CN1467015A - Energy-saving high effective desulfurizing and dust control method and equipment using remaining heat - Google Patents
Energy-saving high effective desulfurizing and dust control method and equipment using remaining heat Download PDFInfo
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- CN1467015A CN1467015A CNA021593477A CN02159347A CN1467015A CN 1467015 A CN1467015 A CN 1467015A CN A021593477 A CNA021593477 A CN A021593477A CN 02159347 A CN02159347 A CN 02159347A CN 1467015 A CN1467015 A CN 1467015A
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- Prior art keywords
- desulfurization
- nozzle
- dedusting
- heat exchanger
- energy
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- 238000000034 method Methods 0.000 title claims abstract description 13
- 230000003009 desulfurizing effect Effects 0.000 title abstract description 6
- 239000000428 dust Substances 0.000 title description 10
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 34
- 230000008602 contraction Effects 0.000 claims abstract description 9
- 238000006477 desulfuration reaction Methods 0.000 claims description 70
- 230000023556 desulfurization Effects 0.000 claims description 69
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims description 31
- 239000003546 flue gas Substances 0.000 claims description 31
- 239000007788 liquid Substances 0.000 claims description 26
- 238000005201 scrubbing Methods 0.000 claims description 13
- 238000000605 extraction Methods 0.000 claims description 9
- 230000000694 effects Effects 0.000 claims description 5
- 239000007789 gas Substances 0.000 claims description 4
- 239000007921 spray Substances 0.000 claims description 4
- 239000003517 fume Substances 0.000 abstract description 4
- 238000010410 dusting Methods 0.000 abstract 3
- 239000002918 waste heat Substances 0.000 description 5
- 238000006243 chemical reaction Methods 0.000 description 4
- 238000005265 energy consumption Methods 0.000 description 2
- 238000002844 melting Methods 0.000 description 2
- 239000000779 smoke Substances 0.000 description 2
- 241000282326 Felis catus Species 0.000 description 1
- 230000002745 absorbent Effects 0.000 description 1
- 239000002250 absorbent Substances 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 238000000889 atomisation Methods 0.000 description 1
- 238000005352 clarification Methods 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000010797 grey water Substances 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 239000002893 slag Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
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Abstract
An energy-saving efficient desulfurizing and dusting method and apparatus using afterheat is disclosed. Said method features that the residual of high-temp fume is used to heat water to become steam, which is then sprayed out at high speed by the nozzle of Venturi tube to provide power for forcing the fume to pass through said apparatus. Said apparatus is composed of Ventiru tube and desulfurizing-dusting tower. In the contraction segment of venturi tube, there are primary heat exchanger, secondary heat exchanger and nozzle. Its advantages are low cost and high efficiency of 90% of desulfurizing and 99.5% for dusting.
Description
Technical field
The present invention relates to a kind of method and device, especially relate to a kind of energy-saving and high efficient desulfurization and dust-removal method and device that utilizes fume afterheat for kiln, boiler fume desulfurizing and dedusting.
Background technology
In the desulfation dust-extraction device of stove and boiler smoke, when desulfurization dust-removing efficiency was had relatively high expectations, the scope of application of Venturi tube was very wide.Venturi tube carrying liqs spray equipment can be used for the flue gas desulfurization and dedusting of various stoves and boiler, the dust-removal and desulfurizing that also can be used for various technical process, have the desulfurization dust-removing efficiency height, the dust granularity of collection is little, investment cost is low, can be used for handling advantages such as sticky dust and combustible dust.But venturi has a very big weakness, and promptly resistance drop is big, and the fall of 500-2000Pa is arranged usually, thereby makes whole desulfurization dust-removal system energy consumption higher.
