CN112694857A - Modified polymerized terpene resin and preparation method thereof - Google Patents

Modified polymerized terpene resin and preparation method thereof Download PDF

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Publication number
CN112694857A
CN112694857A CN202011552913.6A CN202011552913A CN112694857A CN 112694857 A CN112694857 A CN 112694857A CN 202011552913 A CN202011552913 A CN 202011552913A CN 112694857 A CN112694857 A CN 112694857A
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modified
percent
polymerized
terpene resin
resin
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崔程
王松
蔡钊亮
王琳
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Songchuan Industrial Materials Wuxi Co ltd
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Songchuan Industrial Materials Wuxi Co ltd
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    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09JADHESIVES; NON-MECHANICAL ASPECTS OF ADHESIVE PROCESSES IN GENERAL; ADHESIVE PROCESSES NOT PROVIDED FOR ELSEWHERE; USE OF MATERIALS AS ADHESIVES
    • C09J153/00Adhesives based on block copolymers containing at least one sequence of a polymer obtained by reactions only involving carbon-to-carbon unsaturated bonds; Adhesives based on derivatives of such polymers
    • C09J153/02Vinyl aromatic monomers and conjugated dienes
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09JADHESIVES; NON-MECHANICAL ASPECTS OF ADHESIVE PROCESSES IN GENERAL; ADHESIVE PROCESSES NOT PROVIDED FOR ELSEWHERE; USE OF MATERIALS AS ADHESIVES
    • C09J11/00Features of adhesives not provided for in group C09J9/00, e.g. additives
    • C09J11/02Non-macromolecular additives
    • C09J11/06Non-macromolecular additives organic
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09JADHESIVES; NON-MECHANICAL ASPECTS OF ADHESIVE PROCESSES IN GENERAL; ADHESIVE PROCESSES NOT PROVIDED FOR ELSEWHERE; USE OF MATERIALS AS ADHESIVES
    • C09J11/00Features of adhesives not provided for in group C09J9/00, e.g. additives
    • C09J11/08Macromolecular additives
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09JADHESIVES; NON-MECHANICAL ASPECTS OF ADHESIVE PROCESSES IN GENERAL; ADHESIVE PROCESSES NOT PROVIDED FOR ELSEWHERE; USE OF MATERIALS AS ADHESIVES
    • C09J145/00Adhesives based on homopolymers or copolymers of compounds having no unsaturated aliphatic radicals in a side chain, and having one or more carbon-to-carbon double bonds in a carbocyclic or in a heterocyclic system; Adhesives based on derivatives of such polymers
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09JADHESIVES; NON-MECHANICAL ASPECTS OF ADHESIVE PROCESSES IN GENERAL; ADHESIVE PROCESSES NOT PROVIDED FOR ELSEWHERE; USE OF MATERIALS AS ADHESIVES
    • C09J157/00Adhesives based on unspecified polymers obtained by reactions only involving carbon-to-carbon unsaturated bonds
    • C09J157/02Copolymers of mineral oil hydrocarbons
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L2201/00Properties
    • C08L2201/08Stabilised against heat, light or radiation or oxydation
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L2205/00Polymer mixtures characterised by other features
    • C08L2205/02Polymer mixtures characterised by other features containing two or more polymers of the same C08L -group
    • C08L2205/025Polymer mixtures characterised by other features containing two or more polymers of the same C08L -group containing two or more polymers of the same hierarchy C08L, and differing only in parameters such as density, comonomer content, molecular weight, structure
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L2205/00Polymer mixtures characterised by other features
    • C08L2205/03Polymer mixtures characterised by other features containing three or more polymers in a blend
    • C08L2205/035Polymer mixtures characterised by other features containing three or more polymers in a blend containing four or more polymers in a blend

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Adhesives Or Adhesive Processes (AREA)

