CN1222528A - Biological solidification technology of natural latex - Google Patents
Biological solidification technology of natural latex Download PDFInfo
- Publication number
- CN1222528A CN1222528A CN 98122556 CN98122556A CN1222528A CN 1222528 A CN1222528 A CN 1222528A CN 98122556 CN98122556 CN 98122556 CN 98122556 A CN98122556 A CN 98122556A CN 1222528 A CN1222528 A CN 1222528A
- Authority
- CN
- China
- Prior art keywords
- starch
- latex
- rubber
- proteolytic enzyme
- glue
- 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
Landscapes
- Compositions Of Macromolecular Compounds (AREA)
- Tires In General (AREA)
Abstract
During the solidification, protease is utilized to decompose the protecting layer protein of latex granule and to promote the gelatification of lalex granule owing to the destruction of the protecting layer; starch is added into latex and its enormous molecular chain constitutes hydrophilic capillary pipes favorable to the drying of latex granule; hydroxylamine sulfate of certain concentration is used to regulate the Mooney viscosity of raw rubber. The process is simple but practical and can obtain dry rubber with nitrogen content lower than 0.4%, PRI higher than 82, Mooney viscosity not greater than 76, excellent vulcanization property for obtain vulcanized rubber with physical performance meeting the standard of specific rubber for radial ply tyre.
Description
The present invention relates to a kind of biological solidification technology, relate in particular to a kind of biological solidification technology of natural rubber latex.
The clotting method of natural rubber latex can be divided into three major types: chemical process one adds the peptizer of acid, salt, dewatering agent and so on; Physical method-heating, freezing or violent stirring; Biological method one utilizes latex original or the bacterium that adds or the effect of enzyme, makes latex coagulation.Standard rubbers generally adopts the acid cure method to produce, and this class glue can not satisfy the requirement of radial because vulcanization rate is slow, strength and extension property is poor slightly, uniformity in product performance is relatively poor.The special-purpose natural rubber production technique of meridian rubber tire tire mainly contains following two kinds at present: a kind of core of meridian glue production technique is the auxiliary biological coagulation of latex, mixes with high-quality plantation freezing plastic is broken by a certain percentage.But the production of high-quality plantation freezing plastic causes latex can not solidify fully in 20 hours under field conditions (factors) because the nocturnal temperature of rubber woods section usually about 20 ℃, is unfavorable for the breeding of bacterium in the latex, has seriously restricted this implementation of processes.Another kind of meridian glue production technique, based on the auxiliary biological coagulation of latex, the time of drying of its processing requirement is longer than mark glue fully, and the cross-linked rubber strength and extension property is good, but crude rubber Mooney viscosity is too high, and the user hangs back; Therefore, this technology does not formally put into production as yet.
The objective of the invention is to overcome the limitation and the shortcoming of above-mentioned prior art, a kind of simple and direct practicality, biological solidification technology that production efficiency is high are provided, provide product performance more can satisfy the natural rubber latex solidifying process that radial tyre production requires.
In order to reach purpose of the present invention, the invention provides following technical proposals:
The biological solidification technology of natural rubber latex, comprise latex dilution after coagulation, the regulation and control of rubber viscosity, the grumeleuse procedure of processing, with proteolytic enzyme and starch as peptizer, oxammonium sulfate is as the viscosity adjusting control agent, respectively by dried glue with it weight ratio be 1: 0.00001-0.0001,1: 0.01-0.035,1: 0.00025-0.0005 adds liquid proteolytic enzyme, sol starch and oxammonium sulfate and goes in the latex.
In the above-mentioned technology, proteolytic enzyme can be plant protease, also can be microbial protease.
In the above-mentioned technology, starch had both contained amylose starch and had also contained amylopectin, can be to give birth to starch, and also can be pre-gelatinized starch.
In the above-mentioned technology, sol starch concentration is 1-5% preferably.
Concrete preparation steps of the present invention is: proteolytic enzyme is mixed with the aqueous solution, adds an amount of oxammonium sulfate and dissolving, it is 2.5% colloidal sol that starch is modulated into concentration; Measure the drc of fresh latex, add enzyme solution and starch colloidal sol, fully left standstill 18 hours behind the mixing, latex solidifies fully and forms continuous grumeleuse, processes by the mark adhesive process, and drying conditions is identical with mark glue.
