Claims Analysis
Total Claims: 5
Claim 1
Independent Claim
104 words
A method for separating and stabilizing a hydro-treater effluent, comprising the steps of: expanding the effluent from a high pressure to an intermediate pressure in a first expansion drum, resulting in both gaseous and liquid phase hydrocarbon components; drawing off said gaseous phase hydrocarbon components as a gas product; expanding said liquid phase hydrocarbon components from said intermediate pressure to a lower intermediate pressure in a second expansion drum, evolving secondary gaseous and liquid phase hydrocarbon components; compressing and cooling said secondary gaseous phase hydrocarbon components and returning the cooled components to said first expansion drum; and withdrawing said secondary liquid phase hydrocarbon components.
Claim 2
Independent Claim
104 words
A method for separating and stabilizing a hydro-treater effluent, comprising the steps of: expanding the effluent from a high pressure to an intermediate pressure in a first expansion drum, resulting in both gaseous and liquid phase hydrocarbon components; drawing off said gaseous phase hydrocarbon components as a gas product; expanding said liquid phase hydrocarbon components from said intermediate pressure to a lower intermediate pressure in a second expansion drum, evolving secondary gaseous and liquid phase hydrocarbon components; compressing and cooling said secondary gaseous phase hydrocarbon components and returning the cooled components to said first expansion drum; and withdrawing said secondary liquid phase hydrocarbon components.
Claim 3
Dependent Claim
77 words
The method according to claim 1, further comprising, after said withdrawing step, the steps of: expanding said secondary liquid phase hydrocarbon components from said lower intermediate pressure to a lower pressure in a third expansion drum, evolving tertiary gaseous and liquid phase hydrocarbon components; compressing and cooling said tertiary gaseous phase hydrocarbon components and returning the cooled components to said second expansion drum; and withdrawing said tertiary liquid phase hydrocarbon component as a separated stabilized hydrocarbon product.
Claim 4
Dependent Claim
58 words
The method according to claim 2, wherein said hydrotreater effluent comprises hydrotreated whole shale oil and said high pressure is above 800 psia, said intermediate pressure is within the range of from 200-800 psia, said lower intermediate pressure is within the range of from 50-200 psia and said lower pressure is within the range of from 0-50 psia.
Claim 5
Dependent Claim
37 words
The method according to claim 3, wherein said high pressure is about 2450 psia, said intermediate pressure is about 400 psia, said lower intermediate pressure is about 100 psia and said lower pressure is about 10 psia.