CN103881148A - Preparation method for radiated corn starch-based biodegradation particles - Google Patents
Preparation method for radiated corn starch-based biodegradation particles Download PDFInfo
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- CN103881148A CN103881148A CN201410060281.XA CN201410060281A CN103881148A CN 103881148 A CN103881148 A CN 103881148A CN 201410060281 A CN201410060281 A CN 201410060281A CN 103881148 A CN103881148 A CN 103881148A
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Abstract
The invention discloses a preparation method for radiated corn starch-based biodegradation particles. The preparation method comprises the steps: radiating corn starch by utilizing rays to obtain the radiated corn starch; evenly mixing the following ingredients in parts by weight: 100 parts of radiated corn starch, 10-30 parts of plasticizer, 5-15 parts of enhancer, 0.5-2 parts of cross-linking agent and 0.01-1 part of anti-block agent, to obtain a mixture; and granulating the mixture, to obtain the biodegradation particles. The preparation method for the biodegradation particles is simple, low in cost, and the reagent used is safe and non-toxic, and the plasticization effect is good.
Description
Technical field
The present invention relates to bio-degradable plastics, particularly a kind of preparation method of bio-degradable particle of irradiation corn starch base.
Background technology
That plastics have is lightweight, good mechanical property, water-fast, resistance to chemical attack, appearance looks elegant, manufacture and the advantage such as easy for installation and cheap, is widely used that industry, agricultural, medication chemistry, national defence and people produce and the every field of daily life.2012, more than China plastics accumulative total ultimate production 5,830 ten thousand T, occupy second place of the world.
But the non-biodegradable of a large amount of waste plastic goods, has brought huge puzzlement to the mankind's living environment.One) the at present processing of plastic refuse mainly adopts recovery, the mode such as burns, buries.For recycling mode, only there is 25% plastic refuse to be recovered with current scientific and technological level.For plastic refuse, the expense of recycling is very high, and the performance of recovery product is lower, and use value is not high.For burning disposal, can produce a large amount of obnoxious flavoures, environment is caused to great pollution, forbid at present this processing mode.For landfill disposal, both land occupations, can not produce substantive help to the degraded of plastics again.The annual plastic garbage that produces approximately 5,000,000 tons of China, except 30% left and right is by the spontaneous recycling of individual proprietor, all the other major parts are carried out sanitary landfill or are arbitrarily stacked, and cause a large amount of wastings of resources and environmental pollution.Two) in plastics, contain softening agent o-phthalaldehyde(OPA) ester compound.This compound has low water solubility, fat-solubility and biological accumulation.The residual plastics of abandoning, through leaching and can discharge slowly this compounds for a long time, cause murder by poisoning to water source, soil.Meanwhile, the consumption of petroleum-based energy has also been accelerated in a large amount of uses of plastics.As everyone knows, oil is a kind of Nonrenewable resources, and a large amount of consumption will cause the exhaustion of petroleum-based energy.It is reported approximately 80,000,000,000 tons of Global Oil reserves, and the annual consumption of petroleum amount in the whole world exceedes 3,000,000,000 tons, so goes down, after many decades, high molecule plastic industry will face the predicament of scarcity of raw material.
The advantages such as starch has recyclable regenerative, wide material sources, cheap, degradation property is good, become a kind of desirable plastic-substitute.First-generation starch plastic is starch-filled plastic.In such plastics, starch content is between 10%～30%, and after starch degradation, plastics disintegration fragmentates and remains in physical environment.Such plastics can be alleviated the white pollution that high molecule plastic causes, but can not fundamentally solve white pollution problems; S-generation starch plastic is starch blending plastic.In such plastics, starch content brings up to 30%～70%, contains the polyolefine of difficult degradation in mixture, also has ethylene/vinyl alcohol, ethylene/acrylic acid and the ethylene/vinyl acetate copolymer etc. that can comparatively fast degrade.This series products combination very good aspect mechanical property, processing characteristics and degradation property.But because the consistency of starch and resin is poor, cause starch to be difficult to mix in material sample.Increase-volume problem between starch and resin is the problem that s-generation starch plastic need to solve.But in the reaction such as sex change, modification meeting generation ammonification, etherificate or the esterification of polyvinyl alcohol of starch, the macromolecular chain that introducing cannot be degraded, has increased other potential safety hazard.Third generation starch plastic is complete starch degradable plastics.In such plastics, the content of starch, more than 90%, is sheared plasticizing, is directly extruded and obtain by dry method.But the preparation technology of this full starch plastic is incompatible with conventional at present plastics-production equipment.
