Summary of the examples of previous studies onTiO2 photocatalyst
\\n\\n
Released this past November, the list is based on data collected from the Web of Science and highlights some of the world’s most influential scientific minds by naming the researchers whose publications over the previous decade have included a high number of Highly Cited Papers placing them among the top 1% most-cited.
\\n\\nWe wish to congratulate all of the researchers named and especially our authors on this amazing accomplishment! We are happy and proud to share in their success!
Note: Edited in March 2021
\\n"}]',published:!0,mainMedia:{caption:"Highly Cited",originalUrl:"/media/original/117"}},components:[{type:"htmlEditorComponent",content:'IntechOpen is proud to announce that 191 of our authors have made the Clarivate™ Highly Cited Researchers List for 2020, ranking them among the top 1% most-cited.
\n\nThroughout the years, the list has named a total of 261 IntechOpen authors as Highly Cited. Of those researchers, 69 have been featured on the list multiple times.
\n\n\n\nReleased this past November, the list is based on data collected from the Web of Science and highlights some of the world’s most influential scientific minds by naming the researchers whose publications over the previous decade have included a high number of Highly Cited Papers placing them among the top 1% most-cited.
\n\nWe wish to congratulate all of the researchers named and especially our authors on this amazing accomplishment! We are happy and proud to share in their success!
Note: Edited in March 2021
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Examples of previous studies about TiO2 photocatalytic reactions are listed in Table 1. A nanoparticle (NP) of TiO2 also demonstrates photocatalytic activity. Important applications of TiO2 photocatalysts are bactericidal activity [2-4, 6-12] and degradation of chemical pollutants [2-4, 13]. Related physical and chemical mechanisms have been also investigated [2-5, 14-17]. Photo-irradiated TiO2 NPs induce the formation of various reactive species, leading to the damage of biomacromolecules. These reactive species include hole (h+), either free or trapped hydroxyl radicals (OH⋅), superoxide (O2⋅-), hydrogen peroxide (H2O2), and singlet oxygen (1O2), among others. Hydroxyl radicals, O2⋅-, H2O2, and 1O2 are the typical reactive oxygen species. TiO2 photocatalysts have been found to kill cancer cells [18-21] other than bacteria, viruses, and algae under ultraviolet-A (wavelength: 315–400 nm) illumination [2-4, 6-12]. Therefore, one of the potential applications of the TiO2 NP photocatalyst is photodynamic therapy (PDT), which is a promising treatment for cancer and some nonmalignant conditions [22-25]. In general, the mechanism of cytotoxicity by the photocatalysis of TiO2 is based on cell membrane damage via the generation of the aforementioned reactive oxygen species. Furthermore, DNA damage in human cells [26-28], mouse lymphoma cells [29], and phage [30] by the TiO2 NP photocatalyst has been reported. Direct damage of isolated DNA by TiO2 photocatalyst
\n\t\t\t\t | \n\t\t\t\n\t\t\t\t | \n\t\t
Reviews | \n\t\t\t[2], [3], [4], [5] | \n\t\t
Physical experiment | \n\t\t\t[1], [16], [17], [39], [40] | \n\t\t
Chemical compounds | \n\t\t\t[13], [14], [15] | \n\t\t
Nucleic acids | \n\t\t\t[31], [32] | \n\t\t
Microorganism | \n\t\t\t[6], [7], [8], [9], [10], [11], [12], [30] | \n\t\t
Cancer cell | \n\t\t\t[18], [19], [20], [21] | \n\t\t
Mouse lymphoma cells | \n\t\t\t[29] | \n\t\t
Cancer treatment of mouse | \n\t\t\t[20] | \n\t\t
Summary of the examples of previous studies onTiO2 photocatalyst
The crystal of TiO2 is a semiconductor, and the two crystalline forms, anatase and rutile, are well-known (Figure 1) [2-5]. The values of the band gap energy of these crystal forms are 3.26 and 3.06 eV for anatase and rutile, respectively. Photo-irradiation to a TiO2 crystal induces the formation of an excited electron (e-) in the conduction band and an h+ in the valence band, leading to the redox reaction of materials adsorbing on the TiO2 surface, including water and/or molecular oxygen. The photocatalytic reactions with its surface water and oxygen cause the formation of various reactive oxygen species such as free or trapped OH⋅, O2⋅-, H2O2, and 1O2 [2-5].
Band gap energy of the two crystalline forms of TiO2.
An excited electron in the conductive band reduces the oxygen molecule adsorbed on the surface of TiO2 NPs, leading to the generation of various reactive oxygen species as follows (Figure 2):
The reaction (3) is mediated by ultraviolet radiation (hν, wavelength <355 nm), metal ions (Mn+) such as Fe2+, and O2⋅-, as follows [33]:
On the other hand, the formed h+ in the valence band can oxidize water to form OH⋅ as follows:
Furthermore, OH⋅ can produce H2O2 as follows:
Photocatalytic reactive oxygen formation by TiO2.
A photo-irradiated TiO2 NP can induce 1O2 formation. The formation of 1O2 is considered to be an important mechanism of PDT. This reaction can be explained by the following process: O2⋅- formed by TiO2 photocatalysis is reoxidized by the h+ of TiO2 on the particle surface to form 1O2 as follows (Figure 3):
These reactive oxygen species should contribute to the mechanism of the phototoxicity induced by TiO2 NPs.
Photocatalytic 1O2 generation by TiO2
One of the most important medicinal applications of TiO2 NPs is to kill bacteria on its surfaces. TiO2 NPs under ultraviolet radiation produce a strong oxidative effect through the formation of above-mentioned reactive oxygen species and can be used as a photocatalytic disinfectant without other chemical reagents. Fujishima and coworkers reported the bactericidal effect of TiO2 photocatalysts against
Photodynamic therapy, which is a promising and less-invasive treatment for cancer, employs a photosensitizer and visible light to produce oxidative stress in cells and ablate cancerous tumors [22-25]. Photodynamic therapy is also used for treating some nonmalignant conditions that are generally characterized by the overgrowth of unwanted or abnormal cells. In general, porphyrins are used as photosensitizers under visible-light irradiation, since the human tissue has relatively high transparency for visible light, especially red light, and visible light has hardly any side effects. In the case of visible light PDT, 1O2 is considered an important reactive species for PDT because 1O2 can be easily generated by visible light [41-44]. Critical targets of the generated 1O2 include mitochondria and enzyme proteins. Moreover, DNA is also an important target biomolecule of photosensitized reactions [45-49]. Relevantly, photocatalytic 1O2 generation by TiO2 has been reported [38-40].
TiO2, a nontoxic material, is chemically stable, and demonstrates a phototoxic effect. Therefore, an application of TiO2 for PDT has been investigated [2]. The cytotoxicity of an illuminated TiO2 film electrode for HeLa cells [18,19] and T-24 human bladder cancer cells [21] has been reported. Animal experiments also demonstrated the antitumor effect of TiO2 NPs [20]. This report showed an antineoplastic effect on skin cancer in mouse models.
Cellular DNA damage photocatalyzed by TiO2 NPs was demonstrated by the experiment using cancer cells [18,19,21]. TiO2 NPs can be taken into the cancer cell [27]; however, incorporation into the cell nucleus is difficult [18]. Therefore, it is speculated that the indirect mechanism contributes to DNA damage induced by photo-irradiated TiO2 NPs. Hence, model experiments using isolated DNA were performed [31, 32]. In this section, an example of photocatalytic DNA damage by TiO2 NPs was introduced.
Photo-irradiated TiO2 NPs catalyze DNA damage in the presence of copper(II) ion [31]. Relevantly, copper-aided photosterilization of microbial cells on TiO2 was reported [8]. DNA damage by anatase NPs is more severe than that by rutile NPs. The DNA damage is enhanced by piperidine treatment, because photo-irradiated TiO2 NPs cause not only DNA strand breakage but also base oxidation. In general, hot piperidine cleaves DNA strand at modified base. Photo-irradiated TiO2 NPs induce the formation of piperidine-labile products at the bolded site of 5’-
Sequence specificity of DNA damage photocatalyzed by anatase TiO2 NPs. The 32P-end-labeled 211 base pair DNA fragment (
Formation of 8-oxo-G by the photocatalytic reaction of anatase or rutile NPs. Calf thymus DNA was treated by the photocatalytic reaction of anatase or rutile NPs (365 nm, 10 J cm-2) with 20 μM copper(II) ion in a 10 mM sodium phosphate buffer (pH 7.8). After the photocatalytic reaction, the samples were analyzed with a high-performance liquid chromatography.
