CN204672103U - A kind of utilize underground heat collecting carbonic anhydride, generating and mothballed plant - Google Patents
A kind of utilize underground heat collecting carbonic anhydride, generating and mothballed plant Download PDFInfo
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- CN204672103U CN204672103U CN201520275149.0U CN201520275149U CN204672103U CN 204672103 U CN204672103 U CN 204672103U CN 201520275149 U CN201520275149 U CN 201520275149U CN 204672103 U CN204672103 U CN 204672103U
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- regenerator
- decompressor
- reboiler
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Abstract
Utilize the collecting carbonic anhydride of underground heat, generating and a mothballed plant, absorption tower poor rich liquid heat exchanger is communicated with regenerator, and regenerator is communicated with absorption tower through poor rich liquid heat exchanger; Reboiler bottom regenerator is communicated with low-pressure steam, CO
2decompressor is communicated with; Regenerator is communicated with condenser, condenser and reboiler, CO
2cooler is communicated with, CO
2cooler is communicated with compressor, and compressor is connected to geothermal layer; Reboiler and CO
2decompressor is communicated with, CO
2decompressor communicatively thermosphere ejection carbon dioxide, CO
2the electric power that generator produces is sent to electrical network; There is underground in the utility model part carbon dioxide permanent envelope, part carbon dioxide to heat after supercharging by Cemented filling to ground in geothermal layer, in carbon dioxide expanded machine, be converted into mechanical energy drives carbon dioxide generator to produce electric power, carbon dioxide after expansion can be used further to the rich solution desorb trapping workshop section, while slowing down greenhouse gas emission, utilize geothermal energy resources to produce clean electric power, there is economic benefit.
Description
Technical field
The utility model belongs to collecting carbonic anhydride, utilizes and Plugging Technology Applied field, is particularly useful for low concentration CO in the flue gas of the generation such as coal-burning boiler, gas turbine
2trapping, and utilize geother-mal power generation while by carbon dioxide sequestration underground, particularly a kind of utilize underground heat collecting carbonic anhydride, generating and mothballed plant.
Background technology
Climate change is one of the most great survival and development problem of facing mankind in this century.Mankind's activity since the industrial revolution, especially the discharge of developed country's a large amount of greenhouse gases in course of industrialization, cause global climate immediate and mid-term to warm as the marked change of principal character, obvious impact is created on global natural ecosystems, serious challenge is brought to the survival and development of human society, and the carbon dioxide of industrial discharge is considered to the one of the main reasons causing climate warming, for avoiding causing irreversible adverse effect to weather system, must adopt an effective measure and reduce and control generation and the discharge of carbon dioxide, the carbon dioxide sequestration maybe will produced.
Correlative study shows, the CO2 emission of China more than 50% comes from the thermal power generation of coal-burning power plant.Coal-fired plant flue gas discharge capacity is large, and Relatively centralized, the carbon trapping technique based on coal-burning power plant's exploitation is one of important channel of carbon dioxide discharge-reduction.In traditional carbon dioxide geologic sequestration technology, a kind of is by the CO under supercriticality
2the water-bearing layer that press-in underground 800m is dark, utilizes the cap rock layer preventing gas and liquid from permeating to storage layer top, can by CO
2be sealed in underground for a long time, stably, this kind of method cost of investment is high, and without any economic well-being of workers and staff; The another kind of processing mode associated with geological storage is CO
2recycling.CO
2recycling usually have two kinds of modes, one is that coal gas layer is sealed up for safekeeping, refer in the middle of coal seam deep for carbon dioxide injection, displace the coal bed gas containing methane, so this technology has certain economy, but must be selected in darker coal seam, to ensure to cause leakage because of exploitation, problem is that carbon dioxide melts swollen reaction after entering coal gas layer, causes the space of coal gas layer to diminish, injecting carbon dioxide can be more and more difficult, again cannot inject gradually; Another kind is then by CO
2inject just close to exhausted oil field to improve oil recovery, this project plan comparison is attractive, because of its can from the oil additionally exploited partial-compensation CO
2storage cost, but shortcoming to be the geographical distribution in this kind of oil field uneven, and Exploitation Potential is limited.
Summary of the invention
In order to overcome the shortcoming that above-mentioned prior art exists, the purpose of this utility model be to provide a kind of utilize underground heat collecting carbonic anhydride, generating and mothballed plant, this device can be used for low concentration CO in the flue gas that coal-burning boiler, gas turbine etc. produce
2trapping, and again trapped carbon dioxide sequestration is utilized geothermal energy while underground, utilize carbon dioxide as generating working medium, a part of regenerated heat of carbon dioxide capture system is provided simultaneously, this system can not only reduce collecting carbonic anhydride energy consumption, can realize again sealing up for safekeeping and utilizing integration, and produce certain economic benefit, reduce by the great number cost sealing generation up for safekeeping.
In order to achieve the above object, the utility model is by the following technical solutions:
A kind of utilize underground heat collecting carbonic anhydride, generating and mothballed plant, comprise absorption tower 2, rich solution outlet bottom absorption tower 2 is through poor rich liquid heat exchanger 3 and regenerator 4 upper end rich solution inlet communication, and the lean solution outlet bottom regenerator 4 is communicated with packing section on absorption tower 2 through poor rich liquid heat exchanger 3;
Be provided with reboiler 10 bottom described regenerator 4, the thermal source of reboiler 10 is provided by two-way, and a steam inlet, road is communicated with the low-pressure steam from steam pipe system, another road and CO
2the carbon dioxide gas outlet of decompressor 8 is communicated with;
The CO at described regenerator 4 top
2gas vent is communicated with condenser 5 upper end gas feed, and condenser 5 lower end is communicated with regenerator 4 upper end condensate liquid reflux inlet, the CO at condenser 5 top
2gas after being communicated with reboiler 10 carbon dioxide gas outlet again with CO
2cooler 6 entrance is communicated with, CO
2cooler 6 exports and compressor 7 inlet communication, and compressor 7 outlet is connected to geothermal layer;
Described reboiler 10 carbon dioxide entrance and CO
2decompressor 8 gas vent is communicated with, CO
2the carbon dioxide that decompressor 8 gas access and geothermal layer spray is communicated with, CO
2decompressor 8 axle head and CO
2generator 9 is communicated with, CO
2the electric power that generator 9 produces is sent to electrical network.
Described CO
2decompressor 8 is piston type or turbo-expander.
Described reboiler 10 is provided with two-way thermal source, and the carbon dioxide after steam and expansion power generation, is used alone or uses simultaneously.
Compared with prior art, the utility model by collecting carbonic anhydride, seal up for safekeeping and combine with utilization, be compressed in the process of geothermal layer at the carbon dioxide trapped from flue gas, understand some carbon dioxide progressively permeate and be stored in underground, remaining carbon dioxide is heated it by geothermal energy, and the carbon dioxide after heating is pumped to CO
2thermal energy is that mechanical energy drives CO by decompressor
2generator produces electric power, and the carbon dioxide after once discharging heat energy is used further to the rich solution desorb trapping workshop section, greatly reduces energy consumption and the cost of chemical carbon rejection processes.The method, while slowing down greenhouse gas emission, solving climate change problem, can also utilize geothermal energy resources to produce the clean charged power of base, produce certain economic benefit, and naturally combines together.
Accompanying drawing explanation
Accompanying drawing is structural representation of the present utility model.
Detailed description of the invention
Below in conjunction with the drawings and specific embodiments, the utility model is described in more detail.
With reference to accompanying drawing, a kind of utilize underground heat collecting carbonic anhydride, generating and mothballed plant, comprise the absorption tower 2 be communicated with flue gas flow control valve 1, rich solution outlet bottom absorption tower 2 is through poor rich liquid heat exchanger 3 and regenerator 4 upper end rich solution inlet communication, and the lean solution outlet bottom regenerator 4 is communicated with packing section on absorption tower 2 through poor rich liquid heat exchanger 3;
Be provided with reboiler 10 bottom described regenerator 4, the thermal source of reboiler 10 is provided by two-way, and a steam inlet, road is communicated with the low-pressure steam from steam pipe system, another road and CO
2the carbon dioxide gas outlet of decompressor 8 is communicated with;
The CO at described regenerator 4 top
2gas vent is communicated with condenser 5 upper end gas feed, and condenser 5 lower end is communicated with regenerator 4 upper end condensate liquid reflux inlet, the CO at condenser 5 top
2gas after being communicated with reboiler 10 carbon dioxide gas outlet again with CO
2cooler 6 entrance is communicated with, CO
2cooler 6 exports and compressor 7 inlet communication, and compressor 7 outlet is connected to geothermal layer;
Described reboiler 10 carbon dioxide entrance and CO
2decompressor 8 gas vent is communicated with, CO
2the carbon dioxide that decompressor 8 gas access and geothermal layer spray is communicated with, CO
2decompressor 8 axle head and CO
2generator 9 is communicated with, CO
2the electric power that generator 9 produces is sent to electrical network.
Described CO
2decompressor 8 is piston type or turbo-expander.
Described reboiler 10 is provided with two-way thermal source, and the carbon dioxide after steam and expansion power generation, is used alone or uses simultaneously.
Described condenser 5 is the container that can realize steam-condensation and gas-liquid separation.
Technical process of the present utility model and principle are:
Neat stress after desulphurization denitration enters absorption tower 2 by flue gas flow control valve 1 adjust flux, flue gas and spray and under absorbent form counter current contacting, the rich solution absorbing carbon dioxide enters regenerator 4 upper end packing layer deliver to poor rich liquid heat exchanger 3 and lean solution heat exchange bottom absorption tower 2 after and carries out desorption and regeneration.
Lean solution bottom regenerator 4 is gone to after poor rich liquid heat exchanger 3 reclaims heat with rich solution heat exchange, delivers to packing section upper end, absorption tower 2, carries out carbon dioxide absorption.
The regenerating carbon dioxide gas at regenerator 4 top is after condenser 5 gas-water separation, aqueous water is recycled to regenerator 4 upper end bottom condenser 5, the carbon dioxide of regeneration and the outlet of reboiler 10 carbon dioxide heat source side, mixed carbon dioxide is through CO
2cooler 6 cools and is depressed into underground geothermal tomography through compressor 7 again, CO
2heated by deep geothermal heat, reach ultra supercritical state.Beat a bite vertical shaft at tomography far-end, be subject to the CO of powerful extruding in underground
2eruption that can be fierce out, and carries huge energy.This energy is utilized to make CO
2decompressor 8 does work and drives CO
2generator 9 generates electricity.
The reboiler 10 arranged bottom regenerator 4 has two-way thermal source, and preferentially using can rear CO in once release
2the outlet source of the gas of decompressor 8, secondly uses the low-pressure steam thermal source from pipe network.The carbon dioxide and the regeneration gas that again discharge interior energy are together delivered to underground heating by compressor 7, reciprocation cycle again.
During system for geothermal production of electricity runs, some carbon dioxide injected is can penetrate into stratum by during bottom interstitial space, and namely this part carbon dioxide is sealed up for safekeeping in underground, and the carbon dioxide of loss supplements by the carbon dioxide newly trapped from flue gas.
Claims (3)
1. the collecting carbonic anhydride utilizing underground heat, generating and mothballed plant, comprise absorption tower (2), it is characterized in that, the rich solution outlet of bottom, absorption tower (2) is through poor rich liquid heat exchanger (3) and regenerator (4) upper end rich solution inlet communication, and the lean solution outlet of regenerator (4) bottom is communicated with through the upper packing section in poor rich liquid heat exchanger (3) and absorption tower (2);
Described regenerator (4) bottom is provided with reboiler (10), and the thermal source of reboiler (10) is provided by two-way, and a steam inlet, road is communicated with the low-pressure steam from steam pipe system, another road and CO
2the carbon dioxide gas outlet of decompressor (8) is communicated with;
The CO at described regenerator (4) top
2gas vent is communicated with condenser (5) upper end gas feed, and condenser (5) lower end is communicated with regenerator (4) upper end condensate liquid reflux inlet, the CO at condenser (5) top
2gas after being communicated with reboiler (10) carbon dioxide gas outlet again with CO
2cooler (6) entrance is communicated with, CO
2cooler (6) outlet and compressor (7) inlet communication, compressor (7) outlet is connected to geothermal layer;
Described reboiler (10) carbon dioxide entrance and CO
2decompressor (8) gas vent is communicated with, CO
2the carbon dioxide that decompressor (8) gas access and geothermal layer spray is communicated with, CO
2decompressor (8) axle head and CO
2generator (9) is communicated with, CO
2the electric power that generator (9) produces is sent to electrical network.