Abstract

The invention relates to an adhesive raw material and a preparation process thereof, in particular to a modified polymerized terpene resin and a preparation method thereof, which can increase the cohesion of a finished product, improve the initial strength and the retention of the adhesive, improve the process problems of brittleness, large dust and the like in the production process of polymerized terpene products, and comprise the following components in percentage by weight: 5 to 20 percent of styrene butadiene block copolymer A polymerized by a solvent method, 20 to 60 percent of beta-polymerized terpene resin B, 20 to 40 percent of aromatic hydrocarbon modified dicyclopentadiene hydrogenated petroleum resin C, 10 to 20 percent of phenol modified terpene resin D, 0.1 to 1 percent of antioxidant E and 0.1 to 1 percent of antioxidant F; the adopted solvent method for polymerizing the styrene butadiene block copolymer A Sunpolymer S-0100 polymer provides excellent initial viscosity, holding power and toughness, so that the problem of overlarge dust during granulation of most resins is solved; the beta-polymerized terpene resin provides excellent adhesion and holding power and has excellent heat resistance.

Description

Modified polymerized terpene resin and preparation method thereof
Technical Field
The invention relates to an adhesive raw material and a preparation process thereof, in particular to a modified polymerized terpene resin and a preparation method thereof.
Background
Polymerized terpene resins have good tack, compatibility, thermal stability and light stability, and can improve the adhesive properties and holding power of adhesives, and are essential tackifying components for many adhesives. The terpene resin is modified to obtain the terpene resin with better performance, and has stronger viscosity, higher retentivity and initial viscosity and better toughness than the common terpene resin.
At present, a rotary belt type condensation granulator used for common petroleum resin is selected for granulation of the product, and due to the fact that the viscosity is high, the hydrogenated petroleum resin is firmly adhered to a stainless steel belt by cooling a granulation tail end of a conventional rotary belt granulator in a 200 ℃ molten state, a scraper is adopted to scrape off the resin attached to the steel belt, most of the resin formed by granulation is broken, and the quality of the product is greatly reduced.
Disclosure of Invention
In view of the problems mentioned in the background art, the present invention aims to provide a modified polymerized terpene resin and a preparation method thereof, which can increase the cohesion of the finished product and improve the initial strength and the retention of the adhesive, and improve the process problems of brittleness, large dust, etc. in the production process of the polymerized terpene product.
The technical purpose of the invention is realized by the following technical scheme: a modified polymerized terpene resin comprises the following components in parts by weight: 5 to 20 percent of styrene butadiene block copolymer A polymerized by a solvent method, 20 to 60 percent of beta-polymerized terpene resin B, 20 to 40 percent of aromatic hydrocarbon modified dicyclopentadiene hydrogenated petroleum resin C, 10 to 20 percent of phenol modified terpene resin D, 0.1 to 1 percent of antioxidant E and 0.1 to 1 percent of antioxidant F.
Preferably, the solvent-process polymerized styrene butadiene block copolymer A is Sunpolymer S-0100.
Preferably, the β -polymerized terpene resin B is one of SuntackSR105 and SuntackSR 120.
Preferably, the aromatic hydrocarbon modified dicyclopentadiene hydrogenated petroleum resin C is SuntackHW-100P.
Preferably, the phenol-modified terpene resin D is one of SYLVARESTP2040HM and SYLVARESTP 96.
Preferably, the antioxidant E is 1010.
Preferably, the antioxidant F is 168.
The technical purpose of the invention is realized by the following technical scheme: a preparation method of modified polymerized terpene comprises the following reaction steps:
step one, pretreating and processing a solvent-method polymerized styrene-butadiene block copolymer A Sunpolymer S-0100 by using a kneader, and melting the solvent-method polymerized styrene-butadiene block copolymer A Sunpolymer S-0100;
step two, firstly adding aromatic hydrocarbon modified dicyclopentadiene hydrogenated petroleum resin C SuntackHW-100P, an antioxidant E1010 and an antioxidant F168 into a reaction kettle for pre-melting, after the resin is completely melted, adding a solvent method polymerized styrene butadiene block copolymer A Sunpolymer S-0100 in batches in equal parts and three times, after the copolymer is completely melted, adding beta-polymerized terpene resin B, and after the copolymer is completely melted, adding phenol modified terpene resin D;
and step three, vacuumizing the reactor after the materials are completely put into the reactor, wherein the vacuum coefficient is less than-0.08, and discharging the materials after the materials are continuously stirred for 30min at the material temperature of 140 ℃.