Catalase, a well-known scavenger of H2O2, and bathocuproines, a copper(I) ion chelator, inhibit DNA damage photocatalyzed by TiO2 NPs, whereas, typical OH⋅ scavenger cannot inhibit the DNA damage. These results suggest that H2O2 and copper(I) ion participate in DNA damage by photo-irradiated TiO2 NPs. It has been reported that OH⋅ is not the main reactive species involved in DNA damage by H2O2 and copper(I) ions [34-36, 59]. DNA-associated copper(I) ions may generate other oxidants, including a copper–peroxo intermediate, such as Cu(I)-OOH, which is generated from the reaction of H2O2 and copper(I) ions [34-36, 59]. Indeed, methional, which can scavenge Cu(I)-OOH [36, 59], shows inhibitory effect on DNA damage photocatalyzed by TiO2 NPs. The generation of these reactive species may be responsible for the formation of piperidine-labile products and 8-oxo-G.
On the other hand, a high concentration of anatase NPs can catalyze DNA photodamage without copper(II) ions. Typical OH⋅ scavengers, ethanol and sugars, effectively inhibit the DNA photodamage by a high concentration of anatase NPs. The DNA damage induced by photo-irradiated anatase NPs without copper(II) ions is observed at every nucleobases without site specificity. Such DNA damage without sequence-specificity is the typical pattern of OH⋅-mediated DNA damage [34].
A proposed mechanism of DNA damage photocatalyzed by TiO2 NPs is shown in Figure 6. The crystalline forms of TiO2, anatase and rutile, are semiconductors with band gap energies of 3.26 and 3.06 eV, which correspond to the following wavelengths of light: 385 and 400 nm, respectively. When a TiO2 semiconductor NPs absorbs photon with energy greater than their band gap, electrons in the valence band are excited to the conduction band, creating electron-h+ pairs and causing various chemical reactions [2-5]. The electron acts as a reductant, whereas the h+ is a powerful oxidant. In aqueous environments, oxygen molecule can be reduced by the electron into O2⋅-, and water molecule can be oxidized by the h+ into OH⋅. In general, formed O2⋅- can be dismutated into H2O2 by proton. The oxygen reduction may precede the reduction of copper(II) ions under aerobic condition, since the concentration of dissolved oxygen is higher (~250 μM) than that of the copper(II) ion used in this study (20 μM). The copper(II) reduction may be mediated by O2⋅-. Hydrogen peroxide reacts with copper(I) ions to generate other oxidants, including a copper–peroxo intermediate, resulting in the oxidation of DNA bases. Copper ions, which are essential components of chromatin [60,61], are found to bind DNA with high affinity [62,63]. Therefore, copper ions may play an important role in reactive oxygen generation
Proposed mechanism of DNA damage photocatalyzed by TiO2 NPs.
TiO2 NPs might be a potential agent for PDT [22-25]. TiO2 NPs can be incorporated into cancer cells and demonstrate cytotoxicity under photo-irradiation [2-4, 26-28]. Photocatalytic reaction by TiO2 NPs induces a number of functional changes in cell including altered permeability of cellular membranes to potassium and calcium ions, release of RNA and proteins and cytotoxicity [2,18-21]. It has been reported that DNA can be a target biomolecule of the photocatalytic reaction of TiO2 NPs [26-30]. Although incorporation of TiO2 NPs into cell nucleus is difficult [18], the generated H2O2 by a photocatalytic reaction of TiO2 NPs can be easily diffused and incorporated in a cell nucleus, leading to DNA photodamage with metal ions. Relevantly, several studies demonstrated that DNA is a potential target of PDT [47,65,66]. Therefore, the metal-mediated DNA damage through the photocatalysis of TiO2 NPs may participate in cytotoxicity by photo-irradiated TiO2 NPs.
As mentioned above, DNA damage in human cells by TiO2 NPs has also been reported [26-28]. The direct DNA damage by TiO2 NPs photocatalyst
In the case of anatase, a high concentration of TiO2 NPs can damage DNA at every nucleobase by OH⋅ generation in the absence of copper(II) ions. Typical free OH⋅ scavengers inhibited this copper(II)-independent DNA damage. These results indicate that free OH⋅ partly contributes to DNA damage photocatalyzed by TiO2. On the other hand, scavengers of OH⋅, such as a sugar (mannitol), ethanol, and formate, enhanced the copper(II)-dependent DNA damage [31]. These scavengers themselves did not induce DNA damage. Since OH⋅ can oxidize most biomaterials, the oxidized products of biomaterials by the TiO2 photocatalyst may damage DNA via the generation of secondary reactive oxygen species. The addition of sugars, glucose and galactose, which are ubiquitous biomolecules, enhanced the DNA damage photocatalyzed by TiO2 NPs. Enhancement of DNA damage by sugars has seldom been reported, and these sugars themselves could not induce DNA damage. Therefore, the products of the photocatalytic reaction of these sugars by TiO2 NPs is responsible for the copper(II)-dependent damage to DNA. Indeed, the glucose and galactose oxidized by the TiO2 photocatalytic reaction caused DNA damage in the presence of copper(II) ion [37]. The inhibitory effect of various scavengers for DNA damage by the photo-oxidized products of sugars by TiO2 was examined. Catalase inhibited DNA damage by the photocatalyzed glucose, indicating the involvement of H2O2. Bathocuproine, which is a chelator of copper(I) ion, also inhibited DNA damage by the photocatalyzed glucose, suggesting the involvement of copper(I) ion. The free OH⋅ scavengers had no or little inhibitory effect on DNA damage. The inhibitory effect of superoxide dismutase (SOD) was weak, suggesting that O2⋅- itself is not the main reactive species for DNA damage. Similar results were observed in the case of galactose. Fluorometry using folic acid [67] demonstrated the formation of H2O2 from the photocatalyzed sugars (Figure 7). The amount of H2O2 generation was comparable with that of other H2O2-mediated DNA-damaging drugs [68]. H2O2 generation was not observed in the absence of copper(II) ions. These results showed that the oxidized products of sugars generate H2O2 during the reaction with copper(II) ions, resulting in secondary DNA damage.
Hydrogen peroxide generation from photo-oxidized glucose and galactose by TiO2 NPs. The buffer solution with 10 mM sugars was previously irradiated (365 nm, 6 J cm-2) with 100 µg mL-1 anatase NPs. The TiO2 NPs were removed by centrifugation, and the solution containing the oxidized sugars was used. One mL of solution containing the treated sugars and 10 µM of folic acid was incubated (60 min, 37 °C) in the presence of 20 µM copper(II) chloride, and the fluorescence intensity was measured (excitation: 360 nm, detection: 450 nm). The concentration of the generated H2O2 was determined by the calibration curve method.
These sugars act as an electron donor for the photocatalytic reaction [15,37]. Partially oxidized sugars, such as aldehyde compounds, are possibly produced through this photocatalytic oxidation. The mechanism of DNA damage by the photocatalyzed product of sugars is proposed in Figure 8. Aldehydes can generate H2O2 via its further oxidation [69], though these sugars themselves are stable compounds. Many studies have reported DNA damage by H2O2 and copper(II) ions [34-36, 70]. Various chemical compounds, including aldehydes, easily produce O2⋅- through their autoxidation process. The autoxidation is markedly enhanced by copper(II) ion, which is an essential component of chromatin [60, 61]. The formed O2⋅- is rapidly dismutated into H2O2. Although the generated H2O2 itself cannot damage DNA, H2O2 reduces copper(II) into copper(I), leading to the activation of H2O2 through the formation of reactive species, such as Cu(I)-OOH [34-36, 59]. Indeed, methional, a scavenger of Cu(I)-OOH, inhibited the DNA damage. This reactive species cannot be scavenged by the free OH⋅ scavengers; however, it can effectively oxidize the nucleobases [34-36, 59].
Proposed mechanism of secondary DNA damage by photocatalyzed sugars.
Although TiO2 is not likely to be incorporated in a cell nucleus [18], H2O2 generated via a photocatalytic reaction can be easily diffused and incorporated in a cell nucleus. This DNA-damaging mechanism via H2O2 generation may participate in the phototoxicity of TiO2.
In summary, sugars enhance the DNA damage photocatalyzed by TiO2 NPs. This enhancement of DNA damage is due to the secondary generation of a reactive oxygen species, H2O2, which can diffuse in the cell and damage cellular DNA. These findings suggest that the secondary H2O2 generation contributes to the phototoxicity of TiO2 more than the direct formation of reactive oxygen species does.
A contribution of 1O2 in the TiO2 photocatalytic reaction was reported [38]. Singlet oxygen generation by TiO2 photocatalysis has been demonstrated by the emission measurement of 1O2, which is assigned to the transition from 1O2(1Δg) to 3O2(3∑g) [39, 40]. Because 1O2 is considered to be an important reactive species in PDT process [22-25], the clarification of the contribution of 1O2 generated by TiO2 photocatalysis is closely related to a design of photocatalyst for medicinal application. Thus, 1O2 generation in the TiO2 photocatalysis and its importance on biomolecular damage was examined [40].
