WO2020069811A1

WO2020069811A1 - Component for a combustion chamber of a gas turbine

Info

Publication number: WO2020069811A1
Application number: PCT/EP2019/073664
Authority: WO
Inventors: Holger Grote; Alexander Bezold; Benjamin DERMEIK; Marcus Gwenner; Ruth HAMMERBACHER; Friederike Lange; Hannes LORENZ; Andreas Roosen; Nahum Travitzky; Jochen Zwick; Stanley VAN KEMPEN
Original assignee: Siemens Aktiengesellschaft
Priority date: 2018-10-05
Filing date: 2019-09-05
Publication date: 2020-04-09
Also published as: DE102018217059A1

Abstract

The invention relates to a component for a combustion chamber of a gas turbine, which component has a multi-layer structure in the form of ceramic films and/or paper made of pre-ceramic material, the inner and outer structure of the component being matched to the dimensions and conditions in the gas turbine combustion chamber. The invention further relates to a gas turbine combustion chamber having the component and to a method for producing the component.

Description

description

COMPONENT FOR A COMBUSTION CHAMBER OF A GAS TURBINE

The invention relates to a component for an annular combustion chamber of a gas turbine, which has a multilayer ceramic structure. The invention further relates to a method for producing the multilayer ceramic structure.

A combustion chamber is a container in which an exothermic reaction takes place through the supply of an oxidizer (oxygen carrier, mostly air) and one or more fuels. Combustion chambers are used for example in gas turbines. An annular combustion chamber has an annular combustion chamber in which one or more fuel injection valves are arranged. There are subject to combustion chambers high thermal loads. For cooling the combustion chamber wall, e.g. Air is used that enters through small holes in the combustion chamber wall and thus forms a cooling film. The use of ceramic heat shields - for example in silo or ring combustion chambers, where ceramic heat shields correspond to the so-called "hot wall concept" - can reduce the consumption of cooling air and increase the efficiency of the gas turbines.

At the same time, new part costs for ceramic components can usually be considerably reduced compared to a metallic variant. In addition, an increase in the service life of the ceramic heat shields by approx. 12% leads to cost advantages in service and an increased availability of the gas turbines for the operator compared to the metallic components.

The replacement of further metallic components in the combustion chamber by ceramic components will lead to further cooling air savings and a further increased service life of the corresponding components. In currently used ring It is not possible to replace combustion chambers, particularly due to the limited space available for the remaining metallic components, for example intake shell plates, with monolithic ceramic standard components. In principle, the following metallic components of the gas turbine come into question for replacement by ceramic components: a. Inlet bowl plates

b. Burner inserts

c. Ring segment

d. Baskets and Transitions in the PCS Combustion System e. Other burner components, for example nozzles or other metallic components with limited installation space.

This object is achieved by a component with the features of claim 1 and by a method with the features of claim 16. Further advantageous embodiments and embodiments of the invention emerge from the claims at under, the figures and the exemplary embodiments. From the embodiments of the invention can be combined with each other in an advantageous manner.

A first aspect of the invention relates to a component for a combustion chamber of a gas turbine, which has a cold gas side facing a combustion chamber housing of the combustion chamber, a hot gas side facing the hot gas path of the combustion chamber and a core connecting the cold gas side and the hot gas side, the hot gas side, the cold gas side and the core of the component each have at least one material layer comprising a ceramic material.

The use of so-called "layered structures" advantageously enables ceramic components with properties that meet the requirements to be placed in the respective position in the combustion chamber design and provide. Such "layered structures" can be referred to as a multilayer structure. These structures can be produced using the so-called ceramic multilayer technology, which is based on cast films and / or preceramic papers. Both methods in themselves and their combination are completely new for use in The components manufactured using ceramic multilayer technology are characterized by a flexible arrangement of individual layers (also known as hybrid laminates). Furthermore, different materials can be arranged on one level, for example by using preceramic paper strips. The components produced are The combustion chambers for which the component is intended are, in particular, ring combustion chambers, tubular combustion chambers (English, can-type) or tubular ring combustion chambers.

Furthermore, specific component properties can be optimized. This is particularly due to weak and / or strong ones

Enables interfaces that allow targeted absorption of the crack energy. Furthermore, component properties can be optimized through a targeted adjustment of the microstructure and through a targeted adjustment of the residual stresses. In addition, certain geometric requirements (radii, steps and the like) can be realized in the components according to the invention.

The invention is therefore advantageous because, compared to conventional components of ring combustion chambers, additional cooling air is saved and the components are cheaper in terms of manufacturing, service and product costs. Furthermore, the components according to the invention are distinguished by a higher machine availability and a lower reject rate than conventional components. The component according to the invention preferably consists predominantly, particularly preferably completely, of ceramic material. As a result, the advantages described above, brought about by the ceramic material, can be achieved particularly effectively. The component preferably comprises at least one material layer made of an oxide ceramic and / or at least one material layer made of a non-oxide ceramic.