Dry method is sheared plasticizing, extruding and pelletizing process is the conventional preparation technology of current plastic master batch.But, when material of main part is prepared plastic master batch, there is the problem of granulation difficulty take starch.1, the poor mechanical property of starch.After plasticizing, the starch mechanical property of molten state is very poor, is difficult to pull into bar when granulation.2, the water absorbability of starch is strong.In granulation tie rod process, necessary use is air-cooled, can not use water-cooled.Meanwhile, starch can constantly absorb the moisture content of air in air-cooled tie rod process, easily causes the edge of a knife of dicing machine to stop up.3, the viscosity of molten state starch is large, is easy to be attached on the die head of tablets press, blocks filter screen, damages inflation film manufacturing machine.4, the starch after granulation still has very strong water absorbability, need to be kept in drying basin, increases the difficulty of subsequent disposal.In order addressing the above problem, to adopt starch is carried out to modification at present, increase hydrophobic grouping on starch surface, reduce the water absorbability of starch.
The modification of starch has following several method: 1) utilize the poly-hydroxy of starch granules, at its surperficial coupling one deck hydrophobic layer.Silane coupling agent and aluminate coupling agent are two kinds of the most frequently used coupling agents.Silane coupling agent has neurotoxicity and corrodibility more, and aluminate coupling agent is nontoxic, but has increased the viscosity of powder, has increased later stage preparation technology's difficulty.2) nano silicon starch conversion refinement starch.Nano silicon is more expensive.Refine to 300 object starch, 1, increased cost; 2, need to prevent the reunion of refinement starch; 3, refinement starch more easily absorbs water.
Summary of the invention
For deficiency or the defect of above-mentioned prior art existence, the invention provides a kind of preparation method of bio-degradable particle of irradiation corn starch base.
A preparation method for the bio-degradable particle of irradiation corn starch base, is characterized in that, comprising:
Utilize ray to carry out irradiation to W-Gum, obtain irradiation W-Gum;
In parts by weight, 100 parts of irradiation W-Gums, 10-30 part fluidizer, 5-15 part toughener, 0.5-2 part linking agent and 0.01-1 part opening agent are mixed, obtain compound;
By compound granulation, obtain described bio-degradable particle.
Optionally, described irradiation W-Gum is warp
60w-Gum after Co-gamma-ray irradiation.
Optionally, described fluidizer comprises: glycerine, trolamine or urea.
Optionally, described toughener comprises: polyvinyl alcohol or polycaprolactone.
Optionally, described linking agent comprises: glutaraldehyde, paraformaldehyde or oxalic dialdehyde.
Optionally, described opening agent comprises: stearic acid or whiteruss.
Optionally, described in
60the irradiation dose of Co-gamma-ray irradiation is 10-80kGy.
The present invention adopts different irradiation doses
60co-gamma-rays, irradiated starch, obtains a kind of dry, particle diameter reduces, degree of crystallinity declines modified starch,
60effectively Modified Starch of Co-gamma-ray irradiation method, do not need to use coupling agent, do not need the modification of nano silicon, do not need the hydrophobic treatment of starch, preparation method is simple, the reagent safety using is nontoxic, irradiation has reduced the degree of crystallinity of starch, reduced the particle diameter of starch, plasticizing effect is good.
Accompanying drawing explanation
Fig. 1 is bio-degradable particle preparation method schema of the present invention;
Fig. 2 is the changes in weight figure of W-Gum under different irradiation doses;
Fig. 3 is W-Gum change of size figure after different irradiation doses irradiate;
Fig. 4 is W-Gum degree of crystallinity variation diagram after different irradiation doses irradiate;
Fig. 5 is bio-degradable particle natural degradation curve.
