Как выбрать гостиницу для кошек
14 декабря, 2021
Rida Rehman and Alvina Gul Kazi
Contents
9.1 Introduction…………………………………………………………………………………………………….. 142
9.2 Green Management of Sugarcane……………………………………………………………………………. 142
9.3 Traits of Sugarcane Straw…………………………………………………………………………………….. 143
9.3.1 Straw Quality and Availability…………………………………………………………………… 143
9.3.2 Recovery of Straw and Its Final Use………………………………………………………….. 144
9.4 Agronomic Issues……………………………………………………………………………………………… 146
9.4.1 Erosion of Soil……………………………………………………………………………………… 146
9.4.2 Impact of Water…………………………………………………………………………………….. 148
9.4.3 Soil Stocks of Carbon……………………………………………………………………………… 149
9.5 Additional Impingement……………………………………………………………………………………… 151
9.6 Final Remarks…………………………………………………………………………………………………. 152
References…………………………………………………………………………………………………………… 153
Abstract For centuries now, sugarcane is being cultivated and is acting as a source of sugar production. This production is the source of many breeding programs all around the world. The sugarcane straw usually considered as trash is normally burned or is left in the soil depending on the harvesting system. There is an immense amount of straw being wasted yearly. Besides utilizing the straw for energy production or its requirement, there are a lot of other agronomic benefits that enhance the possibility of the straw blanket placed/left on the ground including protection of soil avoiding erosion, increasing organic ratio of content of carbon in the soil, inhibition of growth of weed, recycling of nutrients in textile fiber, and soil water reduction. Although consumption of sugarcane is very popular worldwide, certain factors are to be kept in mind regarding postharvest storage of
R. Rehman • A. G. Kazi (*)
Atta-ur-Rahman School of Applied Biosciences (ASAB), National University of Sciences and Technology (NUST), Islamabad, Pakistan e-mail: alvina_gul@yahoo. com
K. R. Hakeem et al. (eds.), Biomass and Bioenergy: Processing and Properties,
DOI 10.1007/978-3-319-07641-6_9, © Springer International Publishing Switzerland 2014 stalk that involves enzymatic browning. This chapter focuses on ways sugarcane straw can be utilized as a primary source for the production of products having great agronomic value. Balancing the pros of keeping sugarcane fields with a percentage of straw, which significantly outnumber the cons, economists are keen to find out beneficial properties and economic aspects of keeping straw on the ground rather than using it all as possible energy source. The most challenging factor is to maintain the straw quality rendering it useful.
Keywords Sugarcane straw • Soil • Agronomic benefits • Energy • Carbon content
For many centuries, sugarcane has been cultivated. Many breeding programs, all over the world, are driven by production of sugar that resulted in the so-called noble varieties of sugarcane being commercially used at present. Initially, a high value specialty, sugar has now gained laurel of being one of the cheapest calorie food due to immense and rigorous reduction in the cost of its production. Sugarcane is known to be a food crop of high yield. It has also been demonstrated as a splendid feedstock for energy because of its high content of primary content per mg of cane. For whole sugarcane (140 kg of straw included; dry basis), higher heating value (HHV) is 7.4 GJ mg-1 of stalks of cane (which include moisture content up to 70 %), based on average quality of Brazilian cane. The amount of primary energy produced by energy products such as ethanol and bagasse is nearly 2.2 GJ mg-1 or less than 30 % (Leal 2007). Bagasse is the fibrous residue obtained from extraction of juice on industrial scale. Bagasse is consumed in the boiler mills in order to fulfill the energy demand of the mill. In the preharvest, the fibers in the leaves and tops of sugarcane known as straw or trash are normally burned. In the case of nonmechanized harvesting operations, i. e., manual harvesting, the cost of harvesting sugarcane is reduced by practices, which include burning of sugarcane in order to facilitate harvesting and transportation.
Due to certain agronomic, economic, and environmental reasons, mechanical operations have taken over the manual harvesting of sugarcane with dry leaves maintenance (straw) on the ground, in a system named as green cane management in Brazil.
