Converting heat into useful energy using separate closed loops

Claim 3

The method of claim 1 wherein said spent multicomponent working fluid is condensed at a condenser and passed through a recuperative heat exchanger in which heat from said spent multicomponent working fluid is used to recuperatively heat said multicomponent working fluid after being condensed at said condenser.

Claim 4

The method of claim 1 wherein said primary fluid in a vapor state is steam.

Claim 5

The method of claim 3 wherein said steam is generated by heating said primary fluid in a primary closed loop in a boiler.

Claim 6

The method of claim 4 wherein said heating includes burning corrosive or toxic fuels.

Claim 7

The method of claim 5 wherein said primary fluid in a vapor state is split into a first primary stream that is expanded at said first stage expander and a second primary stream that is used to further heat said multicomponent working fluid before it is expanded.

Claim 8

The method of claim 6 wherein said further primary stream is used to heat said multicomponent working fluid before it is heated at said primary heat exchanger.

Claim 9

The method of claim 3 wherein said primary fluid in a vapor state is obtained from a geofluid.

Claim 10

The method of claim 8 further comprising separating said steam from brine in said geofluid, and using said brine to further heat said multicomponent working fluid before it is expanded.

Claim 11

Apparatus for converting heat to useful energy comprising a first stage expander in which a primary fluid in a vapor state is expanded to obtain useful energy and to produce a partially expanded primary fluid stream having vapor and liquid components, a separator/splitter that separates said partially expanded primary fluid stream from said first stage expander into liquid and vapor components and splits said stream into a vapor stream and a further primary stream including liquid, a second stage expander in which said vapor stream from said separator/splitter is expanded to obtain useful energy, a primary heat exchanger connected to use heat in said partially expanded primary fluid stream to heat a multicomponent working fluid, and a separate closed loop containing said multicomponent working fluid, said second closed loop including flow passages in said primary heat exchanger, said second closed loop including a further expander in which said multicomponent working fluid is expanded to obtain useful energy and produce a spent multicomponent working fluid.

Claim 12

Apparatus for converting heat to useful energy comprising a first stage expander in which a primary fluid in a vapor state is expanded to obtain useful energy and to produce a partially expanded primary fluid stream having vapor and liquid components, a separator/splitter that separates said partially expanded primary fluid stream from said first stage expander into liquid and vapor components and splits said stream into a vapor stream and a further primary stream including liquid, a second stage expander in which said vapor stream from said separator/splitter is expanded to obtain useful energy, a primary heat exchanger connected to use heat in said partially expanded primary fluid stream to heat a multicomponent working fluid, and a separate closed loop containing said multicomponent working fluid, said second closed loop including flow passages in said primary heat exchanger, said second closed loop including a further expander in which said multicomponent working fluid is expanded to obtain useful energy and produce a spent multicomponent working fluid.

Claim 13

The apparatus of claim 10 wherein said separate closed loop includes a condenser at which said spent multicomponent working fluid is condensed and a recuperative heat exchanger in which heat from said spent multicomponent working fluid is used to recuperatively heat said multicomponent working fluid after being condensed at said condenser.

Claim 14

The apparatus of claim 10 wherein said primary fluid in a vapor state is steam.

Claim 15

The apparatus of claim 12 further comprising a boiler that generates said steam by heating said primary working fluid.

Claim 16

The apparatus of claim 13 wherein said boiler is a boiler that includes means for burning corrosive or toxic fuels.

Claim 17

The apparatus of claim 14 further comprising a stream splitter at which said primary fluid in a vapor state is split into a first primary stream that is expanded at said first stage expander and a second primary stream that is used to further heat said multicomponent working fluid before it is expanded.

Claim 18

The apparatus of claim 15 wherein said further primary stream is connected to heat said multicomponent working fluid before it is heated at said primary heat exchanger.

Claim 19

The apparatus of claim 12 further comprising a source of geofluid and wherein said primary fluid in a vapor state is obtained from said geofluid.

