Metals and additives to HZSM-5 for CFP.
\r\n\tThe primary objective of this book is to provide the specialists involved in the clinical management and experimental research of acute and chronic leukemias updates on the theoretical aspects as well as state-of-the-art diagnostic and clinical management of acute and chronic leukemias.
\r\n\r\n\tThe book is intended to cover a broad spectrum of leukemia-related topics such as:
\r\n\t-novel and still evolving insights into the biology and diagnosis and how these result in new drug approvals and new therapeutic options with a focus on molecular and immunotherapeutic targeted therapeutics,
\r\n\t- the molecular and functional features of leukemic stem cells and their interaction with the microenvironment,
\r\n\t- preleukemic hematopoiesis and clonal diversity,
\r\n\t- new standard treatment algorithms,
\r\n\t- mechanisms of resistance and disease progression
\r\n\t- diagnosis and management of rare acute leukemia subtypes,
\r\n\t- Covid-19 aspects in specific leukemia categories,
\r\n\t- real-world data
\r\n\t- new drugs in development
Cotton (
The reniform nematode is a semi-endoparasite and derives its name from having a kidney-shaped body, usually of the adult female, and the males are, however, vermiform. The reniform life cycle is in four stages beginning from the egg. The first juvenile stage (J1) molts to become the second juvenile (J2) which also occurs within the egg. The J2 then hatches 1–2 weeks after eggs are laid especially when conditions are favorable [5]. Cuticles may sometimes overlay the other and are seen usually in the third- and fourth-stage juveniles, J3 and J4 [6]. Generally, after molting, there is a reduction in the body size of the reniform nematode [5]. The young adult reniform nematode females move towards the germinating host seedlings and to certain organic substances secreted by the roots [7]. Penetration by the nematode is in the elongation zone of the host plant root, proximal to the meristem. The epidermis and cortex are pierced by the vermiform young female intracellularly with the pericycle being the permanent feeding site [8, 9]. Half to two-thirds of the nematodes’ body usually remains outside the root, and the nematode swells with kidney-like shape morphology.
\nAmong the cellular changes observed after penetration of the cells by the reniform nematode include the formation of dense granular cytoplasm, hardening of cell walls through accumulation of polysaccharides, disintegration of cell walls, and enlargement of cells [10–12]. The adult female reniform nematode oviposits into a gelatinous matrix, produced by the vaginal glands, and the number of eggs within an egg mass varies, from 60 to 200 by a single adult female nematode [13]. The reniform nematode has the capability to undergo anhydrobiosis, a survival mechanism in the absence of water, making it thrive for at least 2 years in the absence of a host in dry soil [14]. The state of anhydrobiosis for the reniform nematode can last for more than 20 years in the absence of host plants [15].
\nRoot-knot nematode (
Studies have shown changes in host gene expression during infection of roots by nematodes especially within the syncytium [21–23]. During the formation of syncytium, a number of changes occur within plant cells, among these are changes in cell cycle mechanisms, hormone regulation events, and cell wall architecture [24, 25]. Establishment of nematode feeding cells is through specific processes which are controlled and directed by encoded products of nematode parasitism genes found within the esophageal glands. These products are then delivered into the feeding cell through the nematode stylet [26]. Processes and events occurring at the nematode feeding sites play roles related to various degrees of susceptibility of cotton plants to the reniform nematode. Among these events are early degradation of syncytia [10], formation of wall deposits, and absence of hypertrophy in pericycle cells. These are some known mechanisms proposed for cotton resistance to reniform nematode.
\nVarious Upland cotton varieties were planted in Unites States (US) in 2015 [27]. Among the varieties grown in United States, the largest and least acreages of cultivation were ‘Deltapine’ (31.2%) and \'Seed Source Genetics\' (0.02%), respectively. ‘Deltapine’ cultivar covered about 50.1% of the acreage planted to Upland cotton in the southeastern states (Alabama, Florida, Georgia, North Carolina, South Carolina, and Virginia). Bayer CropScience (\'FiberMax\' and \'Stoneville\') also covered significantly higher acreages (21.61 and 16.93%), respectively. An early study was conducted on susceptible (DP50-HR: \'Deltapine 50\' with higher reproduction) and resistant (DP50-LR: \'Deltapine 50\' with lower reproduction) genotypes, which were inoculated with 3000 reniform nematodes [28]. Roots collected 3, 6, 9, 12, and 15 days after inoculation (dai) revealed reduced reproduction in susceptible genotypes with degeneration of the syncytial cells and absence of hypertrophy within the pericycle cells.
\nReniform nematodes show significant variations in populations [29–34]. Cotton genotypes will, therefore, have varying reproductive and pathogenicity responses to reniform nematode variants if present in populations. The ‘LONREN ’genotypes (‘LONREN-1’ and \'LONREN-2\' both of which are resistant to the reniform nematode) were used in association with susceptible genotypes (\'FiberMax 966\' and \'Deltapine 555BR\') to six levels of inocula (0, 500, 1000, 5000, 10,000, or 50,000), consisting of eggs and vermiform life stages of reniform nematodes [35]. High inoculum levels (10,000 and 50,000) significantly reduced the root dry mass of \'LONREN\' genotypes; however, higher levels in the susceptible genotypes rather stimulated root mass. Thus, the \'LONREN\' genotypes may be involved in hypersensitive responses to nematode parasitism.
\nAnother study was conducted on five cotton genotypes with various resistance/tolerance levels to reniform nematode isolates obtained from cotton field in Louisiana [36]. High reproduction of isolates was observed from Evan (33,793 juveniles/250 g soil) and Avoyelles (27,800 juveniles/250 g soil) genotypes. Data revealed that the
Exploring of host resistance to nematode parasitism is the most effective and environmentally friendly method of nematode management. Resistant cultivars pose an incompatible interaction with nematodes. A hypersensitive reaction is produced in a response to the feeding or invading nematode leading to lignification of the cells in close proximity to the reniform nematode\'s head, or the cells either collapse or become necrotic [41, 42]. However, in a compatible interaction, there is a formation of active syncytia with cells becoming hypertrophic, dense cytoplasm, enlarged nuclei, in most instances a partial disintegration of cell walls [29]. Application of nematicides to the resistant genotypes of cotton, for example, \'LONREN\' have a positive impact on plant response and yield [43]. This hypersensitivity which is produced can be reduced in seedlings after nematicide applications. Four-resistant breeding lines from (\'LONREN-1\' × \'FM966\') cross, a susceptible line from the \'LONREN\' × \'FM966\' cross, \'LONREN-1\', \'BARBREN-713\', and the \'DP393\' (susceptible cultivar) were explored in a nematicide trial [43]. There was an increase in plant height and yield among plants to which nematicides were applied in greenhouse experiments. Furthermore, the number of reniform nematodes isolated was about 50% lower in resistant genotypes 45 days after planting (DAP). Differences were also observed among \'BARBREN-713\' and \'LONREN\'-derived lines in relation to reniform nematode egg number counts, with lower counts noted on \'BARBREN-713\'. There was also a reduction in stunting of genotypes that received aldicarb treatment.
\nWithin the
Towards the end of the 1980s, some germplasm lines (\'La. RN 4-4\', \'La. RN 909\', \'La. RN 910\', and \'La. RN 1032\') were developed in Louisiana State University in Baton Rouge with low-to-moderate levels of resistance to the reniform nematode [46]. These lines were from Upland cotton and were the first with some levels of resistance to the reniform nematode. Towards the latter part of 1997, the Unites States Department of Agriculture (USDA) Agricultural Research Service (ARS) scientists in Texas released four germplasm lines (\'N220-1-91\', \'N222-1-91\', \'N320-2-91\', and \'N419-1-91\') with slightly higher levels resistance to the reniform nematode compared to earlier released lines [47].
\nFurther screening of
Resistance has also been explored in wild accessions of
Researchers over the years have screened genotypes and believed to have resistance to the reniform nematode. They have proved that these genotypes are not 100% resistant to the reniform nematode [48–50]. This, therefore, has resulted in multi-institutional collaborations on the introgression of resistance into Upland cotton from close and distant relatives of
The introgression of the reniform nematode resistance trait of
Various screens were performed on
Transfer of reniform nematode resistance into Upland cotton has also been successfully achieved through crossing the resistant
Reniform nematode resistance introgression into
Trispecies hybrids with
Large germplasm lines (‘1866’ and ‘907’) of
Greenhouse assays also complement field screening of germplasm lines for nematode resistance in these lines [70]. In one of these assays, a single test plant was screened against six susceptible and resistant plants of
Texas AgriLife Research released two breeding lines \'TAM RKRNR-9\' (Reg. No. GP-941; PI 662039) and \'TAM RKRNR-12\' (Reg. No. CP-942; PI 662040) of Upland cotton in 2010 [58]. Both of these lines poses resistance to
SSR markers associated with reniform nematode quantitative trait loci (QTLs) involved in resistance are known [69]. This was achieved through genotyping of 300 F2 populations of \'GB713\' × \'AcalaNem-X\' crosses. QTLs were localized to chromosomes 21 and 18, respectively. The QTLs on chromosome 21 were on map positions 168 (LOD 28.0) and 182.7 (LOD 24.6), with the specific SSR markers BNL 1551_162 and GH 132_199 on position 154.2 and 177.3 and BNL 4011_155 and BNL 3279_106 on positions 180.6 and 184.5 associated with these loci, respectively. However, the only single QTL on chromosome 18 was on the map position 39.6 (LOD 4.0) with the specific SSR markers BNL 1721_178 and BNL 569_131 on positions 27.6 and 42.9, respectively. The authors, therefore, suggested the following designations
Sequencing of the nematode parasitome usually involves gene products that the nematode secretes during its cycle; critical study of genes will enhance the understanding of the nature of damage caused by nematodes to host plants [22]. Majority of these genes encode cell wall-modifying proteins such as galactosidases, xylanases, pectinases, and expansins [71]. Isolation of the parasitome from plant–parasitic nematodes, for example, β-1-4-endoglucanases (cellulases) was from the subventral glands of
Cellulase genes have been identified within reniform nematode [75–77],
Further BLAST analysis gave hits to
Two cellulase cDNAs (
Parasitism proteins released from the cell of nematodes induce changes in host cell physiology through specific signals in the nucleus within the host cells [95]. The regulation of the host’s cells by nematodes occurs during transcription and direct interaction between nematode-secreted protein and plant-protein target has been observed. In the root knot nematode (RKN), a 13-aa secretory peptide 16D10 has interactions with two SCARECROW-like transcription factors [96].
