# US 12,601,290 B2 · Converting potential energy from a mixture of fluids into electric power

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- Number: US 12,601,290 B2
- Document ID: US12601290B2
- Status: Granted
- Kind: B2
- Application number: 17/192,417
- Filed: 2021-03-04
- Published: 2022-09-08
- Granted: 2026-04-14
- Earliest claimed: 2016-01-07
- Assignees: Bente Fruelund Sorensen Family Trust
- Applicants: Jens Ole Sorensen; Jens Erik Sorensen
- Inventors: Jens Ole Sorensen; Jens Erik Sorensen
- Web page: https://patentgrep.com/patent/US12601290B2

## CPC

- F02C 1/00: Gas-turbine plants characterised by the use of hot gases or unheated pressurised gases, as the working fluid (by the use of combustion products F02C3/00, F02C5/00)
- F25J 3/04763: {Start-up or control of the process; Details of the apparatus used}
- F05D 2220/32: in gas turbines
- F05D 2220/76: an electrical generator
- H02K 7/1823: {structurally associated with turbines or similar engines}
- Y02E 10/46: Conversion of thermal power into mechanical power, e.g. Rankine, Stirling or solar thermal engines
- Y02E 60/50: Fuel cells
- F02C: GAS-TURBINE PLANTS; AIR INTAKES FOR JET-PROPULSION PLANTS; CONTROLLING FUEL SUPPLY IN AIR-BREATHING JET-PROPULSION PLANTS (construction of turbines F01D; jet-propulsion plants F02K; construction of compressors or fans F04; generating combustion products of high pressure or high velocity F23R; using gas turbines in compression refrigeration plants F25B11/00)
- F25J: LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS {OR LIQUEFIED GASEOUS} MIXTURES BY PRESSURE AND COLD TREATMENT {OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE (cryogenic pumps F04B37/08; gas storage vessels, gas holders F17; filing vessels with, or discharging from vessels, compressed, liquefied or solidified gases F17C; refrigeration machines, plants, or systems F25B)}
- F05D: INDEXING SCHEME FOR ASPECTS RELATING TO NON-POSITIVE-DISPLACEMENT MACHINES OR ENGINES, GAS-TURBINES OR JET-PROPULSION PLANTS
- H02K: DYNAMO-ELECTRIC MACHINES (dynamo-electric relays H01H53/00; conversion of DC or AC input power into surge output power {H03K3/53})
- Y02E: REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION

## Abstract

A system for converting potential energy into electric power from a mixture of gases, such as atmospheric air, including a particular lesser-density-gas, such as nitrogen, and a particular larger-density-gas, such as oxygen. The system includes a gas-separator at an upper-elevation; a gas-flow-conduit that has a gas-exit-port at a lesser-elevation, where the lesser-elevation is significantly lower than the upper-elevation; and an energy-converter positioned on the gas-flow-conduit. The gas-separator is coupled to the gas-exit-port via the gas-flow-conduit. The gas-separator separates the particular larger-density-gas from the gas mixture. The gas-flow-conduit conducts the separated particular larger-density-gas from the gas-separator via the gas-flow-conduit to the energy-converter; and the energy-converter generates electric power from the conducted separated particular larger-density-gas.

## Claims

### Claim 1

A method of converting potential energy into electric power from a gas mixture including a first gas having a first density and a second gas having a second density, the second density greater than the first density, the method comprising:
using a gas separator positioned at a first elevation to separate the first gas from the gas mixture, the gas separator coupled to a gas flow conduit having a gas exit port at a second elevation significantly higher than the first elevation, the gas separator in fluid communication via the gas flow conduit with an energy converter;
conducting the first gas from the gas separator to the energy converter via the gas flow conduit; and
using the energy converter to generate electric power from the conducted first gas.

### Claim 2 (depends on 1)

The method of claim 1, additionally comprising introducing a gas into the gas flow conduit, wherein the introduced gas comprises at least one of:
steam, and
water vapor.

### Claim 3 (depends on 1)

The method of claim 1, additionally comprising introducing a gas into the gas flow conduit near the gas separator, wherein the introduced gas comprises at least one of:
nitrogen, and
water vapor.

### Claim 4 (depends on 1)

The method of claim 1, additionally comprising heating a gas comprising the first gas.

### Claim 5 (depends on 4)

The method of claim 4, wherein heating the gas comprises heating the gas after separating the first gas from the gas mixture using the gas separator.

### Claim 6 (depends on 5)

The method of claim 5, wherein heating the gas is performed within the gas flow conduit near the gas separator.

### Claim 7 (depends on 4)

The method of claim 4, wherein heating the gas comprises heating the gas mixture using a solar collector.

### Claim 8 (depends on 4)

The method of claim 4, wherein heating the gas comprises heating the gas mixture prior to separation of the first gas from the gas mixture.

### Claim 9 (depends on 1)

The method of claim 1, wherein the gas mixture comprises atmospheric air, wherein the first gas comprises nitrogen, and wherein the second gas comprises oxygen.

### Claim 10 (depends on 1)

The method of claim 1, additionally comprising collecting nitrogen gas at the second elevation.

### Claim 11 (depends on 1)

The method of claim 1, additionally comprising collecting oxygen gas at an oxygen exit port near the first elevation.

### Claim 12 (depends on 1)

The method of claim 1, wherein the energy converter comprises a turbine.

### Claim 13 (depends on 1)

The method of claim 1, wherein the energy converter is located near the first elevation.

### Claim 14 (depends on 1)

The method of claim 1, additionally comprising:
using a second gas separator positioned at a third elevation to separate the second gas from a second gas mixture comprising the first gas and the second gas, the second gas separator coupled to a second gas flow conduit having a gas exit port at a fourth elevation significantly lower than the third elevation, the second gas separator in fluid communication via the second gas flow conduit with a second energy converter;
conducting the second gas from the second gas separator to the second energy converter via the second gas flow conduit;
using the second energy converter to generate electric power from the conducted second gas; and
inducing heat exchange between the separated first gas conducted by the first gas flow conduit and the separated second gas conducted by the second gas flow conduit.

### Claim 15

A system for converting potential energy into electric power from a gas mixture including a first gas having a first density and a second gas having a second density, the second density greater than the first density, the system comprising:
a gas separator positioned at a first elevation and configured to separate the first gas from the gas mixture,
a gas flow conduit coupled to and in fluid communication with the gas separator, the gas flow conduit having a gas exit port at a second elevation significantly higher than the first elevation, and
an energy converter coupled to and in fluid communication with the gas flow conduit, the energy converter configured to generate electric power from the first gas separated from the gas mixture by the gas separator and conducted to the energy converter via the gas flow conduit.

### Claim 16 (depends on 15)

The system of claim 15, additionally comprising:
a second gas separator positioned at a third elevation and configured to separate the second gas from a second gas mixture including the first gas and the second gas;
a second gas flow conduit coupled to and in fluid communication with the second gas separator, the second gas flow conduit having a gas exit port at a fourth elevation significantly lower than the third elevation;
a second energy converter coupled to and in fluid communication with the second gas flow conduit, the second energy converter configured to generate electric power from the second gas separated from the second gas mixture by the second gas separator and conducted to the second energy converter via the second gas flow conduit; and
a heat exchanger positioned between the first gas flow conduit and the second gas flow conduit, wherein the heat exchanger is adapted to induce heat exchange between the separated first gas conducted by the first gas flow conduit and the separated second gas conducted by the second gas flow conduit.