Claim 20

The apparatus of claim 17 further comprising a separator at which said steam is separated from brine in said geofluid, and a further heat exchanger in which heat from said brine is used to further heat said multicomponent working fluid before it is expanded.

Claim 23

The method of claim 19 wherein said heating includes combusting corrosive or toxic fuels.

Claim 24

The method of claim 20 wherein said primary working fluid is steam.

Claim 25

The method of claim 19 wherein heat in said first primary stream is used to heat said multicomponent working fluid in a second heat exchanger after expansion in said first expander.

Claim 26

The method of claim 22 wherein said first primary stream is separated into liquid and vapor components and is split into third and fourth primary streams after expansion in said first expander, said third primary stream being a vapor that is expanded in a third expander to obtain useful energy, said fourth primary stream passing through said second heat exchanger.

Claim 27

The method of claim 23 wherein heat in said third primary stream is used to heat said multicomponent working fluid in a third heat exchanger after expansion in said third expander.

Claim 28

The method of claim 24 wherein said second, third, and fourth primary streams are combined to provide said primary working fluid that is heated by said heater.

Claim 29

The method of claim 25 wherein said first primary stream is separated into liquid and vapor phases at a separator after expansion in said first expander, part of said vapor phase providing said third primary stream and part of said vapor phase being joined with said liquid phase to provide said fourth primary stream.

Claim 30

The method of claim 19 wherein said multicomponent working fluid is condensed at a condenser, after expansion at said second expander, and passed through a fourth heat exchanger in which heat from said multicomponent working fluid prior to condensing is used to recuperatively heat said multicomponent working fluid after being condensed at said condenser.

Claim 31

Apparatus for converting heat to useful energy comprising a first closed loop containing a primary working fluid and including a heater for heating said primary working fluid, and a first stream splitter that splits said heated primary working fluid into a first primary stream and a second primary stream, said first closed loop also including a first expander in which said first primary stream is expanded to obtain useful energy, said first closed loop also including a flow passage through a first heat exchanger to transfer heat from said second primary stream to a multicomponent working fluid, and a second closed loop containing said multicomponent working fluid, said second closed loop including a flow passage through said first heat exchanger, said second closed loop including a second expander in which said multicomponent working fluid is expanded to obtain useful energy.

Claim 32

Apparatus for converting heat to useful energy comprising a first closed loop containing a primary working fluid and including a heater for heating said primary working fluid, and a first stream splitter that splits said heated primary working fluid into a first primary stream and a second primary stream, said first closed loop also including a first expander in which said first primary stream is expanded to obtain useful energy, said first closed loop also including a flow passage through a first heat exchanger to transfer heat from said second primary stream to a multicomponent working fluid, and a second closed loop containing said multicomponent working fluid, said second closed loop including a flow passage through said first heat exchanger, said second closed loop including a second expander in which said multicomponent working fluid is expanded to obtain useful energy.

Claim 33

The apparatus of claim 28 wherein said heater is a boiler that includes means for combusting corrosive or toxic fuels.

Claim 34

The apparatus of claim 28 wherein said primary working fluid is steam.

Claim 35

The apparatus of claim 28 wherein said first closed loop and said second closed loop include passages in a second heat exchanger in which heat from said first primary stream is used to heat said multicomponent working fluid.

Claim 36

The apparatus of claim 31 wherein said first closed loop includes a separator/splitter that separates said first primary stream into liquid and vapor phases and splits said first primary stream into third and fourth primary streams after expansion in said first expander, said third primary stream being a vapor, said first closed loop also including a third expander thorough which said third primary stream passes and in which said third primary stream is expanded, said fourth primary stream passing thorough said second heat exchanger.

Claim 37

The apparatus of claim 32 wherein said first closed loop and said second closed loop include passages in a third heat exchanger in which heat from said third primary stream is used to heat said multicomponent working fluid.

Claim 38

The apparatus of claim 33 wherein said first closed loop includes a stream combiner at which said second, third, and fourth primary streams are combined to provide said primary working fluid that is heated by said heater.

Claim 39

The apparatus of claim 32 wherein said separator/splitter includes a separator that separates said first primary stream into liquid and vapor phases and a second stream splitter at which said vapor phase is split into said third primary stream and a further stream, and wherein said separator/splitter further comprises a stream combiner that combines said further stream and said liquid phase into said fourth primary stream.

Claim 40

The apparatus of claim 28 wherein said second closed loop includes a condenser in which said multicomponent working fluid is condensed and a fourth heat exchanger in which heat from said multicomponent working fluid prior to condensing is used to recuperatively heat said multicomponent working fluid after being condensed at said condenser.

Claim 43

The method of claim 37 wherein said second stream is throttled after passing through said first heat exchanger and combined with said first stream after said first stream has been expanded in said third expander.

Claim 44

The method of claim 38 wherein the combined first and second streams are condensed and discharged from the system.

Claim 45

Apparatus for converting heat in a geofluid containing steam and brine to useful energy in a power system comprising a separator that separates said steam from said brine in said geofluid, a first expander that expands said steam to obtain useful energy and produces a stream of expanded steam, a separate closed loop containing a multicomponent working fluid, said second closed loop including flow passages in a first heat exchanger in which heat in said steam is used to heat said multicomponent working fluid, said second closed loop including flow passages in a second heat exchanger in which said brine further heats said multicomponent working fluid from said first heat exchanger, said second closed loon including a second expander in which said multicomponent working fluid from said second heat exchanger is expanded to obtain useful energy and produce a spent multicomponent working fluid, and an outflow line connected to discharge said brine from said second heat exchanger from the system, wherein said separate closed loop includes a condenser in which said spent multicomponent working fluid is condensed and a recuperative heat exchanger in which heat from said spent multicomponent working fluid is used to recuperatively heat said multicomponent working fluid after being condensed at said condenser, wherein said heat used to heat said multicomponent working fluid in said first heat exchanger is obtained from steam that has been expanded in said first expander, further comprising a separator/splitter that separates said stream of expanded steam into liquid and vapor components and splits said stream of expanded steam into first and second streams, said first stream being a vapor, and further comprising a third expander through which said first stream passes and in which said first stream is expanded to obtain useful energy, said second stream passing through said first heat exchanger.

Claim 46

Apparatus for converting heat in a geofluid containing steam and brine to useful energy in a power system comprising a separator that separates said steam from said brine in said geofluid, a first expander that expands said steam to obtain useful energy and produces a stream of expanded steam, a separate closed loop containing a multicomponent working fluid, said second closed loop including flow passages in a first heat exchanger in which heat in said steam is used to heat said multicomponent working fluid, said second closed loop including flow passages in a second heat exchanger in which said brine further heats said multicomponent working fluid from said first heat exchanger, said second closed loon including a second expander in which said multicomponent working fluid from said second heat exchanger is expanded to obtain useful energy and produce a spent multicomponent working fluid, and an outflow line connected to discharge said brine from said second heat exchanger from the system, wherein said separate closed loop includes a condenser in which said spent multicomponent working fluid is condensed and a recuperative heat exchanger in which heat from said spent multicomponent working fluid is used to recuperatively heat said multicomponent working fluid after being condensed at said condenser, wherein said heat used to heat said multicomponent working fluid in said first heat exchanger is obtained from steam that has been expanded in said first expander, further comprising a separator/splitter that separates said stream of expanded steam into liquid and vapor components and splits said stream of expanded steam into first and second streams, said first stream being a vapor, and further comprising a third expander through which said first stream passes and in which said first stream is expanded to obtain useful energy, said second stream passing through said first heat exchanger.

Claim 47

The apparatus of claim 40 further comprising a throttle valve in which said second stream is throttled after passing through said first heat exchanger and a junction at which said second stream from said throttle valve is combined with said first stream after said first stream has been expanded in said third expander.

Claim 48

The apparatus of claim 41 wherein the combined first and second streams are condensed and discharged from the system.