers:
application example 2
Application in PLA:
1. mobility test experiments were performed on PLA test pieces (plasticizer addition amount 20%) according to EU food grade test rule food (EU) No1020116112, and the results show that ISP test pieces have smaller mobility compared to conventional plasticizer ESO, TBC, ATBC and the like. Thus demonstrating the good compatibility of ISP with PLA materials, see FIG. 4.
2. The volatile loss rate of the test pieces of PLA added with different plasticizers (ISP, ESO, TBC, ATBC) was tested according to the activated carbon method in HG/T4458-2012, and the volatile loss rate of the test pieces of ISP was significantly lower than that of the test pieces of other products, as shown in FIG. 5.

Claims (3)

1. An isosorbide-based plasticizer, characterized in that: the plasticizer is medium-long/short chain fatty acid isosorbide structural fat, and the molecular structural formula is as follows:
n=6-16;m=0-5。
2. a process for preparing the isosorbide-based plasticizer of claim 1, characterized by the steps of:
(1) Adding isosorbide and medium-long chain fatty acid into a reaction kettle, adding a catalyst, heating to 140-190 ℃ under vacuum to perform esterification reaction, cooling after the reaction is finished, and determining that the acid value is less than 3 to reach the end point to obtain isosorbide fatty acid monoester; the molar ratio of the isosorbide to the medium-long chain fatty acid is 1:1;
(2) Gradually adding short-chain fatty acid anhydride into the isosorbide fatty acid monoester, simultaneously adding a catalyst, heating to 120-140 ℃ under vacuum to perform acylation reaction, cooling after the reaction is finished, and determining that the acid value is less than 3 as an end point; filtering, washing, distilling and refining the obtained crude product; the molar ratio of the isosorbide mono fatty acid ester to the short chain fatty acid anhydride is 1:1;
the catalyst is one or more of tetrabutyl phthalate, benzenesulfonic acid, phosphoric acid and phosphotungstates;
the medium-long chain fatty acid is C8-18 saturated fatty acid;
the short-chain fatty acid anhydride is C2-7 saturated fatty acid anhydride.
3. The method of preparing an isosorbide-based plasticizer according to claim 2, wherein the medium-long chain fatty acid is selected from the group consisting of caprylic acid, iso-caprylic acid, capric acid, lauric acid, palmitic acid, epoxidized oleic acid, and stearic acid; the short chain fatty anhydride is selected from acetic anhydride, butyric anhydride, valeric anhydride or heptanoic anhydride.
CN202310658917.XA 2023-06-05 2023-06-05 Medium-length/short-chain isosorbide-based structured fat plasticizer and preparation method thereof Pending CN116675701A (en)

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Application Number Priority Date Filing Date Title
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CN116675701A true CN116675701A (en) 2023-09-01

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