In order to understand essentiality content of the present invention better, with know-why of the present invention compared with the prior art existing advantage of the present invention and beneficial effect are described below.
The protein of protease hydrolysis rubber particles protective layer impels micelle to destroy inter-adhesive generation gelling because of protective membrane; Only be to add under the situation of proteolytic enzyme, along with the increase of proteolytic enzyme usage quantity, the setting time of latex shortens, and drying is more and more difficult, and the technology of therefore just adding proteolytic enzyme is unsuccessful.Key character of the present invention is to find to use starch can quicken the drying of biological coagulation glue, and starch is the polyose biomacromolecule, the tool wetting ability, and molecular-weight average is hundreds thousand of; After the protective membrane of micelle is destroyed by proteolytic enzyme, the extremely unstable and inter-adhesive generation gelling of micelle, the huge molecular chain of starch is walked therebetween, form the hydrophilic sealing coat between hydrophobic micelle, when grumeleuse through the dehydration and granulation after, these hydrophilic sealing coats constitute the inner flourishing kapillary water system passages of granulation particles, help moisture from particle inside to surface diffusion; Compare with the mark adhesive process, need not prolong time of drying, under equal conditions, drying effect even be better than mark glue; So far, the dry difficult point of biological coagulation glue obtains breaking through.
Compared with prior art, advantage of the present invention and positively effect are easy and simple to handle, excellent product performance.Caouttchouc drying, the nitrogen content that makes with the present invention is lower than 0.4%, PRI surpasses 82, mooney viscosity is not higher than 76, and vulcanization rate improves, and torque increment strengthens, and the cross-linked rubber strength and extension property is good.These performance index reach the development standard of the special-purpose natural rubber of China radial, and wherein part index number is better than the rubber goods that obtain with above-mentioned two kinds of technologies.
Therefore, compare with domestic existing meridian glue production technique, the invention of this technology has following characteristics:
1, operation is simple and direct, and is easy to operate;
2, peptizer proteolytic enzyme and auxiliary material are homemade industrial raw material, steady sources;
3, implementation of processes is not limited by the temperature in rubber reclamation area.
Further specify content of the present invention with embodiments of the invention below, but content of the present invention is not limited to this.
Embodiment 1: get fresh latex, measuring drc is 28.7%, take by weighing 125 kilograms of latex, 1 kilogram of the enzyme solution (containing proteolytic enzyme 1.3 grams, oxammonium sulfate 13.6 grams) that adds preparation in advance, 24 kilograms of starch colloidal sols (starch-containing 0.5 kilogram), 13.6 kilograms in clear water, fully behind the mixing in the workshop standing over night, latex coagulation is complete after 18 hours, whey is turbid and not white.
Embodiment 2: get fresh latex, measuring drc is 35.1%, take by weighing 94 kilograms, 1 kilogram of the enzyme solution (containing proteolytic enzyme 1.2 grams, oxammonium sulfate 12.5 grams) that adds preparation in advance, 25 kilograms of starch colloidal sols (starch-containing 0.45 kilogram), 30 kilograms in clear water, fully behind the mixing in the workshop standing over night, latex coagulation is complete after 18 hours, whey is turbid and not white.
Carry out dehydration, the granulation of grumeleuse by the mark adhesive process, particle is packed into and is marked glue drying cupboard one case, and drying conditions is identical with mark glue fully.Get glue sample (following represent) check of embodiment 1 and embodiment 2 with KS-5 and KS-6, the results are shown in following table, wherein, the data of meridian glue desired indicator and Hainan meridian glue development sample 7182 are selected from " tire industry " nineteen ninety-five the 6th phase 327-334 page or leaf such as Liu Huilun.