\nThe root knot and cyst nematodes both secrete chorismate mutase (CM) which affects the cellular shikimic acid pathway [71]. An overexpression of this protein in
Expansin-like proteins in the potato cyst nematode (
Plant host-pathogen interactions have fascinated plant pathologists over hundreds of years [104]. Contemporary studies on interactions began with seminal work on the gene-for-gene concept in plant host-pathogen interactions [105]. The gene-for-gene concept states that for every host R (resistance) gene, a corresponding Avr (avirulence) gene exists; thus, a successful host-defensive response requires a successful interaction [105]. The ranbpm-like family proteins and chorismate mutase (CM) interact with plant R genes, indicating nematode parasitism proteins act as avirulence genes [106, 107].
\nProteins made by animal parasitic nematodes have been found in some plant parasitic nematode genomes and they are conserved [108]. These proteins function to challenge the host’s immune system invoking specific responses [109]. The last two decades have advanced the global approach to studying gene expression. We now have advanced recombinant DNA technologies to study gene expression at the mRNA or total RNA (transcriptome) and protein (proteome) levels. Approaches employed in the study of plant response to nematode parasitism include differential display [110, 111], promoter-reporter gene fusions [112–114], RNA blotting, protein immunolocalization,
Recently, RNA-Seq analysis has been used in transcriptome sequencing of cotton (
Most gene expression is a regulated process with genes being active in some situations and inactive in others. Gene expression relates to the physical signals from the environment and developmental cues of the organism in question. The rate of protein synthesis was once thought to be proportional to the concentration of mRNA; therefore, gene expression regulation depends on the regulation of the steady-state concentration of mRNAs [123]. However, mRNA levels and protein concentrations only partially correlate, a finding based on thoroughly composed reference datasets accounting for factors where ribosome occupancy and density and open-reading frame (ORF)-specific translation elongation rates were considered [124]. Therefore, many regulatory mechanisms involved with gene expression operate at many levels. The mechanisms influence on alterations in DNA structure, modification of transcription, stability, or translation of mRNA, or alterations in protein activity through post-translational modification.
\nPlants display varying levels of resistance to most pathogens in their environment, often being able to recognize pathogens through specifically distinct methods of detection [125]. A series of mechanisms of defense have been developed by plants, some of which can be constitutive or inducible. Resistance in plants is defined as the inability of a pathogen to propagate and spread on a host plant, usually involving a response referred to as the hypersensitive response (HR) [125]. The lines between a plant and its pathogens are truly battlegrounds where there are deployments of defense. The most current description of the action that takes place applies also to cotton-reniform interactions. Inducible defense responses in this type of interaction follow the ‘zigzag’ model [126].
\nAccording to the model suppression of immune-associated macroscopic programmed cell death (PCD) triggered by MAPK cascades or by the ETI cognate elicitors R3a/Avr3a occurs in susceptible hosts [126, 127]. The study showed that nematodes injected into the plant, thereby suppress PAMP-triggered immunity (PTI) or effector-triggered immunity (ETI) that are associated with the activation of PCD. Therefore, resistance is the ability of the host plant to evade the suppression of PCD. In other words, the host is resistant when its cells are able to undergo PCD and susceptible when the cells cannot undergo PCD.
\nThere has been much progress and success made by researchers in introgression of reniform nematode resistance into Upland cotton from distant and close relatives. However, introgressed genotypes, solely developed to withstand reniform nematode parasitism, may have low crop yields in fields where mixed-populations of nematodes occur. The challenge now is to develop germplasm lines that may be able to withstand more than two nematode types in the same field. The rapid advances in genomics, transcriptomics, and proteomic analysis provide huge datasets, from which several resistance genes to the reniform nematode and other nematodes have been identified. These genes could be further explored and transferred into Upland cotton with various trials initiated in specific cotton-producing localities, for this overarching goal to be achieved.
\npara-Xylene (pX) is a key raw material in the production polyethylene terephthalate (PTA) before it is combined with mono ethylene glycol (MEG) to produce polyethylene terephthalate (PET), one of the largest and fastest globally growing polymers. Demand for pX is driven by the global polyester growth. Global polyester consumption is currently around 80 million tonnes/year. Using application of PET in fiber, this polyester is produced in 57.7 million metric tonne in 2019. Since 2008, the average growth in production has an annual increase of 5.9% (see Figure 1) [1]. Industry forecasts are that polyester will continue to grow at approximately 4% annually. While there is also increased focus on recycling polyester (a.k.a. rPET), most industry experts also see continued demand growth in virgin material due to limits on the availability of recycled polyester and need for virgin material to meet quality and specifications of many applications. Over the span between 2008 and 2019, rPET produced has ranged from 2 to 9% of total global PET for fiber applications. Currently, PTA is produced from pX where 0.58 tonnes of pX are required to produce one tonne of polyester, resulting in global demand for pX of about 50 mm tonnes (Figure 2).
Annual PET Fiber produced from 2008 to 2019.
Pathway from p-xylene to polyethylene terephthalate (PET).
Figure 3 displays the supply chain to produce PET. Virtually all PET is produced from fossil fuel resources. pX is produced from mixed xylenes that are derived from crude oil, and MEG is produced from ethylene primarily derived from natural gas. There is a commercial bio-based route to MEG that starts from ethanol produced from biomass by dehydration to ethylene, oxygenation to ethylene oxide, and hydrolysis to MEG. Bio-based MEG is used to produce a partial bio (~30%) PET. At the current time, there are no commercial routes to bio-pX.
Supply chain to PET.
Conventional pX technology is based on the isomerization of mixed xylenes which has been practiced commercially for decades. The mixed xylenes are produced by catalytic reforming of naphtha, which produces a C8 stream that includes the three xylene isomers and ethylbenzene. Other routes to mixed xylenes are from the pyrolysis gasoline stream produced in a naphtha steam cracker. The main commercial routes used to separate the pX isomer are crystallization, which takes advantage of the different freeze points of the ortho-, meta- and para- isomers, or via selective adsorption separation processes.
As a result of growing concerns about climate change, companies, governments, and consumers are increasing their focus on ways to reduce the carbon footprint of materials and offer more sustainable products. Consequently, companies are looking at new and innovative technologies to produce pX from renewable biomass resources rather than from crude oil, to enable production of a 100% bio polyester product. This report focuses catalytic fast pyrolysis (CFP) of lignocellulose to bio-oils which are refined to bio-pX with the objective to reduce carbon footprint in comparison to petro-pX. There are other processes currently being developed for bio-pX, but a discussion of these processes are beyond the scope of this paper.
As the world is emerging from the global pandemic of 2020–2021, increasingly, big companies have turned their focus on sustainability and establishing aggressive targets to reduce the carbon footprint of their products and over time move toward a net-zero carbon profile. It was earlier in 2009 Coca-Cola announced their rollout of the PlantBottle™ [2]. Coca-Cola’s mission is to reduce reliance on non-renewable resources, and reduce CO2 emission in polyethylene terephthalate (PET). Currently, only 30% of the PET in PlantBottle™ is made from bio-MEG. A commercialized process for bio-PTA process would enable Coca-Cola (and others) to produce 100% bio-PET PlantBottle™. Advantageously, bio-PET production would be a “drop-in” into existing PET assets. By 2012, Coca-Cola, Ford, Heinz, Nike, and Procter & Gamble founded the “Plant PET Technology Collaborative” and announced their mission [3]:
“PTC members are committed to supporting and championing research, expanding knowledge and accelerating technology development to enable commercially viable, more sustainably sourced 100% plant-based PET plastic while reducing the use of fossil fuels”. Similarly, Danone, Nestlé Waters, Origin Materials and PepsiCo formed the NaturALL Bottle Alliance in 2018. Since Coca-Cola’s 2009 announcement, many have gravitated to the challenge to develop bio-PTA.
The reduced carbon footprint of bio-pX, and consequently bio-polyester, can contribute to meeting these carbon reduction goals for companies that participate in the polyester value chain, and this is the key business driver behind the increasing interest in routes to bio pX. The bottom line: once bio-pX is available, oxidation of bio-pX to bio-PTA would produce 100% bio-PET.
Anellotech, a Pearl, NY start-up chemical company founded in 2008, has developed a feedstock flexible, in situ catalytic fast pyrolysis process to convert low-cost lignocellulosic biomass solids to a range of hydrocarbons containing valuable benzene, toluene, and xylenes (BTX). These monoaromatics are further refined to produce bio-pX which are valuable feedstocks for bio-PTA [4, 5, 6, 7, 8, 9, 10, 11, 12, 13]. In situ CFP technology was originally developed by Dr. George W. Huber, Harvey Spangler Professor of Chemical Engineering at the University of Wisconsin-Madison.
Anellotech has partnered with Suntory, a global consumer beverage company. The technology has been jointly developed by IFPEN, Axen (a subsidiary of IFPEN), and Johnson Matthey. IFPEN is tasked with scale-up, Axen for technology marketing, and Johnson Matthey for catalyst development. On May 6, 2019, Anellotech announced successful six months of operations of their Bio-TCatTM continuous process in their Silsbee, TX pilot plant. The bio-pX process yield ranged from 22 to 24%, 98% C6+ aromatics. Currently, Anellotech is seeking partners and funding to construct their first commercial CFP based bio-pX plant (500 bone-dry tonnes/day of loblolly pine and target production of 40,000 tonnes BTX and C9+ aromatics per year).
Pyrolysis is an extraordinarily complex, thermochemical reaction which can be operated in slow or fast mode to yield products ranging from solids to liquids and gas. Pyrolysis is challenged by high feedstock complexity and the multiphasic nature of this process. More than 300 compounds are found in an acidic, aqueous, unstable, and viscous heterogeneous mixture (a.k.a. pyrolysis oil) of esters, alcohols, ketones, aldehydes, and carboxylic acids [14, 15, 16]. By themselves, these oxygenates have little fuel value. However, they can be catalytically upgraded to aromatic hydrocarbons, particularly bio-pX. The upgrading catalyst must maintain stability and tolerate wide range of oxygenates [17]. CFP can convert the entire plant, not just sugars, which makes this thermochemical process advantageous to fermentation [18].
Zeolites, particularly HZMS-5, have proven to be effective catalysts for pyrolysis oil upgrading to benzene, toluene, and xylenes (BTX). Crystalline zeolites have well-defined microporous structures with pore sizes ranging from 5 to 12 Å. Zeolites are acidic materials with controllable acid site densities. CFP must operate under O2-free, optionally ambient pressure, and does not require H2 (a.k.a. hydroprocessing), but operating under H2 atmosphere might offer advantage of decreased coking (discussed later in this chapter).
