Integrated Nitrogen Removal in the Production of Liquefied Natural Gas Using Intermediate Feed Gas Separation
US-2017284737-A1 · Oct 5, 2017 · US
US10648729B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10648729-B2 |
| Application number | US-201615266634-A |
| Country | US |
| Kind code | B2 |
| Filing date | Sep 15, 2016 |
| Priority date | Jul 30, 2010 |
| Publication date | May 12, 2020 |
| Grant date | May 12, 2020 |
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There is provided a system and method for producing liquefied natural gas (LNG). An exemplary method includes flowing a high-pressure stream of LNG through a first series of liquid turbines. The exemplary method also includes generating electricity by reducing the pressure of the high-pressure stream of LNG to form a low-pressure stream of LNG. The exemplary method additionally includes bypassing any one the liquid turbines that has a failure while continuing to produce electricity from the first series.
Opening claim text (preview).
What is claimed is: 1. A method for generating electricity from liquid turbines, comprising: in a normal mode, flowing a high-pressure liquid stream through a first plurality of n liquid turbines coupled in a first series, wherein, after a first turbine in the series, an inlet of each of a second through an n−1 liquid turbine is coupled to an outlet of a liquid turbine; generating electricity from the first series by removing energy from the high-pressure liquid stream to form a low-pressure liquid stream; bypassing any one of the first plurality of liquid turbines that has a failure while continuing to produce electricity with the remaining turbines of the first series; and operating the first plurality of liquid turbines in the first series that are not bypassed to maintain a pressure, temperature, and flow rate of the low-pressure liquid stream to be the same as a pressure, temperature, and flow rate of the low-pressure liquid stream when operating in the normal mode. 2. The method of claim 1 , further comprising: maintaining a total electrical output from the first series as a constant value when a liquid turbine is bypassed. 3. The method of claim 1 , further comprising: removing a portion of the high-pressure liquid stream prior to the first series; flowing the portion through a second plurality of n liquid turbines coupled in a second series, wherein, after a first turbine in the second series, an inlet of each of a second through an n−1 liquid turbine of the second series is coupled to an outlet of a preceding liquid turbine of the second series; and wherein the second series is in parallel with the first series; and generating electricity from the second series by removing energy from the portion of the high-pressure liquid stream to form another low-pressure liquid stream. 4. The method of claim 1 , wherein the high-pressure liquid stream comprises a liquefied natural gas. 5. The method of claim 1 , further comprising: producing liquefied natural gas (LNG). 6. The method of claim 1 , further comprising: driving a variable frequency drive from the electric generator, and if the variable frequency drive fails: adjusting a speed of a turbine coupled to the generator to synchronize a generator frequency with a grid frequency; and directly coupling an output of the generator to the electrical grid.
by liquid expansion with extraction of work · CPC title
Splitting of the feed stream, e.g. for treating or cooling in different ways · CPC title
Multiple expansion turbines in parallel · CPC title
as a dual level SCR refrigeration cascade · CPC title
structurally associated with turbines or similar engines · CPC title
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