The component according to the invention is particularly preferably used as inlet shell plates, burner inserts, liners, ring segments and nozzles and liners for baskets and transitions in CAN combustion systems (tube combustion chambers). The said components are more resistant to corrosion and erosion than conventional metallic components made of metal. The operating temperatures of the new ceramic components are up to 1973 K. For protection against hot gas corrosion, it is particularly advantageous if the inlet shell plates have dense aluminum oxide layers or yttrium aluminum garnet layers (YAG layers) on their component surface.

In the component according to the invention, the at least one layer of the hot gas side preferably has different material properties than the at least one layer of the core. In the respective component areas, materials are used that best meet the local requirements with their property profile, ie the corresponding thermal, chemical and / or mechanical operating loads. The component surface in the combustion chamber atmosphere is exposed to particularly demanding thermal loads. The core is particularly used for thermal insulation and / or resistance to thermal shock, creep fatigue and crack growth. The at least one layer on the cold gas side serves, for example the thermal insulation and / or optimizes the joint to the wall of the combustion chamber.

In this case, erosion and corrosion-resistant material is advantageously used for the at least one layer of the hot gas side. It is therefore particularly preferred if the material on the hot gas side has no silicon, that is to say is provided from a silicon-free ceramic material. Furthermore, it is particularly preferred if the material of the at least one layer on the hot gas side has Al2O3 or YAG.

Furthermore, thermal expansion gradients can advantageously be generated in multilayer structures with the aid of multilayer technology. The integration of a thermal expansion gradient advantageously reduces stresses and deformations of the component under stress from a temperature gradient. Here are thermal expansion differences up to 4.2e ^{~ 6} K ¹ between adjacent

Layers possible. A material is advantageous in the surface area of the component according to the invention, ie on the hot gas side (and the cold gas side), which has a smaller thermal expansion than the materials in the core. This is made possible, for example, by using materials with different coefficients of thermal expansion for the individual layers, the material on the hot gas side having a smaller coefficient of thermal expansion than the material of the core. For example, a layer of MgAl204 can be placed in the core. A material made of this material has a relatively high coefficient of expansion (a = 8.80e ^-6 K ¹ ) compared to AI2O3 (a = 8.00e ^-6 K ^x ). This exemplary type of arrangement advantageously enables a targeted introduction of residual compressive stresses Increase in fracture toughness, as well as the thermal and mechanical load tolerances of the multilayer structure.

The material preferably has in the surface area of the component according to the invention, i.e. on the hot gas side (and the cold gas side), a lower sintering shrinkage than the material of the core. The utilization of a different sintering behavior of individual layers also enables a targeted introduction of compressive residual stresses to increase the fracture toughness, as well as the thermal and mechanical load tolerances of the multilayer structure. The sintering shrinkage difference is achieved by using layers with different grain size distributions and can be varied between 0% and 21% with the multi-layer technology. Not only the absolute sintering shrinkage, but also the sintering rate of the layers as a function of the sintering profile, which also depends on the grain size distribution, influences the residual stresses. As a result, compressive stresses can be generated in layers that have a higher absolute sintering shrinkage than the adjacent layer. The damage behavior of the multilayer structure can be controlled via the local distribution of the compressive stresses. For example, compressive stresses on the outside of a multilayer structure lead to an increased load tolerance, whereas compressive stresses on the inside result in an increased damage tolerance. The maximum difference between the relative free sinter shrinkage should not be more than 6.5%.

The material of the at least one layer on the cold gas side preferably has a higher density than the other layers. Dense materials have an inherent sensitivity to thermal shock, which leads to rapidly growing damage when used in areas with changing temperatures leads. By using dense materials in the cold area of the component, the materials experience smaller temporal temperature differences, but still give the component sufficient mechanical properties and are therefore suitable as a joint.

Porous homogeneous and / or heterogeneous materials are preferably used for the component according to the invention. The damage tolerance on the structure level is increased by the materials. Multi-layer structures have a tolerance of damage that can be achieved by targeted processing of the interfaces. Crack deflection and crack absorption mechanisms can be used in a targeted manner through a suitable material selection and layer arrangement. Crack absorption in pores, growing together of cracks, crack deflection due to differences in rigidity between grains of different phases and a high number of existing crack fronts allow these materials to dissipate relatively large amounts of elastic stored energy by forming new surfaces. In order to integrate the energy-degrading mechanisms, monolithic materials should have a spherical porosity of at least 37%. The porosity required can be significantly reduced by using a different pore morphology or pore distribution. Heterogeneous materials should consist of a two-phase or multi-phase mixture in which there is a difference in stiffness and / or thermal expansion, or there should be weak interfaces between the phases. A combination of porosity and heterogeneity can also be used. In addition, phases can be added in heterogeneous structures, which increase the thermal shock resistance of the material by increasing the thermal conductivity of the layer.