The rubber physicochemical property that table 1 technology of the present invention is solidified and with the development standard contrast
| Project | Technology sample KS-5 KS-6 of the present invention | No. 10 glue of desired indicator | Hainan meridian glue development sample 7182 | |
| Impurity/% | ????0.02 | ????0.01 | ????≤0.1 | ????0.015 |
| Ash content/% | ????0.23 | ????0.25 | ????≤0.6 | ????0.28 |
| Nitrogen content/% | ????0.34 | ????0.36 | ????≤0.5 | ????0.45 |
| Volatile matter/% | ????0.29 | ????0.29 | ????≤0.5 | ????0.32 |
| The plasticity initial value | ????46 | ????43 | ????42±3 | ????39.0 |
| Plasticity retention(percentage) | ????87 | ????88 | ????≥60 | ????80.2 |
| Mooney viscosity [ML (@100 ℃ of 1+4)] | ????71 | ????70 | ????83±10 | ????75.8 |
The vulcanization characteristics of table 2 pure gum compound material of the present invention and with the mark glue contrast
Annotate: 1) test conditions: LHY-II rheometer, 160 ℃ of test temperatures, test period 30min shakes
| Glue sample project | Technology sample of the present invention 1)????KS-6 | Yunnan mark glue | Hainan 7182 2) | Hainan mark glue 2) |
| t 10/min | ????1.58 | ????1.98 | ????3.4 | ????4.1 |
| t 90/min | ????6.02 | ????7.70 | ????5.9 | ????6.4 |
| The sulfurizing time range of decrease/% with respect to mark glue | ????21.8 | ????/ | ????7.8 | ????/ |
| M L/N·m | ????0.663 | ????0.650 | ????0.6 | ????0.72 |
| M H/N·m | ????2.870 | ????2.538 | ????6.65 | ????6.30 |
| M H-M L/ Nm is with respect to the △ torque amplification/% of mark glue | ????2.207 ????16.9 | ????1.888 ????/ | ????6.05 ????8.4 | ????5.58 ????/ |
Swing frequency 1.7Hz, 1 ° of amplitude
Test recipe: rubber 100, zinc oxide 6.0, sulphur 3.5, stearic acid 0.5 promotes
NS 0.7 annotates: 2) test conditions: Meng Shan is the 100S rheometer, 160 ℃ of test temperatures, 3 ° of amplitudes
Test recipe: rubber 100, zinc oxide 6.0, sulphur 3.5, stearic acid 0.5 promotes
NS0.7
The pure glue of table 3 the present invention cooperates the performance of cross-linked rubber
| Project | ????KS-5 | ????KS-6 | ????7182 1) | ||||||
| 143 ℃ * min of cure conditions | ????20 | ????30 | ????45 | ????20 | ????30 | ????45 | ????20 | ????30 | ????45 |
| Shao Er A type hardness tester/degree | ????33 | ????32 | ????33 | ????31 | ????32 | ????31 | ????32 | ????32 | ????33 |
| 300% stress at definite elongation/Mpa | ????1.5 | ????1.4 | ????1.5 | ????1.5 | ????1.5 | ????1.5 | ????1.5 | ????1.6 | ????1.5 |
| 500% stress at definite elongation/Mpa | ????2.4 | ????2.4 | ????2.2 | ????2.4 | ????2.8 | ????2.2 | ????3.4 | ????3.4 | ????3.2 |
| Tensile strength/Mpa | ????21.1 | ????19.4 | ????194 | ????19.6 | ????22.0 | ????21.0 | ????21.4 | ????20.8 | ????21.5 |
| Tensile yield % | ????866 | ????882 | ????902 | ????861 | ????828 | ????935 | ????794 | ????844 | ????836 |
Sizing compound formula: rubber 100, zinc oxide 5.0, sulphur 3.0, stearic acid 0.5, captax 0.7
Can draw to draw a conclusion from table 1, table 2 and table 3: the contrast of the assay of glue sample of the present invention, development standard and Hainan meridian glue sample shows that the physicochemical property of rubber of the present invention reaches the development standard of meridian glue, the plasticity retention(percentage) height, and mooney viscosity is moderate; Vulcanization characteristics is good, shows that incipient cure time and sulfurizing time are shorter, and maximum torque is bigger; Vulcanizating glue physical performance is good.Therefore, compare with domestic existing meridian glue production technique, the invention of this technology has following characteristics: operation is simple and direct, and is easy to operate; Peptizer proteolytic enzyme and auxiliary material are homemade industrial raw material, steady sources; Implementation of processes is not limited by the temperature in rubber reclamation area.
