CN110606524A - System for evaporating and concentrating desulfurization wastewater by efficiently utilizing flue gas waste heat - Google Patents
System for evaporating and concentrating desulfurization wastewater by efficiently utilizing flue gas waste heat Download PDFInfo
- Publication number
- CN110606524A CN110606524A CN201911030786.0A CN201911030786A CN110606524A CN 110606524 A CN110606524 A CN 110606524A CN 201911030786 A CN201911030786 A CN 201911030786A CN 110606524 A CN110606524 A CN 110606524A
- Authority
- CN
- China
- Prior art keywords
- tower
- flue gas
- inlet
- outlet
- air
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
- 239000002351 wastewater Substances 0.000 title claims abstract description 69
- 238000006477 desulfuration reaction Methods 0.000 title claims abstract description 55
- 230000023556 desulfurization Effects 0.000 title claims abstract description 55
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 title claims abstract description 51
- 239000003546 flue gas Substances 0.000 title claims abstract description 51
- 238000001704 evaporation Methods 0.000 title claims abstract description 25
- 239000002918 waste heat Substances 0.000 title claims abstract description 22
- 230000008878 coupling Effects 0.000 claims abstract description 23
- 238000010168 coupling process Methods 0.000 claims abstract description 23
- 238000005859 coupling reaction Methods 0.000 claims abstract description 23
- 239000000428 dust Substances 0.000 claims abstract description 23
- 239000002002 slurry Substances 0.000 claims abstract description 20
- 230000008020 evaporation Effects 0.000 claims abstract description 12
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 79
- 230000003009 desulfurizing effect Effects 0.000 claims description 22
- 238000005406 washing Methods 0.000 claims description 19
- 239000000779 smoke Substances 0.000 claims description 13
- 238000010438 heat treatment Methods 0.000 claims description 4
- 239000007789 gas Substances 0.000 claims description 3
- 230000008676 import Effects 0.000 claims 10
- 235000012489 doughnuts Nutrition 0.000 claims 1
- 230000002093 peripheral effect Effects 0.000 description 17
- 239000007788 liquid Substances 0.000 description 10
- 239000007921 spray Substances 0.000 description 9
- 239000002699 waste material Substances 0.000 description 7
- 238000000034 method Methods 0.000 description 6
- 239000012141 concentrate Substances 0.000 description 5
- 238000002485 combustion reaction Methods 0.000 description 4
- 238000005516 engineering process Methods 0.000 description 4
- 239000003245 coal Substances 0.000 description 3
- 238000001035 drying Methods 0.000 description 3
- 238000000889 atomisation Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000005507 spraying Methods 0.000 description 2
- 238000004065 wastewater treatment Methods 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000009388 chemical precipitation Methods 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 238000002425 crystallisation Methods 0.000 description 1
- 230000008025 crystallization Effects 0.000 description 1
- 238000011010 flushing procedure Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/02—Treatment of water, waste water, or sewage by heating
- C02F1/04—Treatment of water, waste water, or sewage by heating by distillation or evaporation
- C02F1/16—Treatment of water, waste water, or sewage by heating by distillation or evaporation using waste heat from other processes
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
- C02F2103/18—Nature of the water, waste water, sewage or sludge to be treated from the purification of gaseous effluents
Abstract
The invention discloses a system for evaporating and concentrating desulfurization wastewater by efficiently utilizing flue gas waste heat, which relates to the technical field of desulfurization wastewater evaporation and concentration, and comprises an air preheater, a hot air fan, a dryer, a dust remover, an induced draft fan, a booster fan, a coupling evaporator, a desulfurization tower and a slurry discharge pump, wherein the outlet of the air preheater is connected with the inlet of the dust remover, the outlet of the hot air fan is connected with the inlet of the dust remover through the dryer, the outlet of the dust remover is connected with the inlet of the induced draft fan, the outlet of the induced draft fan is respectively connected with the inlets of the desulfurization tower and the booster fan, the outlet of the booster fan is connected with the desulfurization tower through the coupling evaporator, and the coupling evaporator is connected with the dryer through the slurry discharge pump; the waste water is concentrated in grades, so that the heat utilization rate is improved, the tower utilization rate is improved, and the tower height is effectively reduced.