The phases can also have a rough grain morphology, which acts as an obstacle for cracks or redirects them and thus with energy, and thus also advantageously increases the thermal shock resistance of the material.

The component according to the invention preferably has a combination of rather stiff and / or comparatively less stiff layers. The stiffness of a layer is a function of its elasticity, i.e. it describes the resistance of the layers to elastic deformation caused by mechanical forces or moments. Furthermore, the layers preferably have a different layer thickness. Furthermore, the layers preferably have an internal compressive stress. The said properties increase the overall potential of the damage tolerances of the multilayer component in comparison to monolithic structures.

The component according to the invention is preferably produced by a process for ceramic multilayer technology using a ceramic green sheet and / or preceramic paper.

A second aspect of the invention relates to a combustion chamber for a gas turbine with a component according to the invention. The combustion chambers are particularly ring combustion chambers, pipe combustion chambers (English, can-type) or pipe ring combustion chambers.

A third aspect of the invention relates to a method for producing a component according to the invention, comprising the steps:

Manufacture of ceramic foils and / or paper from a preceramic material, Stacking a certain number of layers, each consisting of a ceramic film and / or paper made of a preceramic material, targeted deformation of the multilayer structure formed,

Post processing.

The advantages of the method according to the invention essentially correspond to the advantages of the component according to the invention.

The method is particularly advantageous because the targeted deformation of the component during manufacture exploits the residual stress caused by the different shrinkage and thermal expansion behavior of the individual layers, in order to cause a macroscopic deformation of the component, and thus enables one Minimization of the necessary post-processing. This works both for symmetrical multilayer structures that only have orthotropic deformations, and for asymmetrical structures that can also be manufactured by using thermal expansion differences and the anisotropic sintering shrinkage behavior of the individual layers, either single or double curved.

The method according to the invention is essentially a ceramic multilayer technology based on ceramic green foils and / or preceramic papers. The combination of the comparatively thin starting products for refractory materials, which are processed into multilayer components, enables the provision of ceramic-based components, which are conventionally provided on a metallic basis. General embodiments of the method are explained below.

Ceramic film technology essentially has the following steps:

- powder preparation for slip,

- film casting and drying,

- cutting, stacking and laminating,

- binder burnout and sintering,

- Post processing.

With ceramic film technology, a powder is first processed into a slip. Grain fractions of 100 nm to 3 mm are possible (typically 4 fractions: d50: 1 μm to 3 μm, d50: 12 μm to 20 μm, d50: 400 μm to 500 μm; d50: 850 μm to 950 μm) Packing behavior and the sintering activity (eg for binding a coarse grain phase through a fine-grained matrix) and thus overall influencing the properties. Fibers can be used. The fibers have the following geometry: length> 1 mm and diameter 2 μm to 4 μm. The properties of the fibers, e.g. Toughness can be affected. All conceivable morphologies of the starting materials are possible.

With ceramic film technology, all materials can also be mixed with one another. A mixture of different grain fractions is possible (typically: mono- to tetramodal). This serves, for example, to increase the packing density and to form a storage structure. The material and grain fraction mixture can also be combined with one another. Mixing takes place by means of mills and mixers, eg Eirich mixers, attritors, ball mills, vessels on rollers, tumble mixers and overhead mixers. Grinding balls and tons of different sizes (ball: 1 mm to 10 mm, tons: 5 mm to 20 mm height) and different materials (e.g. AI2O3, stab. Zr02) can be used. The grinding media size is adjusted to the fineness of the powder fractions to be mixed.

Organic auxiliary materials are used in ceramic film technology. Water, ethanol, MEK, hexane, toloul, isopropanol or azeotropic mixtures of the aforementioned solvents (content from 33% by volume to 55% by volume) are used as solvents. The dispersant has an electrical, steri cal or electrosteric effect (content from 0.01 mass% to 3 mass% based on 100 mass% of the weighed powder, typically 0.5 mass% to 3 mass%). Various binders are possible, for example polyvinyl butyral, polyvinyl alcohol, polyvinyl acetate, polymethyl methacrylate and methyl cellulose, PVP, acrylates etc. The binders have a content of 5% by mass to 12% by mass based on 100% by mass of the powders weighed in. Typical molar masses of the binders are around 40,000 g / mol to 100,000 g / mol. The binders are used to adjust the viscosity (5 Pas to 20 Pas) and the rheological behavior of the slip (shear thinning behavior without thixotropic behavior, setting the strength and flexibility of the green sheets and their lamination behavior). Various plasticizers are also possible, for example benzoa testers, waxes, dioctyl phthalate, dibuthyl phthalate, benzyl butyl phthalate, alkylbenzyl phthalate and polyethylene glycol. The plasticizers have a content of 5 to 12 mass% based on 100 mass% of the weighed powder). The plasticizers are used to adjust the strength and flexibility of the green films and thus their processability (especially with regard to lowering the glass transition temperature of the binder in order to achieve low processing temperatures during lamination). In the case of discontinuous pouring, 50 ml to 3 l are added. In the case of continuous casting, slip is continuously fed as long as it is necessary.

