Large scale cost effective direct steam generator system, method, and apparatus
Embodiments of the present disclosure include a system, method, and apparatus comprising a large scale direct steam generator operating on an oxidant of air or enriched air configured to generate steam and combustion exhaust constituents. An exhaust constituent separation system and an energy recovery system to reclaim energy and improve the efficiency of the thermodynamic cycle. An optional CO2 separation system and Non Condensable Gas injection system may be included.
1. A system for generating steam, comprising:
a direct steam generator configured to generate saturated or superheated steam and combustion exhaust constituents, wherein the direct steam generator is configured with counter rotating hydrocyclones to generate the saturated or superheated steam and combustion exhaust constituents, and wherein a turbulence zone of the counter rotating hydrocyclones includes a first turbulence portion and second turbulence portion asymmetric to the first turbulence portion;
a close coupled heat exchanger fluidly coupled to the direct steam generator, the close coupled heat exchanger configured to route the saturated or superheated steam and combustion exhaust constituents through an exhaust constituent removal system; and
an energy recovery system that reclaims the energy from the exhaust constituents, wherein the energy recovery system has greater than one stage of expansion.
2. The system of claim 1 , wherein an oxidant for the direct steam generator is pure air.
3. The system of claim 1 , wherein an oxidant for the direct steam generator is oxygen enriched air that is enriched up to 100%.
4. The system of claim 1 , wherein the energy recovery system includes an energy recovery expansion generator that is connected to a main utility buss.
5. The system of claim 1 , wherein the energy recovery system has greater than 1 stage of compression cooling.
6. A system and an apparatus for generating steam, comprising:
a large scale direct steam generator configured with an annular combustor larger than 200 MMBtu/Hr and counter rotating hydrocyclones to generate saturated or superheated steam and combustion exhaust constituents, wherein a turbulence zone of the counter rotating hydrocyclones includes a first turbulence portion and second turbulence portion asymmetric to the first turbulence portion;
a close coupled heat exchanger fluidly coupled to the direct steam generator, the close coupled heat exchanger configured to route the steam and combustion exhaust constituents through an exhaust constituent removal system; and
an energy recovery system that reclaims the energy from the exhaust constituents, wherein the system further separates CO2 by utilizing a mole sieve.
7. The system of claim 6 , wherein large scale direct steam generator further comprises an asymmetric nozzle, wherein the asymmetric nozzle is located downstream of a water injection system.
8. The system of claim 6 , wherein the exhaust constituents are further reduced by CO2 separation.
9. A system for generating steam, comprising:
a large scale direct steam generator configured with an annular combustor larger than 200 MMBtu/Hr and counter rotating hydrocyclones to generate saturated or superheated steam and combustion exhaust constituents;
a close coupled heat exchanger fluidly coupled to the direct steam generator, the close coupled heat exchanger configured to route the steam and combustion exhaust constituents through an exhaust constituent removal system; and
an energy recovery system that reclaims the energy from the exhaust constituents and transfers the energy to an oxidant being fed to the large scale direct steam generator, wherein N2 is separated from the exhaust constituents via a nitrogen separation system and is injected into an oil well as a non-condensable gas, via a nitrogen injection conduit.
10. The system of claim 9 , further comprising generating O2 for air enrichment by at least 1 vapor swing absorption module.
11. The system of claim 9 , wherein the exhaust constituents are used for oil well injection as a non-condensable gas.
12. The system of claim 9 , wherein CO2 is separated from the exhaust constituents and is used for oil well injection as a non-condensable gas.
13. The system of claim 9 , wherein N2 and CO2 are separated from the exhaust constituents and are blended at a metered ratio and used for well injection as a non-condensable gas.