Description
Technical Field
The invention relates to the technical field of desulfurization wastewater evaporation and concentration, in particular to a system for efficiently utilizing flue gas waste heat to evaporate and concentrate desulfurization wastewater.
Background
The existing desulfurization wastewater treatment process widely applied is a chemical precipitation method, and a separate wastewater treatment system is arranged in the method. The evaporation concentration process is to concentrate the desulfurization wastewater by using an evaporator, the product water is recycled, and the concentrated water can be converted into solid salt for disposal through crystallization and drying processes. The technology has wide applicability to wastewater quality, units and coal types and has wide application prospect, at present, the evaporation concentration technology mainly comprises an MED multi-effect evaporation technology and an MVR mechanical vapor recompression evaporation technology, and the two modes need to additionally consume high-parameter vapor or compression work, so that the concentration cost is increased.
Disclosure of Invention
In order to solve the technical problems, the invention aims to provide a system for evaporating, concentrating and desulfurizing wastewater by efficiently utilizing flue gas waste heat.
The purpose of the invention is realized by the following technical scheme: the utility model provides a system for concentrated desulfurization waste water of high-efficient flue gas waste heat evaporation of utilizing, includes air preheater 1, hot air blower 2, desicator 3, dust remover 4, draught fan 5, booster fan 6, coupling evaporimeter 7, desulfurizing tower 8, slurry discharge pump 9, air preheater 1 give vent to anger the end with the inlet end of dust remover 4 is connected, hot air blower 2 give vent to anger the end and pass through desicator 3 with the inlet end of dust remover 4 is connected, dust remover 4 give vent to anger the end with the inlet end of draught fan 5 is connected, draught fan 5 give vent to anger the end respectively with desulfurizing tower 8 with booster fan 6's inlet end is connected, booster fan 6 give vent to anger the end and pass through coupling evaporimeter 7 with desulfurizing tower 8 is connected, coupling evaporimeter 7 passes through slurry discharge pump 9 with desicator 3 is connected.
In a preferred embodiment, the coupling evaporator 7 comprises a housing 701 and a circulating pump 10, a flue gas outlet 702 connected with the desulfurization tower 8 is arranged at the top end of the housing 701, a slurry outlet 703 connected with the slurry discharge pump 9 is arranged at the bottom of the housing 701, a circulating water inlet 704, a circulating water outlet 705 positioned at the lower part of the circulating water inlet 704 and a washing water inlet 706 positioned at the upper part of the circulating water inlet 704 are arranged on the outer side wall of the housing 701, the circulating water outlet 705 is connected with the circulating water inlet 704 through the circulating pump 10, a washing coil 707 communicated with the washing water inlet 706 and a circulating water coil 708 communicated with the circulating water inlet 704 are arranged inside the housing 701, a demister positioned at the upper part of the washing coil 707 is arranged inside the housing 701, a plurality of washing water nozzles 710 arranged vertically and upwards are uniformly arranged at the top of the washing coil 707, a plurality of circulating water nozzles 711 which are vertically and downwards arranged are uniformly arranged at the bottom of the circulating water coil 708.
In a preferred embodiment, the outer side wall of the housing 701 is sleeved with a tower circumference bellows 712 located between the circulating water inlet 704 and the circulating water outlet 705, the tower circumference bellows 712 is in a hollow circular ring shape, the inner side wall of the tower circumference bellows 712 is the outer side wall of the housing 701, the outer side wall of the tower circumference bellows 712 is provided with a flue gas inlet pipe 713 connected with the outlet of the booster fan 6, the inner side wall ring direction of the tower circumference bellows 712 is uniformly provided with four communicating pipes, the inside of the tower circumference bellows 712 is communicated with the air inlet 714 inside the housing 701, and the air inlet direction of the air inlet 714 is tangent to the inner side wall of the tower circumference bellows 712.
In a preferred embodiment, four wastewater spray nozzles 715 are vertically and downwardly disposed on the top surface of the inside of the tower peripheral wind box 712 with respect to the four gas inlets 714, a wastewater inlet pipe 716 connected to the four wastewater spray nozzles 715 is disposed on the upper end surface of the tower peripheral wind box 712, and the wastewater inlet pipe 716 is connected to the desulfurization tower 8.
