WO2014033206A1

WO2014033206A1 - Method and system for energy storing and short-term power generation

Info

Publication number: WO2014033206A1
Application number: PCT/EP2013/067884
Authority: WO
Inventors: Risto Sormunen; Markku Raiko
Original assignee: Fortum Oyj
Priority date: 2012-08-31
Filing date: 2013-08-29
Publication date: 2014-03-06
Also published as: EP2703610B1; CN104603403A; EP2703610A1; CN104603403B; PL2703610T3

Abstract

In a method for energy storing and short-term power generation,an intermediate storage of a CCS system is used to store the working fluid of a CO₂ based Rankine process. Liquid CO₂ is stored in an underground reservoir (10) arranged to continually receive liquid CO₂ at a first temperature from one or more CO₂ capture sites and to discharge liquid CO₂ to be transported to a final storage. The underground reservoir (10) is kept at a pressure of 8 -10 bar. When short-term power generation is needed, liquid CO₂ is withdrawn from the underground reservoir (10), pressurized to about 40-50 bar, evaporated with the help of a low value heat source, and expanded in an expander turbine (13), which is connected to a generator (14). The expanded CO₂ is then condensed and returned to the underground reservoir (10) at a second temperature which is higher than the first temperature. When short-term power generation is no more needed, liquid CO₂ from the underground reservoir (10) is circulated through a heat pump (23) to cool the CO₂ until its temperature reaches the first temperature.

Description

METHOD AND SYSTEM FOR ENERGY STORING AND SHORT-TERM POWER GENERATION

FIELD OF THE INVENTION

The present invention relates to a method and a system for energy storing and short-term power generation. Quick short-term high capacity power generation is usually needed for back-up or peak load power supply .

BACKGROUND OF THE INVENTION

The ambitious target of the European Renewa^¬ ble Directive is that by 2020 20% of energy is pro^¬ duced from renewable sources. This means renewable power capacity of about 220 GW. About 80% of this ca^¬ pacity is estimated to be coming from variable and less predictable sources, such as onshore and offshore wind power or solar systems. In longer term this trend is expected to continue. This means that the total en- ergy generation will be highly variable, leading to increased price volatility of electricity. The system will be strongly dependent on weather conditions, particularly in the Central and Northern Europe, where cloudy and windless weather conditions often dominate during winter. Without proper energy storages this will lead to a situation where the European electrici^¬ ty system needs substantially more than 100 GW quick short-term and longer-term back-up power available all the time. Old coal-fired power plants can be taken in- to service after certain period of time, in practice within several hours. Thus, quick-term back-up power has to be ready for use from hydroelectric power, which is not always available, or peaking reserve pow^¬ er, such as gas turbines or diesel engines. Anyway, huge investments for back-up capacity are expected. Obviously, there is an increasing need for more cost efficient solutions in the energy market.

At the same time it seems now to be evident that to prevent or at least delay global warming and other problems due to the still growing worldwide C0₂ emissions Carbon Capture and Storage (CCS) solutions have to be implemented extensively. The future of CCS storages at onshore sites seems to be out of the ques^¬ tion especially in Europe because of the public re- sistance. Thus, offshore storages will finally be the only probable solution for CCS, leading to shipping- based transportation of liquefied C0₂. Intermediate storages of C0₂ must then be founded near such harbors where to liquid C0₂ can be pumped via pipeline network from the C0₂ capture sites - power plants and indus^¬ trial plants - before shipping to the final offshore storages .

To be as cost efficient as possible in a to^¬ tal CCS system, the transportation network has to col- lect liquid C0₂ from various sources to an intermedi^¬ ate storage before shipping. According to several studies, the intermediate storage must be of quite a large volume, whereby in most cases steel tanks and other on-the-ground solutions tend to become highly expensive. One of the best alternatives is then to base the storage in the bedrock at a depth where hy^¬ drostatic pressure will minimize the energy needed for keeping the storage conditions at a suitable pressure and temperature.

US 2012/0001429 Al discloses a carbon diox^¬ ide-based geothermal energy generation system compris^¬ ing a reservoir located below a caprock, one or more injection wells for feeding cold C0₂ into the reservoir, and one or more production wells for discharging heated C0₂ from the reservoir. An energy converting apparatus is connected to each injection well and to each production well so that thermal energy contained in the heated C0₂ can be converted to electricity, heat, or combinations thereof. Compressed C0₂ at a pressure of 30 - 70 bar and a temperature below 30°C is injected to the underground reservoir, and heated C0₂ with a temperature greater than 30°C is drawn off the reservoir. The system is quite complicated and high pressure is needed in the underground reservoir. The system cannot be considered feasible for peak load op^¬ eration because of its high nominal investment cost. Also the operational risks are high because of high medium pressure and uncontrolled evaporation of C0₂ in the underground reservoir.