Temperature is an important parameter. In CFP, a moderate temperature of approximately 450 to 550 °C is optimum to produce mainly liquids, but the heating and subsequent cooling rates must be extremely high. The biomass must be ground to a finely divided material with averaged particle sizes of less than 3 mm. The cost of the process is inversely proportional to the averaged particle size. The pyrolysis vapor must condense quickly to avoid unwanted secondary reactions such as cracking. Alkali and alkaline earth metal ions in biomass feed pose substantial challenges to the process (addressed in Pretreatment) [17, 19, 20, 21, 22, 23, 24, 25, 26, 27, 28, 29, 30, 31, 32, 33].
There are two process schemes that can be employed in CFP: in situ and ex situ [32, 34]. Pyrolysis and catalytic upgrading that occur in the same zone is in situ. This “one-pot” process is lower in cost than ex situ. However, in situ CFP is sensitive biomass feed content of inorganics, and minimum catalyst/biomass ratio where 10:1 gives highest yield of aromatics [35].
Pyrolysis and catalytic vapor upgrade that occur in separate zones (two-stage) is ex situ CFP. This mode of operation affords the advantage to exclude biochar and metallic ionic impurities from the catalyst which can extend catalyst lifetime. Additionally, the temperature of pyrolysis and vapor upgrade can be independently controlled, an option not available for in situ CFP. BioBTX operates an ex situ pyrolysis process, and has developed an integrated cascading pyrolysis reactor. Their two-stage process excludes non-volatile impurities from entering catalyst pores and this provides the benefit of improved catalyst vapor contact [26].
A comparison of in situ and ex situ CFP of hybrid poplar at 700 °C was conducted in a microreactor. In situ CFP produced 5.4% olefins and 26.1% aromatics. While operating in an ex situ mode, up to 17.4% olefins and 18.9% aromatics were made. The carbonaceous material yields for in situ and ex situ were 31.3% and 18.6%, respectively. Temperature strongly influenced the product distribution in ex situ. A comparison of both modes of operations in a mini-plant for CFP of pinewood was conducted [36]. An analysis of ex situ economics has also been published [37].
Fast pyrolysis rapidly depolymerizes lignocellulose to its constituents: hemicellulose, cellulose, and lignin. Under these conditions, cellulose is depolymerized to glucose, hemicellulose to C5 sugars, and lignin to phenolic compounds [22, 38, 39]. Once glucose is made, it is quickly dehydrated to anhydrosugars which are then converted to furanics. Furanics are diffused into zeolite pores where it is combined with in situ olefins and undergoe Diels Alder cyclization and dehydration to aromatics. Zeolite imparts a “confinement effect” for chemicals undergoing dehydrocyclization within the catalyst interior and once formed, monoaromatics exit the catalyst [40]. At a molecular level, at 450–600 °C, the furanic oxygen coordinates to Al of the zeolite. Deoxygenation of organics result in elimination of CO2, CO, and H2O. As a test of this hypothesis, furan and olefins were used as models in HZSM-5 catalyzed upgrading. HZSM-5 has a three-dimensional pore structure with intersecting systems of 10-membered ring pores. The dimension of ring pores is nearly ideal for production of pX: 5.1 x 5.5 Å (sinusoidal pores), and 5.3 x 5.6 Å (straight pores) [41]. HZM-5’s utility in conversion of oxygenates to aromatics was demonstrated by Mobil’s commercial methanol-to-gasoline process. Within HZSM-5, ethylene and furan did not yield benzene, but replacement of ethylene by propylene led to toluene [42]. Likewise, 2-methylfuran and propylene produced xylenes. In the absence of olefins, Diels Alder dimerization and dehydration of furan results in benzofuran (Eq. (1)). Graphitic coke was also deposited onto the catalyst, which contributed to catalyst deactivation in about 30 minutes. When the upgrading temperature was increased to 650 °C, the selectivity was shifted to olefins.
Other investigators have examined conversion of methylated furan over Ga/HZSM-5 [43]. Even though model compounds were used, the reaction network was extremely complex due to numerous secondary reactions at 300–500 °C. Coking became a dominant reaction at temperature above 500 °C.
A “technical catalyst” such as extruded Al2O3 -HZSM-5 was explored in CFP of pine wood and cellulose at 500 °C [44]. The focus of the study was on effect of pyrolysis temperature. The type of coke made was highly dependent on the feedstock. Yet, even by 2020, the mechanism of CFP remained elusive. Gaps still exist between theoretical models and applied pyrolysis. Thus far, there is still insufficient information generated from a single biomass source [45]. High aromatics selectivity and strong resistance to catalyst deactivation are keys to the success of CFP for bio-pX. Therefore, extensive efforts have been directed toward zeolite modifications.
Zeolites are microporous crystalline materials of SiO2 and Al2O3 that have Brønsted and Lewis acidic sites [17, 46]. HZSM-5 also have ordered structure microporous structures. In the refining process, zeolites are integral to crude oil conversions in the gas phase. The feed for these refining processes are bereft of minerals, oxygenates, and water. Under these conditions, zeolite lifetimes are quite long. However, conversion of biomass occurs in a condensed, aqueous phase, which are highly challenging conditions for zeolites. Oxygenate conversions are difficult to achieve because of their tendency to coke. In addition to BTX, CFP produces a very large volume of wide variety of hydrocarbons, valuable for fuel (fuel gas, gasoline and diesel blendstock). Therefore, the literature on CFP catalyst development is quite voluminous due to interests in bio-fuels.
A comparison of HZSM-5, HY, H-BEA, and H-mordenite for pyrolysis oil upgrading has been made [37, 47]. A method to evaluate catalysts for ex situ vapor upgrading is the pyroprobe analytical pyrolyzer. This important tool provides high heating rates and means to analyze complex mixtures of products [48]. An examination of feeds ranging from glucose, xylitol, cellulose, to cellobiose was explored with catalyst candidates of HZSM-5, silicalite, H-BEA, HY, and SiO2/Al2O3. Based on this study, HZSM-5 has been found to be the highest performing catalyst. Pore characteristics and shape selectivity for monoaromatics of HZSM-5 are superior to other zeolites. Another comparison study was conducted on HZSM-5, MCM-41, and HY [49]. HZSM-5 was again the most effective zeolite among this group to produce up to 33.1% BTX and 86.4% aromatics selectivity.
The silica-alumina ratio (SAR) of HZSM-5 is also an important parameter for deoxygenation reactions [50]. As the SAR is reduced, the density of Brønsted acids increases. Other zeolites of similar SAR were inferior to HZSM-5 because they were not microporous. Mesoporous zeolites were not selective for aromatics. For example, sulfated ZrO2 is a superacid, a property important for aromatics formation, but this metal oxide was ineffective because of the absence of shape-selectivity. Coupling ZrO2 to MCM-41 resulted in higher levels of pyrolysis vapor deoxygenation and was found to be stable against coking.
Because HZSM-5 plays such a vital role in CFP, numerous investigations have been launched to determine whether modifications of the physical structure can improve aromatics selectivity and minimize coking. Modification of zeolite’s pore mouth sizes can improve the catalyst for improving of BTX selectivities [51, 52]. Specifically, narrowing the pore mouth openings by chemical deposition techniques was explored [53]. The deposited chemicals also covered external acid sites, which can improve pX selectivity [5]. Phosphorous-modified HZSM-5 promoted greater space confinement and increased pX selectivity. A comparison of various deposited silicon materials was conducted by KH550, TEOS, and methyl silicone oil [54, 55]. KH550 modification of HZSM-5 increased furan conversion to 24.5% aromatics vs. 18.8% unmodified HZSM-5 (see reference [5]). Coking of the modified catalyst was also reduced from 44.1 to 26.7%. A decrease in benzene and increase in toluene and naphthalenes selectivities were observed. Chemical liquid depositions of TiO2 to HZSM-5 also resulted in improvements to BTX yields from 17.0 to 23.5%, and reduced levels of coking [56].
The other direction to zeolite modifications is to create mesopores. Unilamellar mesoporous MFI nanosheets (UMN) were tested against another mesoporous material, Al-SBA-15 [57]. UMN has stronger acid sites which result in greater cracking and deoxygenation activities. Ketones and alcohols were converted to furanics and aromatics. Another method to produce mesopores is NaOH desilication of HZSM-5 [58]. This method was successful to create intraparticle mesoporous materials which then improved diffusion. By coupling ZrO2 with desilicated zeolites, a more active zeolite was accompanied with longer catalyst lifetimes [19]. The resulting coke was “softer” (i.e. less aromatic) and was easier to remove. A two-stage microporous and mesoporous vapor upgrading system was examined [59]. In this case, HZSM-5 and MCM-41 (3:1) were evaluated. By increasing the MCM-41 loading, more xylenes were made than toluene. A comparison of chemical liquid deposition (CLD) and acid dealumination (AD) of HZSM-5 was conducted [60]. CLD decreased pore size while AD increased pore size. In both cases, decrease of strong acid sites occurred. CLD boosted BTX yield to 37.2% while AD produced 30.4%. In both cases there was a decrease in indene, naphthalenes, and coke precursors.
Most recently, Li et al. reported development of a core-shell catalyst of HZSM-5@MCM-41 made from an external recrystallization method [61]. HZSM-5@MCM-41 required a lower temperature of 500 °C to produce hydrocarbons, versus 550 °C for unmodified HZSM-5. Monoaromatic hydrocarbons produced from rape straw pyrolysis was as high as 11.43 wt%, which is 2.5 times higher than obtained from HZSM-5. Furthermore, HZSM-5@MCM-41 produced less graphitic coke.
The literature is replete with studies of metals doped HZSM-5 to investigate their effects of CFP catalyst. Zeolites metalated even at low concentrations beneficially resulted in accelerated deoxygenation by decarbonylation, decarboxylation, dehydration, and olefin aromatization of pyrolysis products. In some cases, there were reduced coke formation by decreasing selectivities to polycyclic aromatic hydrocarbons. Table 1 summarizes the metals dopant and their references. Among these metals, gallium, iron, zinc, molybdenum, nickel, and copper increased for deoxygenations, dehydrocyclization, and aromatization.
