Method of manufacturing a sulfide-based ceramic element, particularly for IR-optics applications
10472287 ยท 2019-11-12
Assignee
Inventors
- Noha Hakmeh (Cesson-Sevigne, FR)
- Odile Merdrignac-Conanec (Acigne, FR)
- Xiang-Hua Zhang (Cesson-Sevigne, FR)
Cpc classification
C01B17/20
CHEMISTRY; METALLURGY
C04B2235/3284
CHEMISTRY; METALLURGY
C04B2235/666
CHEMISTRY; METALLURGY
C04B2235/9653
CHEMISTRY; METALLURGY
C04B2235/3208
CHEMISTRY; METALLURGY
C04B35/547
CHEMISTRY; METALLURGY
C04B2235/3227
CHEMISTRY; METALLURGY
C04B2235/6581
CHEMISTRY; METALLURGY
C04B2235/3215
CHEMISTRY; METALLURGY
International classification
C04B35/547
CHEMISTRY; METALLURGY
Abstract
A method of manufacturing a sulfide-based ceramic element, such as a transparent infrared optical element, comprises the steps of: synthesizing a sulfide powder; and sintering the powder to form the ceramic element; wherein the step of synthesizing the sulfide powder is performed by combustion in an aqueous solution, the solution comprising water as its only solvent, or containing water as its main solvent and at most 10%, and preferably at most 1% of the overall solvent mass, of one or more combustible solvents. The sulfide powder may be chosen, in particular, among ZnS, BaLa.sub.2S.sub.4, CaLa.sub.2S.sub.4.
Claims
1. A method of manufacturing a sulfide-based transparent infrared optical ceramic element comprising the steps of: synthesizing a sulfide powder; and sintering said powder to form said ceramic element; wherein said step of synthesizing said sulfide powder is performed by combustion in the presence of water by heating the aqueous solution at a temperature comprised between 400 C. and 800 C., said solution comprising 90-100% water and 0-10% of one or more non-water solvents based on the overall solvent mass.
2. The method according to claim 1 wherein said sulfide powder is chosen among ZnS, BaLa.sub.2S.sub.4 and CaLa.sub.2S.sub.4.
3. The method according to claim 1 wherein said step of synthesizing said sulfide powder comprises preparing an aqueous solution of a metal-containing oxidizing agent and a sulfur-containing organic fuel.
4. The method according to claim 3 wherein said metal-containing oxidizing agent is a metal nitrate.
5. The method according to claim 3 wherein said sulfur-containing organic fuel is a thioamide.
6. The method according to claim 3 wherein said sulfur-containing organic fuel is thioacetamide.
7. The method according to claim 1 wherein said solution is heated at a temperature comprised between 500 C. and 600 C. in a furnace.
8. The method according to claim 1 further comprising a step of performing a thermal post-treatment of said powder under a H.sub.2S/N.sub.2 flow prior to said sintering step.
9. The method according to claim 1 wherein said step of sintering said powder is performed by a method chosen from: hot pressing, spark plasma sintering, hot isostatic pressing, microwave sintering, natural sintering.
10. The method according to claim 1 wherein said step of sintering said powder is performed in a graphite die, using buffer layers of boron nitride powder interposed between the die and the powder to be sintered.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
(1) Additional features and advantages of the present invention will become apparent from the subsequent description, taken in conjunction with the accompanying drawings, which show:
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DETAILED DESCRIPTION
(9) Combustion synthesis is based on a redox reaction in an aqueous solution containing stoichiometric amounts of an oxidizing agent (typically a metal nitrate) and an organic fuel; advantageously, the fuel is also the source of the sulfur which reacts with the metal of the oxidizing agent to form a sulfide; it can then be a thioamide such as thioacetamide.
(10) The reagents used for the synthesis of ZnS were hexahydrated zinc nitride Zn(NO.sub.3).sub.2.6H.sub.2O (Alfa Aesar 99.998%) and thioacetamide (TAA) CH.sub.3CSNH.sub.2 (Sigma Aldrich 99%, ACS Reagent), and distilled water was used as the sole solvent. The masses of the reagents were computed using the following equations:
n.sub.ZnS=m.sub.ZnS/M.sub.ZnSwith m.sub.ZnS=mass of ZnS to be produced and M.sub.Zns=97,445 g/mol
M.sub.Zn(NO3)2.6H2O=n.sub.ZnS.Math.M.sub.Zn(NO3)2.6H2O with M.sub.Zn(NO3)2.6H2O =297.481 g/mol
m.sub.TAA=2n*.sub.ZnS*M.sub.C2H5NS with M.sub.C2H5NS=75,133 g/mol
(11) The reagents were introduced into a beaker containing distilled water (the volume of water is not essential). The mix was heated at a temperature lower than 100 C.preferably between 70 C. and 80 C.and stirred until zinc nitrate and TAA were completely dissolved. The solution was then placed in a muffle furnace pre-heated at 500 C.-600 C. (more broadly, the furnace temperature may be comprised between 400 C. and 800 ). The reaction occurred within about 15 minutes. The beaker was maintained 15-30 additional minutes after the completion of the reaction to eliminate possible residues and to obtain a white, homogeneous powder which was recuperated and grinded.
(12) Due to the fast kinetic of the combustion reaction, the crystallization of the produced ZnS was incomplete, and impurities were present. Therefore, a thermal post-treatment (sulfuration) of the ZnS powder under a gaseous H2S/N2 mixture (10/90) was performed. The powder, placed in a silica reaction tube, was introduced into the isothermal zone of a tunnel furnace. The reaction tube was purged under a nitrogen flow during a few (10-15) minutes, then heated at a temperature between 600 C. and 700 C. at a rate of 10 C./min. The nitrogen flow was then replaced by the H2S/N2 mixture. The treatment at 600 C. and 700 C. was continued for two hours; then cooling to ambient temperature was performed under nitrogen flow. The thermal profile of the post-treatment is illustrated on
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(14) The sintering of the sulfurated ZnS powder is performed at a temperature lower than 1020 C. to avoid a sphaleritewurtzite phase transition.
(15) The powder was sintered under vacuum (10-2mbar or less) at 900 C.-1000 C. (preferably 950 C.) with a heating rate comprised between 5 C./min and 30 min, e.g. of 10 C./min. A pressure of 50 MPa was applied at the sintering temperature for a duration varying between 30 min (quite unsatisfactory, see below) and 6 h or more (optimal), then released during cooling. The thermal profile of the sintering step is illustrated on
(16) Typically 4 to 5 g of ZnS powder are sintered in a graphite die (diameter: 20 mm), between two thin layers of boron nitride (Alfa Aesar, metal basis 99.5%) to hinder carbon diffusionleading to contamination of the ceramicsand to ease the removal of the sintered ceramics from the die. Then, optical elements such as lensesor simply optical windowmay be manufactured from the thus-obtained ceramic element using conventional techniques such as cutting, grinding, polishing, hole drilling etc.
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(19) For the sake of comparison,
(20) The inventive method has been described with reference to the specific case of ZnS ceramic elements, but it can be easily generalized to other sulfur-based ceramics, in particular to other IR-transparent ones, and more particularly to BaLa2S4 and CaLa2S4. Of course, the reagents change: while thioamides and in particular TAA can always be used as a fuel, the oxidizing agents, either hydrated or anhydrous, are lanthanum nitrate and barium nitrate for BaLa2S4 synthesis, and lanthanum nitrate and calcium nitrate for CaLa2S4 synthesis. Sulfuration is performed essentially in the same way as for ZnS, while sintering can be performed at a somehow higher temperature (950-1300 C.).
(21) Sintering pressure is preferably greater than or equal to 30 MPa; the upper pressure limit is set by the die; for graphite dies it is of abut 150 MPa. The sintering temperature is preferably comprised between 850 and 1000 C. for ZnS, and between 950 C. and 1300 C. for ternary sulfides such as BaLa2S4 and CaLa2S4.
(22) The invention has been described with reference to a preferred embodiment wherein water is the sole solvent used in the combustion synthesis step. However, the invention does not exclude alternative embodiments wherein a small (no more than 10% by mass) amount of other solventspossible combustible onesis present. Such complementary solvents may include ethanol, methanol, acetone (all of which are combustible) and/or nitric acid (which is not).
(23) The inventive method have been described with reference to a preferred embodiment wherein sintering is performed by hot-pressing. However, other sintering methodmay be used, such as flash sintering, also known as spark plasma sintering, hot isostatic pressing, microwave sintering and natural sintering.