EP 277777 A2 discloses a system for storing electrical energy in the form of triple-point C0₂ and then using such stored energy plus heat to generate electrical power. A reservoir for liquid C0₂ at about the triple point is created in an insulated vessel. Liquid C0₂ is withdrawn and pumped to a high pressure, which high pressure C0₂ is then heated and expanded to create rotary power which generates electrical power. The discharge stream from the expander is cooled and returned to the vessel where C0₂ vapor is condensed by melting solid C0₂. A fuel-fired gas turbine connected to an electrical power generator is used to heat the high pressure C0₂. The size of an overground C0₂ reser^¬ voir is limited. The investment cost is high. Certain operational risks prevail when acting with a triple point medium.

US 4995234 discloses a method for generating power from liquefied natural gas (LNG) and storing en^¬ ergy. Cold LNG is pressurized, vaporized by removing heat from C0₂ at about triple point temperature, fur^¬ ther heated, and finally expanded to create rotary power. A reservoir of C0₂ at about its triple point is created in an insulated vessel to store energy in the form of refrigeration recovered from the evaporated LNG. During peak electrical power periods, liquid C0₂ is withdrawn from the reservoir, pumped to a high pressure, vaporized, further heated, and expanded to create rotary power which generates additional elec^¬ trical power. During off-peak periods, C0₂ vapor is withdrawn from the reservoir and condensed to liquid by vaporizing LNG. The size of an overground C0₂ res^¬ ervoir is limited. A fuel-fired gas turbine is needed in the system. The investment cost is high. Certain operational risks prevail when acting with a triple point medium.

PURPOSE OF THE INVENTION

The object of the present invention is to eliminate the problems of the prior art and to provide an improved method and system for energy storing and short-term power generation.

Another object is to improve the feasibility of carbon capture and storage (CCS) solutions.

A further object is to create a system that enables the use of low value heat sources and reduces the use of fossil fuels.

SUMMARY

The invention employs an intermediate storage of a CCS system as storage for working fluid used in short-term power generation system that uses C0₂ based Rankine cycle and heat pump in turns .

The invention provides a method for energy storing and short-term power generation, comprising the steps of:

a) storing liquid C0₂ in an underground res^¬ ervoir arranged to continually receive liquid C0₂ at a first temperature from one or more C0₂ capture sites and to discharge liquid C0₂ for shipping to a final offshore storage, the underground reservoir being maintained at a pressure of 8 - 10 bar; b) when short-term power generation is needed, carrying out the following steps:

- withdrawing liquid C0₂ from the underground reser^¬ voir and increasing the pressure of the liquid C0₂ to about 40 - 50 bar;

- evaporating the pressurized C0₂ with the help of a low value heat source;

- expanding the evaporated C0₂ to a pressure of 8 - 10 bar, whereby rotary power is produced which is used for generation of electrical power;

- condensing the expanded C0₂ and returning the condensed C0₂ to the underground reservoir at a second temperature which is higher than the first tempera^¬ ture ;

c) when short-term power generation is no more needed, circulating liquid C0₂ of the underground reservoir through a heat pump to cool the liquid C0₂ until its temperature reaches the first temperature.

The first temperature, i.e., the temperature of fresh C0₂ supplied to the underground reservoir, can be -45°C ... -55°C, preferably about -50°C. The sec^¬ ond temperature, i.e. the temperature of C0₂ returning from the Rankine cycle, can be -15°C ... -25°C, prefera^¬ bly about -20°C.

Advantageously, the underground reservoir is located in the bedrock at a depth of 200 - 300 m. The volume of the underground reservoir is preferably over 50 000 m³, for instance in the range of 50 000 150 000 m³.

The term "underground reservoir" as used herein refers to geological formations beneath the surface of the earth, irrespective of whether they are underground or undersea.

The pressurized liquid C0₂ can be evaporated with the help of sea water, atmospheric air, industri^¬ al waste heat, etc. The invention also provides a system for energy storing and short-term power generation, comprising :

- an underground reservoir arranged to con- tinually receive liquid C0₂ at a first temperature from one or more C0₂ capture sites and to continually discharge liquid C0₂ for shipping to a final offshore storage, the underground reservoir being maintained at a pressure of 8 - 10 bar;

- a pump for withdrawing liquid C0₂ from the underground reservoir and for pressurizing the liquid C0₂ to a pressure of about 40 - 50 bar;

- a heat exchanger for evaporating the pressurized C0₂ with the help of a low value heat source;

- an expander turbine for expanding the evaporated C0₂ to a pressure of 8 - 10 bar, thereby pro^¬ ducing rotary power, and a generator connected to the turbine for generating electrical power from the rota^¬ ry power;

- a condenser for condensing the expanded

C0₂;

- means for feeding the condensed C0₂ back to the underground reservoir at a temperature which is higher than the temperature of liquid C0₂ withdrawn from the underground reservoir;

- means for circulating liquid C0₂ of the un^¬ derground reservoir through a heat pump to cool the liquid C0₂ until its temperature reaches the first temperature .

The system can also comprise means for re^¬ leasing expanded C0₂ to the atmosphere when extreme short-term power generation is needed.

The invention improves the overall economy of Carbon Capture and Storage solutions. Today, CCS is just an expense for power generation systems, which delays the implementation of CCS throughout Europe. For a storage of 50 000 m³, the capacity of the new system is estimated to be about 200 MW during 4 hours. If instead of sea water excess heat from a CHP system can be used for the evaporation, the capac- ity of the system is estimated to be up to 300 MW dur^¬ ing 4 hours. The total storage efficiency is in both cases 70 - 80%, or even more.

The additional cost of the proposed C0₂ based Rankine cycle and heat pump system comprises the cost of additional components, such as an evaporator, an expander turbine and a condenser. These costs are mi^¬ nor compared to the costs of many other back-up power devices, such as gas turbines or diesel generators. Furthermore, the relative size of the components of the new system is definitely smaller than the size of components in hydroelectric systems, or even gas tur^¬ bines. The use of carbon dioxide as the working fluid in a Rankine cycle enables the use of low temperature solutions, which leads into smaller component sizes.

BRIEF DESCRIPTION OF THE DRAWINGS

The accompanying drawing illustrates an embodiment of the invention and together with the de^¬ scription helps to explain the principles of the in- vention.

Fig. 1 is a diagrammatic illustration of a short-term power generation system according to the invention . DETAILED DESCRIPTION OF THE INVENTION

Figure 1 schematically illustrates a system according to the invention. A short-term high capacity power generation cycle employing Rankine cycle comprises an underground reservoir 10 for storage of liq- uid C0₂, a pump 11 for pressurizing liquid C0₂ with^¬ drawn from the underground reservoir 10, an evaporator 12 for evaporating the pressurized C0₂, an expander turbine 13 for expanding the evaporated C0₂, a genera^¬ tor 14 for converting rotary power to electricity, and a condenser 15 for condensing the expanded C0₂ before it is returned back to the underground reservoir 10.

Intermediate storage of liquid C0₂ in a CCS system is usually carried out in geological for^¬ mations, which are located in a bedrock underground or undersea. Such an underground reservoir is arranged to continuously or repeatedly receive liquefied C0₂ from C0₂ capture sites. At the same time, liquid C0₂ is con^¬ tinuously or repeatedly discharged from the intermedi^¬ ate storage to a final storage, which may be offshore or onshore. The intermediate storage is intended for short-term storing only and the content of the storage is changing continually.

The underground reservoir 10 is located in the bedrock 25 at a depth of 200 - 300 m, and the vol^¬ ume of the underground reservoir 10 is preferably in the range of 50 000 - 150 000 m³. Liquefied C0₂ is con^¬ tinually supplied from one or more industrial sources to the underground reservoir 10 via an inlet pipe 16. The temperature of C0₂ supplied via the inlet pipe 16 is about -50°C. Liquid C0₂ is maintained in the inter- mediate storage 10 under a pressure of about 8 - 10 bar. Liquid C0₂ is continually discharged from the in^¬ termediate storage 10 via an outlet pipe 17 to be transported to a final storage (not shown) .

The evaporator 12 is connected to the under- ground reservoir 10 via a pipeline 18 and a pump 11 arranged in the pipeline 18. When short-term power generation is needed, liquid C0₂ is withdrawn from the intermediate storage 10 and compressed with the pump 11 to a pressure of about 40 - 50 bar. Pressurized C0₂ is passed to the evaporator 12, which vaporizes the pressurized C0₂ with the help of heat from a suitable low value heat source. This heat source may comprise, for instance, sea water at a temperature of 5°C - 15°C, waste heat from a district heating system at a temperature of up to 90°C, or atmospheric air. Other possi^¬ ble low value heat sources comprise e.g. water from a river or a lake, geothermal heat, ambient air, and waste heat of an industrial plant or power generation.

The pressurized C0₂ is typically evaporated at a temperature between +5°C and +20°C. From the evap^¬ orator 12 the vaporized C0₂ is fed to the expander turbine 13, where the vaporized C0₂ expands to a pres^¬ sure of about 8 - 10 bar, thereby creating rotary pow^¬ er which is transferred to the generator 14 that con^¬ verts mechanical energy to electrical power.

