Gas Phase Decomposition of an Organometallic Chemical Vapor Deposition Precursor to Ain: [A1(CH3)2NH2]3

1990 ◽  
Vol 204 ◽  
Author(s):  
Carmela C. Amato ◽  
John B. Hudson ◽  
Leonard V. Interrante

ABSTRACTA CVD reactor has been coupled to a molecular beam apparatus in order to study the gas phase decomposition of an organometallic precursor to AIN, tris-dimethylaluminum amide, [(CH3)2AINH2]3. The onset of decomposition occurs at a reactor temperature of 125°C. By 300°C, all mass spectral signals due to precursor have disappeared. With the addition of helium as a carrier gas in the CVD process, the temperature at which all precursor signals disappear is raised to 400°C. The evolution of methane accompanies the precursor decomposition. Mass spectra of the precursor and its deuterated analogue, [(CH3)2 AIND2]3, obtained between 50°C and 90°C, offer support for the existence of trimer-dimer-monomer equilibria in this temperature range.

1989 ◽  
Vol 168 ◽  
Author(s):  
Carmela C. Amato ◽  
John B. Hudson ◽  
Leonard V. Interrante

AbstractA novel technique for probing chemical vapor deposition reaction mechanisms is presented. A conventional hot-wall Pyrex reactor is coupled to a molecular beam apparatus. Preliminary results of the decomposition of an organometallic precursor to AIN, [AI(CH3)2NH2]3, indicate a decomposition temperature between 200 and 270°C. The mass spectrum of the precursor at 100°C provides evidence for the existence of a trimer-dimer equilibrium of the precursor at this temperature


Author(s):  
Sebastian Grimm ◽  
Seung-Jin Baik ◽  
Patrick Hemberger ◽  
Andras Bodi ◽  
Andreas Kempf ◽  
...  

Although aluminium acetylacetonate, Al(C5H7O2)3, is a common precursor for chemical vapor deposition (CVD) of aluminium oxide, its gas phase decomposition is not very well investigated. Here, we studied its thermal...


2017 ◽  
Vol 897 ◽  
pp. 83-86 ◽  
Author(s):  
Keisuke Fukada ◽  
Naoto Ishibashi ◽  
Yoshihiko Miyasaka ◽  
Akira Bandoh ◽  
Kenji Momose ◽  
...  

The depth profiles of n-type doping concentration in thick (>100 μm) and low-doped (< 4 × 1014 cm-3) 4H-SiC epilayers grown by chemical vapor deposition (CVD) were investigated. The variation in doping concentration during epitaxial growth are considered to be caused by: (1) variation in gas flow due to parasitic deposition, (2) variation in precursor decomposition rate due to change in reactor temperature, (3) variation in dopant incorporation rate due to change in wafer temperature, and (4) variation in supply of background dopants. By controlling all these parameters, a constant depth profile in thick (> 100um) epilayers was realized.


1999 ◽  
Vol 606 ◽  
Author(s):  
Carmela Amato-Wierda ◽  
Edward T. Norton ◽  
Derk A. Wierda

AbstractSilane activation, predominantly in the gas phase, has been observed during the chemical vapor deposition of Ti-Si-N thin films using Ti(NMe2)4, tetrakis(dimethylamido)titanium, silane, and ammonia at 450°C, using molecular beam mass spectrometry. The extent of silane reactivity was dependent upon the relative amounts of Ti(NMe2)4and NH3. Additionally, each TDMAT molecule activates multiple silane molecules. Ti-Si-N thin films were deposited using similar process conditions as the molecular beam experiments, and RBS and XPS were used to determine their atomic composition. The variations of the Ti:Si ratio in the films as a function of Ti(NMe2)4 and NH3 flows were consistent with the changes in silane reactivity under similar conditions.


1999 ◽  
Vol 606 ◽  
Author(s):  
Carmela C. Amato-Wierda ◽  
Edward T. Norton ◽  
Derk A. Wierda

AbstractTetrakis(dimethylamino)titanium (TDMAT) is an important precursor for TiN, TiCN, and TiSiN thin films in chemical vapor deposition. In order to better understand how the gas phase chemistry influences the formation of these films, the decomposition of TDMAT has been studied in a high-temperature flow reactor (HTFR) by molecular beam mass spectrometry (MBMS). Two kinetic regimes have been observed as a function of temperature. Rate expressions and mechanistic implications will be presented. Further studies are in progress to identify the gas phase species relevant to the decomposition mechanism of TDMAT.


1994 ◽  
Vol 9 (1) ◽  
pp. 104-111 ◽  
Author(s):  
Ching Yi Tsai ◽  
Seshu B. Desu ◽  
Chien C. Chiu

The kinetics of silicon carbide (SiC) deposition, in a hot-wall chemical vapor deposition (CVD) reactor, were modeled by analyzing our own deposition rate data as well as reported results. In contrast to the previous attempts which used only the first order lumped reaction scheme, the present model incorporates both homogeneous gas phase and heterogeneous surface reactions. The SiC deposition process was modeled using the following reactions: (i) gas phase decomposition of methyltrichlorosilane (MTS) molecules into two major intermediates, one containing silicon and the other containing carbon, (ii) adsorption of the intermediates onto the surface sites of the growing film, and (iii) reaction of the adsorbed intermediates to form silicon carbide. The equilibrium constant for the gas phase decomposition process was divided into the forward and backward reaction constants as 2.0 × 1025 exp[(448.2 kJ/mol)/RT] and 1.1 × 1032 exp[(-416.2 kJ/mol)/RT], respectively. Equilibrium constants for the surface adsorption reactions of silicon-carrying and carbon-carrying intermediates are 0.5 × 1011 exp[(-21.6 kJ/mol)/RT] and 7.1 × 109 exp[(-33.1 kJ/mol)/RT], while the rate constant for the surface reaction of the intermediates is 4.6 × 105 exp[(-265.1 kJ/mol)/RT].


Author(s):  
M. G. Lagally

It has been recognized since the earliest days of crystal growth that kinetic processes of all Kinds control the nature of the growth. As the technology of crystal growth has become ever more refined, with the advent of such atomistic processes as molecular beam epitaxy, chemical vapor deposition, sputter deposition, and plasma enhanced techniques for the creation of “crystals” as little as one or a few atomic layers thick, multilayer structures, and novel materials combinations, the need to understand the mechanisms controlling the growth process is becoming more critical. Unfortunately, available techniques have not lent themselves well to obtaining a truly microscopic picture of such processes. Because of its atomic resolution on the one hand, and the achievable wide field of view on the other (of the order of micrometers) scanning tunneling microscopy (STM) gives us this opportunity. In this talk, we briefly review the types of growth kinetics measurements that can be made using STM. The use of STM for studies of kinetics is one of the more recent applications of what is itself still a very young field.


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