CN1740213A - Production process of fine PVA powder for building material - Google Patents
Production process of fine PVA powder for building material Download PDFInfo
- Publication number
- CN1740213A CN1740213A CN 200510027987 CN200510027987A CN1740213A CN 1740213 A CN1740213 A CN 1740213A CN 200510027987 CN200510027987 CN 200510027987 CN 200510027987 A CN200510027987 A CN 200510027987A CN 1740213 A CN1740213 A CN 1740213A
- Authority
- CN
- China
- Prior art keywords
- polyvinyl alcohol
- production process
- building material
- powder
- pva powder
- 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.)
- Granted
Links
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 19
- 239000000843 powder Substances 0.000 title claims abstract description 17
- 239000004566 building material Substances 0.000 title claims abstract description 13
- 239000004372 Polyvinyl alcohol Substances 0.000 claims description 26
- 229920002451 polyvinyl alcohol Polymers 0.000 claims description 26
- 239000000463 material Substances 0.000 claims description 13
- 238000000034 method Methods 0.000 claims description 12
- 238000001816 cooling Methods 0.000 claims description 9
- 238000012856 packing Methods 0.000 claims description 2
- 239000003292 glue Substances 0.000 abstract description 13
- 238000005516 engineering process Methods 0.000 abstract description 4
- 231100000252 nontoxic Toxicity 0.000 abstract 1
- 230000003000 nontoxic effect Effects 0.000 abstract 1
- 235000019422 polyvinyl alcohol Nutrition 0.000 description 21
- 239000002994 raw material Substances 0.000 description 4
- 230000002939 deleterious effect Effects 0.000 description 3
- 229920002554 vinyl polymer Polymers 0.000 description 3
- 239000011248 coating agent Substances 0.000 description 2
- 238000000576 coating method Methods 0.000 description 2
- 238000004891 communication Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000003595 mist Substances 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 238000010298 pulverizing process Methods 0.000 description 2
- 238000003860 storage Methods 0.000 description 2
- WSFSSNUMVMOOMR-UHFFFAOYSA-N Formaldehyde Chemical class O=C WSFSSNUMVMOOMR-UHFFFAOYSA-N 0.000 description 1
- 208000034189 Sclerosis Diseases 0.000 description 1
- 230000001070 adhesive effect Effects 0.000 description 1
- 238000013019 agitation Methods 0.000 description 1
- 239000012752 auxiliary agent Substances 0.000 description 1
- 238000001311 chemical methods and process Methods 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 125000004122 cyclic group Chemical group 0.000 description 1
- 238000004090 dissolution Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 235000019256 formaldehyde Nutrition 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 239000003112 inhibitor Substances 0.000 description 1
- 238000005304 joining Methods 0.000 description 1
- WSFSSNUMVMOOMR-NJFSPNSNSA-N methanone Chemical compound O=[14CH2] WSFSSNUMVMOOMR-NJFSPNSNSA-N 0.000 description 1
- 239000004005 microsphere Substances 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 229920003023 plastic Polymers 0.000 description 1
- 239000002861 polymer material Substances 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 239000007858 starting material Substances 0.000 description 1
- 231100000167 toxic agent Toxicity 0.000 description 1
- 239000003440 toxic substance Substances 0.000 description 1
- 230000000007 visual effect Effects 0.000 description 1
Images
Landscapes
- Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
- Processes Of Treating Macromolecular Substances (AREA)
- Compositions Of Macromolecular Compounds (AREA)
Abstract
The present invention is production process of superfine PVA powder for building material, belongs to the field of superfine crushing technology, and features that PVA with cold brittleness is deeply cooled and pumped with high speed airflow to be crushed into fine powder finer than 120 mesh. The present invention has greatly raised production efficiency, and the superfine PVA powder is convenient in storing, transportation and use, and non-toxic, and may be used to replace No. 107 glue. The production process of the present invention may be used to replace traditional one.
Description
Technical field: belong to ultra tiny pulverizing technical field.
Background technology: polyvinyl alcohol is a kind of synthesized polymer material with good adhesiveproperties, is used widely as building glue in building materials field.Because there are shortcomings such as dissolving difficulty (need heating and constantly could dissolve under the agitation condition), solubleness are little in the macrobead polyvinyl alcohol, directly the glue use is built in conduct.Must make glue just can be used for putty, coating etc. and use at building material product.
Traditional preparation glue method is after polyvinyl alcohol is made polyvinyl formal class glue (i.e. 107 glue), uses for joining putty and coating.Contain auxiliary agents such as free formaldehyde, mould inhibitor, rust-preventive agent because of in 107 glue, these materials all are deleterious to human body and environment.In July calendar year 2001, the Ministry of Construction clearly proposes to ban use of polyvinyl formal class glue (i.e. 107 glue), requires the substitute products of exploitation 107 glue.
Experiment is found, the polyvinyl alcohol of indissoluble is handled the back by superfine communication technique become the fine Powdered solubility property fast that has, its solvability is relevant with granular size, the particle of polyvinyl alcohol is thin more, its specific surface area is big, and dry powder building materials production process mixing of materials performance is good, and the thin more dissolution rate of particle is fast more, have good workability, visual appearance is good.
It is good that granular size is generally controlled greater than 120 orders, and people attempt with traditional eddy current crushing technology in polyvinyl alcohol, but when fineness is 120 orders, and yield is only about 20%, the production cost height, and efficient is low.
Summary of the invention: the invention provides a kind of formaldehydes material that do not contain, and transportation, storage and use are all convenient, energy substitutes the use of 107 glue, and fineness is greater than 120 orders, and yield is high, the production method of a kind of fine PVA powder for building material that is suitable for producing.
The technical scheme that the present invention takes:
Utilize polyvinyl alcohol to have the physical property of cold shortness, earlier the quick deep cooling of polyvinyl alcohol is arrived cold shortness, temperature to suitable micronizing requirement, equipment by micronizing clashes into high velocity air then, and the polyvinyl alcohol of deep cooling is ground into the detailed catalogue degree greater than 120 fine PVA powder for building material.
Positively effect behind enforcement the present invention: polyvinyl formal class glue production process is a chemical process, and product and raw material have the variation of matter.It is need add human body and all deleterious material of environment by producing and storing.
No-solvent type dry powder building materials are physical processes with the production process of polyvinylalcohol microsphere arogel stick, product and raw material do not have the variation of matter, have only geometrical shape to change (promptly becoming the polyvinyl alcohol micro mist) by the macrobead polyvinyl alcohol, production process does not need to add other materials, does not have human body and the deleterious material of environment in the product.
Polyvinyl alcohol is a kind of thermal plastic material, do not have the pre-cooled system of material and is difficult to get rid of in the crushing process shortcomings such as heat that produced because of " superfine communication technique " of routine, therefore material can not reach the micronizing condition of carrying out at low temperatures, the fineness of pulverizing does not reach greater than 80 purpose requirements, though can use reluctantly, but production efficiency low (yield is about 20%) production cost height, the present invention adopts the air cooling technology, pre-cooled system of material and the cooling performance that improves shredding unit have been increased, improve the fineness of micronizing efficient and product, the polyvinyl alcohol smashing fineness can reach more than 120～200 orders, the super-fine powder yield can reach 90%, and production efficiency greatly improves, and is 20% from original yield, bring up to 90%, building materials become micro mist shape dry powder with polyvinyl alcohol, and convenient the storage and transportation can fully be dissolved at normal temperatures, it is also extremely convenient to use, and does not wherein have toxic substance.
Description of drawings:
Fig. 1, fine PVA powder for building material production method synoptic diagram;
Fig. 2, process flow diagram.
Embodiment:
Now the invention will be further described in conjunction with the accompanying drawings, at first select the polyvinyl alcohol raw material, select to have got 17～18 and 24～88 the polyvinyl alcohol product trade mark of market from the sticking power that satisfies the dry powder building materials and water-proof requirement and be the starting material of dry powder, enter technological operation then.
The gas 1 that enters pulverizer 5 is cooled to cryogenic gas through cooling system 2, cryogenic gas and material 4 are sent into Lowtemperaturepulverizer 5 after the precooling in chilldown system 3, carry out heat exchange with raw material and make the material sclerosis, entering crushing system carries out passing through stage trapping 6 again after the micronization processes, generate primary products, through processing such as sub-sieve 7, checks 8, select the detailed catalogue degree again greater than 120 purpose powder.Form product, packing is dispatched from the factory at last.After gas in the chilldown system 3 and thing were reclaimed by recovery system 9, gas entered cooling system 2, and thing enters chilldown system 3, continues precooling, pulverized after stage trapping 6, and its large granular materials turns back to the former process cyclic process again, pulverizes again.
In order to guarantee production on-site environment, adopt multi-stage, efficient strainer dedusting and with technical measures such as the gas in the production process recycle.So both controlled source of pollution and also cut down the consumption of energy, guaranteed that production on-site environment is up to standard.
Claims (3)
1, a kind of production method of fine PVA powder for building material is characterized in that: with the quick deep cooling of polyvinyl alcohol, make polyvinyl alcohol tool cold shortness, clash into method by micronizing equipment with high velocity air, the polyvinyl alcohol of cold shortness is pulverized, concrete steps are as follows:
(1) polyvinyl alcohol material choice;
(2) quick deep cooling;
(3) the high velocity air bump is pulverized;
(4) select the detailed catalogue degree greater than 120 purpose powder;
(5) packing
2, method according to claim 1 is characterized in that: described quick deep cooling is that temperature is lower than negative 100 degree.
3, method according to claim 1 is characterized in that: described high velocity air is that engine speed is more than 4500 rev/mins.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2005100279877A CN1300222C (en) | 2005-07-21 | 2005-07-21 | Production process of fine PVA powder for building material |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2005100279877A CN1300222C (en) | 2005-07-21 | 2005-07-21 | Production process of fine PVA powder for building material |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1740213A true CN1740213A (en) | 2006-03-01 |
| CN1300222C CN1300222C (en) | 2007-02-14 |
Family
ID=36092752
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNB2005100279877A Expired - Fee Related CN1300222C (en) | 2005-07-21 | 2005-07-21 | Production process of fine PVA powder for building material |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN1300222C (en) |
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101804378A (en) * | 2010-03-01 | 2010-08-18 | 朱建军 | Polyvinyl alcohol micropowder-type dry powder production process with high product yield |
| CN107266761A (en) * | 2016-04-07 | 2017-10-20 | 中国石油化工集团公司 | A kind of thermoplastic polyvinyl alcohol water resistance compound and preparation method thereof |
| CN107266838A (en) * | 2016-04-07 | 2017-10-20 | 中国石油化工集团公司 | A kind of thermoplastic polyvinyl alcohol water-soluble compound and preparation method thereof |
| CN110079172A (en) * | 2019-05-15 | 2019-08-02 | 南阳九鼎材料科技股份有限公司 | A kind of preparation process of salicylic acid isooctyl ester lotion |
| CN110898968A (en) * | 2019-12-16 | 2020-03-24 | 赵虎 | Preparation method of anticorrosive paint raw material |
| CN111286048A (en) * | 2020-03-25 | 2020-06-16 | 宁夏颐星新材料科技有限公司 | Production process of polyvinyl alcohol powder |
| CN111333874A (en) * | 2020-03-13 | 2020-06-26 | 宁夏颐星新材料科技有限公司 | Production process of polyvinyl alcohol ultrafine powder |
| CN112026052A (en) * | 2020-09-02 | 2020-12-04 | 哈尔滨工业大学 | Preparation method of superfine polyvinyl alcohol particles |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2520518B2 (en) * | 1991-03-29 | 1996-07-31 | 信越ポリマー株式会社 | Method for producing polyvinyl alcohol type molded article |
-
2005
- 2005-07-21 CN CNB2005100279877A patent/CN1300222C/en not_active Expired - Fee Related
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101804378A (en) * | 2010-03-01 | 2010-08-18 | 朱建军 | Polyvinyl alcohol micropowder-type dry powder production process with high product yield |
| CN107266761A (en) * | 2016-04-07 | 2017-10-20 | 中国石油化工集团公司 | A kind of thermoplastic polyvinyl alcohol water resistance compound and preparation method thereof |
| CN107266838A (en) * | 2016-04-07 | 2017-10-20 | 中国石油化工集团公司 | A kind of thermoplastic polyvinyl alcohol water-soluble compound and preparation method thereof |
| CN110079172A (en) * | 2019-05-15 | 2019-08-02 | 南阳九鼎材料科技股份有限公司 | A kind of preparation process of salicylic acid isooctyl ester lotion |
| CN110898968A (en) * | 2019-12-16 | 2020-03-24 | 赵虎 | Preparation method of anticorrosive paint raw material |
| CN111333874A (en) * | 2020-03-13 | 2020-06-26 | 宁夏颐星新材料科技有限公司 | Production process of polyvinyl alcohol ultrafine powder |
| CN111286048A (en) * | 2020-03-25 | 2020-06-16 | 宁夏颐星新材料科技有限公司 | Production process of polyvinyl alcohol powder |
| CN112026052A (en) * | 2020-09-02 | 2020-12-04 | 哈尔滨工业大学 | Preparation method of superfine polyvinyl alcohol particles |
Also Published As
| Publication number | Publication date |
|---|---|
| CN1300222C (en) | 2007-02-14 |
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Granted publication date: 20070214 |
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