In summary, the invention mainly has the following beneficial effects: the modified polymerized terpene resin and the preparation method thereof adopt a solvent method to polymerize the styrene butadiene block copolymer A Sunpolymer S-0100 polymer, provide excellent initial viscosity and retention and toughness, and solve the problem of overlarge dust during the granulation of most resins; the beta-polymerized terpene resin provides excellent adhesion and retention and has excellent heat resistance; the phenol modified terpene resin increases the initial viscosity of the polymerized terpene resin to polar base materials, and improves the softening point; the aromatic hydrocarbon modified dicyclopentadiene hydrogenated petroleum resin improves the heat resistance and aging resistance of the polymerized terpene resin.
The modified polymerized terpene resin and the preparation method thereof can effectively solve the problems that the common polymerized terpene resin has overlarge dust, larger resin brittleness and serious appearance breakage during production, and the production and use of customers are influenced, and the common polymerized terpene resin can not increase the cohesion of finished products of the customers and improve the initial strength of the adhesive.
The SuntackSR110P production process is simple and effective, can save a large amount of energy consumption, does not generate hazardous waste, and has good environmental protection, economic benefit and industrial production prospect.
Detailed Description
The technical solutions in the embodiments of the present invention will be clearly and completely described below with reference to the embodiments of the present invention, and it is obvious that the described embodiments are only a part of the embodiments of the present invention, and not all of the embodiments. All other embodiments, which can be derived by a person skilled in the art from the embodiments given herein without making any creative effort, shall fall within the protection scope of the present invention.
Example 1: heating a reaction kettle to 165 ℃, adding naphthenic oil KN-4010130 g, an antioxidant 1010 and 168, each 0.5g of a stirring paddle, rotating at the speed of 100r/min, preheating and stirring for 10min, adding SIS rubber D1111100 g, preheating and stirring for 10min, adding the petroleum resin SU-100150 g after the SIS rubber D1111 is fully pre-melted, continuously preheating and stirring for 20min, adding the SIS rubber D1111100 g after the petroleum resin is fully melted into a liquid state, continuously stirring for about 10min, adding the modified polymerized terpene resin SUNTACKSR110P170g, melting, adding the SIS rubber D1111150 g, vacuumizing until the vacuum coefficient is less than or equal to-0.08, continuously observing the rubber dissolution state for 1h, adding the petroleum resin SU-100200 g, and discharging after the petroleum resin SU-100200 g is fully melted. The whole formulation trial time is controlled within 2.5 h.
The experimental data are as follows in table 1:
Figure BDA0002857705980000051
remarking: TC-A is a polymeric terpene resin formulation modified with SUNTACKSR 110P.
TC-B is a formula of modified polymerized terpene resin using a certain conventional equivalent SP.
Example 2: heating a reaction kettle to 165 ℃, adding naphthenic oil KN-4010130 g, an antioxidant 1010 and 168, each 0.5g of a stirring paddle, rotating at the speed of 100r/min, preheating and stirring for 10min, adding SIS rubber D1111100 g, preheating and stirring for 10min, adding the petroleum resin SU-100150 g after the SIS rubber D1111 is fully pre-melted, continuously preheating and stirring for 20min, adding the SIS rubber D1111100 g after the petroleum resin is fully melted into a liquid state, continuously stirring for about 10min, adding the modified polymerized terpene resin SUNTACKSR110P200g, melting, adding the SIS rubber D1111150 g, vacuumizing until the vacuum coefficient is less than or equal to-0.08, continuously observing the rubber dissolution state for 1h, adding the petroleum resin SU-100170 g, and discharging after the petroleum resin SU-100170 g is fully melted. The whole formulation trial time is controlled within 2.5 h.
The experimental data are as follows in table 2:
Figure BDA0002857705980000061
remarking: TC-C uses 3% more SUNTACKSR110P modified polymerized terpene resin than TC-A and 3% less petroleum resin SU-100 formulation (other ingredients unchanged).
The performance of the SUNTACKSR110P modified polymerization terpene resin in the aspects of heat resistance, retention, initial adhesion and the like is completely superior to that of a certain conventional terpene resin, the cost is controllable, a large amount of energy consumption can be saved in the aspect of process, no hazardous waste is generated, and the modified polymerization terpene resin has good environmental protection, economic benefit and industrial production prospect.
The performance of initial adhesion, holding power, stripping force and the like can also be improved by adding SUNTACKSR110P modified polymerized terpene resin in the same proportion.
Although embodiments of the present invention have been shown and described, it will be appreciated by those skilled in the art that changes, modifications, substitutions and alterations can be made in these embodiments without departing from the principles and spirit of the invention, the scope of which is defined in the appended claims and their equivalents.

