Uso actual y potencial de la nanotecnología en el sector agroalimentario
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Transcript of Uso actual y potencial de la nanotecnología en el sector agroalimentario
El uso actual y potencial de la nanotecnologia en el sector
agroalimentario
Caue RibeiroPesquisador
Coordenador da Rede de Pesquisa em Nanotecnologia Aplicada ao Agronegócio,
EmbrapaTercer Seminario Regional Agricultura y Cambio Climatico:Nuevas tecnologías en la mitigación y adaptación27 y 28 de septiembre 2012
Nanociência, nanotecnologia…
Credits: Prof. Dr. Henrique Toma (USP, Brazil)
Superfícies e Catálise HeterogêneaProdutividade de reações químicas: uma
área nanotecnológica há um século! “catalytic materials [heterogeneous catalysis] have been
nanostructured for at least a century, and this industry – US$ 100 bilion – is (…) estimate of a future trillion dolar nanotechnology economy (Prof. Dr. David J. Eaglesham, in Letter from the President, MRS Bulletin 2005, 30, 260 – 261)
Prêmio Nobel de Química 2007: Prof. Dr. Gerhard Ertl "(...) Chemical reactions on catalytic surfaces play a vital role in many industrial operations, such as the production of artificial fertilizers [processo Haber-Bosch] (...)" (Nobel Prize Press Release)
Processo Haber (1910)
N2 + 3 H2 → 2 NH3
- Produção de fertilizantes e explosivos....
Processo catalisado por ferro metálico
N2
H2
NH3
Exemplo de processo químico catalisado por superfícies e esquema do processo Haber.Fonte http://www.spaceflight.esa.int/impress/text/education/Catalysis/index.html
Superfícies e Catálise Heterogênea
Coordenação: Embrapa Instrumentação158 pesquisadores / 53 Instituições
Linhas de pesquisa:•Sensores e Biossensores•Filmes finos comestíveis e embalagens ativas•Bionanocompósitos•Novos usos de nanomateriais sintéticos na agricultura•Avaliação de Impactos em Nanotecnologia•Transferência para a Sociedade em Nanotecnologia
http://www.redeagronano.cnptia.embrapa.br/
Como a Nanotecnologia chega ao Consumidor Final?
• Três níveis de impacto no consumidor final:– Direto: alimentos com nanotecnologia
• Nanoaditivos e filmes finos comestíveis
– Indireto, com possível contato ou migração: alimentos produzidos, processados ou conservados com auxílio de nanotecnologias
• Insumos agrícolas, descontaminação de água, embalagens ativas
– Indireto, com mínimo contato ou possibilidade de migração : alimentos monitorados e avaliados com auxílio de nanotecnologia
• Sensores de qualidade
Nano’s em alimentos
Credits: Embrapa Instrumentação Agropecuária(Dr. Odílio B. G. Assis)
Revestimentos protetores comestíveis
Quitosana
Zeínas
CMC
Nano’s em alimentos
Nanocápsulas
cápsula (50 – 250 nm)
polímero
Espaçovazio
Nanocápsulas para liberação controlada / lenta e nanoemulsões
Emulsão bifásica convencional (maionese)(em http://tecalim.vilabol.uol.com.br)
eXPRESS Polymer Letters Vol.4, No.8 (2010) 509–515
Nanocápsulas de quitosana
Embalagens Nanocompósitas
Oxygen permeability of PLA, PHB and PET and of their nanocomposites
Nanocargas: Nanocelulose
Source: Teixeira et al, Cellulose, 2010
Embalagens inteligentes
Migração para alimentos?
LDPE: n = 2.6 × 10-7 kg of nanosilver (0.26 mg) after 1 year at 25oCPET: n = 2.2 × 10-10 kg (0.22 μg) of nanosilver after 1 year at 25oC
Rastreabilidade: Biosensores
14
http://www.cnpat.embrapa.br/cnpat/cd/jss/acervo/Dc_117.pdf
Rastreabilidade:Sensores não-seletivos
pro
pri
edad
e
variável
Sensor 1
Sensor 2Sensor 3
Resultado
Sensores não-seletivos
Identificação de sucos de fruta usando a Língua Eletrônica
• Plantio direto na palha• Recuperação de áreas degradadas• Integração Lavoura – pecuária – floresta• Plantio de florestas comerciais• Fixação biológica de nitrogênio• Tratamento de resíduos animais
http://www.agricultura.gov.br/abc/
Estratégias para mitigação deemissões de N2O
Como a nanotecnologia pode colaborar com essas estratégias?