In a preferred embodiment, the desulfurization tower 8 is provided with a desulfurization waste water outlet 801, a smoke inlet 802 and a smoke outlet 803, the desulfurization waste water outlet 801 is connected with the waste water inlet pipe 716, and the smoke inlet 802 is respectively connected with the outlet of the induced draft fan 5 and the smoke outlet 702.
In a preferred embodiment, a heater 11 is disposed between the circulation pump 10 and the circulation water inlet 704, the heater 11 includes a heater outlet 1101 communicated with the circulation water inlet 704, a heater inlet 1102 communicated with the outlet of the circulation pump 10, a hot water inlet 1103, and a hot water outlet 1104, the heater inlet 1102 and the heater outlet 1101 are communicated inside the heater 11, and the hot water inlet 1103 and the hot water outlet 1104 are communicated inside the heater 11 by disposing a heating pipe.
The invention has the beneficial effects that:
1. the method utilizes the flue gas waste heat after the induced draft fan to evaporate and concentrate the desulfurization wastewater, utilizes the waste heat to evaporate, and is close to zero operation cost; the flue gas after mixed heat exchange is sent into a desulfurizing tower for treatment, and the water vapor in the flue gas can be recovered;
2. according to the invention, an air distribution mode is originally created, so that flue gas uniformly enters the coupling evaporator through the four tangential air inlets of the air boxes on the periphery of the tower in a rotating manner, the flue gas enters more uniformly, the internal space is changed into a spiral type from an original straight-up straight-down type, the space utilization rate is greatly improved, and the height of the tower is effectively reduced;
3. the invention concentrates the waste water by stages, improves the heat utilization rate, adopts the atomization spraying liquid inlet, carries out atomization spraying at the air inlet, and carries out the first-stage heat exchange by utilizing the high specific surface area of the high-flow-rate flue gas and the waste liquid fog drops entering the tower peripheral air box and the slight flash evaporation effect generated by the low-speed area after the waste liquid fog drops enter the shell from the high-speed area inside the tower peripheral air box; the concentrated wastewater is sprayed circularly in a large flow, so that the mass transfer times in unit time are increased, and the concentrated wastewater is subjected to secondary concentration; the two sections of concentration multiplying power are in a multiplier relation, so that the utilization rate of the tower is improved, and the height of the tower is effectively reduced.
Drawings
The invention is explained in further detail below with reference to the drawing.
FIG. 1 is a schematic flow chart of a system for evaporating and concentrating desulfurization wastewater by using flue gas waste heat with high efficiency according to an embodiment of the present invention;
FIG. 2 is a schematic structural diagram of a coupling evaporator of a system for evaporating and concentrating desulfurization wastewater by using flue gas waste heat efficiently according to an embodiment of the present invention;
FIG. 3 is a schematic structural diagram of a tower periphery wind box of a system for evaporating and concentrating desulfurization wastewater by utilizing flue gas waste heat efficiently according to an embodiment of the invention;
in the figure:
1. an air preheater; 2. a hot air blower; 3. a dryer; 4. a dust remover; 5. an induced draft fan; 6. a booster fan; 7. a coupling evaporator; 701. a housing; 702. a flue gas outlet; 703. a slurry outlet; 704. a circulating water inlet; 705. a circulating water outlet; 706. a rinse water inlet; 707. flushing the coil pipe; 708. a circulating water coil pipe; 709. a demister; 710. rinsing the water spray head; 711. circulating water spray heads; 712. a tower periphery air box; 713. a flue gas inlet pipe; 714. an air inlet; 715. a waste water spray head; 716. a waste water inlet pipe; 8. a desulfurizing tower; 801. a desulfurization waste water outlet; 802. a smoke inlet; 803. a smoke outlet; 9. a slurry discharge pump; 10. a circulation pump; 11. a heater; 1101. a heater outlet; 1102. a heater inlet; 1103. a hot water inlet; 1104. a hot water outlet.