Claims (8)

1. A modified polymeric terpene resin characterized by: comprises the following components in parts by weight: 5 to 20 percent of styrene butadiene block copolymer A polymerized by a solvent method, 20 to 60 percent of beta-polymerized terpene resin B, 20 to 40 percent of aromatic hydrocarbon modified dicyclopentadiene hydrogenated petroleum resin C, 10 to 20 percent of phenol modified terpene resin D, 0.1 to 1 percent of antioxidant E and 0.1 to 1 percent of antioxidant F.
2. The modified polymeric terpene resin of claim 1 wherein: the solvent method polymerized styrene butadiene block copolymer A is Sunpolymer S-0100.
3. The modified polymeric terpene of claim 1, wherein: the beta-polymerized terpene resin B is one of SuntackSR105 and SuntackSR 120.
4. The modified polymeric terpene of claim 1, wherein: the aromatic hydrocarbon modified dicyclopentadiene hydrogenated petroleum resin C is SuntackHW-100P.
5. The modified polymeric terpene of claim 1, wherein: the phenol modified terpene resin D is SYLVARESTP2040HM, SYLVARESTP 96.
6. The modified polymeric terpene of claim 1, wherein: the antioxidant E is 1010.
7. The modified polymeric terpene of claim 1, wherein: the antioxidant F is 168.
8. A process for the preparation of a modified polymeric terpene as claimed in any one of claims 1 to 7, characterized in that: the method comprises the following reaction steps:
step one, pretreating and processing a solvent-method polymerized styrene-butadiene block copolymer A Sunpolymer S-0100 by using a kneader, and melting the solvent-method polymerized styrene-butadiene block copolymer A Sunpolymer S-0100;
heating a reaction kettle to 165 ℃, adding naphthenic oil KN-4010, adding aromatic hydrocarbon modified dicyclopentadiene hydrogenated petroleum resin C SuntockHW-100P, antioxidant E1010 and antioxidant F168 into the reaction kettle for pre-melting, adding the styrene butadiene block copolymer A Sunpolymer S-0100 in three batches in equal batches after the resin is completely melted, adding beta-polymerized terpene resin B after the copolymer is completely melted, and adding phenol modified terpene resin D after the copolymer is completely melted;
and step three, vacuumizing the reactor after the materials are completely put into the reactor, wherein the vacuum coefficient is less than-0.08, and discharging the materials after the materials are continuously stirred for 30min at the material temperature of 140 ℃.
CN202011552913.6A 2020-12-24 2020-12-24 Modified polymerized terpene resin and preparation method thereof Pending CN112694857A (en)

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Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2000119636A (en) * 1998-10-19 2000-04-25 Yokohama Rubber Co Ltd:The Adhesive sealing material composition and sealing method using the same
CN105969272A (en) * 2016-07-29 2016-09-28 无锡市万力粘合材料股份有限公司 Hot melt adhesive composition for cold storage label and preparation method thereof
CN106085309A (en) * 2016-07-29 2016-11-09 无锡市万力粘合材料股份有限公司 Automobile floor leather melt pressure sensitive glue composition and preparation method thereof

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2000119636A (en) * 1998-10-19 2000-04-25 Yokohama Rubber Co Ltd:The Adhesive sealing material composition and sealing method using the same
CN105969272A (en) * 2016-07-29 2016-09-28 无锡市万力粘合材料股份有限公司 Hot melt adhesive composition for cold storage label and preparation method thereof
CN106085309A (en) * 2016-07-29 2016-11-09 无锡市万力粘合材料股份有限公司 Automobile floor leather melt pressure sensitive glue composition and preparation method thereof

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
李广宇等: "《胶黏剂原材料手册》", 31 August 2004, 国防工业出版社 *

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