Embodiment
Below in conjunction with accompanying drawing, further set forth the present invention.Should be understood that these embodiment are only not used in and limit the scope of the invention for the present invention is described.In addition should be understood that those skilled in the art can make various changes or modifications the present invention after having read the content of the present invention's instruction, these equivalent form of values fall within the application's appended claims limited range equally.
The present invention adopts different irradiation doses
60co-gamma-rays, irradiated starch, obtain a kind of dry, particle diameter reduces, degree of crystallinity declines modified starch, the bio-degradable particle of irradiation corn starch base, it is characterized in that, comprise, in parts by weight, 100 parts of irradiation W-Gums, 10-30 part fluidizer, 5-15 part toughener, 0.5-2 part linking agent and 0.01-1 part opening agents.
Concrete preparation method refers to Fig. 1:
S101: utilize ray to carry out irradiation to W-Gum, obtain irradiation W-Gum.
The present invention adopts different irradiation doses
60co-gamma-rays, irradiated starch, obtains irradiation W-Gum, and the present invention proposes
60effectively Modified Starch of Co-gamma-ray irradiation method, obtains the starch base powder that is easy to plasticizing, is easy to granulation.Experiment show through
60after Co-gamma-ray irradiation, the moisture of W-Gum reduces, powder footpath reduces, degree of crystallinity declines.
A,
60after Co-gamma-ray irradiation, the moisture of W-Gum reduces.
Get the commercially available W-Gum of 100g, in commercially available W-Gum, containing having an appointment the water of 20% left and right, the commercially available W-Gum of 100g is adopted to different irradiation doses
60co-gamma-rays irradiates, and as shown in Figure 2, experimental result shows the relation of its W-Gum weight and irradiation dose:
60after Co-gamma-ray irradiation, the weight of W-Gum has reduced 21%, corresponds to the volatilization of water,
60after Co-gamma-ray irradiation, the moisture of W-Gum reduces.Visible, the starch after irradiation is the starch of complete drying, and irradiation process also can be regarded the process of primary drying as.
B,
60after Co-gamma-ray irradiation, the powder footpath of W-Gum reduces.
To the W-Gum of equivalent, adopt different irradiation doses
60co-gamma-rays irradiates, result as shown in Figure 3, the grain-size graph that in Fig. 3, A figure is original starch, B figure is the grain-size graph of the postradiation starch of 20kGy irradiation dose, C figure is the grain-size graph of the postradiation starch of 40kGy irradiation dose, and D figure is the grain-size graph of the postradiation starch of 50kGy irradiation dose.Experimental result shows:
60after Co-gamma-ray irradiation, W-Gum particle diameter reduces; The particle diameter ratio of the starch of the irradiation dose of 40kGy and 50kGy is more close, and the irradiation dose of 40kGy effectively refinement corn forms sediment, and considers the Cost Problems of irradiation, and all preferred irradiation doses are 40kGy.Visible, irradiation process is the thinning process of a starch.
C,
60after Co-gamma-ray irradiation, the degree of crystallinity of W-Gum declines.
To the W-Gum of equivalent, adopt different irradiation doses
60co-gamma-rays irradiates, and as shown in Figure 4, experimental result shows the result that its intensity irradiation dose changes:
60after Co-gamma-ray irradiation, the degree of crystallinity of W-Gum declines.Visible irradiation process is one and reduces starch crystals degree, increases plastic process.
S102: in parts by weight, 100 parts of irradiation W-Gums, 10-30 part fluidizer, 5-15 part toughener, 0.5-2 part linking agent and 0.01-1 part opening agent are mixed, obtain compound.
Described fluidizer can comprise: glycerine, trolamine or urea etc.; Described toughener can comprise: polyvinyl alcohol or polycaprolactone etc.; Described linking agent can comprise: glutaraldehyde, paraformaldehyde or oxalic dialdehyde etc.; Described opening agent can comprise: stearic acid or whiteruss etc.
