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Article

Analysis of Potential Use of Linear Fresnel Collector for Direct Steam Generation in Industries of the Southwest of Europe

by
Francisco José Sepúlveda
*,
María Teresa Miranda
,
Irene Montero
,
José Ignacio Arranz
,
Francisco Javier Lozano
,
Manuel Matamoros
and
Paloma Rodríguez
Department of Mechanical Engineering, Energy and Materials, Industrial Engineering School, University of Extremadura, Avenue Elvas s/n, 06006 Badajoz, Spain
*
Author to whom correspondence should be addressed.
Energies 2019, 12(21), 4049; https://doi.org/10.3390/en12214049
Submission received: 1 October 2019 / Revised: 21 October 2019 / Accepted: 22 October 2019 / Published: 24 October 2019

Abstract

:
Industry sector has an important impact on primary energy consumption at the international level, and solar energy constitutes a real alternative to cover these energy needs partially. Among thermosolar concentration technologies, Linear Fresnel Collector (LFC) technology has some advantages that make it more accessible to industries. With the aim of providing new tools for easier decision-making processes, in the present work, several energy audits were carried out in industries (located in the south-west of Europe, with considerable steam consumptions), quantifying thermal and energy consumptions and defining both work schedules and seasonality. Afterwards, a comparison based on three factors was carried out: Thermal consumption regarding total industry consumption, the performance of the work during the solar schedule, and the quantification of the monthly average concentrated energy for a certain LFC facility. The analysis carried out according to these criteria showed different results for each case, making a global assessment necessary to suitably ponder each factor. This analysis ranked tomato industries as the most suitable for LFC technology, due to the fact that their main operating period was during the months with the highest solar isolation, and the solar schedule was completely integrated in a 24-h working day. Also, industrial waxes and laundries showed a good combination of both facts.