The typical emission of 1O2 at around 1270 nm was observed during irradiation of TiO2 NPs. Relatively strong emission of 1O2 was observed in nonpolar organic solvents such as dichloromethane. The quantum yield (ΦΔ) of 1O2 generation by TiO2 photocatalysis in ethanol was estimated from the comparison of 1O2 emission intensities by TiO2 NPs and methylene blue (ΦΔ= 0.52) [71] and the absorbance of the TiO2 NP dispersions. Because the scattering by suspended TiO2 NPs makes the calculation of absorbed light intensity complex, the precise estimation of the ΦΔ is difficult. Thus, the ΦΔ was estimated using the apparent absorbance of TiO2 NPs. The calculated value indicates the lowest limit of the ΦΔ by TiO2 photocatalysis in ethanol. The reported lifetime of 1O2 generated via TiO2 photocatalytic reaction is 5 μs [39]. This value is shorter than that by the photosensitized reaction of methylene blue (12 μs) [72]. Since the emission intensity of 1O2 is proportional to its lifetime, the ΦΔ was corrected by the lifetime of 1O2. The estimated value of ΦΔ by both types of TiO2, anatase and rutile, was about 0.02 in ethanol. This value of ΦΔ is enough large to induce oxidative damage to biomolecules. The 1O2 emission in D2O was completely quenched by the addition of SOD, which is the enzyme to dismutate O2⋅- into H2O2. These results can be explained by the fact that 1O2 is formed by the reoxidation of O2⋅-, generated from the photoreduction of oxygen molecules by TiO2 NPs (Figure 3). The intensity of 1O2 emission observed in the case of rutile was significantly larger than that by anatase in D2O. The difference of the 1O2 generation by these two types of TiO2 crystalline forms can be reasonably explained by that in aqueous solution. H2O2 generation proceeds in the photocatalysis of anatase rather than O2⋅- generation, whereas O2⋅- is the main product from oxygen photoreduction mediated by rutile [17]. These results support the mechanism of 1O2 generation via O2⋅- by TiO2 photocatalysis.
The emission spectrum of 1O2 by TiO2 (in both, anatase and rutile type cases) slightly blue-shifted (~4 nm) compared with that by methylene blue. These results suggest that the surroundings of the 1O2 generated on the TiO2 surface are different from that by methylene blue in solution. In the case of the photosensitization of methylene blue, the generated 1O2 deactivates in the homogeneous media of solvents. A possible explanation of the blue-shift is that most of the 1O2 generated by TiO2 NPs deactivates on the TiO2 surface.
The intensity of 1O2 emission by TiO2 photocatalysis in liposome was significantly larger than that in an aqueous solution in both, anatase and rutile type cases. The enhancement of the 1O2 emission can be explained by the elongation of the lifetime of 1O2 or the acceleration of the photocatalytic reaction. This result shows that phospholipids membrane is an important environment of the phototoxic reaction mediated by 1O2 in the photocatalytic reactions of TiO2 NPs. Indeed, high affinity of TiO2 NPs with a cell membrane was reported [18]. Consequently, an environmental effect of a cell membrane is important for the photocatalytic reaction of TiO2 NPs. Since amino acid residues in proteins can be oxidized by 1O2 [42], a membrane protein should be the target biomolecule in cell membrane. Indeed, 1O2 emission was quenched by the addition of bovine serum albumin, a typical water soluble protein, suggesting scavenging of the 1O2 generated by TiO2 photocatalysis through oxidation of protein.
In conclusion, photo-irradiated TiO2 NPs can produce 1O2 through reoxidation of O2⋅-, which is formed by photocatalytic reduction of oxygen molecule on the surface of TiO2 NPs. Since most of the 1O2 deactivated on TiO2 surface, the 1O2 on TiO2 surface cannot induce the oxidation of DNA and NADH. However, the 1O2 generation by TiO2 photocatalysis could be enhanced in the microenvironment of phospholipids membrane. These findings suggest that 1O2 may contribute to phototoxicity of TiO2 NPs through oxidation of membrane protein.
TiO2 NPs photocatalyze DNA oxidation. A relatively small concentration of TiO2 NPs frequently induces tandem base oxidation at guanine and thymine residues through H2O2 generation in the presence of a copper(II) ion. A copper–peroxo complex is considered to be an important reactive species responsible for this DNA damage. In addition, cytosine residues are also photooxidized by TiO2 NPs. In the case of a high concentration of TiO2 NPs, OH⋅ contributes to DNA damage without sequence specificity. In the presence of sugars, TiO2 NPs indirectly induce DNA damage by the secondary H2O2, which is produced through an autoxidation process of the photo-oxidized products of sugars by TiO2 NPs. Furthermore, 1O2 is also produced by photo-irradiated TiO2 NPs. The 1O2 generation is explained by the reoxidation of O2⋅-, which is produced by photocatalytic reduction of the oxygen molecule adsorbed on the surface of TiO2 NPs. The photocatalyzed formation of 1O2 might contribute to the oxidation of the membrane protein. These mechanisms of photocatalytic reactive oxygen formation should be involved in the photocytotoxicity of TiO2 NPs. Because TiO2 is a chemically stable and nontoxic material, the bactericidal activity and cytotoxicity against cancer cells will play more important roles in the field of medical applications of nanomaterials.
The author wishes to thank Professor Shosuke Kawanishi (Suzuka University of Medical Science) for his helpful discussion about DNA damage. The reported works were supported by a Grant-in-Aid for Scientific Research on Priority Areas (417) from the Ministry of Education, Culture, Sports, Science, and Technology (MEXT) of the Japanese Government.
With the increase in population and urbanization, energy use also has grown rapidly worldwide. Energy use in the building sector (commercial and residential buildings) has increased between 20 and 40% in developed countries [1]. Several researchers have worked on moderating the use of fossil fuels by introducing alternative energy sources such as industrial waste heat, biogas and biomass, nuclear energy, geothermal and solar energy, groundwater [2, 3, 4, 5]. The European Union is responsible for 33% of the total CO2 emission [2]. Based on the European Green Deal, the European Commission has provided an action plan to ensure energy transition as the EU aims to become the first climate-neutral continent by 2050 [6]. To oblige with these implications, energy-saving technologies have to be integrated into different energy sectors, especially the building sector since the energy demand is 36% of the global final energy use [7]. Studies have been conducted to analyze the increased use of biomass to reduce CO2 emission in different sectors such as transportation and building sectors [8, 9]. One way of reducing the amount of resource use is to connect several customers’ heat and cold demands with the available sources [10]. District energy systems are said to promise energy security as they offer flexibility in their energy use compared to individual energy systems [11]. The heating or cooling resources can be from renewable sources of energy as well as non-renewable sources.
The cooling energy demand for buildings varies depending on countries and their outdoor temperatures. Buildings have various cooling demands due to the differences in the construction material, size, occupant behavior, the purpose of the building, etc. However, it should be pointed that even identical buildings have different cooling demands depending on the kind of activities within the building. Due to the recent changes in climate and its implications on the energy performance of the buildings and indoor thermal conditions, different space cooling technologies have gained more attention. It is likely to predict the growth of cooling demand in Europe due to rising ambient temperatures (including heat waves), heat island effects, higher thermal insulation levels, increased comfort desires/requirements, and the fact that saturation of cooling demand is significantly lower than in the USA and Asia. Estimated cooling saturation for commercial and residential buildings in the USA was 80 and 65%, respectively, and Japan had 100 and 85%, respectively, in the year 2005. Corresponding cooling saturation numbers for Europe were 27 and 5%, respectively [12]. The cooling saturation for EU27 has passed 40% for the service sector and is around 7% for residential buildings [12]. It has been estimated that 10% of all building areas in EU28 were cooled and covered around 16% of the total cooling demand in the year 2014 [13]. In Europe district cooling was introduced in the 1990s; however, it is still a rather uncommon cooling solution with a market share of only around 1% of the cooling market in 2014 [12].
The desired indoor conditions can be met using individual cooling devices such as air conditioners, central air conditioning systems, or district cooling system (DCS). The district cooling system supplies chilled water for cooling and dehumidification to a group of buildings in a district (city, neighborhood, or campus). The coolant (usually water) is typically generated at a central chiller plant and circulates through a distribution network between a central cooling plant and the buildings in the district [14, 15]. Figure 1 depicts a DCS using a natural source such as a lake/sea to cool the buildings. It is generally referred to as free cooling.
Schematic of a district cooling system (DCS). Reprint with permission from Gävle Energi AB [
Water in the district cooling network gets cold from nearby natural cold sources, such as a river/sea, and if needed from the cooling machines, that is, when the temperature of the cold source (the river) is high. The combination of free-cooling and cooling machines demands less electricity compared to separate heat pumps or cooling machine installations in every building.
Water from the river/sea is used to cool the water in the district cooling network. When the district cooling water is cooled to 6°C, it is pumped to the connected building/consumers through the distribution network that comprises supply and return pipe. The cold and heat carriers in the district network are generally in the form of pressurized water and to be economical, the dense urban areas appear to be a fulfilling choice as the distribution pipes should be short [10].