Conceitos
Liberação comumLiberação lenta
Liberação controlada
tempo
Qu
anti
dad
e A
cum
ula
da
Faixa deinteresse
Estruturas Reticuladas (Hidrogéis)
seco
hidratado
http://www.estadao.com.br/noticias/suplementos,aplicacoes-em-escala-atomica-na-agricultura,640974,0.htm
Values of KF and n were calculated from the inter-cept and slope of the plot of ln qe q versus ln Ce q .The fitted lines of the data modeled using the
Freundlich and Langmuir isotherms for the adsorp-tion of fertilizers from hydrogels composed by 6.0%AAm and 1.0% MC are shown in Figure 5. The ini-tial concentration of the fertilizers varied between 50and 2000 mg L 1 . Based on R2 values, the Freundlichmodel fits the both fertil izers better than the Lang-muir model. It was possible to determine the KF andn Freundlich parameters. The KF parameters calcu-
lated were 1.271 and 1.176 L g 1 for (NH 4 )2SO4 andKH 2PO4 fertilizers, respectively. In addition, the val-ues of n parameter for (NH 4 )2SO4 and KH 2PO4 fertil -izers were 1.727 and 1.641.
CONCLUSIONS
Because it is a simple technique, highly reproduci-ble, low cost, and allows a direct detection withoutprevious treatment of the analyte, the conductivitytechnique was extremely efficient in this study. It
Figure 4 Profiles of ammonium sulfate (NH 4 )2SO4 release from hydrogels constituted by PAAm and MC as a function oftime in different conditions: (a) [AAm] ¼ 9.0 in wt % with 0; 0.5; and 1.0 MC in wt %, and (b) [MC] ¼ 1.0 in wt % with6.0; 9.0; and 12.0 AAm in wt %. Error bars represent standard deviations for the three measurements (mean 6 SD, n ¼ 3).
TABLE IVCumulative Release and Amount of (NH 4 )2SO 4 Ferti l izer
Released for Dif ferent Hydrogels
(AAm-MC)hydrogel
Cumulativerelease (%)
Amount of fertilizerreleased (mg (NH 4 )2SO4 )/ g
hydrogel)
(6.0–1.0) 85.3 6 2.2 49.5 6 4.8(9.0–0) 106.8 6 2.7 14.1 6 0.2(9.0–0.5) 97.0 6 3.4 19.6 6 1.5(9.0–1.0) 96.7 6 2.9 35.5 6 6.3(12.0–1.0) 99.4 6 0.8 15.3 6 0.8
TABLE II ICumulative Release and Amount of KH 2PO 4 Ferti l izer
Released for Di f ferent Hydrogels
(AAm-MC)hydrogel
Cumulativerelease (%)
Amount of fertilizerreleased (mg KH 2PO4 )/ g
hydrogel)
(6.0–1.0) 44.3 6 1.2 54.9 6 7.9(9.0–0) 97.5 6 1.4 30.8 6 1.0(9.0–0.5) 80.6 6 4.1 35.4 6 2.5(9.0–1.0) 50.4 6 0.8 41.0 6 1.0(12.0–1.0) 85.5 6 2.7 22.4 6 0.7
2296 BORTOLIN ET AL.
Journal of Applied Polymer ScienceDOI 10.1002/ app
Values of KF and n were calculated from the inter-cept and slope of the plot of ln qe q versus ln Ce q .The fitted lines of the data modeled using the
Freundlich and Langmuir isotherms for the adsorp-tion of fertilizers from hydrogels composed by 6.0%AAm and 1.0% MC are shown in Figure 5. The ini-tial concentration of the fertilizers varied between 50and 2000 mg L 1 . Based on R2 values, the Freundlichmodel fits the both fertil izers better than the Lang-muir model. It was possible to determine the KF andn Freundlich parameters. The KF parameters calcu-
lated were 1.271 and 1.176 L g 1 for (NH 4 )2SO4 andKH 2PO4 fertilizers, respectively. In addition, the val-ues of n parameter for (NH 4 )2SO4 and KH 2PO4 fertil -izers were 1.727 and 1.641.