Detailed Description
In order to make the objects, technical solutions and advantages of the embodiments of the present invention clearer, the technical solutions in the embodiments of the present invention will be clearly and completely described below with reference to the drawings in the embodiments of the present invention, and it is obvious that the described embodiments are some, but not all, embodiments of the present invention. The components of embodiments of the present invention generally described and illustrated in the figures herein may be arranged and designed in a wide variety of different configurations. Thus, the following detailed description of the embodiments of the present invention, presented in the figures, is not intended to limit the scope of the invention, as claimed, but is merely representative of selected embodiments of the invention. All other embodiments, which can be derived by a person skilled in the art from the embodiments given herein without making any creative effort, shall fall within the protection scope of the present invention.
Reference will now be made in detail to embodiments of the present invention, examples of which are illustrated in the accompanying drawings, wherein like or similar reference numerals refer to the same or similar elements or elements having the same or similar function throughout. The embodiments described below with reference to the drawings are illustrative and intended to be illustrative of the invention and are not to be construed as limiting the invention.
The invention will be further described with reference to the drawings and specific examples.
As shown in fig. 1-3, a system for evaporating and concentrating desulfurization wastewater by efficiently utilizing flue gas waste heat according to an embodiment of the present invention includes an air preheater 1, a hot air blower 2, a dryer 3, a dust remover 4, a draught fan 5, a booster fan 6, a coupling evaporator 7, a desulfurization tower 8, and a slurry discharge pump 9, an air outlet end of the air preheater 1 is connected with an air inlet end of the dust remover 4, an air outlet end of the hot air blower 2 is connected with an air inlet end of the dust remover 4 through the dryer 3, an air outlet end of the dust remover 4 is connected with an air inlet end of the draught fan 5, an air outlet end of the draught fan 5 is connected with air inlet ends of the desulfurization tower 8 and the booster fan 6, an air outlet end of the booster fan 6 is connected with the desulfurization tower 8 through the coupling evaporator 7, and the coupling evaporator 7 is connected with the dryer 3 through the slurry discharge pump 9;
in the embodiment of the invention, the waste heat of the flue gas generated by the boiler is utilized to evaporate and concentrate the desulfurization wastewater, the waste heat is utilized to evaporate, the operation cost is nearly zero, the air preheater 1 is the prior art, namely an air preheater, and the heat of the flue gas in the tail flue of the boiler is utilized to heat primary air and secondary air entering the boiler, so that the smoke exhaust loss is reduced, the air inlet temperature is increased, and the efficiency of the boiler is improved; the air which is fed into the hearth from the lower part of the grate for combustion is called primary air, and the primary air has the main function of providing air for the combustion of the coal according to the oxygen required by the coal in the combustion process in the furnace; the secondary air is formed by a plurality of air flows which are sprayed into the hearth from the upper part of the grate at high speed, is relative to the primary air and is used for reducing incomplete combustion loss; the flue gas discharged by the boiler passes through the air preheater 1 and then enters a dust remover 4 (the prior art) for dust removal; hot secondary air sequentially passes through a hot air fan 2 (prior art) and a dryer 3 (prior art) and then enters a dust remover 4 for dust removal, flue gas subjected to dust removal by the dust remover 4 is divided into two paths by an induced draft fan 5, and one path of flue gas directly enters a desulfurizing tower 8 (prior art) for desulfurization; one path of flue gas enters a coupling evaporator 7 after being pressurized by a booster fan 6 (prior art), the desulfurization wastewater is evaporated and concentrated by utilizing the waste heat of the flue gas in the coupling evaporator 7, and the evaporated and concentrated high-concentration slurry is pumped into a dryer 3 through a slurry discharge pump 9 (prior art) for drying treatment.