The ceramic foils are then poured and dried. The slip is sieved off if the powder size is sufficiently small (<45 gm). The grinding media used, agglomerates or undissolved organic components are separated (mesh size: 10 gm to 500 gm). The slip is degassed using an Eirich mixer, rotary evaporator (suppress: 180 mbar to 250 mbar, 30 rpm to 120 rpm, 20 min to 45 min), Thinky Mixer, vacuum cabinet or using defoamers. It is essential that the slip is pourable (viscosities 5 Pas to 20 Pas). The film width is chosen between 20 cm and 110 cm. The film length is chosen between 1 m and 10 m, unless the film is continuous. Different doctoring techniques are used, e.g. Single / double chamber casting shoe, doctor blade, adjustable or fixed doctor blade / casting blades. The drawing speed is from 0.1 m / min up to 10 m / min. Different drying methods can be used: it warms air, saturated solvent atmosphere, countercurrent process, circulating air, IR, microwave and / or temperature-controlled substrates. Different carrier foils can be used (eg steel tape, siliconized PET foil, uncoated PET foil, ...).

The ceramic foils are then cut, stacked and laminated. Cutting and processing are carried out using hot cutting, guillotine shears, lasers, knife cutting, water jet cutters, saws, band saws, milling machines, punching (cutting dimensions 10 x 10 mm ² to 200 x 200 mm ² ). The surface quality can be changed by roughening or perforation. Corrugated structures are possible (e.g. corrugated cardboard ren). It is possible to integrate materials within one level (inlays and outside areas made of different foils, strips made of different materials, creating cavities).

Stacking is done with or without the help of pins, dies, and or alignment marks. Then thermal compression takes place under conditions of 30 MPa to 50 MPa, 333 K to 373 K, 10 min to 90 min, using matrices (dimensions: 30 x 40 mm ² to 200 x 200 mm ² ). The matrices can themselves have curvatures, radii and chamfers for setting certain geometries. Cold low pressure lamination is carried out at <5 MPa, room temperature, with double-sided adhesive films with or without backbone (backbone thickness 45 gm to 250 gm), optionally with or without a die. Gluing can be done with aqueous or solvent-based liquid glue, without or with ceramic particle filling, optionally with or without a matrix. Lamination is possible with the help of slips (these slurries correspond in composition to the slurries of the casting). Cold low pressure lamination and thermocompression or gluing and thermocompression can be combined.

Generative processes can still be used (e.g. laminated object manufacturing).

Binder burnout and sintering are carried out using dense or porous (especially for better degassing) kiln furniture made from AI2O3, MgO, stab. Zr02 or anamullite (5 x 50 x 50 mm ³ up to 50 x 1000 x 1000 mm ³ ) is provided. AI2O3, Mulit or ZrC> ₂ are used as separating sand; this serves to reduce the friction between sintered material and kiln furniture. The sintered structure is muffled compared to heating elements in order to achieve an even temperature distribution. The position of the components can vary: lying, standing, supported, unsupported, with or without load, with or without supporting pulse bedded, with a gap between the components or edge on edge. The step takes place under an oxidizing atmosphere, a reducing or protective gas atmosphere is also possible, as is sintering under vacuum. Chamber furnaces, tube furnaces and tunnel furnaces can be used, as well as protective gas furnaces. The debinding is adapted to the decomposition temperatures of the organic system (heating rates from 0.25 K / min to 3 K / min, holding times at temperatures between 473 K to 873 K, holding times from 60 min to 120 min). Sintering takes place at temperatures from 1873 K to 2073 K, holding times from 120 min to 600 min and heating rates from 1 K / min to 10 K / min. Cooling takes place at cooling rates of 1 K / min to 10 K / min. Passive or active cooling is possible.

Post-processing includes various activities, e.g. Cutting (band saw, circular saw, low-speed saw, water jet cutting, lasers, ...), milling and grinding (reaching the final format, plane parallelism, edges and corner processing).