Cold is delivered to the consumers (offices, buildings, industries, server halls, etc.) through the district cooling network with the help of the heat exchangers at user buildings [17]. Cold can be delivered to the cooling coils (to cool the supply air in the air handling units) or via chilled beams installed in the building zones.
Overall, as seen in Figure 1, four major parts could be introduced in a district heating or cooling system: the main supply unit, distribution networks, user stations, and finally the heating or cooling system inside the building’s zones. Cold can be supplied for industrial purposes too, such as food preparation, although it is beyond the scope of this chapter.
It is possible to incorporate either a single or multiple cooling technologies in the DCS central chiller plant depending on the available energy sources (thermal or electrical), environmental and economic considerations as well as the demand profile. Absorption chillers are among the available options for chiller plants. Absorption chillers use heat and not electricity as their primary source of energy [18]. They possess a lower COP (coefficient of performance); however, the electricity consumption and primary energy use are reduced in these chillers and the mechanical compressor of a compression chiller is substituted by a thermal compressor [19]. Renewable thermal energy such as biomass waste or solar energy could be utilized using heat-driven chillers or thermal power plants. In such plants, the heat could be transferred to electrical or mechanical energy to drive the vapor compression chillers. The triple-effect lithium bromide absorption chillers could be exploited for DCS as they could be driven by higher-grade sustainable heat sources [20].
Free cooling is another option for a central plant. The available natural cold sources are involved in cooling the building; the heat will naturally flow out without the need of the compressor and the vapor-compression refrigeration system [15, 21, 22, 23]. Rivers, lakes, the sea, and outdoor air are among the natural cold sources. By using seawater air conditioning, deepwater conditioning could be employed as in this situation, and the water temperature is well below the ambient temperature (generally around 5°C). For such DCS, it is possible to utilize 100% free cooling. However, given the lack of natural cold sources, free cooling could be combined with other cooling technologies such as absorption chillers to compensate for the lack of available cold from the lake/sea, especially on a seasonal basis. An approach to using naturally cold water is cold district heating and cooling [24]. In this context, the cold water from the lake, sea, etc., is used for direct or active cooling in the system and serves as the cooling fluid. With the help of the decentralized chillers or pumps, the water is chilled or heated for the district system. A research project introduced seawater district cooling and analyzed the system through a case study in Diego Garcia [25]. It was concluded that the system was economically efficient and reduced maintenance and electricity usage.
This book chapter aims to investigate the implementation of district cooling systems by exploring research studies reported in the literature. The topics addressed include typologies and design parameters, benefits and limitations, applications of the system, and the technology readiness level.
To provide an overview of the available district cooling systems and their performance for different applications in various climate conditions, a literature review was performed.
Different databases have been used to identify available books and academic literature, including ScienceDirect, Google Scholar, and Scopus.
Keywords such as district energy, district cooling system, free cooling, absorption chillers, the resilient building were used. No limitation was applied on the publication period, though recently published works were prioritized.
In this section, three different classification groups are proposed. The primary proposed classification is based on the system: Centralized and decentralized DCS. The former category is suitable for large-scale regions where the energy is distributed among several buildings in an area. The latter category is more suitable for small capacities where the energy conversion takes place in the units outside the buildings and then is transferred to the buildings [2, 26, 27, 28].
The second proposed category is based on the central plant: free cooling systems or the use of heat pumps and chillers [29, 30, 31].
The third category is based on the occupant behavior as well as the building typology, which is design parameters that can affect the energy use in the buildings. Occupant behavior mainly consists of interactions with operable windows, lighting, blinds, thermostats, and plug-in appliances. Building types are such as villa, retail, public office.
Literature covers the benefits and limitations (disadvantages) of DCS. These benefits and limitations are categorized from three perspectives; environmental, operational, and economical.
Environmental advantages:
District heating and cooling (DHC) possesses the ability to be integrated with renewable resources, consequently reducing greenhouse gas (GHG) emissions, and saves energy. The central water-cooled chiller plants on the large scale use a lower amount of energy and appear more efficient compared to the on-site small capacity systems [20, 32, 33, 34]. Therefore, DCS appears more successful in dense areas in a city or municipality since nearby these areas, there are generally some natural cooling or waste energy sources available [35]. However, these two criteria can be found in many areas and cities.
A DHC system aims at saving primary energy, electricity, space, inhibiting air pollution, and reducing environmentally harmful refrigerants [36].
A DHC system aims at saving energy and space, and inhibiting air pollution, and helps to eliminate environmentally harmful refrigerants [36, 37].
District cooling can greatly reduce the electricity use and peak power demand, and thus reduce energy use, during the cooling season [35].
Environmental disadvantages:
Depending on the central plants, DCSs may not totally be environmentally friendly as long-term use of the free cooling sources such as sea or lake might affect the temperature of the sources and limit the cooling capacity if no anticipating measures are considered. It also could affect the ecosystem of the sources [38].
A free cooling system uses a vast amount of water, which is a problem in areas lacking water [30].
Operational advantages:
Prevention of intensive use of chillers and machinery space in the user stations [39].
Noise and structure load reduction [39].
Saves space by removing the cooling tower and chiller plant from the buildings or roofs [39].
A wide range of production methods and always the latest type of equipment are integrated with DCS due to mitigation measures against global warming [30, 40].
District cooling has less requirement for technical staff on building level [34].
Operational disadvantages:
Heat loss within the plant itself as well as the building serviced by the DHC due to distribution losses in pipes and heat exchangers is inevitable [41, 42].
Economic advantages:
The transparency of costs and future proof investment due to easy payment of utility bills [30].
The DCS is relatively flexible as different central plants could be utilized based on the fuel cost, therefore reducing the cooling cost [20, 35, 43].
Owned by the municipality, a district cooling system can capture cash flows that were previously paid for imported natural gas or electricity [35].
DCS can provide more job opportunities as it provides more reliable and flexible services by a specialized professional team [39].
Economic disadvantages:
Selection of a system that shows large environmental benefits may, in fact, end up not being economical as both the environmental and economic aspects have to be considered together [32].
In purpose to utilize cogeneration of district system and electricity, larger DHC is required [44].
High initial investment costs and lack of negotiable prices and tariffs from the customer’s side as DCS are often owned by few local energy companies, and there is a risk of monopoly for the cooling prices and tariffs [10].
In this section, DC cooling technologies, energy sources, operational aspects, and the applications of DC systems are reviewed based on implemented DC technologies through published DC design and analysis research. Before heading to the applications of the DC systems, the concept of resilience is introduced.
The resilience of the building is its ability to withstand extreme weather conditions and recover from the possible incurred damages efficiently and quickly [45]. Chen et al. [46] investigated the resilient cooling strategies and Hay [47] investigated resilience as a developing planning tool for communities. District energy was recommended as the technology that can balance the relationship between the communities and the region [47]. Sharifi et al. advocated for developing district energy systems, net-zero buildings, and neighborhoods as criteria for assessing urban energy resilience [48].
Based on a report from International District Energy Association (IDEA) [49], in 2019, 303 buildings and Ca 10.8 million ft2 were added to the district systems, beyond North America, which is a strong growth in the district systems employment. The number of buildings and the area that was used for the system in 2018 correspond to 156 buildings and Ca 50 million ft2. Based on the statistics in [50], 70% of residential end users in high-population areas in Europe were powered by fossil fuel in 2015. Hence, DHC networks show great potentials that can help in decarbonization and improvement of indoor air quality as these systems help to reduce the primary energy use by utilizing renewable sources of energy and reducing the thermal losses [51].
A few studies are introduced to show the performance of DCS through simulation and real data collection in different climate conditions and their effects on building’s cooling loads. The studies that were dedicated to Asian countries are presented to show the diversity of DHC systems as Asian countries are developing more DHC systems to reduce air pollution, primary energy use, etc. Later in this section, research projects dedicated to DHS in Europe are introduced.
A study was conducted on the performance of DCS vs. individual cooling systems (ICS) in Hong Kong considering different chilled water pump schemes [52, 53] for commercial buildings. Based on the simulation results, DCS consumes around 15% less energy compared to ICS. The annual operation cost of DCS also is 10% lower than ICS under the electrical tariffs of Hong Kong.
Energy modeling of DCS was conducted in [14] in the South East Kowloon Development Project in Hong Kong for residential and commercial buildings. Based on the simulation results, chilled water, eutectic salt, and ice storage could respectively result in a 38, 38, and 22% reduction in installed cooling capacity. An et al. [54], Yan et al. [55], and Nagota et al. [56] analyzed the performance of DCS in districts in China and Japan and concluded the energy-saving effect of DCS. Studies were conducted with absorption chillers as the cooling technology in other parts of Asia such as Thailand [57], Turkey [58], Iran [59] and concluded the energy and carbon emission-saving effect of DCS. As it could be seen from the mentioned studies so far, the positive economic implication of the DHC system is generally observed from the conducted studies.