In a specific embodiment, the coupling evaporator 7 comprises a shell 701 and a circulating pump 10, a flue gas outlet 702 connected with the desulfurizing tower 8 is arranged at the top end of the shell 701, a slurry outlet 703 connected with a slurry discharge pump 9 is arranged at the bottom of the shell 701, a circulating water inlet 704 is arranged on the outer side wall of the shell 701, a circulating water outlet 705 positioned at the lower part of the circulating water inlet 704, and a washing water inlet 706 positioned at the upper part of the circulating water inlet 704, wherein the washing water inlet 706 is used for connecting washing water and is used for regular washing in the coupling evaporator 7, the circulating water outlet 705 is connected with the circulating water inlet 704 through the circulating pump 10, a washing coil 707 communicated with the washing water inlet 706 and a circulating water coil 708 communicated with the circulating water inlet 704 are arranged inside the shell 701, a demister positioned at the upper part of the washing coil 707 is arranged inside the shell 701, and a plurality, the bottom of the circulating water coil 708 is uniformly provided with a plurality of circulating water nozzles 711 which are vertically arranged downwards.
In a specific embodiment, a tower peripheral bellows 712 located between the circulating water inlet 704 and the circulating water outlet 705 is sleeved on an outer side wall of the housing 701, the tower peripheral bellows 712 is in a hollow circular ring shape, an inner side wall of the tower peripheral bellows 712 is an outer side wall of the housing 701, a flue gas inlet pipe 713 connected with an outlet of the booster fan 6 is arranged on the outer side wall of the tower peripheral bellows 712, four air inlets 714 communicated with the inside of the tower peripheral bellows 712 and the inside of the housing 701 are uniformly arranged in an annular direction on the inner side wall of the tower peripheral bellows 712, and an air inlet direction of the air inlets 714 is tangential to the inner side wall of the tower.
In a specific embodiment, four wastewater spray nozzles 715 are vertically and downwardly disposed on the top surface of the inside of the tower peripheral bellows 712 with respect to the four gas inlets 714, a wastewater inlet pipe 716 connected to the four wastewater spray nozzles 715 is disposed on the upper end surface of the tower peripheral bellows 712, and the wastewater inlet pipe 716 is connected to the desulfurization tower 8.
In a specific embodiment, the desulfurization tower 8 is provided with a desulfurization wastewater outlet 801, a smoke inlet 802 and a smoke outlet 803, the desulfurization wastewater outlet 801 is connected with a wastewater inlet pipe 716, and the smoke inlet 802 is respectively connected with an outlet of the induced draft fan 5 and a smoke outlet 702;
in the embodiment of the invention, the desulfurizing tower 8 is the prior art, is used for flue gas desulfurization, simultaneously generates desulfurization waste water, and discharges the desulfurization waste water into the coupling evaporator 7 through the desulfurization waste water outlet 801 to perform evaporation concentration.
In a specific embodiment, a heater 11 is disposed between the circulation pump 10 and the circulation water inlet 704, the heater 11 includes a heater outlet 1101 communicated with the circulation water inlet 704, a heater inlet 1102 communicated with the outlet of the circulation pump 10, a hot water inlet 1103, and a hot water outlet 1104, the heater inlet 1102 and the heater outlet 1101 are communicated inside the heater 11, and the hot water inlet 1103 and the hot water outlet 1104 are communicated inside the heater 11 by disposing a heating pipe.
In the embodiment of the invention, the desulfurization wastewater generated by the desulfurization tower 8 enters the wastewater inlet pipe 716 through the desulfurization wastewater outlet 801, and then is atomized and sprayed into the tower peripheral air box 712 through the four wastewater spray nozzles 715, at the moment, the flue gas pressurized by the booster fan 6 enters the tower peripheral air box 712 through the flue gas inlet pipe 713, and the first-stage heat exchange is carried out by utilizing the high specific surface area of the high-flow-rate flue gas and the waste liquid fog drops entering the shell 701 from the high-speed area in the tower peripheral air box 712 and the slight flash evaporation effect generated by the low-speed area after the waste liquid fog drops enter the shell 701 from the high-speed area in the tower peripheral;
as shown in fig. 3, in the embodiment of the present invention, four tangential air inlets are adopted, so that flue gas carrying waste liquid droplets uniformly enters the housing 701 through the four air inlets 714 of the tower peripheral air box 712 in a rotating manner, so that the flue gas enters more uniformly, the original straight-up and straight-down manner in the housing 701 is changed into a spiral manner, the space utilization rate is greatly improved, and the tower height is effectively reduced;