1. Introduction

There has been a constant increase in energy consumption over the last century. Both energy demand and CO2 emissions are expected to rise to 60% in 2030. Global oil consumption has grown 20% since 1994, and it is expected to grow 1.6% annually [1]. Moreover, global warming and greenhouse gas emissions also generate problems that make the transition from fossil fuels to green energies more important than ever [2,3,4]. Several international agreements have been established regarding this issue with various objectives: Decrease greenhouse gas emissions a minimum of 40% at a national level and a reach 32% share of renewables in gross final energy consumption [5]. In that sense, solar energy is a real alternative to cover a part of the energy needs of our society [6,7]. Amongst many advantages, renewable energies offer a more stable evolution of prices compared to fossil fuels, due to the limited supply capacity and the dependency on the international market of the fossil fuels [8,9,10,11,12,13,14].
On the other hand, industry accounts for approximately 40% of primary energy consumption globally in 2019 [15]. Similarly, at a European level, industry demands 37%, while, in Spain, it represents 26% of primary energy consumption [16]. Furthermore, heat generation processes in industry constitute 54% of the total energy consumption in Europe in contrast with 17% of the total energy consumption corresponding to electric uses. This proportion of energy use justifies the implementation of solar thermal-based systems [17].
Solar thermal systems harness solar energy for heating, either as hot water for domestic use—domestic hot water and heating—as a heating source for fluids in industrial processes or as steam to produce mechanical energy in a turbine to obtain electrical energy. Solar thermal systems may have concentrators to direct solar isolation that strikes the capturing surface area towards a smaller area (absorber area). This configuration obtains higher temperatures in the heat transfer fluid. These devices achieve solar concentration using specular reflection; thus, only direct isolation is used.
There are two different technologies that concentrate direct solar isolation: Point focus type, that concentrates isolation into a single point—solar power tower or Dish-Stirling system—and linear focus type, which concentrates isolation into a linear receptor. Linear focus type reaches higher temperatures, because it concentrates isolation into a larger area. There are two types of linear focus collectors: Parabolic trough collector (PTC) and linear Fresnel collectors [18,19].
Several studies have shown LFC (Linear Fresnel Collector) optical quality and thermal efficiency is slightly lower than in the case of PTC, due to the high influence of the angle of incidence and the cosine factor. Nevertheless, the consecution of higher concentrations or a better optical efficiency does not imply that this system is suitable for any use [20,21]. In that sense, LFC technology shows a number of advantages compared to PTC, such as its greater structural simplicity and the use of flat mirrors (or with low curvature). These aspects considerably reduce manufacture costs. Plus, they require low energy to follow the apparent motion of the sun—only the mirrors have to rotate—and the separation between the concentrator and the heat carrier fluid line remove the problems concerning flexible or rotative connections between concentrators, making the maintenance easier [22,23,24,25,26]. This way, and given the need for implementing efficient, economical and renewable energy sources in industrial applications, LFC technology can comply with these targets, currently finding certain evidences of its implementation in different production plants, for example, in pharmaceutical industry in Jordan [27], in agro-food industry in Italy [28] or automobile manufacturing in Germany [29].
Although the possibilities of solar energy for industrial processes has been widely proved and provided satisfactory results, the role of solar energy in industry is still reduced, possibly due to the lack of knowledge about this technology by the final user. Because of that, it is necessary to carry out new research works to provide simple and direct information about the advantages of the use of this technology. Thus, Shahjadi Hisan Farjana et al. [17] carried out a study about possible industrial processes that could accommodate heating systems through solar processes, pointing out the high volume of thermal energy required in drying, washing, cleaning, water heating, pasteurization, sterilization and other food processes. In another work by the same authors, they identified 10 countries where the use of this kind of system is highlighted—analyzing the potential of integration [30]. Laveet Kumar et al. [31] also classified current industrial process-heat system based on solar collector technologies and heat demand temperatures for the identification of typical applications for solar process heat, stablishing that solar thermal technologies can be used for a variety of industrial applications for sustainable energy system, although solar thermal energy storage is necessary.
Likewise, for the implementation of solar concentration technologies in industries, it is necessary to know a number of factors, such as the location and the space available, temperature and working pressures, energy use, etc. Tengjia et al. [32] specified interesting sectors to use this technology, such as tobacco, food processing, textile, chemical, pharmaceutical, wood, plastics or rubber industries, among others.
Schweiger et al. [33] wrote a state-of-the-art review about the potential of solar heat in industrial processes, in which they showed an interesting list of solar industrial process heat projects. They carried out TRNSYS simulations for five cities in Spain and Portugal, and an estimation of the efficiency of solar process heat plants in the Southern European climate are given for different collector technologies.
In the same way, Lauterbach et al. [34] calculated the potential of solar heat for industrial processes in Germany and selected 11 sectors that were identified to be most promising for the use of solar heat, such as chemicals, food and beverages, motor vehicles, paper, fabricated metal, machinery and equipment, rubber and plastic, electrical equipment, textiles, printing and wood.
Therefore, there are several works concerning the field of solar heat potential for industrial processes, although these papers mainly cover industrial processes and their energy consumption. Nonetheless, seasonality and work schedule must be considered for steam production. This allows to estimate the potential concentrated energy these systems—especially LFC—produce during normal operating conditions. Thus, a new indicator is introduced to study the industries solar heat potential.
On the basis of the above, in the present work, a series of simplified energy audits in industries located in the southwest of Europe were carried out, in order to quantify the thermal and energy consumption and define both working schedules and seasonality. Afterwards, a procedure was established to determine the grade of the susceptibility of industries for the implementation of LFC systems to support traditional systems of thermal energy generation. This procedure was based on the study of three factors: Thermal consumption compared to the total in the industry, performance of the work during the solar schedule, and quantification of the monthly average concentrated energy for a certain LFC facility. In the latter case, a set of energy simulation studies was carried out, paying attention to the optical yield variation and different direct isolation levels throughout the year.

2. Materials and Methods

2.1. Selection of Industries

Different industries with considerable steam consumptions, from the southwest of Europe, were selected. The most relevant data for the analysis were defined, such as production, working hours, seasonality and energy consumption, among others.
Table 1 shows the selected industries for this study, as well as relevant data concerning their capacity in their corresponding sector.

2.2. Definition of the Criteria Used

The following criteria were defined:
  • Thermal energy ratio (RTE), which relates the thermal energy consumed and the total energy demand by each industry analyzed.
  • Solar time ratio (RST) relates to the part of the working schedule of industries matches the hours of sunlight (with solar isolation).
  • Monthly average concentrated energy (E, kWh): This variable quantifies the average solar energy that an LFC system could concentrate during the normal performance of the industry.

