Claims Analysis
Total Claims: 21
Claim 1
Independent Claim
139 words
A method for providing at least one an homogeneous layer containing silicon and oxygen to at least one substrate in a reaction chamber comprising the steps of: evacuating said chamber; elevating the temperature of said at least one substrate in said chamber; and providing a constant pressure of gaseous TEOS in said chamber for a predetermined time, said gaseous TEOS being a reaction source and wherein said constant pressure is provided by the steps of filling a reservoir with liquid TEOS; providing a low pressure area between said reservoir and said reaction chamber; said pressure selected to allow a predetermined amount of said liquid TEOS to be continually drawn from said reservoir; and, providing a vaporizing means in said low pressure area whereby said means is completely vaporizing to the drawn liquid TEOS before same enters said reaction chamber.
Claim 2
Independent Claim
139 words
A method for providing at least one an homogeneous layer containing silicon and oxygen to at least one substrate in a reaction chamber comprising the steps of: evacuating said chamber; elevating the temperature of said at least one substrate in said chamber; and providing a constant pressure of gaseous TEOS in said chamber for a predetermined time, said gaseous TEOS being a reaction source and wherein said constant pressure is provided by the steps of filling a reservoir with liquid TEOS; providing a low pressure area between said reservoir and said reaction chamber; said pressure selected to allow a predetermined amount of said liquid TEOS to be continually drawn from said reservoir; and, providing a vaporizing means in said low pressure area whereby said means is completely vaporizing to the drawn liquid TEOS before same enters said reaction chamber.
Claim 3
Dependent Claim
13 words
The method of claim 1 wherein said providing vaporizing means comprises a heater.
Claim 4
Dependent Claim
21 words
The method of claim 2 wherein said vaporizing comprises heating said drawn TEOS to between about 100° C. and 200° C.
Claim 5
Dependent Claim
27 words
The method of claim 1 wherein said temperature-elevating step comprising elevating the temperature of said at least one substrate to between approximately 700° C. and 750° C.
Claim 6
Dependent Claim
14 words
The method of claim 4 wherein said substrate temperature is elevated to 730° C.
Claim 7
Dependent Claim
29 words
The method of claim 1 further comprising the step of: introducing oxygen gas to said reaction source thereby providing an oxygen percentage in said reaction source which is over-stoichiometric.
Claim 8
Dependent Claim
25 words
The method of claim 1 wherein said gaseous TEOS is provided to said chamber at a constant pressure of between approx. 70 and 700 μbar.
Claim 9
Dependent Claim
37 words
The method of claim 6 wherein said gaseous TEOS is provided to said chamber at a constant pressure of approx. 130 μbar and said oxygen is provided to said chamber at a pressure of approx. 70 μbar.
Claim 10
Dependent Claim
26 words
The method of claim 1 wherein said predetermined time is determined by the linear relationship at constant pressure of time to desired depth of said layer.
Claim 11
Dependent Claim
59 words
The method of claim 1 wherein it is further desired to provide at least one element in addition to silicon and oxygen in the at least one layer comprising: adding at least one additional element-containing source material to said liquid TEOS prior to providing said liquid TEOS to the low pressure area between the reservoir and the reaction chamber.
Claim 12
Dependent Claim
54 words
The method of claim 10 wherein said at least one additional source material is added in liquid phase to said liquid TEOS in a percent of the total liquid volume calculated to correspond to the percent of said element desired in said layer, and whereby said additional source material is vaporized with said TEOS.
Claim 13
Dependent Claim
32 words
The method of claim 10 wherein said at least one additional source material is added in gaseous phase to said vaporized TEOS source prior to providing said source to the reaction chamber.
Claim 14
Dependent Claim
33 words
The method of claim 10 wherein a compound selected from the group comprising triethylphosphite and trimethylphosphite is added to said TEOS as an additional source for phosphorous in said at least one layer.
Claim 15
Dependent Claim
26 words
The method of claim 10 wherein triethylarsenite is added to said TEOS as an additional source of material for arsenic in said at least one layer.
Claim 16
Dependent Claim
34 words
The method of claim 10 wherein a compound selected from the group comprising trimethylborate, triethylborate, and tripropylborate is added to said TEOS as an additional source for boron in said at least one layer.
Claim 17
Dependent Claim
43 words
The method of claim 10 additionally comprising the step of: introducing oxygen gas to said reaction source thereby providing an oxygen percentage in the reaction source which is over-stoichiometric for forming stable oxides of the silicon and of the additional element or elements.
Claim 18
Dependent Claim
80 words
The method of claim 10 wherein said adding step involves adding to said source material amounts of triethylphosphite and trimethylborate to yield a source material comprising 72.7 percent by weight of TEOS, 14.7 percent by weight of triethylphosphite and 12.6 percent by weight of trimethylborate and wherein approximately 0.7 cm 3 of said source material is provided per minute to grow a glass layer comprising approximately 2 percent by weight of phosphorous and approximately 4 percent by weight of boron.
Claim 19
Dependent Claim
23 words
The method of claim 17 further comprising the step of: introducing 100 cm 3 of oxygen gas per minute to said deposition chamber.
Claim 20
Dependent Claim
28 words
The method of claim 16 wherein said gaseous TEOS is provided to said reaction chamber at a rate of about 0.1 to about 1.0 cm 3 per minute.
Claim 21
Dependent Claim
39 words
The method of claim 19 wherein said gaseous TEOS is provided to said reaction chamber at a rate of 0.2 cm 3 per minute and said oxygen gas is provided at a rate of 20 cm 3 per minute.