Hostname: page-component-89b8bd64d-dvtzq Total loading time: 0 Render date: 2026-05-10T19:39:08.724Z Has data issue: false hasContentIssue false

Improvements in Bis(cyclopentadienyl)magnesium Purity as Determined with Gas Chromatography-Mass Spectroscopy

Published online by Cambridge University Press:  13 June 2014

Michael E. Bartram*
Affiliation:
Sandia National Laboratories/New Mexico

Abstract

Bis(cyclopentadienyl)magnesium (MgCp2) is used commonly as a source for doping nitride materials with magnesium. Increased oxygen incorporation known to accompany the use of MgCp2 makes the purity of this precursor an important consideration in nitride CVD. Gas chromatography-mass spectroscopy (GCMS) methods have now been developed for the identification of volatile impurities in MgCp2. Diethylether, an oxygen containing organic compound (CH3CH2OCH2CH3), and additional organic impurities were found in the MgCp2 supplied by three manufacturers. Subsequent refinements in the synthetic processes by these companies have resulted in the availability of MgCp2 free of ether and other organic impurities as determined by GCMS.

Information

Type
Research Article
Copyright
Copyright © 2000 Materials Research Society
Figure 0

Figure 1. Stainless steel gas handling manifold attached to the injection head of a Hewlett Packard 5890 Series II Plus GCMS. All zones (sampling valve, injection head, capillary column, and source inlet) were maintained at 75 °C.

Figure 1

Table I. GC Parameters FOR MgCp2 analyses

Figure 2

Figure 2. Chromatograms of MgCp2 in bubblers from Company “A”. Different processes were used to synthesize the MgCp2 in each bubbler. The MgCp2 in bubbler A2 was produced without using diethyl ether (CH3CH2OCH2CH3). Impurities in each bubbler could be removed by evacuating for a short period of time (~15 min.) at elevated temperatures (~50 °C) as shown in figure 3.

Figure 3

Figure 3. A chromatogram of pure MgCp2 obtained after evacuating bubbler A1 in figure 2. Identical chromatograms were obtained after evacuating bubbler A2 as well as from the optimized MgCp2 processes of companies B and C (bubblers B3 and C2 described in figures 4 and 5).

Figure 4

Figure 4. Chromatograms of MgCp2 in bubblers from Company “B”. Different processes were used to synthesize the MgCp2 in each of the three bubblers. Neither of the processes for bubblers B2 and B3 used diethyl ether. However, only B3 could be purified fully by evacuation. The final result is identical to the chromatogram shown in figure 3.

Figure 5

Figure 5. Chromatograms of MgCp2 in bubblers from Company “C”. Different processes were used to produce the MgCp2 in bubblers C1 and C2. No hydrocarbon impurities were detected in C2.