Entry | Metals/Additives | References |
---|---|---|
1 | Ga | [24, 26, 62, 63, 64, 65, 66, 67, 68, 69, 70, 71, 72, 73, 74, 75, 76, 77, 78, 79] |
2 | Fe | [26, 63, 66, 75, 80, 81, 82, 83, 84, 85, 86, 87, 88] |
3 | Pt | [72, 89, 90, 91, 92] |
4 | Zn | [26, 63, 77, 78, 79, 80, 85, 86, 93, 94, 95, 96] |
5 | Mo | [24, 63, 76, 77, 90, 91, 97, 98, 99, 100] |
6 | Ni | [24, 26, 63, 67, 73, 82, 87, 90, 92, 96, 100, 101, 102] |
7 | Co | [26, 63, 73, 80, 85, 90, 92, 96, 102] |
8 | Cu | [63, 92, 96, 97, 101, 103] |
9 | Mn | [63] |
10 | La | [86, 93, 94] |
11 | Mg | [93, 94, 96] |
12 | Ce | [93, 94] |
13 | Ca | [86, 96, 104] |
14 | Pd | [73] |
15 | Sn | [105] |
16 | WO3 | [91] |
17 | Mo2N | [106] |
18 | W2P | [106] |
19 | MoP | [106] |
20 | WP | [106] |
21 | Zn/P | [107] |
22 | Ga-Ni | [63] |
23 | Ni-Cu | [108, 109] |
24 | Ni-HF | [110] |
25 | Fe-Ni | [82] |
26 | Mo-Mg | [111] |
27 | Ni-Mo2N | [112] |
28 | Ce-Zr | [113] |
29 | Ga-Mo | [114] |
30 | Fe-Ca | [115] |
Metals and additives to HZSM-5 for CFP.
Investigators also examined combinations of metals to determine whether there were accumulated benefits in CFP. For example, Ga and Ni are perhaps the most investigated metal additives, and they have been combined for CFP [63]. Ga-Ni reduced acidity, and reduced formation of polyaromatic hydrocarbons which could explain the reduced coking. Another combination is Cu-Ni which was examined in hydroprocessing (CFP under H2 atmosphere) [108]. Ni-Fe produced an additive effect. Individually, Fe increased yields of monoaromatics, while Ni increased yields of naphthalenes [82]. When combined, this catalyst generated more monoaromatics and naphthalenes. The doping of these metals onto HZSM-5 increased the concentration of strong acid sites, but also resulted in more coke formation.
Molybdenum is already a highly active metal when doped in HZSM-5 in zeolites [111]. When Mg was combined with Mo in HZSM-5, higher selectivities to monoaromatic hydrocarbons and decreased polyaromatics selectivities were achieved. Phosphorous modified HZSM-5 and doped with Zn decreased external acidity of catalyst surface while the internal acid sites were left unchanged. This modification resulted in improvements in this CFP catalyst [107]. HF modification of HZSM-5 and later doped by Ni produced a catalyst that increased yields of BTX [110]. The acid modification created mesopores and reduced Brønsted acidity via dealumination.
Certain combinations of metals and nonmetals behaved as “noble-metal-like” catalysts [106]. Therefore Ni-Mo2N was prepared and confirmed that Ni further extended performance of Mo2N [112].
In almost every publication concerning CFP catalyst or process development, investigators have identified catalyst deactivation to be the single greatest challenge to this process. The catalyst lifetime can be as short as minutes. There are three types of deactivations and of which, two are irreversible deactivations. The most common form of deactivation results from coke buildup on acid sites within the zeolite pores and renders the catalyst inactive [116]. Coking is most rapid when the catalyst/biomass ratio is less than one and particularly at low SAR. The second type of deactivation results from metal oxides deposited in zeolite which can result in irreversible deactivation if these salts are not removed [117]. Thirdly, zeolite dealumination can occur and result in irreversible deactivation.
Coke deactivation most rapidly occurs among highly acidic zeolites of low silica/alumina ratio (SAR) [118]. Ironically, low zeolite SAR are most active for aromatics [82, 119]. Individual lignocellulosic components caused deactivation differently [120]. Depolymerized lignin mainly deactivates by coking on zeolite surfaces because lignin monomers (mostly phenolics) cannot diffuse into the microchannels of HZSM-5 [121]. Cellulose pyrolysis products are responsible for coking within the interior of the zeolite and this leads to occlusion [121]. A study into deactivation mechanism was conducted from in situ CFP pine wood [121]. Fresh catalyst produced mainly aromatics and olefins with no detectable levels of oxygenates. As the campaign progresses, the catalyst/biomass ratio began to decrease, and oxygenates began to breakthrough, including phenolics. When the catalyst/biomass ratio reached 1:3, complete deactivation will have occurred.
Not all oxygenates deactivate HZSM-5 at the same rate [122]. One team examined the effects of upgrading ethanol-only, ethanol+acetic acid, ethanol+ethyl acetate, and ethanol+acetaldehyde. Acetic acid in the vapor strongly adsorbed onto zeolite surfaces and promoted formation of polyaromatic hydrocarbon precursors to coke. Acetaldehyde deactivated 10X more than ethanol. While ethyl acetate did not directly adsorb onto catalyst surfaces, the reaction conditions rapidly hydrolyzed ethyl acetate to acetic acid which then immediately deactivated the catalyst.
An extruded HZSM-5 (a.k.a. “technical catalyst”) containing an alumina binder was also examined in its deactivation in ex situ CFP of cellulose and pinewood [44]. CFP of cellulose generates smaller oxygenates, which diffused into the zeolite to produce a “catalytic coke”, made via a ring-growth mechanism involving H-transfer at temperatures above 200 °C [123]. Initial formation of monoaromatics led to formation of polyaromatic hydrocarbons, coke precursors. It is not surprising to learn that the coking mechanism of oxygenates is similar in pathways to coke formation in petroleum refining [118]. Lignin forms “thermal coke” from condensation of lignin monomers, and easier to remove because they accumulate on the surfaces of the zeolite [118]. High temperature combustion readily regenerates coke-deactivated HZSM-5.
The presence of water liberated from the pyrolysis can accumulate in the catalyst [118, 124]. Later, at high regeneration temperature, steaming can result in dealumination of the zeolite via leaching. In addition to removal of strong acid-site aluminum, there can be a loss of surface area even after one regeneration cycle [44, 51]. As a further complication, during the regeneration, hot spots can appear and irreversibly damage the catalyst. Successive regeneration increases the risk of further dealumination and reduction in micropore volumes, particularly at high regeneration temperature of 650–670 °C [118]. Therefore, these investigators recommended limiting the O2 concentration to 15% and include 5% steam to preserve catalyst lifetime [125]. Use of this method was found to preserve catalyst stability for up to 30 regeneration cycles. The formation of aromatics and olefins was stable at about 31.3% [125].
Alkaline and alkaline earth metal ions (AAEMs) are part of the plant’s nutrient to enable the plant to grow [15, 126]. Lignocellulose is comprised of four different types of materials: lignin, cellulose, hemicellulose, and inorganics. AAEMs and other metal salts are represented by the inorganics fraction. A measurement of ash content provides a direct correlation of mineral concentration in the feed. Mechanistically, alkali metal salts also ion-exchanged with the proton of Brønsted acid sites and this reduces zeolite activity [118]. This was demonstrated from an on-purpose potassium ion exchange with HZSM-5 (up to 2.85 wt%) which resulted in drastic reduction of catalyst acidity, leading to lower yields of carbons [127]. Within the pyrolysis process itself, AAEMs can catalyze unwanted secondary reactions, including cracking, decarboxylation, and dehydration, resulting in a loss of liquid yields [34]. Carbon oxides and water were increased by 10% due to these inorganic components, changing the product distribution [118, 128]. Among the metal ions that are highly detrimental to the process are K > Na > Ca, and the concentration of potassium in the feed is inversely proportional to aromatics [129]. Furthermore, Xiao et al. studied the effect of potassium salts on CFP of a model feed, 2-methylfuran [130]. The experiments were conducted by deposition of potassium salts into HZSM-5. Neutral KCl was less harmful than basic K2CO3 which produced lower yields of aromatic hydrocarbons and gases. The negative effects were due to loss of acidity and erosion of physical structure of HZSM-5, particularly when the K2CO3 concentration was as high as 1.0 wt%.
Magnesium is also present, but it is not as harmful as the other metal ions. Other inorganic ions that need to be monitored include Cl, S, P, and N [131]. Particularly, CFP of guayule, a perennial woody shrub, can produce upgraded products containing 80 to 700 ppm sulfur which can be detrimental to any sulfur sensitive downstream processes [132].
Because of the nature of the process, it is in situ CFP that is most sensitive to AAMEs in the feed. Even at levels as low as 0.1 wt% in the feed, AAEMs can greatly impact the pyrolysis process. Aggravating this situation is the variation of feedstock which also varies the inorganic component concentrations. Switchgrass as a feed results in high ash content [118, 131]. Versus pinewood (0.49 wt%), Switchgrass can contain around 2.6 wt% ash comprised of metal oxides. Crop selection is crucial to preserve performance of CFP [15, 133]. Feed pretreatment can be an option to minimize the deleterious effects of AAEMs.
Two main strategies have been published to combat the challenges of pyrolysis: torrefaction and acid-washing of lignocellulose. Torrefaction is low temperature, slow pyrolysis of less than 60 minutes, and installed upstream to CFP. During torrefaction, removal of undesirable acetic acid and guaiacol from the feed improves the downstream CFP. Typical temperature of torrefaction ranges from 250 to 300 °C [112]. When torrefaction was tested on pinewood conversion at 250 °C, the resulting CFP step produced 30% more aromatics. Other feedstocks such as corn cobs produced a lower O/C ratio in the CFP product [134].
Acid-washing of finely divided lignocellulose can extract AAEMs from the feed. The wash step is conducted under very mild conditions, but it is necessary that thorough drying is conducted prior to CFP [51]. For example, rice husks are washed at 30 °C by acetic acid [84, 135]. Use of acids such as acetic acid or mineral acids can add significant variable costs to the process. One investigator recommended using acetic acid recovered from the pyrolysis process for the wash. Extreme aqueous washing must be avoided as the extraction can result in undesirable changes in hemicellulose and cellulose. Formation of sticky materials can coat catalyst bed particles and risk defluidization [136]. Aqueous HCl washing of the spent catalyst to remove deposited minerals is also necessary to maintain catalyst lifetime [118].