12.6.1 Destructive Sampling-Based Biomass Estimation
Estimating the total biomass in forest ecosystems is challenging due to the difficulties associated with the assessment of carbon stocks below-ground. The above-ground biomass can be easily estimated with highest accuracy in most cases; however, the below-ground biomass estimation is still labour intensive and time consuming. To overcome these limitations, the destructive sampling approach was introduced. The first step in this method involves the chopping of selected trees within some definite plots or transects, and digging out their root systems in order to establish the biomass above — and below-ground with the highest possible accuracy. Further, the field inventory measurements are collected by making use of the tools such as diameter tapes, spring scales, clinometers, pruning saws and shears, shovels, measuring tapes, field data recording accessories and paper bags (Avitabile et al. 2008; Chidumayo 1997; Japanese International Cooperation Agency JICA 2005). In the following step, the segments of stems and branches are weighed first in wet form in the field itself and then in an oven dried form in the laboratory for different significant purposes (De Gier 2003; Nogueira etal. 2008). Up to this level of data analysis provides cumulative information about the biomass levels per tree (both above — and below-ground). To obtain the complete information in a broad way to the whole area of interest by destructive sampling approach, the Allometry equation is employed.
Some rigid carbon materials like carbon nanotubes, graphene, ordered mesoporous carbon, and activated carbon are relatively hard to be sulfonated. Concentrated H2SO4 and fuming H2SO4 are used as the sulfonating agents. However the CBSC prepared with fuming H2SO4 possess much higher catalytic activity (Dehkhoda et al. 2010; Kastner et al. 2012). Researchers have extensively studied the influence of different parameters like sulfonating agent, sulfonation time, and carbon precursor on the activity of such catalysts by direct sulfonation. Directly pyrolysis of the carbon precursors and sulfonation is concentrated at high H2SO4 temperatures, produces sulfonated carbons with low in acid density, lower specific surface area, and poor reusability (Konwar et al. 2013). Figure 15.5 shows the way for the preparation of SO3H-carbon (Konwar et al. 2014).
Studies also indicated that the catalytic activity is primarily determined by total acid density, — SO2H density, surface functional groups, and pore structure. It is established that a high — SO3H density and pore volume favored high activity. These properties in turn are directly influenced by the carbonization temperature (Konwar et al. 2014). Apart from these there are numerous other reports on the preparation of similar sulfonated carbons catalysts, by one-step hydrothermal carbonization/
Fig. 15.6 Proposed schematic structure of the sulfonated carbon materials. Adapted from Okamura et al. (2006), with permission |
Fig. 15.7 Amorphous car bearing SO3H groups as an insoluble Bronsted acid available for various acid-catalyzed reactions (Nakajima and Hara 2012, with permission) |
sulfonation (Xiao et al. 2010), polymerization followed by sulfonation and carbonization (Zhao et al. 2010) , by the thermal treatment of p-toluene sulfonic acid (Zhang et al. 2010) etc.
Here we discussed different system of microalgal biomass production, their problems and future considerations, which is summarized in Table 18.2.
Open pond production is achieved through using a special type of pond called “raceway pond” that is a shallow artificial pond and is commonly used for the cultivation of microalgae. The pond is formed into a rectangular grid, containing an oval channel resembling to an automotive raceway circuit. From an aerial view, many ponds look like a rounded-corner maze (like a puzzle in which we find the way in a closed circuit). It contains a paddle wheel to make the water flow continuously around the circuit (Fig. 18.2).
Raceway ponds (RP) have been used for mass culture of microalgae (Acien Fernandez et al. 1999) since last six decades. A best suited RP for microalgal cultivation is usually 0.3 m deep. Paddle wheel provides mixing and circulation of water in the pond. They are built with solid concrete to avoid water seepage and the floor is lined with a white sheet for enhanced light reflection (to improve the light use efficiency in photosynthesis). Culture is fed continuously in front of paddle wheel during day light and broth is harvested on completion of the loop behind the paddle wheel. The continuous (24/7) operation of paddle wheel prevents the culture sedimentation (Spolaore et al. 2006). Evaporation of water from the RP is a necessary evil, because it is source of water loss but also helps to maintain temperature. Because, in summer cooling effect of evaporation lowers the temperature and in winter heat-retaining capacity of water does not allow the temperature to go too low. Overall, mitigation of water loss in raceway ponds due to seepage and evaporation is an engineering challenge.
Contamination of heterotrophic microbes is another offending challenge in open cultivation systems since it may strongly influence microalgae productivity as the contaminant microbes (bacteria, fungi etc.) become parasite on microalgae. Moreover, RPs may have poor mixing of atmospheric CO2 and least penetration of sunlight (because waste water has a dark color) keeping most of the cells in dark zone. Subsequently, low biomass is produced as compared to the theoretical yield calculated for a raceway pond based on its engineering dimensions. The mixing may be improved by using an aeration system and light penetration may be enhanced by decreasing the depth of pond (maybe 0.2 m instead of 0.3 m). Despite these facts,
Cultivation |
Type of |
|||
system |
bioreactor |
Advantages/benefits |
Challenges/problems |
Considerations/future prospects |
Closed |
Tubular |
• Efficient light utilization |
• Difficult to clean in case of growth |
• The investment cost of the closed |
Cultivation |
photo- |
of microalgae on walls |
photo-bioreactors may be covered by |
|
systems |
bioreactor |
cultivating microalgae capable of producing high-value products |
||
• Suitable for outdoor cultures |
• Expensive installation |
• Use of synthetic biology and |
||
• Relatively cheap |
• Requires large land space |
metabolic pathway engineering may |
||
• Biomass productivity is higher |
• Gradients of pH, dissolved oxygen and C02 |
be used to address the problems such |
||
along the tubes |
as wall growth, temperature |
|||
• Relatively controlled environment |
• Inside temperature may rise in summer due to glass-house effect |
sensitivity |
||
Flat-panel |
• Biomass productivities are higher |
• Scaling up requires many compartments |
||
photo- |
and is difficult |
|||
bioreactor |
• Low oxygen buildup |
• Difficult temperature control especially day-night variation |
||
• Readily tempered |
• Hydrodynamic stress on walls |
|||
• Efficient light utilization • Relatively cheap • Easy cleaning and maintenance |
• Wall growth may occur |
|||
Column |
• High mass transfer |
• Light use efficiency may be low |
||
photo- |
• Low energy consumption |
• Expensive as compared to open ponds |
||
bioreactor |
• Efficient mixing |
• Sophisticated construction makes |
||
• Low shear stress • Easy to sterilize • Good for immobilization • Reduced photo-inhibition • Photo-oxidation threats |
commercialization difficult |
Brennan and Owende (2010), Ugwu et al. (2008), Singh et al. (2011), Park et al. (2011a), Santiago et al. (2013), Saqib et al. (2013) |
production of microalgal biomass for making biodiesel has been extensively studied in RPs (Sheehan et al. 1998) . Although RPs have a low biomass productivity compared with photo-bioreactors yet they balance the equation by lowering the cost of production (Terry and Raymond 1985).
Bamboo processing is a lengthy process and has the following requirements:
1. Machine for separating rough bamboo fiber
2. High temperature pressure-cooking pot
3. Pool for bleaching and softening
4. Steam boiler
5. Equipments for washing
6. Drying room
7. Dehydrator
Table 2.1 Yield and quality of bamboo fibers depending upon their processing technique
|
Several technologies are available for the processing of bamboo fibers. Each of them has its own merits, demerits, and specifications and employs a different process. The following paragraphs include the details of the five of the technologies used for the processing of the bamboo.
1. Although the cultivation of abaca plants is being currently practiced on large scale in Philippines, Ecuador, and other adjacent areas where its plantation is done in the humid regions having an altitude upto 500 m, the studies have also revealed that its cultivation could be extended upto 1,000 m latitudinal extent which is suggestive of the fact that there is a great scope for expanding the cultivation practice of abaca in other neighboring regions or regions with similar climatic conditions so that its production could be increased to the extent that the gap between the demand and supply will be minimized or nullified.
2. Abaca plants in Philippines are generally propagated from vegetative propagules or seeds in a traditional way (without any modern agricultural practice). However, the recent studies have revealed that the use of fertilizers leads to enhancement of growth in abaca thereby paving way for higher fiber yields. Moreover, FIDA (Philippines) is also providing the micropropagated plant material for successful cultivation of abaca.
3. Although about 200 varieties of abaca are known to exist, only a few varieties are cultivated on commercial scale because most of the varieties are either low — yielding or yield fiber of inferior quality. Now, NARC (National Abaca Research Centre, Philippines) and FIDA have been and are promoting research programs so that better (high yielding and good fiber quality) varieties will be introduced to overcome the problem.
4. Keeping in view the advantages of abaca fibers and the processed products over synthetic ones, there is a great expectation that there will be a continuous increase in its demand in the national and international markets. To manage the increasing demands, the most important thing is to increase the supplies but during the last few years, the trend in abaca supply or production has been found otherwise. The main reasons have been found to be the low-income generation from the abaca cultivation, burdensome fiber extraction, and the natural calamities like typhoon or disease-incidence. As far as the income generation (for farmers) and fiber extraction is concerned, the Philippine government as well as the agencies like FIDA and NARC has a role to play. For the control of disease-incidence, different conventional plant breeding approaches coupled with the modern biotechnological techniques should be employed to produce disease-resistant varieties as has been recently initiated in two abaca cultivars Tangongon (TG) and Tinawagan Pula (TP) to produce virus-resistant (BBTV and BBrMV) abaca cultivars.
5. Abaca fiber is considered as the strongest natural fiber and known for its exceptional mechanical strength, durability, and long fiber length. It is because of these properties that it has become an important raw material for various industries like paper and pulp industry, furnishing industry, textile industry, automobile industry, etc. where it is being used in the production of many industrial or domestic products like cordage products, fabrics, speciality papers, bank notes, carpets, rugs, baskets, fiber boards, insulators (for wires/ cables), and automobile components. It is also used as a fuel (Musafel). As per the estimates, paper and pulp industry consumes maximum share (about 80 %) of the fiber production. With the advancement in technology, currently the production of abaca-reinforced polymers is gaining more importance due to their superiority over pure fibers and the synthetic counterparts like nylon, rayon, etc. Keeping in view the above mentioned applications of abaca fibers in various industrial or domestic activities, it has a great potential to be used as an important renewable bio-resource.
6. The production of abaca fibers or its composites is eco-friendly, energy — efficient, and biodegradable, thereby posing no major threat to the environment. Moreover, abaca plantations have been used to control soil erosion and to promote biodiversity rehabilitation. Wastes produced from abaca plant find its use as organic fertilizer to maintain the fertility of soil.
In conclusion, it can be stated that the abaca industry holds a great scope in national as well as international markets providing employment or economic benefits to a large number of people (including farmers, traders, exporters, manufacturers, etc.). The production of high-quality fibers by industrial units creates multiple job opportunities and increase in the income of farmers and laborers. Being renewable natural fiber and superior in qualities, its market demand is expected to strengthen as far as its industrial applications are concerned. Also, the use of abaca fiber composites for automotive and other industrial applications carries ecological as well as economic benefits, thereby leading to sustainable development program. As abaca is mainly grown in Philippines and other adjacent areas, both government and the private sector should coordinate and extend its support in developing the abaca markets at the domestic and international level so that its unfulfilled potential will be attained in future.
As the “low-carbon” concept prevails, abundant kapok fiber has received increasing attention as an eco-friendly textile material for its intrinsic superiorities such as finest and lightest quality, highest hollowness, and most warm nature. With the focus on this green cellulosic fiber, more studies will be carried out to expand the application fields for kapok fiber by combining its higher hollowness and hydrophobic — oleophilic characteristics.
Acknowledgment We are grateful for the support of the National Natural Science Foundation of China (No. 21107116).
10.3.1 Thermosetting Phenol Formaldehyde Resin
Thermosetting and thermoplastic polymers are usually used for making natural fibre composites. These both types of polymers have different applications for their versatile properties. Both polymers have structural similarity as they contain long chains. But the major difference is that thermosetting polymers possess
Table 10.2 Mechanical properties of thermosetting plastics
|
cross-linking chain which gives higher tensile strength and rigidity. That is why they are usually used in structural application and thermoplastics are considered for nonstructural products (Ganga Rao et al. 2007). The application of thermosetting polymers in natural fibre composites is shown in Table 10.2. Thermoset polymers, those that are used as matrices in composites, have sufficient viscosity to flow at some point during the cure process. They can be cast into plate forms to provide blanks. The finished specimens can be machined or moulded into even more complex geometries if necessary to create net-dimension specimens (Fig. 10.3).
The properties and structure of thermosetting resins mostly depends on polycondensation condition. A number of polycondensation resins such as polyester, polyurethane, melamine formaldehyde, urea formaldehyde (UF) and phenol
Processing technique |
Fibre |
References |
Hand lay-up method |
Short banana fibre |
El-Zawawy and Ibrahim (2003) |
Hand lay-up method + compression moulding |
Short banana fibre |
Joseph et al. (2002) |
Compression moulding |
Sisal fibre |
Lu et al. (2006) |
Injection moulding |
wood powder, flax, pulp, glass |
Nystrom et al. (2007) |
Resin transfer moulding |
Glass fibre |
Yan et al. (2002) |
Pultrusion |
Glass fibre |
Ben and Shoji (2003) |
formaldehyde (PF) are commercially available today (Pizzi et al. 1999). Among them, phenolic resins are well known for their tremendous mechanical properties, chemical resistance, thermal stability and strong adhesive capacity (Satapathy and Bijwe 2006; Park et al. 2006). This resin has been keeping its outstanding performance in synthetic polymer industry from the last 90 years (Shafizadeh et al. 1999). Resol is the commercial name of PF resin, which is produced by polycondensation reaction of formaldehyde and phenol under alkaline medium. A wide range of uses in wood industry, impregnation, thermal insulation and moulding is found for its highly cross-linked, versatile, cure capability and stable nature (Holopainen et al. 1997).
In case of heterotrophic cultivation, the culture has a high chance of getting contaminated especially in open pond cultivations. Apart from this, carbon source is also purchased at a high cost. Photoautotrophic system of algae cultivation is the most frequently used method for biomass growth. It is easy to scale up and can easily take carbon dioxide from the surface air.
There are two main cultivation systems used for the production of algal biomass:
The average volumetric yield for this system lies between 0.06 and 0.42 g/L per day. The efficiency of the system depends upon the configuration of the pond and the algal specie that is being cultivated. Open tanks or naturally existing water bodies (ponds, lakes, lagoons, etc.) are collectively termed as open ponds and are unproblematic to construct and maneuver. These ponds are kept shallow for the easy penetration of solar radiations. Water and nutrients are continuously circulated in the culture. Output of the pond is measured by calculating the biomass produced each day per unit area. Circular ponds and raceways have an area of about 1 ha whereas extensive ponds can be about 200 ha. Artificial open ponds are further categorized as:
Enzymatic hydrolysis is the best procedure for degrading cellulose into reducing sugars. It depends on the temperature, time, pH, enzyme loading, and concentration of substrate during the hydrolysis. Hydrolysis and fermentation can be done together for reducing time and avoiding end product inhibition. This process is called simultaneous saccharification and fermentation. Three types of cellulolytic enzymes such as endo-p-1,4-glucanases, cellobiohydrolases, and p-glucosidases are required for enzymatic hydrolysis of cellulose. Duff and Murray (1996) reported that various types of enzymes such as xylanase, b-xylosidase, glucuronidase, acetylesterase, galactomannanase, and glucomannanase are necessary for breaking down the hemicelluloses. Bacteria and fungi are used for enzymatic hydrolysis, but Aspergillus and Trichoderma genera are widely used for enzymatic hydrolysis for cellulose production. The enzyme source is a major effect for effective hydrolysis.
16.5.1 Detoxification ofHemicellulosic Hydrolysate
There are several methods that can be used to detoxify the hydrolysates during ethanol production. These methods are membrane use, ion exchange resins, evaporation, neutralization, and activated charcoal which have been used for ethanol production. The ion exchange resins process are the most effective detoxification method that can remove lignin-derived inhibitors and acetic acid and significantly improve the yield of fermentation (Chandel et al. 2011). This method can be regenerated and reused without disturbing any treatment. On the other hand, adsorption of activated charcoal is widely used to detoxify for lower cost and efficient inhibitor compound removal. This method can remove only phenolic compounds that cannot change the fermentable sugar levels (Canilha et al. 2008). The success of this method depends on charcoal and hydrolysates ratio, contact time, pH, and temperature (Mussatto and Roberto 2004).