2. according to claim 1 a kind of utilize underground heat collecting carbonic anhydride, generating and mothballed plant, it is characterized in that, described CO
2decompressor (8) is piston type or turbo-expander.
3. according to claim 1 a kind of utilize underground heat collecting carbonic anhydride, generating and mothballed plant, it is characterized in that, described reboiler (10) is provided with two-way thermal source, and the carbon dioxide after steam and expansion power generation, is used alone or uses simultaneously.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520275149.0U CN204672103U (en) | 2015-04-30 | 2015-04-30 | A kind of utilize underground heat collecting carbonic anhydride, generating and mothballed plant |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520275149.0U CN204672103U (en) | 2015-04-30 | 2015-04-30 | A kind of utilize underground heat collecting carbonic anhydride, generating and mothballed plant |
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| CN204672103U true CN204672103U (en) | 2015-09-30 |
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Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104785073A (en) * | 2015-04-30 | 2015-07-22 | 中国华能集团清洁能源技术研究院有限公司 | Carbon dioxide capture, power generation and sequestration system utilizing terrestrial heat |
| CN105585015A (en) * | 2016-02-19 | 2016-05-18 | 天津大学 | Gradient utilization system by medium/low-temperature geothermal energy assisted carbon dioxide capture |
| CN107631553A (en) * | 2016-07-18 | 2018-01-26 | 西门子公司 | Mixed working fluid cycle generating system, mixed working fluid circulation waste-heat recovery device and method |
| CN114046172A (en) * | 2021-10-27 | 2022-02-15 | 中国长江三峡集团有限公司 | Coal fire treatment and utilization system and method based on carbon dioxide process and modular design |
| CN115523783A (en) * | 2022-09-19 | 2022-12-27 | 西南交通大学 | Method for integrating carbon dioxide sequestration and carbon dioxide energy storage |
| WO2023019868A1 (en) * | 2021-08-16 | 2023-02-23 | 中国华能集团清洁能源技术研究院有限公司 | Carbon capturing and peak shaving coupling apparatus and method |
-
2015
- 2015-04-30 CN CN201520275149.0U patent/CN204672103U/en active Active
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104785073A (en) * | 2015-04-30 | 2015-07-22 | 中国华能集团清洁能源技术研究院有限公司 | Carbon dioxide capture, power generation and sequestration system utilizing terrestrial heat |
| CN105585015A (en) * | 2016-02-19 | 2016-05-18 | 天津大学 | Gradient utilization system by medium/low-temperature geothermal energy assisted carbon dioxide capture |
| CN107631553A (en) * | 2016-07-18 | 2018-01-26 | 西门子公司 | Mixed working fluid cycle generating system, mixed working fluid circulation waste-heat recovery device and method |
| CN107631553B (en) * | 2016-07-18 | 2020-03-10 | 西门子公司 | Mixed working medium circulating power generation system, mixed working medium circulating waste heat recovery device and method |
| WO2023019868A1 (en) * | 2021-08-16 | 2023-02-23 | 中国华能集团清洁能源技术研究院有限公司 | Carbon capturing and peak shaving coupling apparatus and method |
| CN114046172A (en) * | 2021-10-27 | 2022-02-15 | 中国长江三峡集团有限公司 | Coal fire treatment and utilization system and method based on carbon dioxide process and modular design |
| CN114046172B (en) * | 2021-10-27 | 2023-07-14 | 中国长江三峡集团有限公司 | System and method for treating and utilizing coal fire based on carbon dioxide process and modularized design |
| CN115523783A (en) * | 2022-09-19 | 2022-12-27 | 西南交通大学 | Method for integrating carbon dioxide sequestration and carbon dioxide energy storage |
| CN115523783B (en) * | 2022-09-19 | 2023-07-21 | 西南交通大学 | Method for integrating carbon dioxide sealing and storing with carbon dioxide storing |
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