the flue gas carrying the waste liquid fog drops enters the shell 701 and then spirally moves upwards, at the moment, circulating water circulated by the circulating pump 10 is sprayed downwards through the circulating water spray nozzle 711, the circulating water is fully mixed and contacted with the flue gas carrying the waste liquid fog drops, convection heat transfer, the flue gas carries the steam evaporated by the moisture to flow upwards, the desulfurization waste water flows downwards, the circulating water is low-concentration desulfurization wastewater pumped by the circulating pump after the desulfurization wastewater flows to the bottom of the shell 701, the high-concentration desulfurization wastewater is discharged through the slurry outlet 703 at the bottom, the desulfurization wastewater pumped by the circulating pump 10 is continuously sprayed in a circulating manner, the mass transfer frequency in unit time is increased, two-stage concentration is carried out, the two-stage concentration multiplying power is a multiplier relation, the utilization rate of the tower is increased, the height of the tower is effectively reduced, and the concentration of the desulfurization wastewater is continuously increased in the circulating process, so that the desulfurization wastewater with a certain concentration is discharged through the slurry outlet 703 at the bottom; when the circulating pump 10 circulates the desulfurization waste water, the heater 11 is used for heating the desulfurization waste water to keep the desulfurization waste water at a higher temperature;
the flue gas carries the vapor after the evaporation to pass through the defroster 709 defogging after, carries out desulfurization treatment in flue gas outlet 702 entering desulfurizing tower 8, and the vapor in the flue gas can be retrieved, and the desulfurization waste water that desulfurizing tower 8 formed gets into coupling evaporimeter 7, utilizes the flue gas waste heat to carry out evaporative concentration, and the high concentration thick liquid that forms carries out drying process in getting into the desicator at last, and defroster 709 is prior art for fog grain, the entrapment of thick liquid drop carried to the flue gas get off.
Finally, it should be noted that: the above-mentioned embodiments are only used for illustrating the technical solution of the present invention, and not for limiting the same; although the present invention has been described in detail with reference to the foregoing embodiments, it will be understood by those of ordinary skill in the art that: the technical solutions described in the foregoing embodiments may still be modified, or some or all of the technical features may be equivalently replaced; and the modifications or the substitutions do not make the essence of the corresponding technical solutions depart from the scope of the technical solutions of the embodiments of the present invention.
Claims (6)
1. The utility model provides a system for high-efficient utilization flue gas waste heat evaporation concentration desulfurization waste water which characterized in that: comprises an air preheater (1), a hot air fan (2), a dryer (3), a dust remover (4), a draught fan (5), a booster fan (6), a coupling evaporator (7), a desulfurizing tower (8) and a slurry discharge pump (9), the air outlet end of the air preheater (1) is connected with the air inlet end of the dust remover (4), the air outlet end of the hot air fan (2) is connected with the air inlet end of the dust remover (4) through the dryer (3), the air outlet end of the dust remover (4) is connected with the air inlet end of the induced draft fan (5), the air outlet end of the induced draft fan (5) is respectively connected with the air inlet ends of the desulfurizing tower (8) and the booster fan (6), the air outlet end of the booster fan (6) is connected with the desulfurizing tower (8) through the coupling evaporator (7), the coupling evaporator (7) is connected with the dryer (3) through the slurry discharge pump (9).
2. The system for evaporating, concentrating and desulfurizing waste water by efficiently utilizing the waste heat of flue gas as claimed in claim 1, wherein: the coupling evaporator (7) comprises a shell (701) and a circulating pump (10), a flue gas outlet (702) connected with the desulfurizing tower (8) is arranged at the top end of the shell (701), a slurry outlet (703) connected with the slurry discharge pump (9) is arranged at the bottom of the shell (701), a circulating water inlet (704), a circulating water outlet (705) positioned at the lower part of the circulating water inlet (704) and a washing water inlet (706) positioned at the upper part of the circulating water inlet (704) are arranged on the outer side wall of the shell (701), the circulating water outlet (705) is connected with the circulating water inlet (704) through the circulating pump (10), a washing coil (707) communicated with the washing water inlet (706) and a circulating water coil (708) communicated with the circulating water inlet (704) are arranged inside the shell (701), a demister (709) positioned at the upper part of the washing coil (707) is arranged inside the shell (701), the top of the washing coil pipe (707) is uniformly provided with a plurality of washing water nozzles (710) which are vertically arranged upwards, and the bottom of the circulating water coil pipe (708) is uniformly provided with a plurality of circulating water nozzles (711) which are vertically arranged downwards.