2.3. Thermal Energy Ratio

Through the analysis of thermal and electrical energy bills of each industry, the annual consumptions were obtained, corresponding to each kind of energy: Thermal Energy, TE, in kWh and Electrical Energy, EE, in kWh. Afterwards, the thermal energy ratio was determined according to Equation (1). Thus, a high value of RTE can be interpreted as the high suitability of a certain industry for the implementation of LFC technology,
R T E = T E T E + E E .

2.4. Solar Time Ratio

Concentrated solar power technology limits its use to the hours when the sun is present. Thus, Table 2 shows the average values of sunrise and sunset times, which limit the solar schedule (as a reference, data corresponding to the 15th of each month for the city of Cáceres, located in the southwest of Spain, were used) [35].
This way, it is possible to determine the fraction of time in which the working schedule overlaps with the solar schedule. This fraction of time is called solar ratio, RST, and it was obtained through Equation (2), where SPj and TPj (hours) are the production times in the solar schedule for each month j, and n is the number of months of operation for the industry. On this basis, the industries whose working schedule overlaps with the solar schedule to a larger extent will benefit from this technology to a greater extent,
R S T = j = 1 n ( S P T P ) j n .

2.5. Monthly Average Concentrated Energy

The distribution of the industries production throughout the year was determined using the energy studies detailed in the previous section. This is relevant, as LFC technology will show different yields depending on the time of the year when the industry works. Thus, an energy simulation model was implemented, exclusively focused on the optical behavior of a generic LFC plant. The simulation was done by using Matlab [36], a software that combines an improved environment for the iterative analysis and design processes with a programming language. A generic LFC plant for a steam generation was defined, whose location and main characteristics are shown in Table 3. Moreover, Figure 1 shows a graphical representation of the LFC used.
For the energy simulation, the following considerations were taken into account:
  • As the purpose of the plant was the direct steam generation, the calculation was exclusively carried out for the industries seasonality and work schedules for a 7-day week. Not all the companies analyzed operate regularly every day of the week. However, they all do so at some time to cover demand spikes. Therefore, we decided not to take this factor into account in the study, just as scheduled maintenance stops were not considered.
  • A time step of 90 s was considered, obtaining for each case the new position of the sun. Similarly, the optimum angle of the mirrors—which allows the highest incident solar isolation concentration—was modified every 90 s.
  • Optical losses were quantified considering the following factors: Shadow between rows, optical losses and non-lite pipe factor. The model used to calculate these losses is based on the procedure described by Pino et al. [37] for an E-O orientation. Thus, it was necessary to make some changes to consider other different orientations. A detailed description of these changes is included in the Annex section.
Concerning the optical losses, a shadow between rows factor, fshading,i,t, is directly related to the total isolation that the field of mirrors can reflect on the absorber tube. Once the shaded area is known, it is divided by the total reflective Surface, according to Equation (3), where swi,t (m) is the shaded width of each row of mirrors i for each calculation step t, and L (m) and A (m2) are the length and the area for a row of mirrors of the LFC, respectively;
f s h a d i n g , i , t = 1 s w i , t · L A .
In turn, the solar beam isolation that hits the mirrors is not completely exploited. As the latter reflect the isolation to the absorber tube, the rays of the sun do not strike the mirror surface in a perpendicular position. The difference between the real inclination of the mirror and the one that it should have to make the most of the incident isolation determines the effective surface of the mirror. Optical losses, fol,i,t, are given by the cosine of the angle formed by the solar incidence vector and the direction normal to the surface of the row of mirrors i for each calculation step δi,t, according to Equation (4),
f o l , i , t = cos ( δ i , t ) .
Due to the azimuthal component of the solar disk for each instance, a section of one of the edges of the absorber tube is not illuminated. This effect will be produced in a direction, or the opposite one before the sun reaches the midday and overtakes it, respectively. The length of this non-illuminated section for each calculation step t, Zi,t (m), will proportionally affect the optical yield, with La being the length of the absorber tube in the LFC system. Equation (5) allows the calculation of the losses in the non-lite pipe factor, fnlp,i,t;
f n l p , i , t = 1 Z i , t L a .
Finally, the optical yield µi,t for each row of mirrors i and for each calculation step t is given by the product of the above-mentioned factors, as it is shown in Equation (6):
μ i , t = f s h a d i n g , i , t ·   f o l , i , t · f n l p , i , t
The energy concentrated by each row of mirrors i in each calculation step t, Ei,t (kWh), will be given by Equation (7), where Ib,t is the beam irradiance (kW·m−2), ρpr and fcl_pr, are the reflectance and the cleanliness factor of the primary mirrors, ρsd and fcl_sd are the reflectance and the cleanliness factor of the secondary receiver, and T (h) is the duration of each time step,
E i , t = I b , t · A · μ i ,     t · ρ p r · f c l _ p r · ρ s d · f c l _ s d · T .
Ib,t data were provided by Meteonorm software (7.1 version) [38], that offers a unique combination of reliable data sources and sophisticated calculation tools. It provides access to typical years and historical time series. Figure 2 shows the values of the beam, diffuse and global insolation (sum of the first two) on a horizontal plane (kWh·m−2), obtained throughout a year for the location showed in Table 3.
Finally, the concentrated energy values for each calculation step t, Et (kWh), and month, Ej (kWh), and the monthly average considering the number of working months, E (kWh), are obtained by Equations (8)–(10), respectively. On the basis of this, the industries that will benefit from these criteria will be those that, on one hand, show higher optical yields, and, on the other hand, intensify their production during the months with the highest solar isolation,
E t = i = 1 r E i , t ,
E j = t E t ,
E = j = 1 n E j n .