From the expander turbine 13 the expanded C0₂ is transferred via a pipeline 19 to the condenser 15, where the expanded C0₂ is condensed with the help of liquid C0₂ pumped from the underground reservoir 10 via a pipeline 20. Condensed C0₂ is then returned back to the underground reservoir 10 via a pipeline 21.

Liquid C0₂ fed to the underground reservoir

10 via the pipeline 21 has a higher temperature than the liquid C0₂ leaving the underground reservoir 10 via the pipeline 18. As a consequence, the temperature of the intermediate storage 10 can gradually rise from about -50°C to about -20°C during a short-term power generation period.

At a point of time when back-up or peak load power is no more needed, the underground reservoir 10 may be "recharged" by chilling the liquid C0₂ back to a temperature of about -50°C. This can be done by cir^¬ culating liquid C0₂ through a pipeline 24 and a heat pump 23 to cool the liquid C0₂ until the temperature in the underground reservoir 10 has reached the de^¬ sired level.

The system also comprises an option to excep^¬ tionally release a part of the expanded C0₂ to the at- mosphere via a pipeline 22 to increase the power gen^¬ eration capacity of the system.

It is obvious to a person skilled in the art that with the advancement of technology, the basic idea of the invention may be implemented in various ways. The invention and its embodiments are thus not limited to the examples described above; instead they may vary within the scope of the claims.

Claims

1. A method for energy storing and short-term power generation, comprising the steps of:

a) storing liquid C0₂ in an underground res- ervoir (10) arranged to continually receive liquid C0₂ at a first temperature from one or more C0₂ capture sites and to discharge liquid C0₂ to be transported to a final storage, the underground reservoir (10) being maintained at a pressure of 8 - 10 bar;

b) when short-term power generation is needed, carrying out the following steps:

- withdrawing liquid C0₂ from the underground reser^¬ voir (10) and increasing the pressure of the liquid C0₂ to about 40 - 50 bar;

- evaporating the pressurized C0₂ with the help of a low value heat source;

- condensing the expanded C0₂ and returning the con^¬ densed C0₂ to the underground reservoir (10) at a sec^¬ ond temperature which is higher than the first temper^¬ ature ;

c) when short-term power generation is no more needed, circulating liquid C0₂ from the under^¬ ground reservoir (10) through a heat pump (23) to cool the liquid C0₂ until its temperature reaches the first temperature .

2. A method according to claim 1, wherein the first temperature is -45°C ... -55°C, preferably about -

50°C, and the second temperature is -15°C ... -25°C, preferably about -20°C.

3. A method according to claim 1, wherein the underground reservoir (10) is located in the bedrock (25) at a depth of 200 - 300 m, and the volume of the underground reservoir (10) is over 50 000 m³, for in^¬ stance in the range of 50 000 - 150 000 m³.

4. A method according to any one of claims 1 to 3, wherein the pressurized liquid C0₂ is evaporated with the help of a low value heat source, such as for instance sea water, atmospheric air, industrial waste heat, etc.

5. A system for energy storing and short-term power generation, comprising:

- an underground reservoir (10) arranged to continually receive liquid C0₂ at a first temperature from one or more C0₂ capture sites and to continually discharge liquid C0₂ to be transported to a final storage, the underground reservoir (10) being main^¬ tained at a pressure of 8 - 10 bar;

- a pump (11) for withdrawing liquid C0₂ from the underground reservoir (10) and for pressurizing the liquid C0₂ to a pressure of 40 - 50 bar;

- a heat exchanger (12) for evaporating the pressurized C0₂ with the help of a low value heat source ;

- a turbine (13) for expanding the evaporated

C0₂ to a pressure of 8 - 10 bar, thereby producing ro^¬ tary power, and a generator (14) connected to the turbine (13) for generating electrical power from the ro^¬ tary power;

- a condenser (15) for condensing the expanded C0₂;

- means (21) for feeding the condensed C0₂ back to the underground reservoir (10) at a higher temperature than the temperature of liquid C0₂ with- drawn from the underground reservoir (10);

- means (24) for circulating liquid C0₂ withdrawn from the underground reservoir (10) via a heat pump (23) to cool the liquid C0₂ back to the first temperature during periods when short-term power gen- eration is not needed.

6. A system according to claim 5, wherein the underground reservoir (10) is located in the bedrock (25) at the depth of 200 - 300 m, and the volume of the underground reservoir (10) is over 50 000 m³, for instance in the range of 50 000 - 150 000 m³.

7. A system according to claim 5 or 6, fur- ther comprising means (22) for releasing expanded C0₂ to the atmosphere when extreme short-term power generation is needed.

8. A system according to any one of claims 5 to 7, wherein the heat exchanger (12) is arranged to utilize low value heat sources, such as sea water, at^¬ mospheric air, industrial waste heat, etc.