3. The system for evaporating, concentrating and desulfurizing waste water by efficiently utilizing the waste heat of flue gas as claimed in claim 2, wherein: cup joint on the lateral wall of casing (701) and be equipped with and be located circulating water import (704) with tower week bellows (712) between circulating water export (705), tower week bellows (712) are inside hollow donut shape, the inside wall of tower week bellows (712) does the lateral wall of casing (701), be equipped with on the lateral wall of tower week bellows (712) with exit linkage's of booster fan (6) flue gas import pipe (713), the inside wall hoop of tower week bellows (712) evenly is equipped with four intercommunications tower week bellows (712) inside with inside air inlet (714) of casing (701), the air inlet direction of air inlet (714) with the inside wall of tower week bellows (712) is tangent.
4. The system for evaporating, concentrating and desulfurizing waste water by efficiently utilizing the waste heat of flue gas as claimed in claim 3, wherein: four on the inside top surface of tower week bellows (712) relatively air inlet (714) are equipped with four vertical waste water shower nozzle (715) that set up downwards, the up end of tower week bellows (712) is equipped with four waste water import pipe (716) that waste water shower nozzle (715) are connected, waste water import pipe (716) with desulfurizing tower (8) are connected.
5. The system for evaporating, concentrating and desulfurizing waste water by efficiently utilizing the waste heat of flue gas as claimed in claim 4, wherein: desulfurizing tower (8) are equipped with desulfurization waste water export (801), advance mouth of smoke (802), exhaust port (803), desulfurization waste water export (801) with waste water inlet pipe (716) are connected, advance mouth of smoke (802) respectively with the export of draught fan (5) with exhanst gas outlet (702) are connected.
6. The system for evaporating, concentrating and desulfurizing waste water by efficiently utilizing the waste heat of flue gas as claimed in claim 5, wherein: the circulating pump (10) with be equipped with heater (11) between circulating water import (704), heater (11) include with heater export (1101) of circulating water import (704) intercommunication, with heater import (1102), hot water import (1103), hot water export (1104) of the export intercommunication of circulating pump (10), heater import (1102) with heater export (1101) in heater (11) inside intercommunication, hot water import (1103) with hot water export (1104) in heater (11) inside is through setting up the heating pipe intercommunication.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201911030786.0A CN110606524A (en) | 2019-10-28 | 2019-10-28 | System for evaporating and concentrating desulfurization wastewater by efficiently utilizing flue gas waste heat |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201911030786.0A CN110606524A (en) | 2019-10-28 | 2019-10-28 | System for evaporating and concentrating desulfurization wastewater by efficiently utilizing flue gas waste heat |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN110606524A true CN110606524A (en) | 2019-12-24 |
Family
ID=68895231
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201911030786.0A Pending CN110606524A (en) | 2019-10-28 | 2019-10-28 | System for evaporating and concentrating desulfurization wastewater by efficiently utilizing flue gas waste heat |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN110606524A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113816451A (en) * | 2021-09-16 | 2021-12-21 | 山东电力工程咨询院有限公司 | Desulfurization wastewater treatment system and process combining low-temperature waste heat concentration and hot secondary air drying |
| CN116428607A (en) * | 2023-06-14 | 2023-07-14 | 浙江程润云环境科技有限公司 | Denitration anti-blocking air preheater method and system |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105174342A (en) * | 2015-09-02 | 2015-12-23 | 江苏中顺节能科技有限公司 | Desulfurization wastewater pre-evaporation zero discharge treatment apparatus |
| CN109607907A (en) * | 2018-10-17 | 2019-04-12 | 北京国电龙源环保工程有限公司 | A kind of desulfurization wastewater multi-heat source coupled processing system and processing method |