Claims (5)
1. the biological solidification technology of natural rubber latex, comprise latex dilution after coagulation, the regulation and control of rubber viscosity, the grumeleuse procedure of processing, it is characterized in that with proteolytic enzyme and starch as peptizer, oxammonium sulfate is as the viscosity adjusting control agent, respectively by dried glue with it weight ratio be 1: 0.00001-0.0001,1: 0.01-0.035,1: 0.00025-0.0005 adds liquid proteolytic enzyme, sol starch and oxammonium sulfate and goes in the latex.
2. biological solidification technology according to claim 1 is characterized in that proteolytic enzyme can be plant protease, also can be microbial protease.
3. biological solidification technology according to claim 1 is characterized in that starch had both contained amylose starch and also contained amylopectin, can be to give birth to starch, and also can be pre-gelatinized starch.
4. biological solidification technology according to claim 1 is characterized in that preferably 1-5% of sol starch concentration.
5. according to claim 1 or 2 or 3 or 4 described biological solidification technologies, it is characterized in that proteolytic enzyme can be plant protease, it also can be microbial protease, starch had both contained amylose starch and had also contained amylopectin, can be to give birth to starch, also can be pre-gelatinized starch, sol starch concentration is 1-5% preferably.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN98122556A CN1077895C (en) | 1998-11-18 | 1998-11-18 | Biological solidification technology of natural latex |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN98122556A CN1077895C (en) | 1998-11-18 | 1998-11-18 | Biological solidification technology of natural latex |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1222528A true CN1222528A (en) | 1999-07-14 |
| CN1077895C CN1077895C (en) | 2002-01-16 |
Family
ID=5227799
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN98122556A Expired - Fee Related CN1077895C (en) | 1998-11-18 | 1998-11-18 | Biological solidification technology of natural latex |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN1077895C (en) |
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100429008C (en) * | 2005-09-30 | 2008-10-29 | 大连理工大学 | Process for preparing functional heat transfer surface |
| CN100482690C (en) * | 2005-08-26 | 2009-04-29 | 中国热带农业科学院农产品加工研究所 | Method of coagulating natural rubber fresh latex with fungus culture medium |
| CN102002119A (en) * | 2010-10-09 | 2011-04-06 | 中国热带农业科学院农产品加工研究所 | Method for coagulating natural rubber fresh latex by enzymatic method |
| CN102504051A (en) * | 2011-11-10 | 2012-06-20 | 中国热带农业科学院农产品加工研究所 | Method for solidifying nature rubber fresh latex through double parallel-flow solidification liquid adding |
| CN109369827A (en) * | 2018-10-29 | 2019-02-22 | 青岛科技大学 | A kind of clear flucculation process of glue |
| CN109485752A (en) * | 2018-10-29 | 2019-03-19 | 青岛科技大学 | A kind of concentrated natural latex flucculation process |
| WO2020087952A1 (en) * | 2018-10-29 | 2020-05-07 | 青岛科技大学 | Method for flocculating fresh latex |
| CN111909290A (en) * | 2020-08-27 | 2020-11-10 | 吴胜文 | Natural rubber latex coagulating additive |
| CN115028758A (en) * | 2022-06-23 | 2022-09-09 | 云南省热带作物科学研究所 | Latex treatment method for improving drying efficiency of low-protein natural rubber |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB2098222B (en) * | 1981-05-07 | 1984-08-15 | Malaysia Rubber Res Inst | Processing of hevea latex |
| JPH10279607A (en) * | 1997-04-01 | 1998-10-20 | Sumitomo Rubber Ind Ltd | Deproteinized natural rubber latex and vulcanized rubber |
-
1998
- 1998-11-18 CN CN98122556A patent/CN1077895C/en not_active Expired - Fee Related
Cited By (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100482690C (en) * | 2005-08-26 | 2009-04-29 | 中国热带农业科学院农产品加工研究所 | Method of coagulating natural rubber fresh latex with fungus culture medium |
| CN100429008C (en) * | 2005-09-30 | 2008-10-29 | 大连理工大学 | Process for preparing functional heat transfer surface |
| CN102002119A (en) * | 2010-10-09 | 2011-04-06 | 中国热带农业科学院农产品加工研究所 | Method for coagulating natural rubber fresh latex by enzymatic method |