A comparison of both processes was studied to determine their effects on aromatics yield. Acid-leaching promoted the formation of levoglucosan. Torrefaction promoted the formation of catechols and guaicols. It was determined that acid leaching + CFP made less aromatics than torrefaction + CFP [137]. Both processes were conducted in series in the CFP of rice husk [135]. Lower levels of volatiles were made in the pyrolysis result in lower yields of oxygenates and higher yields of aromatics. However, severe torrefaction conditions due to longer residence time can result in cross-linking of lignocellulose, resulting in more charring and reduced formation of aromatics. A combination of both processes did result in higher yields of products [136].
One team of investigators described development of ultrasonic pretreatment [138]. This mechanical method excludes use of toxic chemicals. Ultrasound promotes cleaving of α-O-4 and β-O-4 linkages and overall decreased crystallinity of lignocellulose and increased yield of pyrolysis oils. CFP can accommodate a wide variety of feedstocks. Table 2 summarizes the feedstocks examined, which include woody plants of varying levels of lignin, cellulose, and hemicellulose. The most frequently studied woody biomass for pyrolysis was pinewood. Also included in this table are references to studies of model feeds.
Beatle killed trees | [139] |
Pine wood | [36, 60, 67, 97, 101, 106, 111, 121, 128, 140, 141, 142, 143, 144, 145, 146] |
Pine bark | [58] |
Pinecones | [145] |
Pinyon juniper | [58] |
Beech wood | [58] |
Maple wood | [148] |
Hybrid poplar | [58, 147] |
Yellow poplar | [76] |
Red oak | [147] |
Oakwood | [149] |
Quercus Mongolia | [74] |
Eucalyptus | [63, 68, 87] |
Willow wood | [66] |
Guayule Bagasse | [150] |
Corn cobs | [141, 151] |
Corn stover residue | [58] |
Corn stalk | [88] |
Straw | [141, 152] |
Sunflower Stalk | [153] |
Switch grass | [58, 127, 131] |
Mandarin residue | [72] |
Citrus unshiu | [119] |
Rice Husk | [84, 109, 135, 154, 155, 156] |
Bamboo sawdust | [56, 157] |
Giant cane | [158] |
Sugarcane bagasse | [147] |
Wheat straw | [91, 98, 159] |
Rape straw | [61] |
Xylitol | [160] |
Cotton stalk | [80] |
Jatroha residues | [73] |
Miscanthus | [57, 161] |
Peanut shells | [162] |
Microalgae | [70, 140] |
Seaweed | [140] |
Fish discards | [140] |
Guaiacol | [52] |
Acetic Acid | [52] |
Furanics | [5, 38, 42, 43, 52, 54, 78, 130, 148, 163, 164, 165, 166, 167, 168] |
Glucose | [148, 160, 169, 170] |
Lignin | [121, 141, 171] |
Hemicellulose | [141, 171] |
Cellulose | [44, 57, 80, 113, 120, 121, 141, 160, 161, 171, 172, 173, 174] |
Cellbios | [160] |
Glycerol | [175, 176] |
Feedstocks used in CFP.
Glucose is one of the intermediate products made in pyrolysis [169]. This monosaccharide is rapidly converted to anhydrosugars before they are dehydrated to furanics and subsequently to aromatics. Sophisticated isotopically labeled glucose experiments permitted an elucidation of the mechanism of glucose conversion [170]. Single ring aromatics contained 13C labels and later these labels began to appear in naphthalene rings, evidence for a ring growth mechanism from monoaromatics to polyaromatics. Other studies included a study of the conversion of other model feeds to aromatics under identical conditions [80, 121, 140, 141, 142, 147, 160, 161, 171]. Glycerol CFP is of interest because of its availability from the production of fatty acid methyl esters for bio-diesel [175, 176].
Investigators recognized that pyrolysis produced improved product quality when a second feed was added to the process [22, 24]. The co-feed can include coal, plastics, tire, and sludge. N.Y. Chen et al. first reported in 1986 that the hydrogen to carbon effective ratio (H/Ceff) can predict the outcome of pyrolysis [177]. This ratio is calculated according to the following formula (Eq. (2)).
When this ratio is less than one, coke is expected to be made in high yields. For example, glucose has a ratio of zero, sorbitol has 0.333, glycerol has 0.667, xylitol has 0.400 and petroleum is greater than two [160]. As a feed, lignocellulose is highly deficient in hydrogen. It might be plausible to increase this ratio by co-feeding a material rich in hydrogen [19, 27]. By increasing this ratio, not only is coke reduced, but higher yields of aromatics and olefins result. Other means to increase this ratio is to pretreat the feed by hydrogenolysis [178]. An ex situ co-pyrolysis strategy to increase BTX yield was cleverly conducted by removing BTX from the product stream to leave behind polyaromatic hydrocarbons. This high molecular weight material was then hydrogenated to produce polycyclic aliphatic hydrocarbons. This hydrogenated fraction was then co-pyrolyzed with glycerol to produce higher yields of BTX [176].
The upgrading of furanics to aromatics was benefitted by the co-addition of olefins [42, 119, 163, 177, 179, 180]. While co-addition of ethylene and propylene was effective to produce more aromatics, investigators recognized that the process must now incorporate flammable gases. An alternative to olefins utilization was to co-add methanol to the pyrolysis. Under the upgrading conditions, methanol to in situ olefins can occur to produce the dienophiles required for furanic Diels Alder reactions. Therefore, 2-methylfuran (2-MF) and methanol co-addition resulted in boosting aromatics yield while coke was reduced [168]. When the MeOH/2-MF ratio was increased from zero to 3:1, 2-MF conversion was increased from 39.8% to as high as 96.5% at an optimal ratio of 2:1. Of course, not all furanics were equally converted. A comparison of 2,5-dimethylfuran (DMF), furan, and furfural revealed that electron-rich DMF quickly reacted while the electron-deficient furfural lagged behind: DMF > furan > furfural [94]. In addition to aromatics, CO2, CO, and other olefins were also made at 400–600 °C [38]. Unavoidably, formation of graphitic coke on catalyst surfaces resulted in its deactivation within 30 minutes. Methane was examined as a co-feed in the catalytic upgrading [164]. This co-feed was beneficial, an indication that methane could be activated by this catalyst to yield more aromatics, but coke formation also increased.
CCP was applied to a mixture of sawdust and methanol. This combination reduced coke and char and improved aromatics yields [77, 93, 181]. However, the researchers could not exclude the possibility that a background methanol to aromatics process was also occurring. Another team examined CCP of other co-feeds such as methanol, polyethylene terephthalate (PET), and calcium formate with pinewood [182]. Of these three, calcium formate was found to be most effective at calcium formate/pinewood of 3:1. In fact, co-feeding calcium formate did not produce a large increase in aromatics vs. control (10.65% vs. 9.23%), but this co-pyrolysis reduced the polyaromatic hydrocarbons yield (1.94% vs. 2.49%). The authors speculated that the calcium salt helped to maintain catalyst activity within the hydrocarbon pool of the zeolite.
A patent was granted to Anellotech for co-feeding oxygenates such as acetone into pyrolysis to enhanced pX yield [183]. The oxygenates utilized are low value byproducts from other industrial processes. Such oxygenates include acetone from the phenol process, furfural, hexanol, and hexanoic acid from other sources. Furfural was less effective, but the formation of xylenes was enhanced by hexanol and hexanoic acid co-additions. Other oxygenates include fermentation products [184]. Co-pyrolysis of citrus unshiu peel and alcohols, ketones, and furanics has been reported [119]. In this case, two different zeolites were compared: HZSM-5 (23) and HBEA (25). The key difference between both zeolites was that HBEA produced more coke.
Tail Gas Reactive or Recycle Pyrolysis (TGRP) is an interesting process that recycles non-condensable pyrolysis gases to the pyrolysis step [150, 166, 185, 186]. Recycling this gas to pyrolysis provides a reductive, low acidic atmosphere which benefits CFP by increasing the H/Ceff. The condensable gas fraction was separated, including unwanted carboxylic acids and furfural which are detrimental to vapor upgrading. Up to 10X more BTX was produced when TGRP was incorporated in comparison to CFP-only.
Other non-conventional processes could also improve CFP yields. One example is addition of ball bearings to the catalyst bed to increase residence time which provided higher hot surface areas [187]. This modification increased cracking reaction and produced 3X more BTX. The downside is formation of more polyaromatic hydrocarbons. An alternative to thermal heating, microwave energy can also be used. Microwave assisted pyrolysis (MOP) does not require agitation and fluidization [56, 188].
CFP is a rapid process to produce a high volume of hydrocarbons of which BTX is a small fraction. CFP must be co-located with a petroleum refining complex to take in bio-naphtha which could be directed to bio-gasoline production. The refining complex must also include a pX extraction process to separate pX from mX and oX as well as a process to isomerize the pX lean stream. Every means to improve CFP should be taken, including pretreatment, torrefaction, co-pyrolysis with hydrogen-rich feed, and tail gas recycled pyrolysis to increase BTX yields. Investigations into development of an even more active metalated HZSM-5 catalyst to increase monoaromatics selectivity and resistance to coking will remain subjects of intense interests.
This is a brief overview of the main steps involved in publishing with IntechOpen Compacts, Monographs and Edited Books. Once you submit your proposal you will be appointed a Author Service Manager who will be your single point of contact and lead you through all the described steps below.
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\n\nPlease complete the publishing proposal form. The completed form should serve as an overview of your future Compacts, Monograph or Edited Book. Once submitted, your publishing proposal will be sent for evaluation, and a notice of acceptance or rejection will be sent within 10 to 30 working days from the date of submission.
\n\n2. SUBMIT YOUR MANUSCRIPT
\n\nAfter approval, you will proceed in submitting your full-length manuscript. 50-130 pages for compacts, 130-500 for Monographs & Edited Books.Your full-length manuscript must follow IntechOpen's Author Guidelines and comply with our publishing rules. Once the manuscript is submitted, but before it is forwarded for peer review, it will be screened for plagiarism.
\n\n3. PEER REVIEW RESULTS
\n\nExternal reviewers will evaluate your manuscript and provide you with their feedback. You may be asked to revise your draft, or parts of your draft, provide additional information and make any other necessary changes according to their comments and suggestions.
\n\n4. ACCEPTANCE AND PRICE QUOTE
\n\nIf the manuscript is formally accepted after peer review you will receive a formal Notice of Acceptance, and a price quote.
\n\nThe Open Access Publishing Fee of your IntechOpen Compacts, Monograph or Edited Book depends on the volume of the publication and includes: project management, editorial and peer review services, technical editing, language copyediting, cover design and book layout, book promotion and ISBN assignment.