CONCLUSIONS
Because it is a simple technique, highly reproduci-ble, low cost, and allows a direct detection withoutprevious treatment of the analyte, the conductivitytechnique was extremely efficient in this study. It
Figure 4 Profiles of ammonium sulfate (NH 4 )2SO4 release from hydrogels constituted by PAAm and MC as a function oftime in different conditions: (a) [AAm] ¼ 9.0 in wt % with 0; 0.5; and 1.0 MC in wt %, and (b) [MC] ¼ 1.0 in wt % with6.0; 9.0; and 12.0 AAm in wt %. Error bars represent standard deviations for the three measurements (mean 6 SD, n ¼ 3).
TABLE IVCumulative Release and Amount of (NH 4 )2SO 4 Ferti l izer
Released for Dif ferent Hydrogels
(AAm-MC)hydrogel
Cumulativerelease (%)
Amount of fertilizerreleased (mg (NH 4 )2SO4 )/ g
hydrogel)
(6.0–1.0) 85.3 6 2.2 49.5 6 4.8(9.0–0) 106.8 6 2.7 14.1 6 0.2(9.0–0.5) 97.0 6 3.4 19.6 6 1.5(9.0–1.0) 96.7 6 2.9 35.5 6 6.3(12.0–1.0) 99.4 6 0.8 15.3 6 0.8
TABLE II ICumulative Release and Amount of KH 2PO 4 Ferti l izer
Released for Dif ferent Hydrogels
(AAm-MC)hydrogel
Cumulativerelease (%)
Amount of fertilizerreleased (mg KH 2PO4 )/ g
hydrogel)
(6.0–1.0) 44.3 6 1.2 54.9 6 7.9(9.0–0) 97.5 6 1.4 30.8 6 1.0(9.0–0.5) 80.6 6 4.1 35.4 6 2.5(9.0–1.0) 50.4 6 0.8 41.0 6 1.0(12.0–1.0) 85.5 6 2.7 22.4 6 0.7
2296 BORTOLIN ET AL.
Journal of Applied Polymer ScienceDOI 10.1002/ app
Fonte: Bernardi et al, 2010
0
2
4
6
8
10
0 2 4 6 8 10 12 14 16 18 20 22
Period (days)
N v
olat
ilize
d (m
g pe
r po
t)
Urea
Urea_inc
Urea_NBT
Urea_Zeo
NH4NO3
NH4SO4
Control
Ureia (comum) por cobertura
Ureia + zeolita por cobertura
Ureia incorporada no solo
UréiaZeólita
Uréia + Zeólita 5%
Zeólitas para redução da Volatilização de Nitrogênio
Nanocompósitos fertilizantes
urea
Test.
Form. 1
composites is noteworthy, with negligible di erences observedbetween them. This suggests that the mechanical behavior isdominated by the intercalated fraction of the material, whichdeforms continuously when solicited. This is an interestingbehavior for thepractical useof thosematerials, because fragilegranules are more prone to produce dust during application,which may be avoided or minimized by the nanocompositematerials.Figure 8 shows the urea release for the three produced
nanocompositescompared to urearelease. Theureadissolutionoccurred in <1h, dueto thesolution saturation around theureagranule. We performed a reference test, by mixing (withoutextrusion) a composition of 1:1 montmorillonite/ urea, that is,where theclay wasnot properly exfoliated (not shown here). Inthis case, the liberation test in the same conditions of theextrudegranulesdid not shown any in uenceof theclay in urearetention, with almost thesamepro leof pureureadissolution,asshown in Figure8. Thispro leprobably isrelated to the factthat any interaction of montmorillonite and urea would occurin longer times, because the compound would need to adsorbin montmorillonite platelets after its dissolution. Then, in thisvery aggressive test condition (immersion in water), anydi erence could be observed. In fact, this also shows theimportance of exfoliation to the controlled release.