The Scandinavian market is taking the lead with 49 operating DCS, followed by Germany (28 operating DCS) and Italy (14 operating DCS) [30].
A detailed study on the market of DCS in Sweden is done by [60]. Major district cooling systems appear in Stockholm, Gothenburg, Linköping, Solna-Sundbyberg, Lund, and Uppsala. Based on the statistics reported by Energiförtagen [61], deliveries for 2018 totaled 1156 GWh. It was a record year for Swedish district cooling and an increase of 26 percent compared to 2017, due to an exceptionally hot summer. The total length of district cooling pipelines increased to 627 km, while in 2019, deliveries totaled 991GWh. Figure 2 shows deliveries and network length from 1996 to 2019 [61].
District cooling deliveries (GWh) and network length (km) in Sweden [
From Figure 2, and the economic and environmental benefits provided through the expansion of DC capacity, a continued growth in DCS is expected.
Fahlén et al. [62] presented a study based on the DHC system of Gothenburg. Combined heat and power (CHP) plants and excess heat from industries supply about 80% of the heat. The study assesses the potential of absorption cooling technology to improve the economic and environmental performance of the DHC system. The results show potentials for cost-effective CO2 emission reduction.
The use of absorption chillers in a DCS in Sweden was studied in [63, 64] and the energy performance of the system appeared to improve. A DCS was initiated in 1995, in the city center in Södermalm, Stockholm. Later, it was expanded and another area was added to the system. Both the districts are connected by pipes located in lake Mälaren [65]. In the Södermalm DCS, existing heat pumps in Hammarbyverket were used.
DCS design has evolved over the years from for example constant to variable flow in the distribution loop. These evolutions and updates in design practices have continuously been upgraded and employed in the system. A long-term security of supply is a driving factor in the heating/cooling systems especially in DHC since the heat/cold is generally supplied by local units. Therefore, it is important to upgrade the design in such a way as to achieve this aim. To be able to express a general reliability level, a definition has been anticipated as the system reliability rate for a DH system [10]. The rate is regarded as the ratio between the numbers of supplied available district heating to the customers during a year by total hours in a year [10]. Many factors are responsible for low system reliability rates such as the fuel supply, pipe failures in the distribution networks, water leakages caused by corrosion or pressure surges, and power outages. The latter mentioned factor also influences the short-term reliability of the system. All the mentioned incidents affect the resilience of the system. To compensate for the power outage, a backup electricity generation is generally anticipated for the main distribution pump. To measure the technology readiness level also, the U.S. Department of Energy has introduced a method to calculate the readiness level [66].
Another problem associated with DHC systems that affect the resilience of the system is the high delta-T syndrome. Due to several reasons, degradations occur over time, which deteriorates the standard temperature difference between the supply and return water that in turn affects the performance of the system. A research project was conducted on the low delta-T problem of the DCS in Gothenburg, Sweden [67]. The problem was analyzed by collecting operational data from the Gothenburg district cooling system along with chilled water systems from 37 of the connected buildings. The results depicted several solutions in the district cooling system to overcome a low delta-T and increase the return temperature. For instance, it was recommended to comply with the building design guidelines as well as limit the flow on the primary side of the heat exchanger, and this helps to restrict the operation in the saturation zone of the heat exchanger. A similar study was carried out by Henze et al. [68] on two university campuses in Massachusetts and Colorado and proposed a solution that provided additional cooling load to the campuses with the same central plant system. The mentioned issues raise the importance of maintenance of the system since the system has to be able to retain its ability to withstand future shocks such as those mentioned above, as well to extend its technical lifetime to remain resilient.
To quantify the energy efficiency of the DCS, three energy efficiency factors were proposed [55]. These factors are presented using Eqs. (1)-(3) and each is explained in this section.
“Coefficient of performance” of the chiller plant is represented by
SCOP represents the “system coefficient of performance,” which is the overall energy efficiency of the chiller plant and the distribution system (Eq. (3)). Based on the previous studies, 80% of the energy consumed by the chilled water pumps leads to cooling loss, which is due to the chilled water distribution; therefore, it must be accounted for in the calculation process.
Keeping the efficiency of the system aside, the feasibility of a DHC system could be investigated by taking into account the cost analysis. To provide an effective evaluation of the energy system and the cost-effective alternatives, life cycle cost analysis (LCCA) could be considered. The energy performance and cost analysis of DCS have been evaluated in several studies [69, 70, 71].
LCCA takes into account the costs involving the construction, operation, and demolition phases [72]. The life cycle cost (LCC) is as below [71]:
where
The dynamic payback period (PP) of investment, considering the time value of the capital, is calculated using Eq. (6):
where
With the increase in energy demand, especially cooling energy due to climate changes and the rise in comfort requirements in buildings, meeting the future energy demand has gained more attention. Resilient, economic, and environmentally friendly solutions are required to meet the future energy demand. To fulfill the growing cooling demand and the community’s growing concern about carbon footprint reduction and energy resilience, DC systems are becoming increasingly attractive to communities. District energy is a flexible system in terms of the sources as they can accommodate both cooling and heating. The main focus of the chapter was the district cooling systems and it was aimed to outline the possibilities and benefits of using a district energy system specifically the DCS. Three classification groups based on the system, central plant, and occupant behavior were proposed.
DCS can reduce electricity use and peak demands and be integrated with renewable resources, and, therefore, contributes to reducing greenhouse gas emissions and air pollution. Several sources can be used—free cooling together with electricity or thermally driven chillers. These systems are more efficient in more populated districts. Since the coolant is produced in the central chiller plant, not only the use of space in the building is minimized, but the noise pollution also is reduced. District cooling systems have been reported as economic and environmentally friendly solutions to meet the cooling demand of buildings. The investigated studies in this chapter reported a decrease in energy use when DCS was implemented.
The authors declare no conflict of interest.
Funding of the study by the Swedish Energy Agency, Termo program, is greatly acknowledged (District cooling vs. local solutions for space cooling, project number 48296-1, Dnr: 2019-003410).
CHP | combined heat and power plant |
CO2 | carbon dioxide |
COP | coefficient of performance |
COPplant | coefficient of performance of a chiller plant |
DC | district cooling |
DCS | district cooling system |
delta-T | temperature rise of the cooling water |
DH | district heating |
DHC | district heating and cooling |
GHG | greenhouse gases |
ICS | individual cooling system |
SCOP | system coefficient of performance |
Q | cooling supply of a chiller plant |
Wdistri | energy use of a cooling distribution system |
Wplant | energy use of a chiller plant |
WTFdistri | water transport factor |
PWFin | present worth factor |
CIC | initial capital cost |
Cfuel | natural gas cost |
COM | operational and management cost |
CDispose | abandoned equipment cost |
Ccool | cooling cost |
Cheat | heating cost |
Chotwater | hot water cost |
n | life cycle period |
i | interest rate |
