The power generating system of coal-gas turbine of no CO2 emission and method
One. technical field
The present invention relates to field of environment protection. it is the coal fired boiler blower in the conventional coal generating system to be sent into air change into and send into pure oxygen and CO
2Coal is fully burnt, and do not have nitrogen oxide and generate and to make it all become CO
2, collect CO then
2Utilization makes it the method for zero-emission, the CO that produces in its tail gas based on coal-gas turbine generating discharge
2Make chemical product (dry ice, chemical fertilizer etc.).The method comprises generating, chemical product production method.
Two. background technique
Technology related to the present invention mainly comprises at present: power generating system of coal-gas turbine, CO
2Treatment technology, chemical product are produced it, and development situation and feature are as follows separately:
1. power generating system of coal-gas turbine is based on the coal-fired gas technology that produces of fluidized bed boiler. with the generating of combustion gas propelling gas turbine engine, utilize high-temperature exhaust air in exhaust heat boiler, to produce the generating of steam driving steam turbine again.Because what send into boiler is that tail gas that pressurized air burning back produces is one and had both contained CO
2, mixed tail gas such as nitrogen oxide are difficult to CO
2Separate.
2. carbon dioxide treatment technology in the power generating system of coal-gas turbine tail gas of discharging: a large amount of dischargings of carbon dioxide cause that the problem of global warming is serious day by day, and heat energy power-generating produces a large amount of CO
2Be to cause CO in the atmosphere
2The basic reason that increases. therefore in the coal-gas turbine power generation process, effectively utilize and handle CO
2Be the ten minutes key technology. and the CO that gas turbine power generation at present produces in combustion back, firing chamber
2, be owing to be to introduce air burning, the CO in the smoke evacuation
2By gas dilutions such as nitrogen oxides. make CO
2It is very low that concentration becomes, and intractability is big. as handle this part CO
2Need to consume a large amount of energy consumptions. uneconomical economically.
Three. summary of the invention
The objective of the invention is to overcome the worn-out end in the power generating system of coal-gas turbine production, solve CO
2Waste gas is to the pollution of atmosphere.
1. the objective of the invention is to utilize in the coal-gas turbine power generation process. introduce pure oxygen and make it produce a large amount of CO
2By Physical Absorption system and CO
2Compress and liquefy production chemical product K (as dry ice, carbonic hydroammonium, chemical fertilizer or the like.)
2. for obtaining the CO of capacity
2. in for gas turbine combustion coal gas, supply pure oxygen, make CO perfect combustion formation CO in the coal gas
2. produce a large amount of waste heats simultaneously. obtain the high temperature saturated vapor through exhaust heat boiler and come the pushing turbine generating, the tail steam also can be for the city heat supply heating; Because for pure oxygen, it is to obtain through supercharging from air separation facility to the firing chamber.
3. for preventing from fluidized bed boiler burning, to produce harmful gas such as nitrogen oxide, also send into CO when introducing pure oxygen
2Gas is removed tail gas and is absorbed CO
2By the difficult problem of gas dilutions such as nitrogen oxide.
Purpose of the present invention can realize by following measure:
No CO
2The power generating system of coal-gas turbine of discharging, this system comprises air separation facility A, oxygen pressurized machine B, fluidized bed boiler C, firing chamber D, cooling jacket E, gas turbine F, exhaust heat boiler G, steam turbine H, CO
2Physical Absorption I, CO
2Compression J, chemical product K. wherein air separation facility A links to each other with firing chamber D again with fluidized bed boiler C through oxygen pressure-increasing machine B simultaneously, the coal gas that fluidized bed boiler C produces enters pure oxygen that firing chamber D and air separation facility A supply with and fully burns and produce high-temperature high-pressure air flow propelling gas turbine engine F and generate electricity, wherein, the operating temperature of alleviating gas turbine F enters exhaust heat boiler G after cooling water is heated for feeding, the high temperature saturated vapour pushing turbine H generating of its backheat, its waste heat can be for the city heating; (5) CO in the gas turbine F tail gas
2Feed back to fluidized bed boiler C through a Physical Absorption I part, remaining makes CO through liquefaction compression J production chemical product K
2All transform and realize CO
2Zero-emission.
Four. technological scheme
Purpose of the present invention can also be come reality by following measure:
No CO
2The power generating system of coal-gas turbine and the method for discharging comprises the steps: that (1) is from fluidized bed boiler supply coal gas C:(2) obtain pure oxygen from air separation facility A through supercharging; (3) cooling water enters the cooling jacket E of firing chamber D; (4) entering pure oxygen that the coal gas of firing chamber D and air separation facility A supply with fully burns and produces high-temperature high-pressure air flow propelling gas turbine engine F generating, wherein, the operating temperature of alleviating gas turbine F enters exhaust heat boiler G after cooling water is heated for feeding, the high temperature saturated vapour pushing turbine H generating of its backheat, its waste heat can be for the city heating; (5) CO in the gas turbine F tail gas
2Again through liquefaction compression J production chemical product K, (6) are CO partly through Physical Absorption I
2Return and send into fluidized bed boiler C again.
The present invention compared with prior art has following advantage:
1, the present invention organically is combined into circulating generation and chemical product K, has made full use of intrasystem resource, reality the high efficiency of system, the superior feature of environmental protection and good and economic.
2. the present invention adopts pure oxygen for the coal burning in the fluidized bed boiler, sends into CO simultaneously again
2, prevent that the nitrogen oxide that is harmful to from producing, and makes tail gas both not have CO
2, discharging does not have harmful discharged nitrous oxides again, has improved the environmental protection quality greatly.
3. the present invention adopts pure oxygen and gas firing for the gas turbine work done, has improved exerting oneself of generator, produces a large amount of CO again
2, after absorbing, make chemical product K (dry ice). and solved CO
2Zero-emission obtains this advanced novel combination of chemical product K. again and has improved whole economic benefit and social benefit.
4. the present invention sends into firing chamber G by air separation facility A through the pure oxygen of oxygen pressurized machine B, can also save the gas compressor of gas turbine prime, the cost that has reduced the combustion machine helps improving the stability and the safety reliability of unit operation again. and also increase generated output, increased the heat circulation and both helped the combustion gas cooling at firing chamber increase water-cooled overcoat.
5. the present invention is fuel with coal not only, and can adopt other fuel, as living beings, petroleum coke, residual oil, municipal waste etc., has good fuel tolerance.
Five. description of drawings
Fig. 1 no CO of the present invention
2The power generating system of coal-gas turbine of discharging and the flow chart of method
Six. specific embodiment: as shown in Figure 1
The present invention includes the combined cycle generation subtense angle, CO
2The process for producing subtense angle. A-air separation facility in this system, B-oxygen pressurized machine, the C-fluidized bed boiler, the D-firing chamber, the E-cooling jacket, the F-gas turbine, the G-exhaust heat boiler, the H-steam turbine,, I-CO
2Physical Absorption, J-CO
2Compression, the K-chemical product.
Present embodiment provides a kind of coal-gas turbine power generation sub-system of the CO2 of nothing discharging, this system comprises air separation facility A, oxygen pressurized machine B, fluidized bed boiler C, cooling jacket E, firing chamber D, gas turbine F, exhaust heat boiler G, steam turbine H. wherein cooling water send into exhaust heat boiler G by cooling jacket E and utilize heat exchange to produce the high pressure saturated vapor; Form high pressure high temperature vapor pushing turbine H generating.
Present embodiment also provides a kind of CO
2The process for producing subtense angle: this system comprises I-CO
2Physical Absorption, J-CO
2Compression.
Present embodiment also provides a kind of inhibition and generation chemical product K (as system dry ice, chemical fertilizer or the like) subtense angle: this system comprises the CO after the gas turbine work done
2Physical Absorption I and CO
2Compressed J links to each other with chemical product K.
The flow process of this method following (with reference to Fig. 1)
Oxygen 1 enters firing chamber D through supercharging 2 and enters fluidized bed boiler C simultaneously, the coal gas 3 that fluidized bed boiler produces enters firing chamber D, cooling water 4 enters the cooling jacket E of firing chamber D, coal gas 3 produces high-temperature high-pressure fuel gas 7 propelling gas turbine engine F generating with pure oxygen in firing chamber D burning back, the tail gas 8 of its generation enters exhaust heat boiler G, CO in the tail gas
2Feed back to fluidized bed boiler C by a Physical Absorption I part 14, the CO of all the other absorptions
211 send into and compress and liquefy J, liquid CO
2Make dry ice K, the high pressure steam 9 that exhaust heat boiler G produces is used for pushing turbine H generating, and the tail steam 10 of outflow can supply urban heat supplying, and cooling water 4 injects its steam 6 input exhaust heat boilers heating of producing of firing chamber D cooling jacket E, for the generation high temperature and high pressure steam.
This method embodiment adopts coal. and it has related parameter as follows:
Coal consumption amount 19.20 (Kg/s)
Gas turbine power generation 21.2 ten thousand KW steam turbine power generations 12.3 ten thousand KW
Air separation facility wasted work 2.1 ten thousand KW CO
2Compressor wasted work 1.4 ten thousand KW
Can supply generated energy 300,000 KW CO
2The recovery rate 100%.