The changes or variations in the above-mentioned parameters of the process influence the processing behavior and the properties of the green foils, the laminates and the sintered components. The following property ranges can be achieved on the sintered components or the properties mentioned below can be varied: the sintering shrinkage between 0 and 21%, the porosity between 0 and 45%, the thermal conductivity between 7 W / (mK) and 35 W / (mK), the modulus of elasticity between 20 GPa and 400 GPa, the strength between 8 MPa and 350 MPa, the fracture toughness (K _IC ), the permeability, the coefficient of thermal expansion between 5 · 10 ⁶ 1 / K and 19 · 10 ⁶ 1 / K, the behavior of corrosion and erosion, thermal fatigue, creep behavior, emission behavior, behavior under temperature change load and thermal shock, and anisotropic behavior in and perpendicular to the casting direction and in thickness. In laminates, the interfacial strength and internal stresses can be varied.

Paper technology essentially has the following steps:

- preparation of a paper suspension,

- manufacture of the paper,

- calendering,

- coating,

- cutting, stacking and laminating,

- binder burnout and sintering,

- Post processing.

A ceramic powder is prepared for the preparation of the paper suspension (d50: 500 nm to 5 ml). Ceramic fibers can also be used (diameter 2 gm to 4 gm, length> 1 mm). All conceivable geometries of the starting material are possible, spherical being preferred. All usable materials can be mixed together. Organic auxiliaries include cellulose fibers: length: 0.5 mm to 2.5 mm; Diameter: 15 gm, anionic and cationic starches, latex and retention aids such as polyethylene enimine.

For papermaking, a pulp suspension is first homogenized. The order of the addition steps is essential. Continuous and discontinuous papermaking is possible. The thickness of the paper layer produced be between 200 gm and 1000 gm, the width between 25 cm and 50 cm. The belt speeds are between 1 m / min and 3 m / min. Then the papers produced are dried. Humidification is adjustable for calendering. Different types of rollers can be used, smooth, corrugated, made of steel or plastic. The temperature of the rollers is between 293 K to 513 K. The line pressure is between 50 kN / m and 400 kN / m. The roller speed is between 0.5 m / min and 5 m / min.

The goal of the coating is the production of multilayer structures and surface sealing. The thickness of the coating is between 10 μm and 100 μm. Coating is carried out using a ceramic suspension based on water, ceramic powder and organic glue (polyvinyl acetate). Coating is carried out by knife coating or coating system.

The cutting is done mechanically, by laser cutting, punching or water jet. Stacking and laminating are carried out as described above for the ceramic films. Binder burnout and sintering also take place as described above for the ceramic foils.

Post-processing is carried out, among other things. by cutting with a band saw, circular saw, low-speed saw, water jet cutting, by milling and grinding (reaching the final format, parallelism of the plan, edges and corner processing).

The following property ranges can be achieved on the sintered components or the properties mentioned below can be varied: the sintering shrinkage between 8 and 30%, the porosity between 20% and 75%, the thermal conductivity between 2 W / (mK) and 12 W / (mK), the elastic modulus between 10 GPa and 245 GPa, the strength between 5 Pa and 70 MPa, the fracture toughness (Ki _{, c)} , the permeability, the thermal expansion coefficient between 0.5 · IO ^-6 1 / K and 9 · IO ^-6 1 / K, that

Corrosion and erosion behavior, thermal fatigue, creep behavior, emission behavior, behavior under thermal shock and thermal shock, and anisotropic behavior in and perpendicular to the casting direction and in the thickness. The interfacial strength and the inherent stresses can be varied in laminates.

The invention is explained in more detail with reference to the figures. Show it

Figure 1 is a representation of a conventional Ringbrennkam mer.

FIG. 2 shows an embodiment of the component according to the invention.

Figure 3 is a flow diagram of an embodiment of the inventive method.

An annular combustion chamber 1 of a gas turbine has an outer shell 2, which surrounds a cavity 3 forming the combustion chamber 1, as shown in FIG. 1. The Brennkam mer 1 has in Fig. 1 an example of a burner 4, which is arranged in the upper part of the combustion chamber 1; Several burners can be arranged in the combustion chamber. The Bren ner 4 has, as shown in FIG. 1, an access for fuel 5 and two accesses for an oxidation carrier 6, for example compressed air. In the inlet opening 7, the supplied fuel and the air are mixed. The cavity 3 is provided for the combustion of the fuel-air mixture formed. The hot combustion gases pass through outlet 8 into a turbine chamber of the gas turbine (not shown).

The cavity 3 is tetat tet with ceramic heat shields 9. The heat shields of the last row before the outlet 8 are referred to as inlet plates 10. The inlet plates 10 are conventionally made of metal. According to the invention, ceramic inlet plates 10 for the ring combustion chamber 1 are provided.

2 shows an embodiment of an inlet shell plate 10 constructed according to the invention. The inlet plate shell 10 is divided into a hot gas side 11 directed towards the cavity 3, a core 12 adjoining the hot gas side 11 and a cold gas side 3 directed towards the outer shell 2. The hot gas side 11 and the cold gas side 13 each have a layer 15. The core has a number of 17 layers 15 (fewer layers of the core are shown in FIG. 2 for illustration). The number of layers in the individual areas can alternatively be different.

The layers 15 are provided from cast ceramic foils or preceramic paper. The Einlaufschalenplat te 10 has a thickness of up to 16 mm.

The material of the hot gas side 11 layer is AI2O3. The location of the hot gas side 11 has a thermal expansion coefficient of 8.0e ⁶ K ¹ . One layer of the hot gas side 11 has a thickness of 2790 μm. The particle size distribution is 15% fine grain (1 μm to 3 μm) and 85% coarse grain (1 μm to 45 μm). The layer has a porosity of 34.2%. The free sintering shrinkage is 4.7%, the modulus of elasticity is 83.2 GPa and the strength is 33.0 MPa. The material of the layers of the core 12 is AI2O3. For example, MgA ^ Cg and / or a mixture of Al2O3 and MgA ^ Cg can also be used as the material. The layers of the core 12 have a thermal expansion coefficient of 8.80e ^-6 K ¹ . The thickness of the foils forming the individual layers is 620 μm each. The particle size distribution is 15% fine grain (1 μm to 3 μm) and 85% coarse grain (1 μm to 45 μm). The layers have a porosity of 21.1%. The free sinter shrinkage is 10.7%, the elastic modulus 131.6 GPa and the strength 97.5 MPa.

The material of the cold gas side 13 layer is AI2O3. The location of the cold gas side 13 has a thermal expansion coefficient of 8.0e ⁶ K ¹ . One layer of the cold gas side 13 has a thickness of 2390 μm. The particle size distribution is 45% fine grain (1 µm to 3 µm) and 55% coarse grain (1 µm to 45 µm). The layer has a porosity of 22.5%. The free sintering shrinkage is 8.9%, the elastic modulus 352.5 GPa and the strength 71.0 MPa.

In a method according to FIG. 3 for producing a component according to FIG. 2, ceramic foils and / or paper are produced from a preceramic material in a first step S1. If specifically named substances and devices with a reference to their origin are given below, it is clear that the specialist can of course use adequate substances and devices.

For the production of ceramic foils and / or paper, a slip approach is provided, which is then cast into foils and / or paper. For a construction part to be made from two different foils, a slip approach is provided for each foil. An 11-polyethylene bottle is used as the mixing vessel. The grinding balls are six 15 mm high grinding bowls, twelve 10 mm high grinding bowls and Grinding balls with a diameter of 3 mm are used, all of which consist of Al ₂ O ₃ . A slip mixture of 600 ml is produced.

Two different Al ₂ O ₃ powders are used for the first film (60 vol% from d ₅ o: 1 ym to 3 ym and 40 vol%, d ₅ o: 12 ym to 20 ym). Two different A ^ Cy powders are also used for the second film (30% by volume from d ₅ o: 1 μm to 3 μm and 70% by volume, d ₅ o: 12 μm to 20 μm).

A 44.59% by volume azeotropic mixture of ethanol and toluene is used as solvent (68% by mass of ethanol, 32% by mass of toluene). Hypermer ™ (Croda Inc., Edison, USA) is used as a dispersant in a 1% by mass based on 100% by mass of the weighed powder. PVB 98 (Solutia Inc., St. Louis, USA) is used as a binder to a 5% by mass based on 100% by mass of the weighed powders. Santizer (Ferro, Antwerp, Belgium) is used as a plasticizer to a 5% by mass based on 100% by mass of the weighed powder. The dispersion and homogenization takes place for 24 hours in a tumble mixer.

To cast the foils, both slurries are sieved using a sieve with a mesh size of 500 μm. Both slips are degassed for 30 min at 230 mbar and 60 rpm. A double chamber casting shoe is used for casting. The casting gap for both slurries is 1500 ym (casting knife), and the casting speed is 1800 mm / min. A siliconized polyethylene terephthalate film is used as the carrier film. The viscosity of the first film is 11.3 Pas at a shear rate of 20 s-1; the viscosity of the second film be 9.4 Pas at a shear rate of 20 s-1. Then the films are dried in a saturated solvent atmosphere for 24 hours. The film thickness of both films is approximately 600 μm. The green foils produced are cut and stacked in a second step S2 of the method according to FIG. 3. Both foils are cut to size 40 x 40 mm ² using a hot cutter. The blanks are stacked in a steel die with brass stamps with the structure foil 2 / foil 1 / foil 2. As many foils are stacked as are required for the component.

In a third step S3, the multilayer structure is deformed in a targeted manner in accordance with the desired target structure. The films are laminated via thermal compression (353 K, 42 MPa, 15 min). There are used matrices that have geometric characteristics that are already suitable for setting certain characteristics of the component to be manufactured. For the targeted deformation, there are also different ones

Shrinkage and thermal expansion behavior of the individual layers controlled, which lead to residual stresses that are used to cause a macroscopic deformation of the part.

The laminates are sintered in an oxidizing atmosphere. Dense A ^ Cg plates without separating sand are used as kiln furniture, with complete muffling of the samples. Chamber furnaces are used.

For debinding, the laminates are heated from room temperature at 1 K / min to 423 K, then from 423 K to 523 K at 0.25 K / min and kept at this temperature for 2 hours, then from 523 K to 693 K at 0. 25 K / min heated and held at this temperature for 2 h, then heated from 693 K to 773 K at 0.25 K / min and held at this temperature for 2 h, and then cooled from 773 K to room temperature at 3 K / min. For sintering, the laminates are heated from room temperature to 1323 K at 3 K / min and held at this temperature for 1 h, then heated from 1323 K to 1973 K at 3 K / min and held at this temperature for 5 h, and then from 1973 K to room temperature at 3 K / min.

In a fourth step S4, the manufactured component is reworked so that it can be used in an annular combustion chamber according to FIG. 1. This step mainly includes cutting, milling and grinding the component.

The laminates produced have a green thickness of 1575 gm and a green density (geometric density according to EN 623-2 and 993-1) of 74.6% TD. The sinter thickness is 1436 gm and the sinter density (immersion measurement according to EN 623-2 and 993-1) 77.2% TD. The sintering shrinkage is laterally 7.0% in the pouring direction and 7.6% perpendicular to the pouring direction and 8.8% vertical. The modulus of elasticity (determined over the US term according to DIN EN 843-2 and DIN EN ISO 12680-2) is 200 GPa in the casting direction and 198 GPa perpendicular to the casting direction. The characteristic strength (via likelihood from double ring bending tests) is 101.4 MPa and the Weibull modulus (via likelihood from double ring bending tests) 5.4.

Alternatively, a laminate can also be produced from a combination of ceramic foils and paper made of preceramic material using film technology. For this purpose, a slip approach is provided for film and paper. An 11-polyethylene bottle is used as the mixing vessel for the film. Six 15 mm high grinding bowls, twelve 10 mm high grinding bowls and grinding balls with a diameter of 3 mm are used as grinding balls, all of which consist of Al ₂ O ₃ . A slip mixture of 600 ml is produced. Two different Al203 powders are used for the film (15 vol% from d ₅ o: 1 ym to 3 ym and 85 vol%, d ₅ o:

12 ym to 20ym). A 44.8% by volume azeotropic mixture of ethanol and toluene is used as solvent (68% by mass of ethanol, 32% by mass of toluene). Hypermer ™ (Croda Inc., Edison, USA) is used as a dispersant at 1% by mass based on 100% by mass of the weighed powders. PVB 98 (Solutia Inc., St. Louis, USA) is used as a binder to a 5% by mass based on 100% by mass of the weighed powders. Santicizer® (Ferro, Antwerp, Belgium) is used as a plasticizer to a 5 mass% based on 100 mass% of the weighed powder. The dispersion and homogenization takes place for 24 hours in a tumble mixer.

A ^ Cy powder (d50: 0.8 ym) and / or Al ₂ O ₃ fibers (diameter 2 ym - 4 ym, length> 1 mm) is used for the paper. Water is used as the solvent. The additives used are potato starch, Nychem® (Emerald Performance Materials, Acron, OH, USA) and / or Polymin® (BASF, Ludwigshafen, Germany).

To cast the film, the slip is sieved off using a sieve with a mesh size of 500 μm. The slip is degassed for 30 min at 230 mbar and 60 rpm. A double chamber casting shoe is used for casting. The casting gap is 2500 ym (pouring knife), and the casting speed 3000 mm / min. A siliconized polyethylene terephthalate film is used as the carrier film. The viscosity of the first film is 10.8 Pas at a shear rate of 20 s-1; the viscosity of the second film is 9.4 Pas at a shear rate of 20 s-1. Then the films are dried in a saturated solvent atmosphere for 24 h. The film thickness of both films is approximately 1100 μm. A dynamic sheet former is used to produce the paper. The drum speed is 1200 rpm. The pulp suspension is sprayed onto a sieve.

The paper is dried at 383 K for 15 min. Then the paper is coated with an adhesive layer and then dried at 323 K.

In step S2, film and paper are cut and stacked. Foil and paper are cut to the 40 x 40 mm ² format. The foils are cut using a hot cutter, and that of the paper using a paper cutter. The blanks are then stamped in a steel die with brass and stacked with the structure foil / paper / foil. As many foils are stacked as are necessary for the component.

In a third step S3, the multilayer structure is deformed in a targeted manner in accordance with the desired target structure. The deformation occurs among other things. during lamination. It is laminated via thermal compression (353 K, 42 MPa, 15 min). Matrices are used which have geometric features that are already suitable for setting certain features of the component to be manufactured. For the targeted deformation, different shrinkage and thermal expansion behavior of the individual layers are also controlled, which lead to residual stresses that are used to cause a macroscopic deformation of the component.

The laminates are sintered in an oxidizing atmosphere. Dense A ^ Cg plates without separating sand are used as kiln furniture, with complete muffling of the samples. Chamber furnaces are used. For debinding, the laminates are heated from room temperature at 1 K / min to 423 K, then from 423 K to 523 K at 0.25 K / min and kept at this temperature for 2 hours, then from 523 K to 693 K at 0. 25 K / min heated and held at this temperature for 2 h, then heated from 693 K to 773 K at 0.25 K / min and held at this temperature for 2 h, and then cooled from 773 K to room temperature at 3 K / min.

For sintering, the laminates are heated from room temperature to 1323 K at 3 K / min and held at this temperature for 1 h, then heated from 1323 K to 1973 K at 3 K / min and held at this temperature for 5 h, and then from 1973 K to room temperature at 3 K / min.

Here too, in a fourth step S4, the finished component is reworked, so that it can be used in an annular combustion chamber according to FIG. 1. This

The step mainly involves cutting, milling and grinding the component.

The laminates produced have a green thickness of 2248 gm and a green density (geometric density according to EN 623-2 and 993-1) of 69.5% TD. The sintering thickness is 2045 gm and the sintering density (immersion measurement according to EN 623-2 and 993-1) is 78.2% TD. The sintering shrinkage is 6.4% laterally in the pouring direction and 6, 6% perpendicular to the pouring direction and 9, 0% vertically.

The modulus of elasticity (determined over the US term according to DIN EN 843-2 and DIN EN ISO 12680-2) is 175 GPa in the casting direction and 169 GPa perpendicular to the casting direction.

To produce pure paper laminates, the papers produced as described are laminated. Modifications and changes of the invention which are obvious to a person skilled in the art fall within the scope of the patent claims.

Claims

1. Component (10) for a combustion chamber (1) of a gas turbine, which has a cold gas side (13) facing a combustion chamber housing (2) of the combustion chamber, a hot gas side (11) facing the hot gas path of the combustion chamber and one the cold gas side (13) and the hot gas side (11) connecting core (12),

the hot gas side (11), the cold gas side (13) and the core (12) of the component each have at least one material layer (15) comprising a ceramic material.

2. component (10) according to claim 1,

in which the component (10) consists predominantly of ceramic material.

3. Component (10) according to claim 1 or 2,

in which the component consists entirely of ceramic material.

4. Component (10) according to one of the preceding claims,

in which the component comprises at least one material layer (15) made of an oxide ceramic and / or at least one material layer made of a non-oxide ceramic.

5. Component (10) according to one of the preceding claims,

selected from the group comprising inlet bowl plates (10), burner inserts, ring segments and nozzles as well as liners for baskets and transitions in CAN combustion systems.

6. Component (10) according to one of the preceding claims, wherein the at least one layer of the hot gas side (11) has different material properties than the at least one layer of the core (12).

7. component (10) according to any one of the preceding claims,

in which the material of the at least one layer of the hot gas side (11) has Al ₂ O ₃ .

8. component (10) according to any one of the preceding claims,

in which the at least one layer of the hot gas side (11) has a Si-free ceramic material.

9. component (10) according to one of the preceding claims,

in which the material of the at least one layer of the hot gas side (11) has a lower thermal expansion coefficient than the material of the at least one layer of the core (12).

10. Component (10) according to one of the preceding claims, wherein the material of the hot gas side (11) and the cold gas side (13) has a lower sintering shrinkage than the material of the core (12).

11. Component (10) according to one of the preceding claims, in which the material of the layers comprises porous and / or heterogeneous materials.

12. Component (10) according to one of the preceding claims, wherein the material of the at least one layer on the cold gas side (13) has a higher density than the other layers.

13. Component (10) according to one of the preceding claims, in which the layers are arranged in a combination of rather stiff and / or comparatively less stiff layers.

14. Component (10) according to one of the preceding claims, which is produced by a method for ceramic multilayer technology using a ceramic green sheet and / or preceramic paper.

15. Combustion chamber (1) of a gas turbine with one component

(10) according to one of claims 1-14.

16. A method for producing a component (10) according to one of claims 1-14, comprising the steps:

Manufacture of ceramic foils and / or paper from a preceramic material,

Stacking a certain number of layers (15), each consisting of a ceramic film and / or paper made of a preceramic material,

targeted deformation of the multi-layer structure formed,

Post processing.