| CN110240212A (en) * | 2019-07-09 | 2019-09-17 | 青岛达能环保设备股份有限公司 | A kind of waste water evaporation concentration system and technique based on low temperature spray desulfurization |
| CN210915395U (en) * | 2019-10-28 | 2020-07-03 | 卢浮恩环境科技(北京)有限公司 | System for evaporating and concentrating desulfurization wastewater by efficiently utilizing flue gas waste heat |
-
2019
- 2019-10-28 CN CN201911030786.0A patent/CN110606524A/en active Pending
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105174342A (en) * | 2015-09-02 | 2015-12-23 | 江苏中顺节能科技有限公司 | Desulfurization wastewater pre-evaporation zero discharge treatment apparatus |
| CN109607907A (en) * | 2018-10-17 | 2019-04-12 | 北京国电龙源环保工程有限公司 | A kind of desulfurization wastewater multi-heat source coupled processing system and processing method |
| CN110240212A (en) * | 2019-07-09 | 2019-09-17 | 青岛达能环保设备股份有限公司 | A kind of waste water evaporation concentration system and technique based on low temperature spray desulfurization |
| CN210915395U (en) * | 2019-10-28 | 2020-07-03 | 卢浮恩环境科技(北京)有限公司 | System for evaporating and concentrating desulfurization wastewater by efficiently utilizing flue gas waste heat |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113816451A (en) * | 2021-09-16 | 2021-12-21 | 山东电力工程咨询院有限公司 | Desulfurization wastewater treatment system and process combining low-temperature waste heat concentration and hot secondary air drying |
| CN116428607A (en) * | 2023-06-14 | 2023-07-14 | 浙江程润云环境科技有限公司 | Denitration anti-blocking air preheater method and system |
| CN116428607B (en) * | 2023-06-14 | 2023-10-20 | 浙江程润云环境科技有限公司 | Denitration anti-blocking air preheater method and system |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN109289430B (en) | Dry-wet coupling integrated smoke whitening and dust removing device | |
| CN105238904B (en) | A kind of flue gas of converter is based on transpiration-cooled low energy consumption semidry method dust pelletizing system | |
| CN105561721B (en) | The processing method of tail gas is calcined in production process of titanium pigment | |
| CN104180381A (en) | System and method for desulfurization cooling efficiency improvement and waste heat recovery | |
| CN110606524A (en) | System for evaporating and concentrating desulfurization wastewater by efficiently utilizing flue gas waste heat | |
| CN104150552A (en) | Distillation drying tower for treating desulfurized waste water in thermal power plant | |
| CN110182874A (en) | A kind of super low energy consumption flash concentration desulfurization wastewater and industrial brine waste zero emission system | |
| CN109354090A (en) | A kind of desulfurization wastewater evaporator and method with inert carrier circulation | |
| CN210915395U (en) | System for evaporating and concentrating desulfurization wastewater by efficiently utilizing flue gas waste heat | |
| CN111072091A (en) | System and method for treating desulfurization wastewater by using flue gas waste heat | |
| CN110975584A (en) | Novel flue gas purification tower | |
| CN208700619U (en) | A kind of vaporising device of high-concentration salt-containing wastewater | |
| CN203959868U (en) | Strong brine processing system | |
| CN109737439B (en) | Water cooling-whitening device for removing condensable pollutants and recycling water in flue gas | |
| CN209468148U (en) | The evaporating column of fume treatment high salt waste water | |
| CN106861378A (en) | A kind of wet desulfurization flue gas processing method | |
| CN207918477U (en) | A kind of dope drying system concentrating desulfurization wastewater using fume afterheat | |
| CN113104916B (en) | Evaporation treatment system for salt-containing sewage | |
| CN214218469U (en) | Wastewater zero-discharge treatment process device | |
| CN109437295A (en) | Sulfate process titanium dioxide calciner plant and method | |
| CN206454416U (en) | A kind of exhaust treatment system | |
| CN211676943U (en) | Wet flue gas desulfurization white-removing device | |
| CN209263621U (en) | Sulfate process titanium dioxide calcination system | |
| CN211971805U (en) | Zero discharge system for concentrating desulfurization wastewater by flash evaporation with ultralow energy consumption and industrial salt-containing wastewater | |
| CN209997405U (en) | flue gas whitening system for thermal power plant |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination |