CN203655374U - Dry and hot rock heat energy recovery and power generation device based on organic Rankine cycle - Google Patents
Dry and hot rock heat energy recovery and power generation device based on organic Rankine cycle Download PDFInfo
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- CN203655374U CN203655374U CN201320793856.XU CN201320793856U CN203655374U CN 203655374 U CN203655374 U CN 203655374U CN 201320793856 U CN201320793856 U CN 201320793856U CN 203655374 U CN203655374 U CN 203655374U
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Abstract
A dry and hot rock heat energy recovery and power generation device based on the organic Rankine cycle comprises an evaporator, a power machine, a power generator, a condenser, a cycle working medium storage tank, a working medium circulating pump, a geotherm extracting well and a geotherm recharge well. Geothermal water extracted from the geotherm extracting well is pressurized through a geotherm working medium pump and pumped into the evaporator to transmit heat, enters a heat supply user after transmitting the heat, and then enters the geotherm recharge well. The geothermal water transfers the heat to a low-boiling-point organic medium pumped by the working medium circulating pump in the evaporator to carry out heat exchange, the low-boiling-point organic medium is heated and evaporated in the evaporator, enters the power machine after exiting from the evaporator, pushes the power machine and drives the power generator to generate power. Steam exiting from the power machine is condensed into the low-boiling-point organic medium, then the low-boiling-point organic medium enters the cycle working medium storage tank and is pumped into the evaporator through the working medium circulating pump, heated and evaporated, and therefore the power machine drives the power generator to generate the power continuously. According to the dry and hot rock heat energy recovery and power generation device, the potential heat energy benefit of the heat energy of dry and hot rock is fully achieved, and a new way is provided for the electric energy and the heat energy needed in national building.
Description
Technical field
The present invention relates to hot dry rock system power field, particularly the hot dry rock heat energy recovery generating set based on organic Rankine circulation.
Background technique
Underground heat is a kind of energy from earth interior.It is estimated, the heat that is stored in earth interior is about 1.7 hundred million times of global coal reserves, is equivalent to the heat of 1,000 hundred million barrels of oil every year from earth interior through earth's surface dispersed heat.Geothermal power has the outstanding advantages such as reserves are large, renewable, clean environment firendly, can supplement preferably and take over the fossil energy day by day reducing.
Hot dry rock refers to that general temperature is greater than 200 DEG C, the thousands of rice of buried depth, the inner high temperature rock mass that does not have fluid or only have a small amount of underground fluid.Hot dry rock geothermal energy utilization mainly contains two broad aspect: directly utilize and generate electricity.Generation mode comprises live steam reclaiming process, dilatation method and organic Rankine circulating generation.Organic rankie cycle (Organic Rankine Cycle, be called for short ORC) be taking environmentally friendly organic substance as working medium, thermodynamic cycle using low temperature heat energy as driving source, because its power generation system has that the low temperature exhaust heat amount of recovery is large, facility compact, generating efficiency high, be considered to one of effective technical way reclaiming low grade heat energy.
Having a high potential of hot dry rock generating.Rational exploitation and utilization geothermal resources, for alleviate energy situation anxiety, improve energy resource structure and realize low-carbon economy development significant.
Summary of the invention
The object of this invention is to provide a kind of hot dry rock heat energy recovery generating set based on organic Rankine circulation.Utilize this dress to solve the problem of utilizing hot dry rock heat energy power-generating.
Technological scheme of the present invention is achieved in the following ways:
The present invention includes vaporizer, power engine, generator, condenser, cycle fluid storage tank, working medium circulating pump, underground heat production well and geothermal reinjection well, it is characterized in that pumping into vaporizer transferring heat from the underground heat hot water of underground heat production well extraction through the supercharging of underground heat working medium pump, residue water after heat output enters heat supply user, and the water after heat supply enters geothermal reinjection well; Geothermal water passes to heat the low boiling organic media heat exchange pumping into through working medium circulating pump in vaporizer, and the vaporization of being heated in vaporizer of low boiling organic media out enters power engine in vaporizer, and propulsion power machine also drives generator to generate electricity; Enter condenser from power engine gas out, in condenser, condense into low boiling organic media and enter cycle fluid storage tank, the vaporization of being heated in working medium circulating pump pumps into vaporizer of low boiling organic media in cycle fluid storage tank, enter power engine, moving power engine drives generator uninterruptable power generation again.
Vaporizer 3 is provided with level meter, working medium flow control valve 12 and level meter interlock controlled medium flow.
Between the cooling water intake of condenser and the outlet of condenser organic Rankine circulation low boiling working fluid, be provided with cooling water control valve, adopt cooling water flow control valve 9 and the outlet temperature interlock of organic Rankine circulation low boiling working fluid to control the flow of cooling water in condenser 8.
Organic Rankine circulation low boiling working fluid is R134a or R236fa or R114 or R236ea or R245fa or R11 or R245ca.
Hot dry rock heat energy is developed the optional water of working medium or carbon dioxide, and carbon dioxide CO2 expansibility is large, and viscosity is lower, very low to the dissolving validity of rock forming mineral as solvent, can extract and effectively eliminate fouling by acceleration energy, and agree with the storage of greenhouse gases geology.
The present invention has the following advantages:
1, can make full use of the heat energy of hot dry rock, making it to become electric energy is that nation-building is used, makes big profits with a small capital.
2, can utilize the hot dry rock heat energy that oilfield produced waste water is taken out of to generate electricity through temperature raising, then the displacement of reservoir oil of re-injection oil reservoir, kills two birds with one stone, and has both reduced cost for oil production, has prevented again environmental pollution
The carbon dioxide that 3, can make full use of the trapping of hot coal power-plant flue gas is as hot dry rock heat energy exploitation working medium, generate electricity through temperature raising, the then re-injection oil reservoir displacement of reservoir oil forms benign cycle, can produce huge production power, and carbon dioxide expanded property is large, viscosity is lower, very low to the dissolving validity of rock forming mineral as solvent; Select carbon dioxide not only can acceleration energy extract and effectively eliminate fouling as thermal conductance working medium, and agree with greenhouse gases geology and store this imagination.
Brief description of the drawings
Accompanying drawing 1 is schematic flow sheet of the present invention.
Accompanying drawing 1 description of symbols: 1-hot dry rock heat energy production well, 2-underground heat working medium pump, 3-vaporizer, 4-heat supply user, 5-geothermal reinjection well, 6-generator, 7-power engine, 8-condenser, 9-cooling water flow control valve, 10-cycle fluid storage tank, 11-working medium circulating pump, 12-working medium flow control valve.
Embodiment
Disclose technological scheme of the present invention for entering one, in conjunction with Figure of description, the present invention elaborated:
The present invention includes vaporizer 3, power engine 7, generator 6, condenser 8, cycle fluid storage tank 10, working medium circulating pump 11, hot dry rock heat energy production well 1 and geothermal reinjection well 5, it is characterized in that pumping into vaporizer 3 transferring heats from the underground heat hot water of hot dry rock heat energy production well 1 extraction through 2 superchargings of underground heat working medium pump, residue water after heat output enters heat supply user, and the water after heat supply enters geothermal reinjection well; Geothermal water passes to heat the low boiling organic media heat exchange pumping into through working medium circulating pump in vaporizer, and the vaporization of being heated in vaporizer of low boiling organic media out enters power engine in vaporizer, and propulsion power machine also drives generator to generate electricity; Enter condenser from power engine gas out, in condenser, condense into low boiling organic media and enter cycle fluid storage tank 10, the vaporization of being heated in working medium circulating pump pumps into vaporizer of low boiling organic media in cycle fluid storage tank, makes power engine drive generator 6 uninterruptable power generations.
Water or carbon dioxide heat-conducting flow from hot dry rock heat energy production well 1 enter vaporizer 3 through underground heat working medium pump 2, carry out heat exchange with the low boiling point working medium R245ca in vaporizer 3.Heat-conducting flow after heat exchange can be sent into heat supply user etc., carries out the continuation utilization of tow taste heat, afterwards, imports recharge well.
The gasification of being heated in vaporizer 3 of low boiling organic media, propulsion power machine 7 also drives generator 6 to generate electricity.The gas of discharging from power engine 7 condenses into liquid state in condenser 8, is stored in cycle fluid storage tank 10.With working medium circulating pump 11, the low temperature low boiling working fluid in storage tank is sent into vaporizer 3, continue heat absorption evaporation and become gaseous state, so go round and begin again, the heat of ground heat-conducting flow constantly passes to low boiling point working medium and carries out uninterruptable power generation.
Vaporizer 3 is provided with level meter, working medium flow control valve 12 and level meter interlock controlled medium flow.Adopt cooling water flow control valve 9 and the outlet temperature interlock of organic working medium to control the flow of cooling water in condenser 8.
Case one:
System operating mode: thermal source is 120 DEG C of saturation waters, generated energy 50KW, organic working medium is selected R245fa, and cooling water temperature is 20 DEG C.In vaporizer, organic working medium evaporating temperature is 105 DEG C, and in condenser, organic working medium condensing temperature is 35 DEG C, and the internal efficiency of power engine gets 0.6, and generator efficiency gets 0.96.
(1) power engine design proposal
| Power engine | Temperature (DEG C) | Pressure (MPa) |
| Import | 105 | 1.41 |
| Outlet | 62.30 | 0.21 |
| Flow (kg/s) | Effectively enthalpy drop KJ/kg | Efficiency |
| 2.48 | 20.13 | 0.6 |
(2) hot-water type thermal source ORC system evaporator design proposal
| Vaporizer | Ground heat-conducting flow side | Organic working medium side |
| Inlet temperature (DEG C) | 120 | 40 |
| Outlet temperature (DEG C) | 95 | 105 |
| Flow (kg/s) | 5.38 | 2.48 |
(3) design of condenser scheme
| Condenser | Organic working medium side | Cooling water side |
| Inlet temperature (DEG C) | 62 | 20 |
| Outlet temperature (DEG C) | 35 | 28 |
| Flow (kg/s) | 2.48 | 15.7 |
Scheme hypothesis cooling water temperature is 20 DEG C, considers seasonal variations, and this temperature and the situation in season in spring and autumn are comparatively approaching.Suppose that summer, cooling water temperature was 30 DEG C, winter, cooling water temperature was 10 DEG C, calculated Various Seasonal system core parameter, saw the following form.
Various Seasonal system core parameter comparison
Case two:
System operating mode: thermal source is 120 DEG C of saturated steams, generated energy 50KW, organic working medium is selected R245fa, 20 DEG C of cooling water temperatures.Having organic working medium evaporating temperature in vaporizer is 105 DEG C, and in condenser, organic working medium condensing temperature is 35 DEG C, and the internal efficiency of power engine gets 0.6, and the efficiency of generator gets 0.96.
(1) power engine design proposal
| Power engine | Temperature (DEG C) | Pressure (MPa) |
| Import | 105 | 1.41 |
| Outlet | 62.30 | 0.21 |
| Flow (kg/s) | Effectively enthalpy drop KJ/kg | Efficiency |
| 2.48 | 20.13 | 0.6 |
(2) steam type thermal source ORC system evaporator design proposal
| Vaporizer | Ground heat-conducting flow side | Organic working medium side |
| Inlet temperature (DEG C) | 120 DEG C of saturated vapours | 35 |
| Outlet temperature (DEG C) | 120 DEG C of saturation waters | 105 |
| Flow (kg/s) | 0.25 | 2.48 |
(3) design of condenser scheme
| Condenser | Organic working medium side | Cooling water side |
| Inlet temperature (DEG C) | 62 | 20 |
| Outlet temperature (DEG C) | 35 | 28 |
| Flow (kg/s) | 2.48 | 15.7 |
Consideration cooling water temperature, with the variation in season, supposes that summer, cooling water temperature was 30 DEG C, and winter, cooling water temperature was 10 DEG C, calculated Various Seasonal system core parameter, saw the following form.
The contrast of Various Seasonal system major parameter
Case three:
System operating mode: thermal source is 120 DEG C of supercritical COs
2thermal source, 20 DEG C of cooling water temperatures, generated energy 50KW, organic working medium is selected R245fa.105 DEG C of organic working medium evaporating temperatures, 30 DEG C of organic working medium condensing temperatures, the internal efficiency of power engine gets 0.6, and the efficiency of generator gets 0.96.
(1) power engine design proposal
| Power engine | Temperature (DEG C) | Pressure (MPa) |
| Import | 105 | 1.41 |
| Outlet | 62.30 | 0.21 |
| Flow (kg/s) | Effectively enthalpy drop KJ/kg | Efficiency |
| 2.48 | 20.13 | 0.6 |
(2) hot-water type thermal source ORC system evaporator design proposal
| Vaporizer | Hot water side | Working medium side |
| Inlet temperature (DEG C) | 120 | 35 |
| Outlet temperature (DEG C) | 96 | 105 |
| Flow (kg/s) | 17.78 | 2.48 |
(3) design of condenser scheme
| Condenser | Working medium side | Cooling water side |
| Inlet temperature (DEG C) | 62 | 20 |
| Outlet temperature (DEG C) | 35 | 28 |
| Flow (kg/s) | 2.48 | 15.7 |
Consideration cooling water temperature, with the variation in season, supposes that summer, cooling water temperature was 30 DEG C, and winter, cooling water temperature was 10 DEG C, calculated Various Seasonal system core parameter, saw the following form.
The contrast of Various Seasonal system major parameter
Consideration cooling water temperature, with the variation in season, supposes that summer, cooling water temperature was 30 DEG C, and winter, cooling water temperature was 10 DEG C, calculated Various Seasonal system core parameter, saw the following form.
The contrast of key parameter in Various Seasonal system
Above-mentioned three embodiments are carried out to technical parameter contrast, and result is as follows.
Each scheme contrast
Three steamer major parameter contrasts
| Parameter | Hot-water type thermal source vaporizer | Steam type thermal source vaporizer | CO 2Thermal source vaporizer |
| Overall coefficient of heat transfer (W/m 2k) | 1004 | 3116 | 800 |
| Mean temperature difference (DEG C) | 11.7 | 21.1 | 12.1 |
| Heat exchange area (m^2) | 51 | 9 | 66 |
| Design margin (%) | 7.88 | 8.22 | 14.7 |
| Evaporator shell external diameter (m) | 0.5 | 0.27 | 0.5 |
| Vaporizer total length (m) | 3 | 2.3 | 3.5 |
Claims (5)
1. the hot dry rock heat energy recovery generating set of an organic Rankine circulation, comprise vaporizer, power engine, generator, condenser, cycle fluid storage tank, working medium circulating pump, underground heat production well and geothermal reinjection well, it is characterized in that pumping into vaporizer transferring heat from the underground heat hot water of underground heat production well extraction through the supercharging of underground heat working medium pump, water after heat output enters heat supply user, and the water after heat supply enters geothermal reinjection well; Geothermal water passes to heat the low boiling organic media heat exchange pumping into through working medium circulating pump in vaporizer, and the vaporization of being heated in vaporizer of low boiling organic media out enters power engine in vaporizer, and propulsion power machine also drives generator to generate electricity; Enter condenser from power engine gas out, in condenser, condense into low boiling organic media and enter cycle fluid storage tank, the vaporization of being heated in working medium circulating pump pumps into vaporizer of low boiling organic media in cycle fluid storage tank, then enter power engine, power engine drives generator uninterruptable power generation.
2. the hot dry rock heat energy recovery generating set of organic Rankine circulation according to claim 1, is characterized in that being provided with level meter on vaporizer, working medium flow control valve, working medium flow control valve and level meter interlock controlled medium flow.
3. the hot dry rock heat energy recovery generating set of machine Rankine cycle, it is characterized in that being provided with cooling water control valve between the cooling water intake of condenser and the outlet of condenser organic Rankine circulation low boiling working fluid, adopt the flow of cooling water flow control valve and the outlet temperature interlock control condenser cooling water of organic Rankine circulation low boiling working fluid.
4. the hot dry rock heat energy recovery generating set of organic Rankine circulation according to claim 1, is characterized in that organic Rankine circulation low boiling working fluid is R134a or R236fa or R114 or R236ea or R245fa or R11 or R245ca.
5. the hot dry rock heat energy recovery generating set of organic Rankine circulation according to claim 1, is characterized in that the hot dry rock heat energy exploitation optional water of working medium or carbon dioxide.
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| CN201320793856.XU CN203655374U (en) | 2013-12-04 | 2013-12-04 | Dry and hot rock heat energy recovery and power generation device based on organic Rankine cycle |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103758593A (en) * | 2013-12-04 | 2014-04-30 | 中石化石油工程设计有限公司 | Hot dry rock heat energy recovery and generating set based on organic Rankine cycle |
| CN112065521A (en) * | 2020-09-16 | 2020-12-11 | 天津大学 | Based on CO2Mixed working medium supercharging heat absorption transcritical circulation hot dry rock geothermal power generation model |
| CN116428034A (en) * | 2023-05-06 | 2023-07-14 | 西南石油大学 | High-pressure gas well pressure energy and geothermal energy combined utilization device and method thereof |
-
2013
- 2013-12-04 CN CN201320793856.XU patent/CN203655374U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103758593A (en) * | 2013-12-04 | 2014-04-30 | 中石化石油工程设计有限公司 | Hot dry rock heat energy recovery and generating set based on organic Rankine cycle |
| CN112065521A (en) * | 2020-09-16 | 2020-12-11 | 天津大学 | Based on CO2Mixed working medium supercharging heat absorption transcritical circulation hot dry rock geothermal power generation model |
| US11549495B2 (en) | 2020-09-16 | 2023-01-10 | Tianjin University | Power generation model based on a transcritical cycle with an increasing-pressure endothermic process using CO2-based mixture working fluids for an enhanced geothermal system |
| CN116428034A (en) * | 2023-05-06 | 2023-07-14 | 西南石油大学 | High-pressure gas well pressure energy and geothermal energy combined utilization device and method thereof |
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Effective date of registration: 20151203 Address after: 100029 Beijing Chaoyang District Hui Xin a No. twelve layer 6 Patentee after: SINOPEC OILFIELD SERVICE CORPORATION Patentee after: SINOPEC PETROLEUM ENGINEERING DESIGN CO., LTD. Patentee after: Shandong Sairui Petroleum Science & Technology Development Co., Ltd. Address before: 257026 No. 49, Ji'nan Road, Dongying District, Shandong, Dongying Patentee before: SINOPEC PETROLEUM ENGINEERING DESIGN CO., LTD. Patentee before: Shandong Sairui Petroleum Science & Technology Development Co., Ltd. |
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Granted publication date: 20140618 Termination date: 20171204 |