Abstract:The principles of Process Intensification and Miniaturization technology, originally developed for chemicals processing, biotechnology and tissue engineering were applied to achieve plant growth and crop yield enhancement, which can be described as AgroProcess Intensification (A-PI). The basic principle of A-PI is the enhancement of multiple interactions between plant roots, water, nutrients, bacteria using micro-(bio)reactors as synthetic rhizosphere in soil (SRS) which is a highly porous nano-structured hydr… Show more
“…The results for all treatments for the first harvest suggest that during the first harvest, the effect of SRS media and A. brasilense are not significant due to lack of any water and nutrient stress. The effect of SRS media starts showing at the second harvest for treatment 2 (grass+PHP), which suggests that the PHP is acting as a slow release fertiliser capturing any runaway nutrients, similar to observations made previously [1][2][3][4]. However, there is no corresponding enhancement in treatment 4 (grass+PHP+ A. brasilense ).…”
“…The results for all treatments for the first harvest suggest that during the first harvest, the effect of SRS media and A. brasilense are not significant due to lack of any water and nutrient stress. The effect of SRS media starts showing at the second harvest for treatment 2 (grass+PHP), which suggests that the PHP is acting as a slow release fertiliser capturing any runaway nutrients, similar to observations made previously [1][2][3][4]. However, there is no corresponding enhancement in treatment 4 (grass+PHP+ A. brasilense ).…”
“…Due to these attributes, PHPs and their metallic, ceramic or composite forms have been used in the emerging technology of Process Intensification (PI), which facilitates the establishment of green processes. In addition to use of PHPs in analytical sciences, the important specific applications of PHPs in PI include: Agro‐PI, Bio‐PI, Chemical‐PI, including Separation processes, Energy and Environmental‐PI, and medicine and tissue engineering . A recent review of some of these applications is available…”
Section: Introductionmentioning
confidence: 99%
“…In most of the large scale applications of PHPs, such as agriculture and separation and energy‐environmental processes, the bulk and surface functionality of PHP requires ion‐exchange capacity. The required anionic or cationic characteristics are dictated by the nature of the application.…”
Section: Introductionmentioning
confidence: 99%
“…The most important difference between the commercial and PHP‐based ion‐exchangers is the accessibility of the ion‐exchange sites in PHP which accelerates the exchange kinetics and allows the utilization of full exchange capacity.…”
Section: Introductionmentioning
confidence: 99%
“…Cation exchange PHPs have been used at large scale in agricultural and separation processes which resulted in large levels of intensification compared with the well established techniques. It is likely that in agricultural and separation processes as well as in biological applications, there is a real need for PHPs with anionic functionality.…”
The
theoretical bases of a novel intensified catalytic multi-reaction-zone
reactor (M-RZR) system are described. The M-RZR with two reaction
zones (RZ-1 and RZ-2) was used for ammonia synthesis. In the catalytic
nonthermal plasma reaction zone (RZ-1), ammonia was synthesized and
it was immediately sequestrated by a highly porous polymeric solid
acid absorbent in the ammonia neutralization reaction zone (RZ-2).
The solid acid was a sulfonated cross-linked porous polystyrene foam
known as polyHIPE polymer (s-PHP, HIPE = high internal phase emulsion).
The s-PHP and its neutralized version (sn-PHP) were previously developed
as an advanced symbiotic fertilizer (or synthetic root system) for
agro-process intensification for the enhancement (50–300%)
of crop yield and nitrogen fixation especially under water and nutrient
stress. In this first ever “proof-of-concept” study
of the M-RZR system, without any attempt for optimization, it was
shown that the ammonia conversion per pass reached ca. 40% and ammonia
concentration was ca. 20 vol %. The energy cost of ammonia was 0.76
MJ/g NH3 which was 2 times smaller than optimized systems
in which the ammonia concentration in the product stream was ca. 1.5
vol %. Direct conversion of hydrogen enhanced clean syngas (a
1CO + a
2CO2 + a
3H2 + a
4N2 + a
5CH4) to ammonia and its reversible sequestration by CO2 to form solid ammonium carbamate/carbonate was demonstrated. This
method is not only useful for direct conversion of syngas to ammonium
carbonate/urea fertilizers but also for obtaining anhydrous ammonia
for fuel applications. The reactive in situ air separation was also
demonstrated for the generation of nitrogen for ammonia synthesis
and oxygen for the gasification of biomass as a sustainable source
of hydrogen.
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