3. Results and Discussion

3.1. Summary of the Energy Studies Carried Out

Table 4 shows the stages and processes that require thermal energy, as well as the working pressure of the steam boiler, schedule, seasonality and energy consumptions.

3.2. Thermal Energy Ratio

Figure 3 shows the classification obtained according to the thermal energy ratio criterion. The industry that showed the highest percentage was the industrial waxes manufacturer, because it uses a considerable amount of steam to avoid the solidification of wax during the production process (passing through pipes, etc.). The following industries are the industrial laundries and tomato industries. The former showed high thermal energy demands during washing, drying and ironing. The latter, spent thermal energy in processes such as pre-heating, evaporation and sterilization.
At an intermediate level, there are industries that work with rice, cardboard packaging and chemical products, where the drying, corrugation and homogenization, respectively, represent a considerable thermal consumption, although not as high as in the case of the former. At a final level, the meat industries can be found, where the electricity use was higher than the thermal consumption for high and small capacity industries.
In that sense, 11 out of 13 industries that were studied exceeded 50% thermal energy ratio, possibly being a good starting point for LFC implementation. Nevertheless, values higher than 30% also represent a considerable part of production costs in industries; their relevance should not be underestimated.

3.3. Solar Time Ratio

Table 5 shows the results obtained according to the solar time ratio criterion.
Figure 4 shows the classification obtained. The best-rated industry, according to this criterion, was the processing nuts industry. Its working schedule, from 08:00 to 20:00 from July to December, coincides with sunrise and sunset to a larger extent. The second best-rated industry is the laundry industry, which offers its service throughout the year, albeit the working schedule is extended during the summer, due to the increase in the demand. In third place, meat industries can be found, which operate throughout the year. The beginning of the working day is similar throughout the year or during campaigns. This is the case of the tomato industry. This fact provokes that sunshine hours can only be exploited during half of the work schedule, and, because of this, their ranking is poor.
On the other hand, there were many differences when thermal energy ratio was considered. Process in the nuts industry showed a high suitability value for solar schedule, even though its thermal processes only imply 53% of total energy demand. The same happens in meat industries, with solar time ratios above 75% and having a low ranking concerning thermal energy ratio. Instead, the analyzed laundries showed very high values in both cases, which implies high suitability when implementing LFC technologies.

3.4. Monthly Average Concentrated Energy

As an example of the simulation studies carried out, Figure 5 shows the results obtained for one of the industries visited, namely, the medium capacity laundry. It could be observed how the monthly concentrated energy considerably increased during the months with the highest isolation (23,363 kWh in July, whereas, December showed 2782 kWh, that is, 8.4 times greater compared to the latter). Instead, the monthly optical yields were kept between 40 and 52% in the year. These data were within the range obtained by other authors. Thus, Kincaid et al. [39] found that the yearly optical efficiency, according to their models, was 40%. Mohamed H. Ahmed et al. [40] simulated the optical performance of a linear Fresnel obtaining 67% with their optical model and 38.8% accounting the sun-to-electric annual average efficiency. According to Ghodbane et al. [41], the optical efficiency of the solar reflector in their simulation reaches 53.7%.
Therefore, the variation in optical yield was significantly lower than the registered one for the concentrated energy, demonstrating the importance of beam isolation in energy analysis.
Therefore, and due to the fact that solar time ratio was directly incorporated to the energy simulations carried out, Figure 6 relates the criteria used—thermal energy ratio vs monthly average concentrated energy—and graphically shows the susceptibility level for the different industries for the implementation of LFC technology.
Thus, in the upper-right corner, the industries that showed higher suitability to implement this technology were located. In this case, tomato industries should be highlighted, due to the great yield or performance that LFC technology showed during the seasonality of these companies—July and August—and the high specific weight of the processes that demand thermal energy (around 90%). In turn, they have a working schedule that includes all the available sunshine hours (solar time ratio of 59%).
There is a second group of industries with monthly average concentrated energy values close to 12,000 kWh, sharing seasonality levels and working hours, and whose thermal energy ratio varied from 35% (high capacity meat) and 92% (industrial waxes manufactures). In these cases, thermal energy ratio is a decisive parameter for LFC implementation. Among the laundries, the medium capacity laundry showed a higher monthly average concentrated energy value, as its work schedule goes to 22:00, and can make the most of the solar schedule.
Thirdly, there is a third group, composed of the high capacity laundry and the medium and small capacity meat industries, which showed monthly average concentrated energy values below 9000 kWh. In turn, the lower values of thermal energy ratio were due to higher use of electrical energy for refrigeration.
Finally, it should be pointed out that the joint analysis of the energy simulation studies and the thermal energy ratio showed further information than in the case of a separate study of both criteria. Thus, for industries that work with the same seasonality and schedules, thermal energy ratio might be a differentiating factor for decision-making.

4. Conclusions

The most relevant findings in the present work were the following:
  • The analysis carried out following different criteria showed that a global analysis is necessary to suitably weight both the energy and thermal needs and the coincidence with the solar schedule.
  • The operating characteristics of all the industries analyzed are suitable for LFC technology. In fact, they showed thermal energy ratios above 30%—significant possibilities of savings in energy costs related to thermal processes—and solar time ratios above 50%—high coincidence between solar and work schedules.
  • The joint analysis ranked tomato industries as the most suitable ones for LFC technology, due to their operating work during the months with the highest solar isolation, integrating the solar schedule in a 24-h working day. Also, industrial waxes manufacturer and laundries, especially in the case of medium capacity industries, showed a good combination of both factors.

5. Annex

In this section, the modifications applied to the optical model by Pino et al. [37] to consider different orientations to E-O are included. Even though optical losses and non-lite pipe factor do not depend on orientation, for the determination of the shadow between rows, it is necessary to consider some additional cases. Thus, for an N-S orientation, like the one used in this work—Y axis in Figure 7—the row of mirrors are located on the left of this axis and also casts shadows on the row of mirrors on the right at certain periods of the day.
Thus, two new cases, when the angle of inclination of the shaded mirror, incl_i, is negative, were defined. In turn, Figure 8 represents the case when the row of mirrors that casts shadows has a negative inclination angle, calculating the shadow cast from the position of point D. On the other hand, Figure 9 represents the complementary case, in which the row of mirrors that casts shadows have a positive inclination angle, calculating the shadow cast from the position of the other edge of the row, that is, point F.

Author Contributions

Regarding the contribution of each author to the article, the original idea and work coordination corresponded to F.J.S. and M.T.M. The analysis of data was carried out by I.M., J.I.A., F.J.L., M.M. and P.R. Finally, the wording of the conclusions was made by F.J.S.

Funding

This research was funded by Research, Development and Renewable energies for the improvement of business fabric in Centro, Extremadura and Alentejo Project (0330_IDERCEXA_4_E).

Acknowledgments

The authors would like to thank the Junta de Extremadura and FEDER (Fondo Europeo de Desarrollo Regional “Una manera de hacer Europa”) for its support through the economic aid for research groups (GR18137), as well as Research, Development and Renewable energies for the improvement of business fabric in Centro, Extremadura and Alentejo Project (0330_IDERCEXA_4_E).

Conflicts of Interest

The authors declare no conflict of interest.

Abbreviations

δangle between normal vector row and Y axe (°)
µioptical performance of LFC row
ρprprimary mirrors reflectance
ρsdsecondary receiver reflectance
Amirror row area of the LFC (m2)
Emonthly average concentrated energy (kWh)
EEelectrical energy (kWh)
fcl_prprimary mirrors cleanliness factor
fcl_sdsecondary receiver cleanliness factor
fnlpnon-lite pipe factor
foloptical losses factor
fshadingshadow between rows factor
Ibbeam irradiance (kW m−2)
imirror rows
incinclination angle (°)
Laabsorber tube length of the LFC (m)
Lmirror length of the LFC (m)
nmonths of production
rnumber of mirror rows
jmonth
RECenergy concentration ratio
RSTsolar time ratio
RTEthermal energy ratio
SPproduction time during solar time (h)
tcalculation step
Ttime step (h)
TEthermal energy (kWh)
TPtotal production time (h)
swshaded width (m)
Znon-lite pipe (m)

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Figure 1. Front (a) and top view (b) of a module, and 3D diagram of LFC (c).
Figure 1. Front (a) and top view (b) of a module, and 3D diagram of LFC (c).
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Figure 2. Beam, diffuse and global insolation on a horizontal plane for the selected location (kWh·m−2).
Figure 2. Beam, diffuse and global insolation on a horizontal plane for the selected location (kWh·m−2).
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Figure 3. Classification according to thermal energy ratio.
Figure 3. Classification according to thermal energy ratio.
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Figure 4. Classification according to solar time ratio.
Figure 4. Classification according to solar time ratio.
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Figure 5. Monthly concentrated energy and optical yield obtained for medium capacity laundry.
Figure 5. Monthly concentrated energy and optical yield obtained for medium capacity laundry.
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Figure 6. Thermal energy ratio vs monthly average concentrated energy.
Figure 6. Thermal energy ratio vs monthly average concentrated energy.
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Figure 7. Axis defined for Fresnel module.
Figure 7. Axis defined for Fresnel module.
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Figure 8. Both mirrors with negative inclination.
Figure 8. Both mirrors with negative inclination.
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Figure 9. Mirror rows with a negative inclination and previous mirror rows with positive inclination.
Figure 9. Mirror rows with a negative inclination and previous mirror rows with positive inclination.
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Table 1. Industries selected for the study.
Table 1. Industries selected for the study.
IndustriesCapacityIndustrial Sector
Small capacity meat industry5800 pigs/yearTransforming
Medium capacity meat industry116,000 pigs/yearTransforming
High capacity meat industry170,000 pigs/yearTransforming
Processing nuts industry180 Tons nuts/yearTransforming
Fat processing industry19,800 Tons fats/year Transforming
Rice industry34,500 Tons rice/yearTransforming
Tomato industry 1420,000 Tons tomato/yearTransforming
Tomato industry 253,500 Tons tomato/yearTransforming
Cleaning products manufacturer90,000 Tons cleaning products/yearManufacturer
Industrial waxes manufacturer13,000 Tons waxes/yearManufacturer
Cardboard packaging manufacturer96,000 m2 cardboard/yearManufacturer
Medium capacity laundry1650 Tons clothes/yearServices
High capacity laundry2000 Tons clothes/yearServices
Table 2. Average values of sunrise and sunset used in the study.
Table 2. Average values of sunrise and sunset used in the study.
MonthSunriseSunset
Jan.08:4418:26
Feb.08:1719:02
Mar.07:3719:32
Apr.07:4821:03
May07:1121:33
Jun.06:5821:54
Jul.07:1121:52
Aug.07:3821:21
Sep.08:0720:34
Oct.08:3519:46
Nov.08:1018:10
Dec.08:3918:03
Table 3. Geographic and sizing data used.
Table 3. Geographic and sizing data used.
Geographic DataLatitude39.467° N
Longitude−6.333° W
OrientationN–S
Sizing DataLFC (Linear Fresnel Collector) modules8
Mirror rows10
Mirror length (m)6.0
Mirror width (m)0.5
Distance between mirrors (m)0.1
Absorber tube height (m)3.0
Table 4. Data from studies to industries.
Table 4. Data from studies to industries.
IndustriesProcessesPressure (bar)ScheduleSeasonalityTE (kWh)EE (kWh)
M.C. Laundry
H.C Laundry
Washing
Drying
Ironing
10
13
08:00–22:00
06:00–14:00
12 months1,891,604
3,740,652
242,956
623,148
Tomato ind. 1
Tomato ind. 2
Preheating
Evaporating
Sterilization
12
9
24 h
24 h
2 months during summer50,000,000
130,000,000
7,000,000
17,000,000
S.C. Meat ind.
M.C. Meat ind.
H.C. Meat ind.
Scalding
Baking
Cleaning
7
6
6
06:00–14:00
06:00–14:00
06:00–22:00
12 months405,600
2,493,288
7,000,000
794,667
1,079,184
13,000,000
Fat processing industriesFusion
Drying
624 h12 months5,952,9851,621,828
Rice industryVaporization1024 h12 months13,061,6573,486,770
Cleaning products man.Heating
Homogenization
724 h12 months1,890,000780,000
Industrial waxes man.Heating924 h12 months12,500,0001,200,000
Cardboard packaging man.Undulation1524 h12 months12,688,0685,079,228
Processing nuts industryDrying608:00–20:006 months from July to December121,680108,738
Table 5. Percentage of production time in solar time.
Table 5. Percentage of production time in solar time.
IndustriesJan.Feb.Mar.Apr.MayJun.Jul.Aug.Sep.Oct.Nov.Dec.
S.C. meat industry65.871.579.877.585.287.985.279.673.567.772.966.9
M.C. meat industry65.871.579.877.585.287.985.279.673.567.772.966.9
H.C. meat industry60.667.274.582.889.893.391.885.777.869.962.558.8
Processing nuts ind.------100.0100.099.093.283.378.3
Fat processing industry40.444.849.755.259.962.261.257.251.946.641.739.2
Rice industry40.444.849.755.259.962.261.257.251.946.641.739.2
Tomato industry 1------61.257.2----
Tomato industry 2------61.257.2----
Cleaning prod.40.444.849.755.259.962.261.257.251.946.641.739.2
Industrial waxes40.444.849.755.259.962.261.257.251.946.641.739.2
Cardboard packaging40.444.849.755.259.962.261.257.251.946.641.739.2
M.C. Laundry69.376.882.493.296.899.361.257.288.979.971.467.1
H.C. Laundry65.871.579.877.585.287.990.987.473.567.772.966.9

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MDPI and ACS Style

Sepúlveda, F.J.; Miranda, M.T.; Montero, I.; Arranz, J.I.; Lozano, F.J.; Matamoros, M.; Rodríguez, P. Analysis of Potential Use of Linear Fresnel Collector for Direct Steam Generation in Industries of the Southwest of Europe. Energies 2019, 12, 4049. https://doi.org/10.3390/en12214049

AMA Style

Sepúlveda FJ, Miranda MT, Montero I, Arranz JI, Lozano FJ, Matamoros M, Rodríguez P. Analysis of Potential Use of Linear Fresnel Collector for Direct Steam Generation in Industries of the Southwest of Europe. Energies. 2019; 12(21):4049. https://doi.org/10.3390/en12214049

Chicago/Turabian Style

Sepúlveda, Francisco José, María Teresa Miranda, Irene Montero, José Ignacio Arranz, Francisco Javier Lozano, Manuel Matamoros, and Paloma Rodríguez. 2019. "Analysis of Potential Use of Linear Fresnel Collector for Direct Steam Generation in Industries of the Southwest of Europe" Energies 12, no. 21: 4049. https://doi.org/10.3390/en12214049

APA Style

Sepúlveda, F. J., Miranda, M. T., Montero, I., Arranz, J. I., Lozano, F. J., Matamoros, M., & Rodríguez, P. (2019). Analysis of Potential Use of Linear Fresnel Collector for Direct Steam Generation in Industries of the Southwest of Europe. Energies, 12(21), 4049. https://doi.org/10.3390/en12214049

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