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Kim"}],equalEditorOne:null,equalEditorTwo:null,equalEditorThree:null,productType:{id:"1",chapterContentType:"chapter",authoredCaption:"Edited by"}},{type:"book",id:"7661",title:"Heat and Mass Transfer",subtitle:"Advances in Science and Technology Applications",isOpenForSubmission:!1,hash:"c29b5c2ce24925a935ca52b8344fbb99",slug:"heat-and-mass-transfer-advances-in-science-and-technology-applications",bookSignature:"Alfredo Iranzo",coverURL:"https://cdn.intechopen.com/books/images_new/7661.jpg",editedByType:"Edited by",editors:[{id:"67352",title:"Dr.",name:"Alfredo",middleName:null,surname:"Iranzo",slug:"alfredo-iranzo",fullName:"Alfredo Iranzo"}],equalEditorOne:null,equalEditorTwo:null,equalEditorThree:null,productType:{id:"1",chapterContentType:"chapter",authoredCaption:"Edited by"}}],booksByTopicTotal:2,seriesByTopicCollection:[],seriesByTopicTotal:0,mostCitedChapters:[{id:"67726",doi:"10.5772/intechopen.86322",title:"CFD Simulation of Heat and Mass Transfer for Climate Control in Greenhouses",slug:"cfd-simulation-of-heat-and-mass-transfer-for-climate-control-in-greenhouses",totalDownloads:1143,totalCrossrefCites:3,totalDimensionsCites:3,abstract:"Greenhouse plant production involves a number of processes such as transpiration, condensation, photosynthesis, and climate control. Such processes, in turn, set off mass and heat transfer phenomena that influence not only the quality and quantity of crop production but also its environmental cost. While these processes have considerably been analyzed in separate, they strongly interact with one another. For instance, increased radiation (mainly thermal infrared) increases temperature, reduces humidity, consequently increases transpiration, and affects CO2 exchange as well as other reaction rates. Computational fluid dynamics (CFD) is a numerical tool with a solid physical basis which allows, through the construction of a computational model, to simulate the fluid flow environment. Heating, ventilation, and condensation have been analyzed in the greenhouse environment with CFD techniques. The current challenge is the interaction of these processes and their impact on the production system. The present work summarizes some CFD investigations carried out in this topic, in order to analyze the processes of heat and mass transfer in a greenhouse for agronomic purposes.",book:{id:"7661",slug:"heat-and-mass-transfer-advances-in-science-and-technology-applications",title:"Heat and Mass Transfer",fullTitle:"Heat and Mass Transfer - Advances in Science and Technology Applications"},signatures:"Cruz Ernesto Aguilar Rodriguez and Jorge Flores Velazquez",authors:[{id:"173578",title:"Dr.",name:"Jorge",middleName:null,surname:"Flores-Velazquez",slug:"jorge-flores-velazquez",fullName:"Jorge Flores-Velazquez"}]},{id:"66158",doi:"10.5772/intechopen.84706",title:"Numerical Solution to Two-Dimensional Freezing and Subsequent Defrosting of Logs",slug:"numerical-solution-to-two-dimensional-freezing-and-subsequent-defrosting-of-logs",totalDownloads:631,totalCrossrefCites:3,totalDimensionsCites:3,abstract:"Two-dimensional mutually connected mathematical models have been created, solved, and verified for the transient non-linear heat conduction in logs during their freezing and subsequent defrosting. The models reflect the influence of the internal sources of latent heat of both the free and bound water on the logs’ freezing process and also the impact of the temperature on the fiber saturation point of wood species, with whose participation the current values of the thermo-physical characteristics in each separate volume point of the subjected to freezing and subsequent defrosting logs are computed. The chapter presents solutions of the models with explicit form of the finite-difference method and their validation towards own experimental studies. Results from experimental and simulative investigation of 2D non-stationary temperature distribution in the longitudinal section of beech and pine logs with a diameter of 0.24 m and length of 0.48 m during their many hours freezing in a freezer and subsequent defrosting at room temperature are presented, visualized, and analyzed.",book:{id:"7661",slug:"heat-and-mass-transfer-advances-in-science-and-technology-applications",title:"Heat and Mass Transfer",fullTitle:"Heat and Mass Transfer - Advances in Science and Technology Applications"},signatures:"Nencho Deliiski and Natalia Tumbarkova",authors:[{id:"43040",title:"Prof.",name:"Nencho",middleName:"Stanev",surname:"Deliiski",slug:"nencho-deliiski",fullName:"Nencho Deliiski"},{id:"284649",title:"Dr.",name:"Natalia",middleName:"Yordanova",surname:"Tumbarkova",slug:"natalia-tumbarkova",fullName:"Natalia Tumbarkova"}]},{id:"67626",doi:"10.5772/intechopen.86738",title:"The Boundary Element Method for Fluctuating Active Colloids",slug:"the-boundary-element-method-for-fluctuating-active-colloids",totalDownloads:943,totalCrossrefCites:0,totalDimensionsCites:2,abstract:"The boundary element method (BEM) is a computational method particularly suited to solution of linear partial differential equations (PDEs), including the Laplace and Stokes equations, in complex geometries. The PDEs are formulated as boundary integral equations over bounding surfaces, which can be discretized for numerical solution. This manuscript reviews application of the BEM for simulation of the dynamics of “active” colloids that can self-propel through liquid solution. We introduce basic concepts and model equations for both catalytically active colloids and the “squirmer” model of a ciliated biological microswimmer. We review the foundations of the BEM for both the Laplace and Stokes equations, including the application to confined geometries, and the extension of the method to include thermal fluctuations of the colloid. Finally, we discuss recent and potential applications to research problems concerning active colloids. The aim of this review is to facilitate development and adoption of boundary element models that capture the interplay of deterministic and stochastic effects in the dynamics of active colloids.",book:{id:"8416",slug:"non-equilibrium-particle-dynamics",title:"Non-Equilibrium Particle Dynamics",fullTitle:"Non-Equilibrium Particle Dynamics"},signatures:"William E. Uspal",authors:[{id:"279308",title:"Prof.",name:"William",middleName:null,surname:"Uspal",slug:"william-uspal",fullName:"William Uspal"}]},{id:"66487",doi:"10.5772/intechopen.85735",title:"Mean Aspects Controlling Supercritical CO2 Precipitation Processes",slug:"mean-aspects-controlling-supercritical-co-sub-2-sub-precipitation-processes",totalDownloads:750,totalCrossrefCites:1,totalDimensionsCites:2,abstract:"The use of supercritical CO2 is an excellent alternative in extraction, particle precipitation, impregnation and reaction processes due to its special properties. Solubility of the compound in supercritical CO2 drives the precipitation process in different ways. In supercritical antisolvent process, mass and heat transfers, phase equilibria, nucleation, and growth of the compound to be precipitated are the main phenomena that should be taken into account. Mass transfer conditions the morphology and particle size of the final product. This transfer could be tuned altering operating conditions. Heat transfer in non-isothermal process influences on mixing step the size of generated microparticles. In rapid expansion of supercritical solution, phenomena as the phase change from supercritical to a CO2 gas flow, rapid mass transfer and crystallization of the compound, and expansion jet define the morphology and size of the final product. These phenomena a priori could be modulated tuning a large number of operating parameters through the experiments, but the correlations and modeling of these processes are necessary to clarify the relative importance of each one. Moreover, particle agglomeration in the expansion jet and CO2 condensation are determinant phenomena which should be avoided in order to conserve fine particles in the final product.",book:{id:"7661",slug:"heat-and-mass-transfer-advances-in-science-and-technology-applications",title:"Heat and Mass Transfer",fullTitle:"Heat and Mass Transfer - Advances in Science and Technology Applications"},signatures:"Antonio Montes, Clara Pereyra and Enrique J. Martínez de la Ossa",authors:[{id:"55991",title:"Mr.",name:"Antonio",middleName:null,surname:"Montes",slug:"antonio-montes",fullName:"Antonio Montes"},{id:"55992",title:"Dr.",name:"Clara",middleName:null,surname:"Pereyra",slug:"clara-pereyra",fullName:"Clara Pereyra"},{id:"55993",title:"Dr.",name:"Enrique",middleName:null,surname:"Martinez De La Ossa",slug:"enrique-martinez-de-la-ossa",fullName:"Enrique Martinez De La Ossa"}]},{id:"66815",doi:"10.5772/intechopen.84707",title:"Nonequilibrium Statistical Operator",slug:"nonequilibrium-statistical-operator",totalDownloads:749,totalCrossrefCites:1,totalDimensionsCites:1,abstract:"Nonequilibrium statistical physics is concerned with a fundamental problem in physics, the phenomenon of irreversibility, which is not rigorously solved yet. Different approaches to the statistical mechanics of nonequilibrium processes are based on empirical assumptions, but a rigorous, first principle theory is missing. An important contribution to describe irreversible behavior starting from reversible Hamiltonian dynamics was given by Zubarev, who invented the method of the nonequilibrium statistical operator (NSO). We discuss, in particular, the extended von Neumann equation and the entropy concept in this approach. The method of NSO proved to be a general and universal approach to different nonequilibrium phenomena. Typical applications are the quantum master equation, kinetic theory, and linear response theory which are outlined and illustrated solving standard examples for reaction and transport processes. Some open questions are emphasized.",book:{id:"8416",slug:"non-equilibrium-particle-dynamics",title:"Non-Equilibrium Particle Dynamics",fullTitle:"Non-Equilibrium Particle Dynamics"},signatures:"Gerd Röpke",authors:[{id:"260373",title:"Prof.",name:"Gerd",middleName:null,surname:"Roepke",slug:"gerd-roepke",fullName:"Gerd Roepke"}]}],mostDownloadedChaptersLast30Days:[{id:"66878",title:"Design of Industrial Falling Film Evaporators",slug:"design-of-industrial-falling-film-evaporators",totalDownloads:1776,totalCrossrefCites:0,totalDimensionsCites:1,abstract:"The