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The evaluation results confirm the potential of the proposed system for real-time temporal and spatial monitoring of air quality. 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The unintentional introduction of stoats and rats into a once pristine ecosystem has resulted in the devastation of large parts of New Zealand’s native flora and fauna. Other equally harmful mammalian species, including possum, for their fur, and domestic cats, were introduced intentionally. Abundant vegetation and a lack of predators lead to rampant population growth, further exacerbating their destructive impact. Effective monitoring, trapping and control of mammalian pests have proven difficult, time-consuming and expensive, primarily relying on socially controversial methods such as aerially delivered toxins. Despite advances in technology, costly and time-intensive manual checking of lures, toxins, traps and tracking devices remains a limiting factor. Together with WSN-based remote monitoring capability, these advances look set to have a significant impact. This chapter discusses opportunities for WSN in conservation management. It outlines a mammalian pest management project utilising a series of possum-specific self-resetting traps. A WSN designed for remotely monitoring possum trap activity is detailed, and the process for reconfiguring and presenting field-trial data via alpha-numeric and graphical user interface applications is described.",book:{id:"6038",slug:"wireless-sensor-networks-insights-and-innovations",title:"Wireless Sensor Networks",fullTitle:"Wireless Sensor Networks - Insights and Innovations"},signatures:"Akbar Ghobakhlou and Shane Inder",authors:[{id:"209937",title:"Dr.",name:"Akbar",middleName:null,surname:"Ghobakhlou",slug:"akbar-ghobakhlou",fullName:"Akbar Ghobakhlou"},{id:"214817",title:"Dr.",name:"Shane",middleName:null,surname:"Inder",slug:"shane-inder",fullName:"Shane Inder"}]},{id:"56523",title:"Fuzzy Adaptive Setpoint Weighting Controller for WirelessHART Networked Control Systems",slug:"fuzzy-adaptive-setpoint-weighting-controller-for-wirelesshart-networked-control-systems",totalDownloads:1167,totalCrossrefCites:0,totalDimensionsCites:1,abstract:"Gain range limitation of conventional proportional‐integral‐derivative (PID) controllers has made them unsuitable for application in a delayed environment. These controllers are also not suitable for use in a Wireless Highway Addressable Remote Transducer (WirelessHART) protocol networked control setup. This is due to stochastic network‐induced delay and uncertainties such as packet dropout. The use of setpoint weighting strategy has been proposed to improve the performance of the PID in such environments. However, the stochastic delay still makes it difficult to achieve optimal performance. This chapter proposes an adaptation to the setpoint weighting technique. The proposed approach will be used to adapt the setpoint weighting structure to variation in WirelessHART network‐induced delay through fuzzy inference. Result comparison of the proposed approach with both setpoint weighting and proportional‐integral (PI) control strategy shows improved setpoint tracking and load regulation. For the first‐, second‐ and third‐order systems considered, analysis of the results in the time domain shows that in terms of overshoot, undershoot, rise time, and settling times, the proposed approach outperforms both the setpoint weighting and the PI controller. The approach also shows faster recovery from disturbance effect.",book:{id:"6038",slug:"wireless-sensor-networks-insights-and-innovations",title:"Wireless Sensor Networks",fullTitle:"Wireless Sensor Networks - Insights and Innovations"},signatures:"Sabo Miya Hassan, Rosdiazli Ibrahim, Nordin Saad, Vijanth Sagayan\nAsirvadam, Kishore Bingi and Tran Duc Chung",authors:[{id:"206524",title:"MSc.",name:"Sabo",middleName:"Miya",surname:"Hassan",slug:"sabo-hassan",fullName:"Sabo Hassan"},{id:"206525",title:"Dr.",name:"Rosdiazli",middleName:null,surname:"Ibrahim",slug:"rosdiazli-ibrahim",fullName:"Rosdiazli Ibrahim"},{id:"206529",title:"Dr.",name:"Nordin",middleName:null,surname:"Saad",slug:"nordin-saad",fullName:"Nordin Saad"},{id:"206530",title:"Dr.",name:"Vijanth Sagayan",middleName:null,surname:"Asirvadam",slug:"vijanth-sagayan-asirvadam",fullName:"Vijanth Sagayan Asirvadam"},{id:"206532",title:"Mr.",name:"Tran",middleName:"Duc",surname:"Chung",slug:"tran-chung",fullName:"Tran Chung"},{id:"206540",title:"Ph.D. Student",name:"Kishore",middleName:null,surname:"Bingi",slug:"kishore-bingi",fullName:"Kishore Bingi"}]},{id:"56900",title:"Mobile Wireless Sensor Networks: An Overview",slug:"mobile-wireless-sensor-networks-an-overview",totalDownloads:2730,totalCrossrefCites:23,totalDimensionsCites:30,abstract:"Mobile wireless sensor networks (MWSNs) have emerged and shifted the focus from the typical static wireless sensor networks to networks with mobile sensor nodes that are capable to sense the various types of events. Also, they can change their position frequently in a specific sensing area. The applications of the MWSNs can be widely divided into time-driven, event-driven, on-demand and tracking based applications. Mobile sensor node architecture, residual energy utilization, mobility, topology, scalability, localization, data collection routing, Quality of Service (QoS), etc., are the key factors to design an energy efficient MWSNs for some specific purpose. This chapter deals with an overview of the MWSNs and a few significant phenomena to design an energy efficient MWSNs to the large-scale environment.",book:{id:"6038",slug:"wireless-sensor-networks-insights-and-innovations",title:"Wireless Sensor Networks",fullTitle:"Wireless Sensor Networks - Insights and Innovations"},signatures:"Velmani Ramasamy",authors:[{id:"206195",title:"Dr.",name:"Velmani",middleName:null,surname:"Ramasamy",slug:"velmani-ramasamy",fullName:"Velmani Ramasamy"}]}],onlineFirstChaptersFilter:{topicId:"565",limit:6,offset:0},onlineFirstChaptersCollection:[],onlineFirstChaptersTotal:0},preDownload:{success:null,errors:{}},subscriptionForm:{success:null,errors:{}},aboutIntechopen:{},privacyPolicy:{},peerReviewing:{},howOpenAccessPublishingWithIntechopenWorks:{},sponsorshipBooks:{sponsorshipBooks:[],offset:8,limit:8,total:0},allSeries:{pteSeriesList:[{id:"14",title:"Artificial Intelligence",numberOfPublishedBooks:9,numberOfPublishedChapters:90,numberOfOpenTopics:6,numberOfUpcomingTopics:0,issn:"2633-1403",doi:"10.5772/intechopen.79920",isOpenForSubmission:!0},{id:"7",title:"Biomedical Engineering",numberOfPublishedBooks:12,numberOfPublishedChapters:107,numberOfOpenTopics:3,numberOfUpcomingTopics:0,issn:"2631-5343",doi:"10.5772/intechopen.71985",isOpenForSubmission:!0}],lsSeriesList:[{id:"11",title:"Biochemistry",numberOfPublishedBooks:33,numberOfPublishedChapters:330,numberOfOpenTopics:4,numberOfUpcomingTopics:0,issn:"2632-0983",doi:"10.5772/intechopen.72877",isOpenForSubmission:!0},{id:"25",title:"Environmental Sciences",numberOfPublishedBooks:1,numberOfPublishedChapters:19,numberOfOpenTopics:4,numberOfUpcomingTopics:0,issn:"2754-6713",doi:"10.5772/intechopen.100362",isOpenForSubmission:!0},{id:"10",title:"Physiology",numberOfPublishedBooks:14,numberOfPublishedChapters:145,numberOfOpenTopics:4,numberOfUpcomingTopics:0,issn:"2631-8261",doi:"10.5772/intechopen.72796",isOpenForSubmission:!0}],hsSeriesList:[{id:"3",title:"Dentistry",numberOfPublishedBooks:9,numberOfPublishedChapters:139,numberOfOpenTopics:2,numberOfUpcomingTopics:0,issn:"2631-6218",doi:"10.5772/intechopen.71199",isOpenForSubmission:!0},{id:"6",title:"Infectious Diseases",numberOfPublishedBooks:13,numberOfPublishedChapters:122,numberOfOpenTopics:4,numberOfUpcomingTopics:0,issn:"2631-6188",doi:"10.5772/intechopen.71852",isOpenForSubmission:!0},{id:"13",title:"Veterinary Medicine and Science",numberOfPublishedBooks:11,numberOfPublishedChapters:112,numberOfOpenTopics:3,numberOfUpcomingTopics:0,issn:"2632-0517",doi:"10.5772/intechopen.73681",isOpenForSubmission:!0}],sshSeriesList:[{id:"22",title:"Business, Management and Economics",numberOfPublishedBooks:1,numberOfPublishedChapters:21,numberOfOpenTopics:3,numberOfUpcomingTopics:0,issn:"2753-894X",doi:"10.5772/intechopen.100359",isOpenForSubmission:!0},{id:"23",title:"Education and Human Development",numberOfPublishedBooks:0,numberOfPublishedChapters:10,numberOfOpenTopics:1,numberOfUpcomingTopics:1,issn:null,doi:"10.5772/intechopen.100360",isOpenForSubmission:!0},{id:"24",title:"Sustainable Development",numberOfPublishedBooks:1,numberOfPublishedChapters:19,numberOfOpenTopics:5,numberOfUpcomingTopics:0,issn:"2753-6580",doi:"10.5772/intechopen.100361",isOpenForSubmission:!0}],testimonialsList:[{id:"6",text:"It is great to work with the IntechOpen to produce a worthwhile collection of research that also becomes a great educational resource and guide for future research endeavors.",author:{id:"259298",name:"Edward",surname:"Narayan",institutionString:null,profilePictureURL:"https://mts.intechopen.com/storage/users/259298/images/system/259298.jpeg",slug:"edward-narayan",institution:{id:"3",name:"University of Queensland",country:{id:null,name:"Australia"}}}},{id:"13",text:"The collaboration with and support of the technical staff of IntechOpen is fantastic. The whole process of submitting an article and editing of the submitted article goes extremely smooth and fast, the number of reads and downloads of chapters is high, and the contributions are also frequently cited.",author:{id:"55578",name:"Antonio",surname:"Jurado-Navas",institutionString:null,profilePictureURL:"https://s3.us-east-1.amazonaws.com/intech-files/0030O00002bRisIQAS/Profile_Picture_1626166543950",slug:"antonio-jurado-navas",institution:{id:"720",name:"University of Malaga",country:{id:null,name:"Spain"}}}}]},series:{item:{id:"22",title:"Business, Management and Economics",doi:"10.5772/intechopen.100359",issn:"2753-894X",scope:"\r\n\tThis series will provide a comprehensive overview of recent research trends in business and management, economics, and marketing. Topics will include asset liability management, financial consequences of the financial crisis and covid-19, financial accounting, mergers and acquisitions, management accounting, SMEs, financial markets, corporate finance and governance, managerial technology and innovation, resource management and sustainable development, social entrepreneurship, corporate responsibility, ethics and accountability, microeconomics, labour economics, macroeconomics, public economics, financial economics, econometrics, direct marketing, creative marketing, internet marketing, market planning and forecasting, brand management, market segmentation and targeting and other topics under business and management. This book series will focus on various aspects of business and management whose in-depth understanding is critical for business and company management to function effectively during this uncertain time of financial crisis, Covid-19 pandemic, and military activity in Europe.
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His research interests and specialties include financial econometrics, financial economics, international economics and finance, housing markets, financial markets, among others.",institutionString:null,institution:{name:"University of Southampton",institutionURL:null,country:{name:"United Kingdom"}}},editorTwo:null,editorThree:null},subseries:{paginationCount:5,paginationItems:[{id:"91",title:"Sustainable Economy and Fair Society",coverUrl:"https://cdn.intechopen.com/series_topics/covers/91.jpg",isOpenForSubmission:!0,annualVolume:11975,editor:{id:"181603",title:"Dr.",name:"Antonella",middleName:null,surname:"Petrillo",slug:"antonella-petrillo",fullName:"Antonella Petrillo",profilePictureURL:"https://mts.intechopen.com/storage/users/181603/images/system/181603.jpg",biography:"Antonella Petrillo, Ph.D., is a professor in the Department of Engineering, University of Naples “Parthenope,” Italy. She received her Ph.D. in Mechanical Engineering from the University of Cassino and Southern Lazio, Italy. Her research interests include multi-criteria decision analysis, industrial plants, logistics, manufacturing, and safety. She serves as an associate editor for the International Journal of the Analytic Hierarchy Process and is an editorial board member for several other journals. She is also a member of the Analytic Hierarchy Process (AHP) Academy.",institutionString:"Parthenope University of Naples",institution:{name:"Parthenope University of Naples",institutionURL:null,country:{name:"Italy"}}},editorTwo:null,editorThree:null},{id:"92",title:"Health and Wellbeing",coverUrl:"https://cdn.intechopen.com/series_topics/covers/92.jpg",isOpenForSubmission:!0,annualVolume:11976,editor:{id:"348225",title:"Prof.",name:"Ann",middleName:null,surname:"Hemingway",slug:"ann-hemingway",fullName:"Ann Hemingway",profilePictureURL:"https://s3.us-east-1.amazonaws.com/intech-files/0033Y000035LZFoQAO/Profile_Picture_2022-04-11T14:55:40.jpg",biography:"Professor Hemingway is a public health researcher, Bournemouth University, undertaking international and UK research focused on reducing inequalities in health outcomes for marginalised and excluded populations and more recently focused on equine assisted interventions.",institutionString:null,institution:{name:"Bournemouth University",institutionURL:null,country:{name:"United Kingdom"}}},editorTwo:null,editorThree:null},{id:"93",title:"Inclusivity and Social Equity",coverUrl:"https://cdn.intechopen.com/series_topics/covers/93.jpg",isOpenForSubmission:!0,annualVolume:11977,editor:{id:"210060",title:"Prof. Dr.",name:"Ebba",middleName:null,surname:"Ossiannilsson",slug:"ebba-ossiannilsson",fullName:"Ebba Ossiannilsson",profilePictureURL:"https://s3.us-east-1.amazonaws.com/intech-files/0030O00002g6LkBQAU/Profile_Picture_2022-02-28T13:31:48.png",biography:"Professor Dr. Ebba Ossiannilsson is an independent researcher, expert, consultant, quality auditor and influencer in the fields of open, flexible online and distance learning (OFDL) and the 'new normal'. Her focus is on quality, innovation, leadership, and personalised learning. She works primarily at the strategic and policy levels, both nationally and internationally, and with key international organisations. She is committed to promoting and improving OFDL in the context of SDG4 and the future of education. Ossiannilsson has more than 20 years of experience in her current field, but more than 40 years in the education sector. She works as a reviewer and expert for the European Commission and collaborates with the Joint Research Centre for Quality in Open Education. Ossiannilsson also collaborates with ITCILO and ICoBC (International Council on Badges and Credentials). She is a member of the ICDE Board of Directors and has previously served on the boards of EDEN and EUCEN. Ossiannilsson is a quality expert and reviewer for ICDE, EDEN and the EADTU. She chairs the ICDE OER Advocacy Committee and is a member of the ICDE Quality Network. She is regularly invited as a keynote speaker at conferences. She is a guest editor for several special issues and a member of the editorial board of several scientific journals. She has published more than 200 articles and is currently working on book projects in the field of OFDL. Ossiannilsson is a visiting professor at several international universities and was recently appointed Professor and Research Fellow at Victoria University of Wellington, NZ. Ossiannilsson has been awarded the following fellowships: EDEN Fellows, EDEN Council of Fellows, and Open Education Europe. She is a ICDE OER Ambassador, Open Education Europe Ambassador, GIZ Ambassador for Quality in Digital Learning, and part of the Globe-Community of Digital Learning and Champion of SPARC Europe. On a national level, she is a quality developer at the Swedish Institute for Standards (SIS) and for ISO. She is a member of the Digital Skills and Jobs Coalition Sweden and Vice President of the Swedish Association for Distance Education. She is currently working on a government initiative on quality in distance education at the National Council for Higher Education. She holds a Ph.D. from the University of Oulu, Finland.",institutionString:"Swedish Association for Distance Education, Sweden",institution:null},editorTwo:null,editorThree:null},{id:"94",title:"Climate Change and Environmental Sustainability",coverUrl:"https://cdn.intechopen.com/series_topics/covers/94.jpg",isOpenForSubmission:!0,annualVolume:11978,editor:{id:"61855",title:"Dr.",name:"Yixin",middleName:null,surname:"Zhang",slug:"yixin-zhang",fullName:"Yixin Zhang",profilePictureURL:"https://s3.us-east-1.amazonaws.com/intech-files/0030O00002aYWJgQAO/Profile_Picture_2022-06-09T11:36:35.jpg",biography:"Professor Yixin Zhang is an aquatic ecologist with over 30 years of research and teaching experience in three continents (Asia, Europe, and North America) in Stream Ecology, Riparian Ecology, Urban Ecology, and Ecosystem Restoration and Aquatic Conservation, Human-Nature Interactions and Sustainability, Urbanization Impact on Aquatic Ecosystems. He got his Ph.D. in Animal Ecology at Umeå University in Sweden in 1998. He conducted postdoc research in stream ecology at the University of California at Santa Barbara in the USA. After that, he was a postdoc research fellow at the University of British Columbia in Canada to do research on large-scale stream experimental manipulation and watershed ecological survey in temperate rainforests of BC. He was a faculty member at the University of Hong Kong to run ecological research projects on aquatic insects, fishes, and newts in Tropical Asian streams. He also conducted research in streams, rivers, and caves in Texas, USA, to study the ecology of macroinvertebrates, big-claw river shrimp, fish, turtles, and bats. Current research interests include trophic flows across ecosystems; watershed impacts of land-use change on biodiversity and ecosystem functioning; ecological civilization and water resource management; urban ecology and urban/rural sustainable development.",institutionString:null,institution:{name:"Soochow University",institutionURL:null,country:{name:"China"}}},editorTwo:null,editorThree:null},{id:"95",title:"Urban Planning and Environmental Management",coverUrl:"https://cdn.intechopen.com/series_topics/covers/95.jpg",isOpenForSubmission:!0,annualVolume:11979,editor:{id:"181079",title:"Dr.",name:"Christoph",middleName:null,surname:"Lüthi",slug:"christoph-luthi",fullName:"Christoph Lüthi",profilePictureURL:"https://s3.us-east-1.amazonaws.com/intech-files/0030O00002bRHSqQAO/Profile_Picture_2022-04-12T15:51:33.png",biography:"Dr. Christoph Lüthi is an urban infrastructure planner with over 25 years of experience in planning and design of urban infrastructure in middle and low-income countries. He holds a Master’s Degree in Urban Development Planning from the University College of London (UCL), and a Ph.D. in Urban Planning & Engineering from TU Berlin. He has conducted applied research on urban planning and infrastructure issues in over 20 countries in Africa and Asia. In 2005 he joined Eawag-Sandec as Leader of the Strategic Environmental Sanitation Planning Group. Since 2015 he heads the research department Sanitation, Water and Solid Waste for Development (Sandec) at the Swiss Federal Institute of Aquatic Research and Technology (Eawag).",institutionString:"Swiss Federal Institute of Aquatic Science and Technology, Switzerland",institution:{name:"Swiss Federal Institute of Aquatic Science and Technology",institutionURL:null,country:{name:"Switzerland"}}},editorTwo:{id:"290571",title:"Dr.",name:"Rui Alexandre",middleName:null,surname:"Castanho",slug:"rui-alexandre-castanho",fullName:"Rui Alexandre Castanho",profilePictureURL:"https://mts.intechopen.com/storage/users/290571/images/system/290571.jpg",biography:"Rui Alexandre Castanho has a master\\'s degree in Planning, Audit, and Control in Urban Green Spaces and an international Ph.D. in Sustainable Planning in Borderlands. Currently, he is a professor at WSB University, Poland, and a visiting professor at the University of Johannesburg, South Africa. Dr. Castanho is a post-doc researcher on the GREAT Project, University of Azores, Ponta Delgada, Portugal. He collaborates with the Environmental Resources Analysis Research Group (ARAM), University of Extremadura (UEx), Spain; VALORIZA - Research Center for the Enhancement of Endogenous Resources, Polytechnic Institute of Portalegre (IPP), Portugal; Centre for Tourism Research, Development and Innovation (CITUR), Madeira, Portugal; and AQUAGEO Research Group, University of Campinas (UNICAMP), Brazil.",institutionString:"University of Johannesburg, South Africa and WSB University, Poland",institution:{name:"University of Johannesburg",institutionURL:null,country:{name:"South Africa"}}},editorThree:null}]},overviewPageOFChapters:{paginationCount:20,paginationItems:[{id:"82991",title:"Diseases of the Canine Prostate Gland",doi:"10.5772/intechopen.105835",signatures:"Sabine Schäfer-Somi",slug:"diseases-of-the-canine-prostate-gland",totalDownloads:0,totalCrossrefCites:0,totalDimensionsCites:0,authors:null,book:{title:"Recent Advances in Canine Medicine",coverURL:"https://cdn.intechopen.com/books/images_new/11580.jpg",subseries:{id:"19",title:"Animal Science"}}},{id:"82956",title:"Potential Substitutes of Antibiotics for Swine and Poultry Production",doi:"10.5772/intechopen.106081",signatures:"Ho Trung Thong, Le Nu Anh Thu and Ho Viet Duc",slug:"potential-substitutes-of-antibiotics-for-swine-and-poultry-production",totalDownloads:1,totalCrossrefCites:0,totalDimensionsCites:0,authors:null,book:{title:"Antibiotics and Probiotics in Animal Food - Impact and Regulation",coverURL:"https://cdn.intechopen.com/books/images_new/11578.jpg",subseries:{id:"20",title:"Animal Nutrition"}}},{id:"82905",title:"A Review of Application Strategies and Efficacy of Probiotics in Pet Food",doi:"10.5772/intechopen.105829",signatures:"Heather Acuff and Charles G. 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She obtained her Ph.D. in Veterinary Sciences from the University of Trás-os-Montes e Alto Douro, Portugal. After almost 32 years of teaching at the University of Trás-os-Montes and Alto Douro, she recently moved to the University of Évora, Department of Veterinary Medicine, where she teaches in the field of Animal Reproduction and Clinics. Her primary research areas include the molecular markers of the endometrial cycle and the embryo–maternal interaction, including oxidative stress and the reproductive physiology and disorders of sexual development, besides the molecular determinants of male and female fertility. She often supervises students preparing their master's or doctoral theses. She is also a frequent referee for various journals.",institutionString:null,institution:{name:"University of Évora",institutionURL:null,country:{name:"Portugal"}}}]},{type:"book",id:"7144",title:"Veterinary Anatomy and Physiology",subtitle:null,coverURL:"https://cdn.intechopen.com/books/images_new/7144.jpg",slug:"veterinary-anatomy-and-physiology",publishedDate:"March 13th 2019",editedByType:"Edited by",bookSignature:"Catrin Sian Rutland and Valentina Kubale",hash:"75cdacb570e0e6d15a5f6e69640d87c9",volumeInSeries:2,fullTitle:"Veterinary Anatomy and Physiology",editors:[{id:"202192",title:"Dr.",name:"Catrin",middleName:null,surname:"Rutland",slug:"catrin-rutland",fullName:"Catrin Rutland",profilePictureURL:"https://mts.intechopen.com/storage/users/202192/images/system/202192.png",biography:"Catrin Rutland is an Associate Professor of Anatomy and Developmental Genetics at the University of Nottingham, UK. She obtained a BSc from the University of Derby, England, a master’s degree from Technische Universität München, Germany, and a Ph.D. from the University of Nottingham. She undertook a post-doctoral research fellowship in the School of Medicine before accepting tenure in Veterinary Medicine and Science. Dr. Rutland also obtained an MMedSci (Medical Education) and a Postgraduate Certificate in Higher Education (PGCHE). She is the author of more than sixty peer-reviewed journal articles, twelve books/book chapters, and more than 100 research abstracts in cardiovascular biology and oncology. She is a board member of the European Association of Veterinary Anatomists, Fellow of the Anatomical Society, and Senior Fellow of the Higher Education Academy. Dr. Rutland has also written popular science books for the public. https://orcid.org/0000-0002-2009-4898. www.nottingham.ac.uk/vet/people/catrin.rutland",institutionString:null,institution:{name:"University of Nottingham",institutionURL:null,country:{name:"United Kingdom"}}}]},{type:"book",id:"8524",title:"Lactation in Farm Animals",subtitle:"Biology, Physiological Basis, Nutritional Requirements, and Modelization",coverURL:"https://cdn.intechopen.com/books/images_new/8524.jpg",slug:"lactation-in-farm-animals-biology-physiological-basis-nutritional-requirements-and-modelization",publishedDate:"January 22nd 2020",editedByType:"Edited by",bookSignature:"Naceur M'Hamdi",hash:"2aa2a9a0ec13040bbf0455e34625504e",volumeInSeries:3,fullTitle:"Lactation in Farm Animals - Biology, Physiological Basis, Nutritional Requirements, and Modelization",editors:[{id:"73376",title:"Dr.",name:"Naceur",middleName:null,surname:"M'Hamdi",slug:"naceur-m'hamdi",fullName:"Naceur M'Hamdi",profilePictureURL:"https://mts.intechopen.com/storage/users/73376/images/system/73376.jpg",biography:"Naceur M’HAMDI is Associate Professor at the National Agronomic Institute of Tunisia, University of Carthage. He is also Member of the Laboratory of genetic, animal and feed resource and member of Animal science Department of INAT. He graduated from Higher School of Agriculture of Mateur, University of Carthage, in 2002 and completed his masters in 2006. Dr. M’HAMDI completed his PhD thesis in Genetic welfare indicators of dairy cattle at Higher Institute of Agronomy of Chott-Meriem, University of Sousse, in 2011. 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Possible contributions can address (but are not limited to) the following research topics: Bioinspired design and control of exoskeletons, orthoses, and prostheses; Experimental evaluation of the effect of assistive devices (e.g., influence on gait, balance, and neuromuscular system); Bioinspired technologies for rehabilitation, including clinical studies reporting evaluations; Application of neuromuscular and biomechanical models to the development of bioinspired technology.',annualVolume:11404,isOpenForSubmission:!0,coverUrl:"https://cdn.intechopen.com/series_topics/covers/8.jpg",editor:{id:"144937",title:"Prof.",name:"Adriano",middleName:"De Oliveira",surname:"Andrade",fullName:"Adriano Andrade",profilePictureURL:"https://s3.us-east-1.amazonaws.com/intech-files/0030O00002bRC8QQAW/Profile_Picture_1625219101815",institutionString:null,institution:{name:"Federal University of Uberlândia",institutionURL:null,country:{name:"Brazil"}}},editorTwo:null,editorThree:null,editorialBoard:[{id:"49517",title:"Prof.",name:"Hitoshi",middleName:null,surname:"Tsunashima",fullName:"Hitoshi Tsunashima",profilePictureURL:"https://s3.us-east-1.amazonaws.com/intech-files/0030O00002aYTP4QAO/Profile_Picture_1625819726528",institutionString:null,institution:{name:"Nihon University",institutionURL:null,country:{name:"Japan"}}},{id:"425354",title:"Dr.",name:"Marcus",middleName:"Fraga",surname:"Vieira",fullName:"Marcus Vieira",profilePictureURL:"https://s3.us-east-1.amazonaws.com/intech-files/0033Y00003BJSgIQAX/Profile_Picture_1627904687309",institutionString:null,institution:{name:"Universidade Federal de Goiás",institutionURL:null,country:{name:"Brazil"}}},{id:"196746",title:"Dr.",name:"Ramana",middleName:null,surname:"Vinjamuri",fullName:"Ramana Vinjamuri",profilePictureURL:"https://mts.intechopen.com/storage/users/196746/images/system/196746.jpeg",institutionString:"University of Maryland, Baltimore County",institution:{name:"University of Maryland, Baltimore County",institutionURL:null,country:{name:"United States of America"}}}]},{id:"9",title:"Biotechnology - Biosensors, Biomaterials and Tissue Engineering",keywords:"Biotechnology, Biosensors, Biomaterials, Tissue Engineering",scope:"The Biotechnology - Biosensors, Biomaterials and Tissue Engineering topic within the Biomedical Engineering Series aims to rapidly publish contributions on all aspects of biotechnology, biosensors, biomaterial and tissue engineering. We encourage the submission of manuscripts that provide novel and mechanistic insights that report significant advances in the fields. Topics can include but are not limited to: Biotechnology such as biotechnological products and process engineering; Biotechnologically relevant enzymes and proteins; Bioenergy and biofuels; Applied genetics and molecular biotechnology; Genomics, transcriptomics, proteomics; Applied microbial and cell physiology; Environmental biotechnology; Methods and protocols. Moreover, topics in biosensor technology, like sensors that incorporate enzymes, antibodies, nucleic acids, whole cells, tissues and organelles, and other biological or biologically inspired components will be considered, and topics exploring transducers, including those based on electrochemical and optical piezoelectric, thermal, magnetic, and micromechanical elements. Chapters exploring biomaterial approaches such as polymer synthesis and characterization, drug and gene vector design, biocompatibility, immunology and toxicology, and self-assembly at the nanoscale, are welcome. Finally, the tissue engineering subcategory will support topics such as the fundamentals of stem cells and progenitor cells and their proliferation, differentiation, bioreactors for three-dimensional culture and studies of phenotypic changes, stem and progenitor cells, both short and long term, ex vivo and in vivo implantation both in preclinical models and also in clinical trials.",annualVolume:11405,isOpenForSubmission:!0,coverUrl:"https://cdn.intechopen.com/series_topics/covers/9.jpg",editor:{id:"126286",title:"Dr.",name:"Luis",middleName:"Jesús",surname:"Villarreal-Gómez",fullName:"Luis Villarreal-Gómez",profilePictureURL:"https://mts.intechopen.com/storage/users/126286/images/system/126286.jpg",institutionString:null,institution:{name:"Autonomous University of Baja California",institutionURL:null,country:{name:"Mexico"}}},editorTwo:null,editorThree:null,editorialBoard:[{id:"35539",title:"Dr.",name:"Cecilia",middleName:null,surname:"Cristea",fullName:"Cecilia Cristea",profilePictureURL:"https://s3.us-east-1.amazonaws.com/intech-files/0030O00002aYQ65QAG/Profile_Picture_1621007741527",institutionString:null,institution:{name:"Iuliu Hațieganu University of Medicine and Pharmacy",institutionURL:null,country:{name:"Romania"}}},{id:"40735",title:"Dr.",name:"Gil",middleName:"Alberto Batista",surname:"Gonçalves",fullName:"Gil Gonçalves",profilePictureURL:"https://s3.us-east-1.amazonaws.com/intech-files/0030O00002aYRLGQA4/Profile_Picture_1628492612759",institutionString:null,institution:{name:"University of Aveiro",institutionURL:null,country:{name:"Portugal"}}},{id:"211725",title:"Associate Prof.",name:"Johann F.",middleName:null,surname:"Osma",fullName:"Johann F. 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