For example, can adopt following component, in parts by weight, its component and content are as follows: take irradiation W-Gum 100 as radix: glycerine (fluidizer) 10-30; Glutaraldehyde 0.5-2, stearic acid 1-3, polyvinyl alcohol 5-15, whiteruss 0.01-0.05.
When mixing, can be by the denaturation cornstarch after irradiation, glycerine, stearic acid, glutaraldehyde and whiteruss, be placed in high speed/low speed mixer and mix.
S103: by compound granulation, obtain described bio-degradable particle.
Particularly, the compound in step S102 can be placed in to twin screw extruder granulation, obtain bio-degradable particle.
The bio-degradable particle being prepared from by above-mentioned steps has good degradation property, get its natural degradation curve of bio-degradable particle of the present invention of 1.5g as shown in Figure 5, result shows that the bio-degradable particle degradation rate of 90 days is 77%, and it has good degradation property.
Utilize bio-degradable particle of the present invention can make different plastic prods, for example, bio-degradable particle of the present invention is placed in to the inflation film manufacturing machine of different bores, can prepare the starch-based film of different in width; Its Preparation equipment and method are prior art, no longer describe in detail.
Above, it is only preferred embodiment of the present invention, not the present invention is done to any pro forma restriction, although the present invention discloses as above with preferred embodiments, but not in order to limit the present invention, any those skilled in the art, do not departing within the scope of technical solution of the present invention, when can utilizing the method for above-mentioned announcement and technology contents to make a little change or being modified to the equivalent embodiment of equivalent variations, in every case be the content that does not depart from technical solution of the present invention, foundation technical spirit of the present invention is to any simple modification made for any of the above embodiments, equivalent variations and modification, still belong in the scope of technical solution of the present invention.
Claims (7)
1. a preparation method for the bio-degradable particle of irradiation corn starch base, is characterized in that, comprising:
Utilize ray to carry out irradiation to W-Gum, obtain irradiation W-Gum;
In parts by weight, 100 parts of irradiation W-Gums, 10-30 part fluidizer, 5-15 part toughener, 0.5-2 part linking agent and 0.01-1 part opening agent are mixed, obtain compound;
By compound granulation, obtain described bio-degradable particle.
2. preparation method according to claim 1, is characterized in that, described irradiation W-Gum is warp
60w-Gum after Co-gamma-ray irradiation.
3. preparation method according to claim 1, is characterized in that, described fluidizer comprises: glycerine, trolamine or urea.
4. preparation method according to claim 1, is characterized in that, described toughener comprises: polyvinyl alcohol or polycaprolactone.
5. preparation method according to claim 1, is characterized in that, described linking agent comprises: glutaraldehyde, paraformaldehyde or oxalic dialdehyde.
6. preparation method according to claim 1, is characterized in that, described opening agent comprises: stearic acid or whiteruss.
7. preparation method according to claim 2, is characterized in that, preferred, described in
60the irradiation dose of Co-gamma-ray irradiation is 10-80kGy.
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| CN107573421A (en) * | 2017-09-11 | 2018-01-12 | 江苏省农业科学院 | A kind of preparation method of high-performance converted starch |
| CN109126730A (en) * | 2018-09-10 | 2019-01-04 | 江苏省农业科学院 | A kind of biomass porous adsorbent material and the preparation method and application thereof |
| CN115850529A (en) * | 2022-11-28 | 2023-03-28 | 北京爱特康医疗科技有限公司 | Sodium carboxymethyl starch, preparation method thereof and absorbable hemostatic powder |
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| CN109126730A (en) * | 2018-09-10 | 2019-01-04 | 江苏省农业科学院 | A kind of biomass porous adsorbent material and the preparation method and application thereof |
| CN109126730B (en) * | 2018-09-10 | 2021-05-18 | 江苏省农业科学院 | Biomass porous adsorption material and preparation method and application thereof |
| CN115850529A (en) * | 2022-11-28 | 2023-03-28 | 北京爱特康医疗科技有限公司 | Sodium carboxymethyl starch, preparation method thereof and absorbable hemostatic powder |
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Application publication date: 20140625 |