| CN102002119B (en) * | 2010-10-09 | 2013-02-20 | 中国热带农业科学院农产品加工研究所 | Method for coagulating natural rubber fresh latex by enzymatic method |
| CN102504051A (en) * | 2011-11-10 | 2012-06-20 | 中国热带农业科学院农产品加工研究所 | Method for solidifying nature rubber fresh latex through double parallel-flow solidification liquid adding |
| CN102504051B (en) * | 2011-11-10 | 2013-07-03 | 中国热带农业科学院农产品加工研究所 | Method for solidifying nature rubber fresh latex through double parallel-flow and solidification liquid |
| CN109369827A (en) * | 2018-10-29 | 2019-02-22 | 青岛科技大学 | A kind of clear flucculation process of glue |
| CN109485752A (en) * | 2018-10-29 | 2019-03-19 | 青岛科技大学 | A kind of concentrated natural latex flucculation process |
| WO2020087952A1 (en) * | 2018-10-29 | 2020-05-07 | 青岛科技大学 | Method for flocculating fresh latex |
| CN111909290A (en) * | 2020-08-27 | 2020-11-10 | 吴胜文 | Natural rubber latex coagulating additive |
| CN115028758A (en) * | 2022-06-23 | 2022-09-09 | 云南省热带作物科学研究所 | Latex treatment method for improving drying efficiency of low-protein natural rubber |
Also Published As
| Publication number | Publication date |
|---|---|
| CN1077895C (en) | 2002-01-16 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN1077895C (en) | Biological solidification technology of natural latex | |
| CN107686564B (en) | Preparation method of hydrophobic white carbon black | |
| CN104072832B (en) | A kind of oil-filled oxygenation functionalized graphene emulsion beta-rubber and preparation method thereof altogether | |
| EP4108689A1 (en) | Processing method for creaming natural latex | |
| CN111234336B (en) | Epoxidized natural rubber composite material and preparation method thereof | |
| CN105218882A (en) | Improve rubber combination and the application of vulcanized rubber stability | |
| CN104693818A (en) | Composite-SBS (Styrene Butadiene Styrene block polymer)-particle modified asphalt with storage stability and aging resistance and preparation method thereof | |
| CN101864004B (en) | Preparation method of natural rubber with constant viscosity | |
| CN101240041A (en) | Method for increasing drying efficiency of natural rubber | |
| CN110423430A (en) | Complete biodegradable ABS material and preparation method thereof, and application | |
| CN1906231B (en) | Method for producing composition containing polymer from liquid containing polymer component and drying apparatus for same | |
| CN111423633A (en) | Nano hybrid filler reinforced rubber material and preparation process thereof | |
| CN113861533A (en) | White carbon black filled tire tread rubber composition, mixing method and tire | |
| CN111138581B (en) | Isoprene latex and preparation method thereof | |
| CN110819060B (en) | Method for improving viscosity of waste ABS plastic | |
| CN110204803B (en) | Light-weight rubber product and preparation method thereof | |
| WO2016014037A1 (en) | A process to prepare high-quality natural rubber-silica masterbatch by liquid phase mixing | |
| CN109880386B (en) | High-performance composite modified asphalt and preparation method thereof | |
| CN108570121A (en) | A kind of preparation method of the polymer support of pre-dispersed rubber chemicals | |
| CN111269470A (en) | Organic silicon emulsion modified wet-process wear-resistant rubber and preparation method thereof | |
| CN110734593A (en) | Method for preparing emulsion polymerized styrene butadiene rubber from modified graphene | |
| US20030073775A1 (en) | Electropolymerization modified carbon black and articles including tires having at least one component containing such modified carbon black | |
| CN115286822B (en) | Polar natural rubber masterbatch and preparation method thereof | |
| CN115651330B (en) | Antibacterial PVC material and preparation method thereof | |
| CN110734589A (en) | Method for preparing emulsion polymerized styrene butadiene rubber from modified graphene |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C06 | Publication | ||
| PB01 | Publication | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C19 | Lapse of patent right due to non-payment of the annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |