properties of granular materials for use as heat transfer · 0 10 20 30 40 50 60 70 80 90 0 50000...

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0 10 20 30 40 50 60 70 80 90 0 50000 100000 150000 200000 250000 Shear strain [-] Attrition [wt.%] Qartz flint Corundum Alumina grinding balls Basalt Sintered bauxite Attrition behavior Wear debris occurs not only due to thermally induced stress, but is also caused by mechanical stress. Attrition tests have been conducted in an annular shear cell, applying a ? normal stress of 84 kPa ? mean track speed of 3 m/s The results are plotted as mass fraction of attrition versus shear strain, as shown in fig. 4. Alumina grinding balls generate no wear debris at all. Attrition of quartz flint and bauxite reaches saturation levels at values of about 50 %, while corundum and basalt do not reach any saturated state in the given testing period. Properties of Granular Materials for Use as Heat Transfer Media for a Moving Bed Heat Exchanger in CSP Application Torsten Baumann Stefan Zunft Thermal Process Technology Thermal Process Technology E-Mail: [email protected] E-Mail: [email protected] Introduction ? good thermo-physical properties and flowability ? high resistance to thermal shock and attrition To this end, thermophysical, thermomechanical, mechanical and rheological properties were investigated experimentally. Material Investigations Ceramics and natural products were selected for the tests, see table 1 below for details. Thermal Conductivity of the Bulk Thermophysical properties, such as conductivity of the bulk are decisive for heat transfer behaviour and thus the thermal design of the MBHE. Bulk conductivity was measured using the hot wire method. Though the solid's level of molecular thermal conductivity covers a relatively wide range (1 to 20 W/mK), the effective bulk conductivities turn out to be in a narrow range between 0.1 W/mK and 1.0 W/mK for all tested materials, see fig. 2. These low values are attributed to the high thermal resistance of the voids. An increasing bulk conductivity with increasing temperature reflects a significant contribution of thermal radiation. Hence, it can be concluded that the level of thermal conductivity of a solid has only limited effect on the thermal design of the MBHE. Particulate materials are promising heat storage and heat transport media for high temperature applications like industrial processes, conventional power plants or Concentrating Solar Power (CSP). The investigated target application is a solar driven Rankine cycle based on a central particle receiver as shown in fig. 1. In this process, a moving bed heat exchanger (MBHE, fig. 1) is one of the core components and its design is highly dependent on material's properties. Major requirements are: Thermal shock resistance Since high temperature gradients are expected for the material passing through the heat exchanger, the granules resistance to thermal cycling is of significant importance. Cyclic thermo-shock tests have been applied: ? heating to approximately 810°C, ? water quenching at 20°C and ? subsequent drying at 110°C ? post test particle size distribution analysis (see fig. 3) The results indicate that ceramics have a very good thermal shock resistance. In the case of quartz sand, thermally induced stress exceeds the material‘s strength and thus leads to damage of the grains. This results in a smaller mean grain size and lower porosity, which influences the flow behavior and not at least the thermal properties of the bulk. Fig. 1: Flow diagram of a solar tower plant with an integrated Moving Bed Heat Exchanger Material Vol . mean grain size [mm] Standard deviation [mm] Sintered bauxite 1.49 0.56 ± 0.26 ± 0.09 Alumina grinding balls 2.01 1.17 ± 0.50 ± 0.20 Basalt 2.89 ± 1.08 Quartz flint Quartz sand 2.02 0.80 ± 0.57 ± 0.18 Normal corundum F14 NC F16 1.83 1.61 ± 0.42 ± 0.36 0 0.1 0.2 0.3 0.4 0.5 0.6 0.7 0.8 0.9 1 0 200 400 600 800 T [°C] ë SO [W/mK] Quartz flint Quartz sand Normal Corundum F14 NC F16 Bauxite 1.5 Bauxite 0.6 Alumina 2.0 Alumina 1.2 Basalt Fig. 2: Thermal bulk conductivity from 20 to 800°C for a variety of granular materials 0% 20% 40% 60% 80% 100% 0 200 400 600 800 1000 1200 1400 Grain size [ìm] Fraction [%] Quartz-Sand_orig. Quartz-Sand_30cyc Bauxite_orig Bauxite_30cyc Fig. 3: Cumulated grain size distribution of quartz sand and bauxite after 0 und 30 cycles Flowability The flow behavior of the bulk not only influences the design of the heat exchanger, but also the thermal behaviour, since the contact time at the walls strongly depends on particle flowability. Rheological measurements have been conducted with an annular shear-tester. Testing reveals that the resulting flow functions are in the range of “easy flowing” or even “free flowing”, as shown in fig. 5 for quartz sand and bauxite. Occurence of attrition leads to a deteriorated flow behaviour, because both mean grain size and bulk porosity decrease as grain size distribution widens. This again has a significant impact on the MBHE design: for quartz sand, the critical spacing between the tubes would have to be increased by 340% to 9 mm, cleary worsening the device's power density. Conclusions Properties of granular materials for the design of a moving bed heat exhanger application were investigated. Thermal bulk conductivity of the tested candidate materials show a variation in a narrow range below 1.0 W/mK, mainly depending on the material, temperature and grain size. The use of natural products including quartz phases and in particular quartz materials, bears the risk of desintegration of the inventory material due to thermal and mechanical load in the MBHE. The flowability of the investigated products is rated as “easy” or “free flowing”. However, attrition may lead to significant changes in flow behavior and therefore has to be taken into account for heat exchanger design. 0 0.1 0.2 0.3 0.4 0.5 0.6 0.7 0 2 4 6 8 10 Consolidating Stress [kPa] Failure Strength [kPa] Bauxite Bauxite 66% attrtion Quartz sand Quartz sand 28% attrtion not flowing very cohesive cohesive easy flowing free flowing Fig. 4: Attrion vs. shear strain for a variety of bulk materials Table 1: Overview of tested granular materials Fig. 5: Flow functions of quartz sand and bauxite with and without attrition HTS LTS G Particle-Receiver Solar Radiation from Heliostats Steam Turbine and Generator Condenser Eco 800 – 1000°C 300- 500°C SO,in T SO,out T FL,in T FL,out T MBHE Evaporator and Superheater German Aerospace Center Institute of Technical Thermodynamics

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Page 1: Properties of Granular Materials for Use as Heat Transfer · 0 10 20 30 40 50 60 70 80 90 0 50000 100000 150000 200000 250000 Shear strain [-] A t t r i t i o n [w t. %] Qartz flint

0

10

20

30

40

50

60

70

80

90

0 50000 100000 150000 200000 250000

Shear strain [-]

Att

riti

on

[wt.

%]

Qartz flint

Corundum

Alumina grinding balls

Basalt

Sintered bauxite

Attrition behaviorWear debris occurs not only due to thermally induced stress, but is also caused by mechanical stress. Attrition tests have been conducted in an annular shear cell, applying a?normal stress of 84 kPa ?mean track speed of 3 m/sThe results are plotted as mass fraction of attrition versus shear strain, as shown in fig. 4. Alumina grinding balls generate no wear debris at all. Attrition of quartz flint and bauxite reaches saturation levels at values of about 50 %, while corundum and basalt do not reach any saturated state in the given testing period.

Properties of Granular Materials for Use as Heat Transfer Media for a Moving Bed Heat Exchanger in CSP Application

Torsten Baumann Stefan Zunft Thermal Process Technology Thermal Process TechnologyE-Mail: [email protected] E-Mail: [email protected]

Introduction

? good thermo-physical properties and flowability? high resistance to thermal shock and attritionTo this end, thermophysical, thermomechanical, mechanical and rheological properties were investigated experimentally.

Material InvestigationsCeramics and natural products were selected for the tests, see table 1 below for details.

Thermal Conductivity of the BulkThermophysical properties, such as conductivity of the bulk are decisive for heat transfer behaviour and thus the thermal design of the MBHE.Bulk conductivity was measured using the hot wire method.Though the solid's level of molecular thermal conductivity covers a relatively wide range (1 to 20 W/mK), the effective bulk conductivities turn out to be in a narrow range between 0.1 W/mK and 1.0 W/mK for all tested materials, see fig. 2. These low values are attributed to the high thermal resistance of the voids. An increasing bulk conductivity with increasing temperature reflects a significant contribution of thermal radiation.Hence, it can be concluded that the level of thermal conductivity of a solid has only limited effect on the thermal design of the MBHE.

Particulate materials are promising heat storage and heat transport media for high temperature applications like industrial processes, conventional power plants or Concentrating Solar Power (CSP). The investigated target application is a solar driven Rankine cycle based on a central particle receiver as shown in fig. 1. In this process, a moving bed heat exchanger (MBHE, fig. 1) is one of the core components and its design is highly dependent on material's properties. Major requirements are:

Thermal shock resistanceSince high temperature gradients are expected for the material passing through the heat exchanger, the granules resistance to thermal cycling is of significant importance. Cyclic thermo-shock tests have been applied:?heating to approximately 810°C, ?water quenching at 20°C and ?subsequent drying at 110°C ?post test particle size distribution analysis (see fig. 3)The results indicate that ceramics have a very good thermal shock resistance. In the case of quartz sand, thermally induced stress exceeds the material‘s strength and thus leads to damage of the grains. This results in a smaller mean grain size and lower porosity, which influences the flow behavior and not at least the thermal properties of the bulk.

Fig. 1: Flow diagram of a solar tower plant with an integrated Moving Bed Heat Exchanger

Material Vol . mean grain size [mm] Standard deviation [mm]

Sintered bauxite 1.49 0.56

± 0.26 ± 0.09

Alumina grinding balls 2.01 1.17

± 0.50 ± 0.20

Basalt

2.89

± 1.08

Quartz flint

Quartz sand

2.02

0.80

± 0.57

± 0.18

Normal corundum F14

NC F16

1.83

1.61

± 0.42

± 0.36

0

0.1

0.2

0.3

0.4

0.5

0.6

0.7

0.8

0.9

1

0 200 400 600 800T [°C]

ëS

O[W

/mK

]

Quartz flint Quartz sandNormal Corundum F14 NC F16Bauxite 1.5 Bauxite 0.6Alumina 2.0 Alumina 1.2Basalt

Fig. 2: Thermal bulk conductivity from 20 to 800°C for a variety of granular materials

0%

20%

40%

60%

80%

100%

0 200 400 600 800 1000 1200 1400

Grain size [ìm]

Fra

cti

on

[%]

Quartz-Sand_orig. Quartz-Sand_30cycBauxite_orig Bauxite_30cyc

Fig. 3: Cumulated grain size distribution of quartz sand and bauxite after 0 und 30 cycles

FlowabilityThe flow behavior of the bulk not only influences the design of the heat exchanger, but also the thermal behaviour, since the contact time at the walls strongly depends on particle flowability. Rheological measurements have been conducted with an annular shear-tester.Testing reveals that the resulting flow functions are in the range of “easy flowing” or even “free flowing”, as shown in fig. 5 for quartz sand and bauxite. Occurence of attrition leads to a deteriorated flow behaviour, because both mean grain size and bulk porosity decrease as grain size distribution widens. This again has a significant impact on the MBHE design: for quartz sand, the critical spacing between the tubes would have to be increased by 340% to 9 mm, cleary worsening the device's power density.

ConclusionsProperties of granular materials for the design of a moving bed heat exhanger application were investigated.Thermal bulk conductivity of the tested candidate materials show a variation in a narrow range below 1.0 W/mK, mainly depending on the material, temperature and grain size.The use of natural products including quartz phases and in particular quartz materials, bears the risk of desintegration of the inventory material due to thermal and mechanical load in the MBHE.The flowability of the investigated products is rated as “easy” or “free flowing”. However, attrition may lead to significant changes in flow behavior and therefore has to be taken into account for heat exchanger design.

0

0.1

0.2

0.3

0.4

0.5

0.6

0.7

0 2 4 6 8 10

Consolidating Stress [kPa]

Fa

ilu

reS

tren

gth

[kP

a]

Bauxite Bauxite 66% attrtion

Quartz sand Quartz sand 28% attrtion

not flowing

very cohesive

cohesive

easy flowing

free flowing

Fig. 4: Attrion vs. shear strain for a variety of bulk materials

Table 1: Overview of tested granular materials

Fig. 5: Flow functions of quartz sand and bauxite with and without attrition

HTS LTS

G

Particle-Receiver

Solar Radiation from Heliostats

Steam Turbine and Generator

Condenser Eco

800 –1000°C

300-500°C

SO,in

T

SO,out

T

FL,in

T

FL,out

T

MBHE Evaporator and Superheater

German Aerospace Center

Institute ofTechnical Thermodynamics