high performance evaporators are important for process industries such as food, desalination and refineries. The falling film evaporators have many advantages over flooded and vertical tubes that make them best candidate for processes industries application. The heat transfer area is the key parameter in designing of an evaporator and many correlations are available to estimate the size of tube bundle. Unfortunately, most of the correlation is available only for pure water and above 322 K saturation temperatures. Out of these conditions, the areas are designed by the extrapolation of existing correlations. We demonstrated that the actual heat transfer values are 2–3-fold higher at lower temperature and hence simple extrapolated estimation leads to inefficient and high capital cost design. We proposed an accurate heat transfer correlation for falling film evaporators that can capture both, low temperature evaporation and salt concentration effectively. It is also embedded with unique bubble-assisted evaporation parameter that can be only observed at low temperature and it enhances the heat transfer. The proposed correlation is applicable from 280 to 305 K saturation temperatures and feed water concentration ranges from 35,000 to 95,000 ppm. The uncertainty of measured data is less than 5% and RMS of regressed data is 3.5%. In this chapter, first part summarized the all available correlations and their limitations. In second part, falling film evaporation heat transfer coefficient (FFHTC) is proposed and model is developed. In the last part, experimentation is conducted and FFHTC developed and compared with conventional correlations.",book:{id:"7661",slug:"heat-and-mass-transfer-advances-in-science-and-technology-applications",title:"Heat and Mass Transfer",fullTitle:"Heat and Mass Transfer - Advances in Science and Technology Applications"},signatures:"Muhammad Wakil Shahzad, Muhammad Burhan and Kim Choon Ng",authors:[{id:"174208",title:"Dr.",name:"Muhammad Wakil",middleName:null,surname:"Shahzad",slug:"muhammad-wakil-shahzad",fullName:"Muhammad Wakil Shahzad"},{id:"249811",title:"Dr.",name:"Muhammad",middleName:null,surname:"Burhan",slug:"muhammad-burhan",fullName:"Muhammad Burhan"},{id:"254696",title:"Prof.",name:"Kim Choon",middleName:null,surname:"Ng",slug:"kim-choon-ng",fullName:"Kim Choon Ng"}]},{id:"66102",title:"Heat and Mass Transfer of Additive Manufacturing Processes for Metals",slug:"heat-and-mass-transfer-of-additive-manufacturing-processes-for-metals",totalDownloads:1318,totalCrossrefCites:0,totalDimensionsCites:0,abstract:"Additive manufacturing (AM), a method in which a part is fabricated layer by layer from a digital design package, provides the potential to produce complex components at reduced cost and time. Many techniques (using many different names) have been developed to accomplish this via melting or solid-state joining. However, to date, only a handful can be used to produce metallic parts that fulfill the requirements of industrial applications. The thermal physics and weld pool behaviors in metal AM process have decisive influence on the deposition quality, the microstructure and service performance of the depositions. Accurate analysis and calculation of thermal processes and weld pool behaviors are of great significance to the metallurgy analysis, stress and deformation analysis, process control and process optimization etc. Numerical modeling is also a necessary way to turn welding from qualitative description and experience-based art into quantitative analysis- and science-based engineering branch. In this chapter, two techniques for producing metal parts are explored, with a focus on the thermal science of metal AM: fluid flow and heat transfer. Selective laser melting (SLM) is the one that is most widely used because it typically has the best resolution. Another is named metal fused-coated additive manufacturing (MFCAM) that is cost competitive and efficient in producing large and middle-complex components in aerospace applications.",book:{id:"7661",slug:"heat-and-mass-transfer-advances-in-science-and-technology-applications",title:"Heat and Mass Transfer",fullTitle:"Heat and Mass Transfer - Advances in Science and Technology Applications"},signatures:"Zhengying Wei and Jun Du",authors:[{id:"47614",title:"Prof.",name:"Zhengying",middleName:null,surname:"Wei",slug:"zhengying-wei",fullName:"Zhengying Wei"},{id:"282052",title:"Dr.",name:"Jun",middleName:null,surname:"Du",slug:"jun-du",fullName:"Jun Du"}]},{id:"66563",title:"Heat and Mass Transfer in Outward Convex Corrugated Tube Heat Exchangers",slug:"heat-and-mass-transfer-in-outward-convex-corrugated-tube-heat-exchangers",totalDownloads:1050,totalCrossrefCites:0,totalDimensionsCites:1,abstract:"Heat and mass transfer in outward convex corrugated tube heat exchangers is of significant importance for the optimization, fabrication, and application of outward convex corrugated tube heat exchangers. This chapter gives a deep investigation of the heat and mass transfer in outward convex corrugated tube heat exchangers. Based on the experimental setup developed, the performances of a novel outward convex corrugated tube heat exchanger are presented. Simulation methods are then used to detail the heat and mass transfer at tube side and shell side of the outward convex corrugated tube heat exchanger, and these include the flow structure, temperature distribution, and turbulence kinetic energy. Heat and mass transfer enhancements of the outward convex corrugated tube heat exchanger are also studied, and they are from tube side, shell side, and overall system aspects. Finally, multi-objective optimization of the outward convex corrugated tube heat exchanger is conducted to obtain the optimal performances through using Response Surface Methodology (RSM) and Non-dominated Sorting Genetic Algorithm (NSGA-II). Main conclusions and future outlook are then briefly stated and summarized. We firmly believe that the contents presented in this chapter can not only enrich the knowledge of heat exchangers but also develop methods for studying heat exchangers.",book:{id:"7661",slug:"heat-and-mass-transfer-advances-in-science-and-technology-applications",title:"Heat and Mass Transfer",fullTitle:"Heat and Mass Transfer - Advances in Science and Technology Applications"},signatures:"Huaizhi Han, Bingxi Li, Yaning Zhang, Quan Zhu and Ruitian Yu",authors:[{id:"23828",title:"Dr.",name:"Quan",middleName:null,surname:"Zhu",slug:"quan-zhu",fullName:"Quan Zhu"},{id:"148369",title:"Prof.",name:"Bingxi",middleName:null,surname:"Li",slug:"bingxi-li",fullName:"Bingxi Li"},{id:"196928",title:"Dr.",name:"Yaning",middleName:null,surname:"Zhang",slug:"yaning-zhang",fullName:"Yaning Zhang"},{id:"281875",title:"Prof.",name:"Huaizhi",middleName:null,surname:"Han",slug:"huaizhi-han",fullName:"Huaizhi Han"},{id:"282268",title:"Mr.",name:"Ruitian",middleName:null,surname:"Yu",slug:"ruitian-yu",fullName:"Ruitian Yu"}]},{id:"66317",title:"Review Heat Transfer of Non-Newtonian Fluids in Agitated Tanks",slug:"review-heat-transfer-of-non-newtonian-fluids-in-agitated-tanks",totalDownloads:1010,totalCrossrefCites:1,totalDimensionsCites:1,abstract:"The heating and cooling of non-Newtonian liquids in tanks with mechanical impellers are operations commonly employed as chemical reactors, heat exchangers, distillers, extractors, thinners and decanters. In particular, the design of heat exchangers (jackets, helical coils, spiral coils and vertical tubular baffles) in tanks requires the prior knowledge of the rheology of the liquid for the calculation of the convection coefficients and the Reynolds number, in order to obtain the area thermal exchange. This chapter aimed to present the basic concepts of tanks with agitation, non-Newtonian liquids, hydrodynamics, heat transfer and, finally, with a practical design example for engineers and undergraduate students.",book:{id:"7661",slug:"heat-and-mass-transfer-advances-in-science-and-technology-applications",title:"Heat and Mass Transfer",fullTitle:"Heat and Mass Transfer - Advances in Science and Technology Applications"},signatures:"Vitor da Silva Rosa and Deovaldo de Moraes Júnior",authors:[{id:"187128",title:"Ph.D.",name:"Vitor",middleName:null,surname:"Rosa",slug:"vitor-rosa",fullName:"Vitor Rosa"},{id:"188792",title:"Dr.",name:"Deovaldo",middleName:null,surname:"Moraes Júnior",slug:"deovaldo-moraes-junior",fullName:"Deovaldo Moraes Júnior"}]},{id:"65692",title:"Advances in Concentrated Solar Power: A Perspective of Heat Transfer",slug:"advances-in-concentrated-solar-power-a-perspective-of-heat-transfer",totalDownloads:1127,totalCrossrefCites:0,totalDimensionsCites:0,abstract:"Solar energy has the potential to reduce the dependence on the dwindling supply of fossil fuels through concentrated solar power (CSP) technology. CSP plants utilize solar thermal energy to produce electrical energy based on different thermodynamic power cycles. Solar collectors, reflectors, receivers, thermal fluid, and turbines are the main components of each CSP plant and involve intensive heat transfer at all stages. This chapter illustrates the thermal characteristics of the main components used in CSP technology. In addition, the solar thermal fluid characteristics and its stable operational ranges are discussed in this chapter. Heat capacity, vapor pressure, volume expansion, density and viscosity of the thermal fluid should not