Claims Analysis
Total Claims: 11
Claim 1
Independent Claim
166 words
A method of producing a controlled unsaturated vapour pressure of a volatile liquid at a temperature T t in a heat treatment chamber, said method comprising the steps of passing a stream of a carrier gas through a vapouriser containing the volatile liquid at a temperature T s , passing the mixture of the carrier gas and the vapour of the volatile liquid through the heat treatment chamber which is at the temperature T t , leading the mixture of the carrier gas and the vapour of the volatile liquid from the heat treatment chamber to a condenser from which the carrier gas is vented to waste and in which condenser the volatile liquid is condensed at a temperature T c , that the condensate is recycled through the vapouriser, that T t >T s >T c , and that the volatile liquid in a tube through which the condensate passes from the condenser to the vapouriser fills the cross-section of a length of the tube.
Claim 2
Independent Claim
166 words
A method of producing a controlled unsaturated vapour pressure of a volatile liquid at a temperature T t in a heat treatment chamber, said method comprising the steps of passing a stream of a carrier gas through a vapouriser containing the volatile liquid at a temperature T s , passing the mixture of the carrier gas and the vapour of the volatile liquid through the heat treatment chamber which is at the temperature T t , leading the mixture of the carrier gas and the vapour of the volatile liquid from the heat treatment chamber to a condenser from which the carrier gas is vented to waste and in which condenser the volatile liquid is condensed at a temperature T c , that the condensate is recycled through the vapouriser, that T t >T s >T c , and that the volatile liquid in a tube through which the condensate passes from the condenser to the vapouriser fills the cross-section of a length of the tube.
Claim 3
Dependent Claim
39 words
A method according to claim 1, wherein the partial pressure P s of volatile liquid in the mixture leaving the vapouriser is substantially equal to the partial pressure of vapour in equilibrium with the liquid at T s .
Claim 4
Dependent Claim
22 words
A method according to claim 2, wherein the pressure of the carrier gas entering the vapouriser is greater than P s .
Claim 5
Dependent Claim
12 words
A method according to claim 1, wherein the volatile liquid is mercury.
Claim 6
Dependent Claim
117 words
In the method of growing a layer of a compound, a component of which is a volatile liquid, on a substrate by a liquid phase epitaxy growth process, in which process a controlled unsaturated vapor pressure of said volatile liquid is produced in a treatment chamber containing said substrate and a liquid source of said compound positioned in said treatment chamber apart from said substrate, said liquid source is heated to a temperature sufficient to vaporize said liquid source and the resultant vapor is caused to condense on said substrate maintained at a temperature below the melting point of said compound, the improvement wherein said controlled unsaturated vapor pressure is produced by the method of claim 1.
Claim 7
Dependent Claim
70 words
In the method of annealing a compound, a component of which is a volatile liquid, by heating said compound at a temperature T t in a heat treatment chamber containing a controlled unsaturated vapor pressure of said volatile liquid at said temperature T t , the improvement wherein said controlled unsaturated vapor pressure of said volatile liquid is produced in said heat treatment chamber by the method of claim 1.
Claim 8
Dependent Claim
30 words
A method according to claim 5, wherein the substance has a composition defined by the formula Cd x Hg 1-x Te, that 0.4>x>0.15 and that the volatile liquid is mercury.
Claim 9
Dependent Claim
11 words
The method of claim 5 wherein the volatile liquid is mercury.
Claim 10
Dependent Claim
11 words
The method of claim 6 wherein the volatile liquid is mercury.
Claim 11
Dependent Claim
32 words
A method according to claim 5, characterized in that the compound has a composition defined by the formula Cd x Hg 1-x Te, that 0.4>x>0.15 and that the volatile liquid is mercury.