CN110511363A - A kind of forming method of resin - Google Patents

A kind of forming method of resin Download PDF

Info

Publication number
CN110511363A
CN110511363A CN201910705568.6A CN201910705568A CN110511363A CN 110511363 A CN110511363 A CN 110511363A CN 201910705568 A CN201910705568 A CN 201910705568A CN 110511363 A CN110511363 A CN 110511363A
Authority
CN
China
Prior art keywords
resin
reaction
temperature
forming method
dimethylbenzene
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
CN201910705568.6A
Other languages
Chinese (zh)
Inventor
张博
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Zhongshan Jinghe Electronic Materials Co Ltd
Original Assignee
Zhongshan Jinghe Electronic Materials Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Zhongshan Jinghe Electronic Materials Co Ltd filed Critical Zhongshan Jinghe Electronic Materials Co Ltd
Priority to CN201910705568.6A priority Critical patent/CN110511363A/en
Publication of CN110511363A publication Critical patent/CN110511363A/en
Pending legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G63/00Macromolecular compounds obtained by reactions forming a carboxylic ester link in the main chain of the macromolecule
    • C08G63/02Polyesters derived from hydroxycarboxylic acids or from polycarboxylic acids and polyhydroxy compounds
    • C08G63/12Polyesters derived from hydroxycarboxylic acids or from polycarboxylic acids and polyhydroxy compounds derived from polycarboxylic acids and polyhydroxy compounds
    • C08G63/46Polyesters chemically modified by esterification
    • C08G63/48Polyesters chemically modified by esterification by unsaturated higher fatty oils or their acids; by resin acids

Abstract

The invention discloses a kind of forming methods of resin, the forming method of the resin passes through step 1, step 2, step 3, step 4, step 5 and step 6 are effectively prepared, consequently facilitating resin preparation forming, and it is formed in preparation process in resin, it is prepared in this way by six steps, so that improving the working efficiency of preparation, and the polyesterification reaction of step 3 will pay close attention to the rate of output water and water yield, and it samples in required time, measure acid value and viscosity, consequently facilitating personnel learn pet reaction state, and personnel pass through the control amount of reflux dimethylbenzene, so that the effectively whole reaction of control carries out, so that more convenient when producing preparation, and in polyesterification reaction, it is connected by the molecular structure of reinforcing agent, so that effectively changing molecule connection type, so that resin is when artificial synthesized formation , there is good bending strength and compressive strength, mechanical property and weatherability are changed.

Description

A kind of forming method of resin
Technical field
The invention belongs to associated resin technical fields, and in particular to a kind of forming method of resin.
Background technique
Resin typically refer to it is heated after be softened or melted range, there are liquidity preference, room temperature in when softening under external force Under be solid-state, semisolid, be also possible to the organic polymer of liquid sometimes.Broadly upper definition, can be used as plastic products and adds Any high-molecular compound of work raw material is referred to as resin.
Relative molecular weight is uncertain but usually higher, is in solid-state, middle solid-state, pseudo-solid condition under room temperature, is also possible to liquid sometimes The organic substance of state.With temperature range is softened or melted, there is liquidity preference under external force, rupture is in conchoidal often. Broadly refer to polymer or prepolymer as plastic basis material.It is general not soluble in water, organic solvent can be dissolved in.Can by sources it divide For natural resin and synthetic resin;It is divided into thermoplastic resin and thermosetting resin again by the different feature of its processing behavior.
Existing resin technology has the following problems: existing resin does not have fine when artificial synthesized formation Bending strength and compressive strength, mechanical property is influenced by temperature larger, and weatherability is poor, so that it is competing not have good market Strive dynamics.
Summary of the invention
The purpose of the present invention is to provide a kind of forming methods of resin, mentioned above in the background art existing to solve Resin when artificial synthesized formation, do not have good bending strength and compressive strength, shadow of the mechanical property by temperature Sound is larger, and weatherability is poor, so that not having the problem of good market competition dynamics.
To achieve the above object, the invention provides the following technical scheme:
A kind of forming method of resin, the forming step of the resin are as follows:
Step 1: choosing resin and form material, and it includes: phthalic anhydride, glycerol, oil that wherein Albertol, which synthesizes material, Acid, diluted solvent, reflux dimethylbenzene and reinforcing agent.
Step 2: the phthalic anhydride of selection, glycerol, oleic acid, reflux dimethylbenzene and reinforcing agent are passed through into metering respectively Device, which is added in reaction kettle, to be chemically reacted, and is inputted during the reaction by external nitrogen device, thus anti- It answers and forms antioxygen protection inside kettle, be passed through after nitrogen in this way, start to mix slowly inside reaction kettle.
Step 3: during the reaction, being heated by external heating device, so that on reaction kettle internal temperature It rises, in this way by external heating device, so that temperature is slowly brought up to 180 DEG C in 2h, and 1h is kept the temperature, so that warm Degree maintains 180 DEG C, later by heating device, so that reaction kettle internal temperature is warming up in 210 DEG C in 2h, and ties up Hold heat preservation 2h.
Step 4: being manually sampled, and is reached by sampling survey acid value and viscosity is sticked when acid value of sampling reaches 10mgKOH/g Degree (Gardner-Holdt bubble tube) reaches 10s, then stops heating, if not reaching, continues to keep temperature, carries out repetition measurement every 0.5h, thus Until reaching requirement.
Step 5: diluted solvent is added later and is stirred dilution, later by filtering and detection.
Step 6: molding resin material is packed, to be put in storage storage.
Preferably, first slow rear fast principle should be deferred to by nitrogen protection Gas Stirring in the step 2, avoided out Now quickly agitation.
Preferably, in the reaction process of the step 3, reflux dimethylbenzene, which obtains additional amount, influences rate of water loss, and flow back diformazan Benzene dosage improves, although regurgitant volume can be increased, also reduces reaction temperature simultaneously, therefore the dimethylbenzene dosage that flows back does not surpass generally 8% is crossed, and as reaction carries out, when the rate of output water reduces, gradually to release some reflux dimethylbenzene, to improve temperature, Allow to further reaction be promoted to carry out.
Preferably, the step 4 is when keeping temperature to be heated, depending on holding temperature and time are with formula, and And it is related with oil product and oil content.
Preferably, the polyesterification reaction of the step 3 will pay close attention to the rate of output water and water yield, and sample in required time, Measure acid value and viscosity.
Preferably, the dilution mixing time of the step 5 is 0.5h, and temperature maintains to be filtered in 65 DEG C.
Compared with prior art, the present invention provides a kind of forming method of resin, have it is following the utility model has the advantages that
The forming method of resin of the present invention pass through Step 1: Step 2: Step 3: Step 4: step 5 and step 6 into Row effectively preparation, consequently facilitating resin preparation forming, and formed in preparation process in resin, pass through six step systems in this way It is standby, so that the working efficiency of preparation is improved, and in polyesterification reaction, it is connected by the molecular structure of reinforcing agent, so that having Effect changes molecule connection type, so that resin when artificial synthesized formation, has good bending strength and compression Intensity, mechanical property and weatherability are changed, and have good market competition dynamics.
Specific embodiment
Technical scheme in the embodiment of the invention is clearly and completely described, it is clear that described embodiment is only It is a part of the embodiment of the present invention, instead of all the embodiments.Based on the embodiments of the present invention, ordinary skill people Member's every other embodiment obtained without making creative work, shall fall within the protection scope of the present invention.
The present invention provides a kind of technical solution:
A kind of forming method of resin, the forming step of resin are as follows:
Step 1: choosing resin and form material, and it includes: phthalic anhydride, glycerol, oil that wherein Albertol, which synthesizes material, Acid, diluted solvent, reflux dimethylbenzene and reinforcing agent.
Step 2: the phthalic anhydride of selection, glycerol, oleic acid, reflux dimethylbenzene and reinforcing agent are passed through into metering respectively Device, which is added in reaction kettle, to be chemically reacted, and is inputted during the reaction by external nitrogen device, thus anti- It answers and forms antioxygen protection inside kettle, be passed through after nitrogen in this way, start to mix slowly inside reaction kettle.
Step 3: during the reaction, being heated by external heating device, so that on reaction kettle internal temperature It rises, in this way by external heating device, so that temperature is slowly brought up to 180 DEG C in 2h, and 1h is kept the temperature, so that warm Degree maintains 180 DEG C, later by heating device, so that reaction kettle internal temperature is warming up in 210 DEG C in 2h, and ties up Hold heat preservation 2h.
Step 4: being manually sampled, and is reached by sampling survey acid value and viscosity is sticked when acid value of sampling reaches 10mgKOH/g Degree (Gardner-Holdt bubble tube) reaches 10s, then stops heating, if not reaching, continues to keep temperature, carries out repetition measurement every 0.5h, thus Until reaching requirement.
Step 5: diluted solvent is added later and is stirred dilution, later by filtering and detection.
Step 6: molding resin material is packed, to be put in storage storage.It is formed in preparation process in resin, people Member is prepared by six steps, so that the working efficiency of preparation is improved, and in polyesterification reaction, pass through reinforcing agent Molecular structure connection, so that effectively molecule connection type is changed, so that resin when artificial synthesized formation, has very Good bending strength and compressive strength, mechanical property and weatherability are changed, and have good market competition dynamics.
Further, first slow rear fast principle should be deferred to by nitrogen protection Gas Stirring in step 2, avoided the occurrence of fast Speed agitation.It is protected in step 2 addition nitrogen gas, so that avoiding internal gas from carrying out participation reaction, and stirring is deferred to Fast principle, avoids the occurrence of quick agitation after first slow, makes that polymerization is steady, goes on smoothly reaction in this way, so that polymerizeing quality It is guaranteed.
Further, in the reaction process of step 3, reflux dimethylbenzene, which obtains additional amount, influences rate of water loss, and reflux dimethylbenzene is used Amount improves, although regurgitant volume can be increased, also reduces reaction temperature simultaneously, therefore the dimethylbenzene dosage that flows back is usually no more than 8%, and as reaction carries out, when the rate of output water reduces, gradually to release some reflux dimethylbenzene is made with improving temperature Obtaining can further promote reaction to carry out.In this way during reaction, added by the control to reflux dimethylbenzene, so as to To control regurgitant volume state well, allows to effectively carry out reaction controlling, passes through the control amount of reflux dimethylbenzene in this way, So that the effectively whole reaction of control carries out, so that more convenient when producing preparation.
Further, step 4 is when keeping temperature to be heated, depending on holding temperature and time are with formula, Er Qieyu Oil product is related with oil content.When preparation, by keeping temperature to be heated, so that effectively guaranteeing the abundant of internal-response It completes, so that there is certain difference in surface, so that depending on preparation is more efficient, and holding temperature and time are with formula, and It is and related with oil product and oil content, so as to can be very good to carry out manual control, so that more increasing when controlling preparation Effect.
Further, the polyesterification reaction of step 3 will pay close attention to the rate of output water and water yield, and sample in required time, measurement Acid value and viscosity.In this way in production preparation, it can be very good to obtain pet reaction state by the rate of output water and water yield, from And controlled convenient for personnel, and sample in required time, acid value and viscosity are measured, consequently facilitating control is adjusted in personnel, It is convenient for preparing.
Further, the dilution mixing time of step 5 is 0.5h, and temperature maintains to be filtered in 65 DEG C.It is preparing in this way It is more convenient efficient when letdown resin, and the resin temperature prepared is maintained and is filtered in 65 DEG C, is allowed to Filtering inner material well, and be convenient for filtering, so that whole resin quality is improved.
The working principle of the invention and process for using: a kind of forming method of resin of the present invention, the forming step of resin It is as follows:
Step 1: choosing resin and form material, and it includes: phthalic anhydride, glycerol, oil that wherein Albertol, which synthesizes material, Acid, diluted solvent, reflux dimethylbenzene and reinforcing agent.
Step 2: the phthalic anhydride of selection, glycerol, oleic acid, reflux dimethylbenzene and reinforcing agent are passed through into metering respectively Device, which is added in reaction kettle, to be chemically reacted, and is inputted during the reaction by external nitrogen device, thus anti- It answers and forms antioxygen protection inside kettle, be passed through after nitrogen in this way, start to mix slowly inside reaction kettle.
Step 3: during the reaction, being heated by external heating device, so that on reaction kettle internal temperature It rises, in this way by external heating device, so that temperature is slowly brought up to 180 DEG C in 2h, and 1h is kept the temperature, so that warm Degree maintains 180 DEG C, later by heating device, so that reaction kettle internal temperature is warming up in 210 DEG C in 2h, and ties up Hold heat preservation 2h.
Step 4: being manually sampled, and is reached by sampling survey acid value and viscosity is sticked when acid value of sampling reaches 10mgKOH/g Degree (Gardner-Holdt bubble tube) reaches 10s, then stops heating, if not reaching, continues to keep temperature, carries out repetition measurement every 0.5h, thus Until reaching requirement.
Step 5: diluted solvent is added later and is stirred dilution, later by filtering and detection.
Step 6: molding resin material is packed, to be put in storage storage.It is carried out in this way by six steps effective Preparation, consequently facilitating resin preparation forming, and in polyesterification reaction, it is connected by the molecular structure of reinforcing agent, so that effectively Change molecule connection type so that resin is when artificial synthesized formation, have good bending strength and compression strong Degree, mechanical property and weatherability are changed, and have good market competition dynamics.
It although an embodiment of the present invention has been shown and described, for the ordinary skill in the art, can be with A variety of variations, modification, replacement can be carried out to these embodiments without departing from the principles and spirit of the present invention by understanding And modification, the scope of the present invention is defined by the appended.

Claims (6)

1. a kind of forming method of resin, it is characterised in that: the forming step of the resin is as follows:
Step 1: choose resin formed material, wherein Albertol synthesize material include: phthalic anhydride, glycerol, oleic acid, Diluted solvent, reflux dimethylbenzene and reinforcing agent;
Step 2: the phthalic anhydride of selection, glycerol, oleic acid, reflux dimethylbenzene and reinforcing agent are passed through into metering device respectively It is added in reaction kettle and is chemically reacted, is inputted during the reaction by external nitrogen device, thus in reaction kettle Inside forms antioxygen protection, is passed through after nitrogen in this way, starts to mix slowly inside reaction kettle;
Step 3: during the reaction, being heated by external heating device, so that reaction kettle internal temperature rises, In this way by external heating device, so that temperature is slowly brought up to 180 DEG C in 2h, and 1h is kept the temperature, so that temperature is tieed up It holds at 180 DEG C, later by heating device, so that reaction kettle internal temperature is warming up in 210 DEG C in 2h, and maintains to protect Warm 2h;
Step 4: being manually sampled, and surveys acid value by sampling and reaches and viscosity, when acid value of sampling reaches 10mgKOH/g, viscosity (Gardner-Holdt bubble tube) reaches 10s, then stops heating, if not reaching, continues to keep temperature, repetition measurement is carried out every 0.5h, thus directly Reach requirement;
Step 5: diluted solvent is added later and is stirred dilution, later by filtering and detection;
Step 6: molding resin material is packed, to be put in storage storage.
2. a kind of forming method of resin according to claim 1, it is characterised in that: protected in the step 2 by nitrogen Shield Gas Stirring should defer to first slow rear fast principle, avoid the occurrence of quick agitation.
3. a kind of forming method of resin according to claim 1, it is characterised in that: the reaction process of the step 3 In, reflux dimethylbenzene, which obtains additional amount, influences rate of water loss, and reflux dimethylbenzene dosage improves, although regurgitant volume can be increased, simultaneously Reaction temperature is also reduced, therefore the dimethylbenzene dosage that flows back is usually no more than 8%, and as reaction carries out, works as the rate of output water When reduction, some reflux dimethylbenzene are gradually released, to improve temperature, allow to further reaction be promoted to carry out.
4. a kind of forming method of resin according to claim 1, it is characterised in that: the step 4 keep temperature into When row heating, depending on holding temperature and time are with formula, and also it is related with oil product and oil content.
5. a kind of forming method of resin according to claim 1, it is characterised in that: the polyesterification reaction of the step 3 The rate of output water and water yield are paid close attention to, and is sampled in required time, acid value and viscosity are measured.
6. a kind of forming method of resin according to claim 1, it is characterised in that: when the dilution stirring of the step 5 Between be 0.5h, temperature maintains to be filtered in 65 DEG C.
CN201910705568.6A 2019-08-01 2019-08-01 A kind of forming method of resin Pending CN110511363A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201910705568.6A CN110511363A (en) 2019-08-01 2019-08-01 A kind of forming method of resin

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201910705568.6A CN110511363A (en) 2019-08-01 2019-08-01 A kind of forming method of resin

Publications (1)

Publication Number Publication Date
CN110511363A true CN110511363A (en) 2019-11-29

Family

ID=68624018

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201910705568.6A Pending CN110511363A (en) 2019-08-01 2019-08-01 A kind of forming method of resin

Country Status (1)

Country Link
CN (1) CN110511363A (en)

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
MD20060164A (en) * 2006-06-23 2008-01-31 Svetlana Bordian Process for obtaining paintwork material on alkyd base
CN101506267A (en) * 2006-06-27 2009-08-12 沙伯基础创新塑料知识产权有限公司 Weatherable, thermostable polymers having improved flow composition
CN102993925A (en) * 2012-10-12 2013-03-27 张家港市永法涂料有限公司 Air-drying type alkyd resin paint with high solid content and preparation method ofe air-drying type alkyd resin paint
CN103694463A (en) * 2013-12-02 2014-04-02 安庆菱湖涂料有限公司 Preparation method of soya alkyd resin
CN105037696A (en) * 2015-08-12 2015-11-11 安徽菱湖漆股份有限公司 Preparation method of alkyd resin for self-drying coating modified by tall oil acid
CN106750215A (en) * 2016-12-21 2017-05-31 中国林业科学研究院林产化学工业研究所 A kind of unsaturated polyester (UP) biological nano hybrid resin and its synthetic method and application

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
MD20060164A (en) * 2006-06-23 2008-01-31 Svetlana Bordian Process for obtaining paintwork material on alkyd base
CN101506267A (en) * 2006-06-27 2009-08-12 沙伯基础创新塑料知识产权有限公司 Weatherable, thermostable polymers having improved flow composition
CN102993925A (en) * 2012-10-12 2013-03-27 张家港市永法涂料有限公司 Air-drying type alkyd resin paint with high solid content and preparation method ofe air-drying type alkyd resin paint
CN103694463A (en) * 2013-12-02 2014-04-02 安庆菱湖涂料有限公司 Preparation method of soya alkyd resin
CN105037696A (en) * 2015-08-12 2015-11-11 安徽菱湖漆股份有限公司 Preparation method of alkyd resin for self-drying coating modified by tall oil acid
CN106750215A (en) * 2016-12-21 2017-05-31 中国林业科学研究院林产化学工业研究所 A kind of unsaturated polyester (UP) biological nano hybrid resin and its synthetic method and application

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
王渴望,等: "水型醇酸树脂的合成及改性研究进展", 《涂料技术与文摘》 *

Similar Documents

Publication Publication Date Title
CN102532450B (en) Production method for quickly curing nitrogen-free furane resin
CN205007944U (en) A automatic material conveying equipment for preparing polyimide resin
CN104610902A (en) Rapidly post-cured polyurethane hot melt adhesive and preparation method thereof
CN104004156B (en) A kind of anti-migration method for preparing thermoplastic polyurethane elastomer
CN104530429B (en) High-fluidity wide-processing-widow polyimide pre-polymer and preparation method thereof
CN107915623A (en) A kind of solvent-free 4 chloro methyl acetoacetate continuous stream synthetic method and system
CN110294675B (en) Method and system for preparing methyl acetoacetate by adopting tubular continuous flow reactor
CN105712865B (en) Solid citric acid aluminum crosslinker, preparation method and its application
CN108586265A (en) Pentanediamine sebacate and its crystal
CN110511363A (en) A kind of forming method of resin
CN109851778A (en) A kind of method that anionic ring-opening polymerization prepares polybutyrolactam
US8754256B2 (en) Process for preparation of L-Arginine α-ketoglutarate 1:1 and 2:1
CN103897089B (en) Low viscous modified polyvinyl alcohol of a kind of crystalloid and preparation method thereof
CN103073707B (en) Alkyd resin and preparation method thereof
CN108948338B (en) End-capped unsaturated polyester resin and synthesis process thereof
CN106188497A (en) A kind of synthetic method of modified epoxy acrylate resin
CN104744250A (en) Method for synthesizing diacetylglycine
CN106883447B (en) A kind of application of high-strength polymer film, preparation method and diluent
CN106317279B (en) A kind of preparation method of weather-proof toughness white glue with vinyl
CN111533903B (en) Nitrogen-containing nutritional type biodegradable material, preparation method thereof and application of nitrogen-containing nutritional type biodegradable material in preparation of mulching film
CN105778724B (en) A kind of cathode Water-borne Coatings Emulsion and its production technology
CN209254662U (en) A kind of automatic salting device
CN105985519A (en) Synthesis method of phenoxy resin
CN109232893A (en) A kind of high-efficiency synthesis method of polyphenylene sulfide
CN111057160A (en) Preparation method of high amylose starch for fluid loss additive

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
RJ01 Rejection of invention patent application after publication
RJ01 Rejection of invention patent application after publication

Application publication date: 20191129