differ significantly at different temperatures during various operation stages because these variations can cause failure in the system, which is designed at the fixed material properties. Currently, CSP technology is associated with a higher cost compared to the electricity generated through gas power plants. Many efforts are made to search for sustainable and inexpensive materials to minimize the cost of CSP. One critical issue faced by CSP technology is the intermittent nature of the sun. Modern CSP plants integrate thermal energy storage (TES) unit to smoothen the power production or to shift the production from peak sunshine hours to peak demand hours.",book:{id:"7661",slug:"heat-and-mass-transfer-advances-in-science-and-technology-applications",title:"Heat and Mass Transfer",fullTitle:"Heat and Mass Transfer - Advances in Science and Technology Applications"},signatures:"Fadi Alnaimat and Yasir Rashid",authors:[{id:"151722",title:"Dr.",name:"Fadi",middleName:null,surname:"Alnaimat",slug:"fadi-alnaimat",fullName:"Fadi Alnaimat"},{id:"291252",title:"Mr.",name:"Yasir",middleName:null,surname:"Rashid",slug:"yasir-rashid",fullName:"Yasir Rashid"}]}],onlineFirstChaptersFilter:{topicId:"954",limit:6,offset:0},onlineFirstChaptersCollection:[],onlineFirstChaptersTotal:0},preDownload:{success:null,errors:{}},subscriptionForm:{success:null,errors:{}},aboutIntechopen:{},privacyPolicy:{},peerReviewing:{},howOpenAccessPublishingWithIntechopenWorks:{},sponsorshipBooks:{sponsorshipBooks:[],offset:0,limit:8,total:null},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:104,numberOfOpenTopics:3,numberOfUpcomingTopics:0,issn:"2631-5343",doi:"10.5772/intechopen.71985",isOpenForSubmission:!0}],lsSeriesList:[{id:"11",title:"Biochemistry",numberOfPublishedBooks:32,numberOfPublishedChapters:320,numberOfOpenTopics:4,numberOfUpcomingTopics:0,issn:"2632-0983",doi:"10.5772/intechopen.72877",isOpenForSubmission:!0},{id:"25",title:"Environmental Sciences",numberOfPublishedBooks:1,numberOfPublishedChapters:12,numberOfOpenTopics:4,numberOfUpcomingTopics:0,issn:"2754-6713",doi:"10.5772/intechopen.100362",isOpenForSubmission:!0},{id:"10",title:"Physiology",numberOfPublishedBooks:11,numberOfPublishedChapters:141,numberOfOpenTopics:4,numberOfUpcomingTopics:0,issn:"2631-8261",doi:"10.5772/intechopen.72796",isOpenForSubmission:!0}],hsSeriesList:[{id:"3",title:"Dentistry",numberOfPublishedBooks:8,numberOfPublishedChapters:133,numberOfOpenTopics:2,numberOfUpcomingTopics:0,issn:"2631-6218",doi:"10.5772/intechopen.71199",isOpenForSubmission:!0},{id:"6",title:"Infectious Diseases",numberOfPublishedBooks:13,numberOfPublishedChapters:113,numberOfOpenTopics:3,numberOfUpcomingTopics:1,issn:"2631-6188",doi:"10.5772/intechopen.71852",isOpenForSubmission:!0},{id:"13",title:"Veterinary Medicine and Science",numberOfPublishedBooks:11,numberOfPublishedChapters:107,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:19,numberOfOpenTopics:3,numberOfUpcomingTopics:0,issn:"2753-894X",doi:"10.5772/intechopen.100359",isOpenForSubmission:!0},{id:"23",title:"Education and Human Development",numberOfPublishedBooks:0,numberOfPublishedChapters:5,numberOfOpenTopics:1,numberOfUpcomingTopics:1,issn:null,doi:"10.5772/intechopen.100360",isOpenForSubmission:!0},{id:"24",title:"Sustainable Development",numberOfPublishedBooks:0,numberOfPublishedChapters:17,numberOfOpenTopics:5,numberOfUpcomingTopics:0,issn:null,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:"6",title:"Infectious Diseases",doi:"10.5772/intechopen.71852",issn:"2631-6188",scope:"This series will provide a comprehensive overview of recent research trends in various Infectious Diseases (as per the most recent Baltimore classification). Topics will include general overviews of infections, immunopathology, diagnosis, treatment, epidemiology, etiology, and current clinical recommendations for managing infectious diseases. Ongoing issues, recent advances, and future diagnostic approaches and therapeutic strategies will also be discussed. This book series will focus on various aspects and properties of infectious diseases whose deep understanding is essential for safeguarding the human race from losing resources and economies due to pathogens.",coverUrl:"https://cdn.intechopen.com/series/covers/6.jpg",latestPublicationDate:"June 25th, 2022",hasOnlineFirst:!0,numberOfPublishedBooks:13,editor:{id:"131400",title:"Prof.",name:"Alfonso J.",middleName:null,surname:"Rodriguez-Morales",slug:"alfonso-j.-rodriguez-morales",fullName:"Alfonso J. Rodriguez-Morales",profilePictureURL:"https://mts.intechopen.com/storage/users/131400/images/system/131400.png",biography:"Dr. Rodriguez-Morales is an expert in tropical and emerging diseases, particularly zoonotic and vector-borne diseases (especially arboviral diseases). He is the president of the Travel Medicine Committee of the Pan-American Infectious Diseases Association (API), as well as the president of the Colombian Association of Infectious Diseases (ACIN). He is a member of the Committee on Tropical Medicine, Zoonoses, and Travel Medicine of ACIN. He is a vice-president of the Latin American Society for Travel Medicine (SLAMVI) and a Member of the Council of the International Society for Infectious Diseases (ISID). Since 2014, he has been recognized as a Senior Researcher, at the Ministry of Science of Colombia. He is a professor at the Faculty of Medicine of the Fundacion Universitaria Autonoma de las Americas, in Pereira, Risaralda, Colombia. He is an External Professor, Master in Research on Tropical Medicine and International Health, Universitat de Barcelona, Spain. He is also a professor at the Master in Clinical Epidemiology and Biostatistics, Universidad Científica del Sur, Lima, Peru. In 2021 he has been awarded the “Raul Isturiz Award” Medal of the API. Also, in 2021, he was awarded with the “Jose Felix Patiño” Asclepius Staff Medal of the Colombian Medical College, due to his scientific contributions to COVID-19 during the pandemic. He is currently the Editor in Chief of the journal Travel Medicine and Infectious Diseases. His Scopus H index is 47 (Google Scholar H index, 68).",institutionString:"Institución Universitaria Visión de las Américas, Colombia",institution:null},editorTwo:null,editorThree:null},subseries:{paginationCount:12,paginationItems:[{id:"38",title:"Pollution",coverUrl:"https://cdn.intechopen.com/series_topics/covers/38.jpg",editor:{id:"110740",title:"Dr.",name:"Ismail M.M.",middleName:null,surname:"Rahman",slug:"ismail-m.m.-rahman",fullName:"Ismail M.M. Rahman",profilePictureURL:"https://mts.intechopen.com/storage/users/110740/images/2319_n.jpg",biography:"Ismail Md. Mofizur Rahman (Ismail M. M. Rahman) assumed his current responsibilities as an Associate Professor at the Institute of Environmental Radioactivity, Fukushima University, Japan, in Oct 2015. He also has an honorary appointment to serve as a Collaborative Professor at Kanazawa University, Japan, from Mar 2015 to the present. \nFormerly, Dr. Rahman was a faculty member of the University of Chittagong, Bangladesh, affiliated with the Department of Chemistry (Oct 2002 to Mar 2012) and the Department of Applied Chemistry and Chemical Engineering (Mar 2012 to Sep 2015). Dr. Rahman was also adjunctly attached with Kanazawa University, Japan (Visiting Research Professor, Dec 2014 to Mar 2015; JSPS Postdoctoral Research Fellow, Apr 2012 to Mar 2014), and Tokyo Institute of Technology, Japan (TokyoTech-UNESCO Research Fellow, Oct 2004–Sep 2005). \nHe received his Ph.D. degree in Environmental Analytical Chemistry from Kanazawa University, Japan (2011). He also achieved a Diploma in Environment from the Tokyo Institute of Technology, Japan (2005). Besides, he has an M.Sc. degree in Applied Chemistry and a B.Sc. degree in Chemistry, all from the University of Chittagong, Bangladesh. \nDr. Rahman’s research interest includes the study of the fate and behavior of environmental pollutants in the biosphere; design of low energy and low burden environmental improvement (remediation) technology; implementation of sustainable waste management practices for treatment, handling, reuse, and ultimate residual disposition of solid wastes; nature and type of interactions in organic liquid mixtures for process engineering design applications.",institutionString:null,institution:{name:"Fukushima University",institutionURL:null,country:{name:"Japan"}}},editorTwo:{id:"201020",title:"Dr.",name:"Zinnat Ara",middleName:null,surname:"Begum",slug:"zinnat-ara-begum",fullName:"Zinnat Ara Begum",profilePictureURL:"https://mts.intechopen.com/storage/users/201020/images/system/201020.jpeg",biography:"Zinnat A. Begum received her Ph.D. in Environmental Analytical Chemistry from Kanazawa University in 2012. She achieved her Master of Science (M.Sc.) degree with a major in Applied Chemistry and a Bachelor of Science (B.Sc.) in Chemistry, all from the University of Chittagong, Bangladesh. Her work affiliations include Fukushima University, Japan (Visiting Research Fellow, Institute of Environmental Radioactivity: Mar 2016 to present), Southern University Bangladesh (Assistant Professor, Department of Civil Engineering: Jan 2015 to present), and Kanazawa University, Japan (Postdoctoral Fellow, Institute of Science and Engineering: Oct 2012 to Mar 2014; Research fellow, Venture Business Laboratory, Advanced Science and Social Co-Creation Promotion Organization: Apr 2018 to Mar 2021). 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