However, by comparing the nanocomposites, one can notethat all of the formulations retarded urea release for up to 120h. It wasvery important to notethat thisdissolution experimentwas very aggressive, because a complete immersion of theproduced materials in water is done. Even in this aggressivecondition, the release iscomparable to other controlled releasesystems with very di erent action principles, as observed byTomaszewska and Jarosiewicz1 4 (for some polymeric coatingsapplied in urea granules) or in PMMA hydrogels, as reportedby Bortolin et al.,2 2 denoting that those valuesobtained for thenanocompositesarepromising. In conventional application, thematerialswould beexposed to lowwater contents, and onecanexpect a better retention e ect by the nanocomposites.A particular aspect is the di erent kinetic behavior observed
for each system. Therewasnot aclear correlation between thetotal Mt in the nanocomposite and the total urea released. Infact, the 1:1 formulation caused higher urea retention, but onlysmall di erenceswere observed using the1:2 and 1:4mixtures.This may mean that the e ect of the Mt clay in minorquantities is less considerable, but, in any case, it is veryimportant to note that even those nanocomposites showedslower release when compared to pure urea.To separate possible solution equilibrium e ects, a second
experiment to measure urea release was performed, comparingpure urea and formulation 1:1 when protected by a dialysismembrane. In this case, one can consider that the osmoticpressure between the inner and outer parts of the membrane
Figure 6. Scheme of the proposed path for urea intercalation in theextrusion process.
Figure 7. Stress−strain curves for the pure urea and for the Mt/Ur composites.
Figure 8. Release rate of urea asa function of time for pure ureaandeach of the composites at pH 7 and room temperature.
Journal of Agricultural and Food Chemistry Article
dx.doi.org/10.1021/jf3001229 | J. Agric. Food Chem. 2012, 60, 5267−52725271
shown in Table 2. The ratios of Si, Al, C, N, and O content inatomic percent in the individual points marked accordingFigure 5 are summarized in Table 2. The regions labeled “1” inthe SEM images correspond to urea crystals redispersed,because theelementsdetected are predominantly N, C, and O,that is, urea constituents. On the other hand, the regionslabeled “2” correspond to urea-intercalated Mt, becausesigni cant amountsof Si and Al (clay constituents) and smallerN amounts were detected.
By the above results, one may propose a path of the ureaintercalation in the extrusion process, as shown in Figure 6. Atthe rst urea loadings, the solubilized material intercalates inclay platelets, properly forming the composite. However, thesubsequent additions do not interfere with the Mt separation,but will crystallize independently, forming some small ureacrystals, which can grow by addingmore urea into the process.A comparative analysis of the mechanical resistance of the
granuleswasperformed by diametral compression, because thisproperty is very important for the practical application as afertilizer material. As observed in Figure 7, the behavior of aurea granule is similar to that of a fragile material, with poorplasticity and fracturing at low pressure. On theother hand, allof the nanocomposites were very deformable, without ruptureeven until the maximum deformation supported by theequipment. It is noticeable that this behavior can not beassumed to besolely due to theMt structure, because thesameanalysis in the pure Mt extruded revealed a low mechanicalresistance. However, the similarity among the three nano-
Figure 4. Thermogravimetric curve (a) and derivate thermogravimetric curve (b) of Mt, pureurea, and thenanocompositesMt/ Ur 1:1, Mt/Ur 1:2,and Mt/Ur 1:4.
Figure 5. SEM images of (a) Mt and the nanocomposites (b) Mt/Ur1:1, (c) Mt/Ur 1:2, and (d) Mt/Ur 1:4. Magni cation of 500 (left)and 20000 (right).
Table 2. Ratios of C, N, O, Al, and Si in the Composites(Marked by Numbers in Figure 5) Measured by EDX inAtomic Percent
C N O Al Si
Mt/ Ur 1:1P1 5.2 21.8 14.0 3.9 5.1P2 1.8 35.1 16.5 33.9
Mt/ Ur 1:2P1 3.7 17.7 16.2 7.0 11.2P2 2.8 23.6a 12.8 28.5
Mt/ Ur 1:4P1 4.7 21.3 14.3 4.0 6.5P2 0.2 2.4 25.5 12.6 27.3
aThe value corresponds to the sum of O and N signals.
Table 3. Values of Mechanical Parameters
σa (MPa) Eb
urea 2.083 ± 0.4507 3.32 ± 1.45extruded Mt 12.32 ± 13.71 6.00 ± 1.90Mt/ Ur 1:1 >35.13 ± 3.627 0.99 ± 0.64Mt/ Ur 1:2 >31.24 ± 3.516 1.06 ± 0.51Mt/ Ur 1:4 >33.20 ± 3.495 2.01 ± 0.90
aσ = stress. bE = elasticity modulus.
Journal of Agricultural and Food Chemistry Article
dx.doi.org/10.1021/jf3001229 | J. Agric. Food Chem. 2012, 60, 5267−52725270
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