Chinese patent ZL01214669.2 discloses a kind of high-efficient desulfation dust-extraction device, comprise king-tower, secondary tower, the grey water out of the diversion column of king-tower center, bottom, the Venturi scrubber that joins with king-tower, the king-tower upper end is provided with demister, and the bottom of secondary tower is provided with air outlet.The upper and lower of king-tower is provided with the recirculated water shower nozzle around body of the tower, the middle part is provided with the absorbent shower nozzle along body of the tower, and diversion column is the big down little conical diversion column of, and the cross section of the linkage section of Venturi scrubber and king-tower is the tangent line involute shape.The mode that this utility model adopts Venturi scrubber to be connected in series with the desulfurization and dedusting tower, and pass through to improve the shape in diversion column shape and Venturi scrubber and king-tower linkage section cross section, and the setting of different shower nozzles, improved the desulfurization and dedusting effect of installing.But it is very big that flue gas resistance falls in the setting of the shower nozzle of this Venturi scrubber, needs high-power air-introduced machine that whole system is worked well, and energy consumption is quite big.And the entrained energy of high-temperature flue gas fails to make full use of, and causes waste.
Summary of the invention
The present invention proposes a kind of energy-saving and high efficient desulfurization and dust-removal method of UTILIZATION OF VESIDUAL HEAT IN, in the desulfurization and dust-removal method of Venturi scrubbing device and desulfurization and dedusting tower, introduce energy conversion system, the waste heat of high-temperature flue gas is utilized, be used to overcome the resistance drop of Venturi tube, energy-efficient.
The present invention proposes a kind of energy-saving and high efficient desulfation dust-extraction device of UTILIZATION OF VESIDUAL HEAT IN, the waste heat of high-temperature flue gas is utilized, desulfurization and dedusting liquid recycles, and makes whole device operating cost low, the desulfurization dust-removing efficiency height.
Technical scheme of the present invention is:
A kind of energy-saving and high efficient desulfurization and dust-removal method of UTILIZATION OF VESIDUAL HEAT IN, flue gas carries out desulfurization and dedusting by Venturi scrubbing device, the desulfurization and dedusting tower of serial connection, the Venturi scrubbing device is made up of Venturi tube and nozzle, desulfurization and dedusting liquid sprays by nozzle, and flue gas is heated into steam by heat-exchange system with water before entering the Venturi scrubbing device; Steam enters the nozzle of Venturi scrubbing device, after flue gas carries out preliminary desulfurization and dedusting by the high velocity vapor of nozzle ejection and the desulfurization and dedusting liquid jet turbulence effect by Venturi tube, is driven by steam and to discharge after entering the further desulfurization and dedusting of desulfurization and dedusting tower.
Described heat-exchange system is made up of clear water reserviors, water pump, main heat exchanger, secondary unit; Main heat exchanger and secondary unit are located in the exhaust gases passes, and main heat exchanger enters nozzle after clear water is heated into steam; Secondary unit enters nozzle after desulfurization and dedusting liquid is heated.
Described desulfurization and dedusting liquid is carried by the circulatory system, and the circulatory system is made up of circulating pump, circulating water pool; Circulating water pool is handled using back desulfurization and dedusting liquid in the desulfurization and dedusting tower, and the desulfurization and dedusting liquid of circulating pump after with the processing in the circulating water pool is transported to the desulfurization and dedusting tower and recycles, and another part is transported to nozzle.
A kind of energy-saving and high efficient desulfation dust-extraction device of UTILIZATION OF VESIDUAL HEAT IN, form by Venturi scrubbing device, desulfurization and dedusting tower, the Venturi scrubbing device is made up of Venturi tube and nozzle, Venturi tube is made up of contraction section, mixer and diffuser, be provided with main heat exchanger and nozzle in the contraction section of described Venturi tube, tube inlet is communicated with clear water reserviors by water pump in the described main heat exchanger, and outlet is communicated with nozzle; Nozzle also is provided with pipeline and is communicated with by the circulating water pool of circulating pump with the desulfurization and dedusting tower.
Be provided with supplementary heat exchanger in the contraction section of described Venturi tube, the inlet of pipe links to each other with water circulating pump in the supplementary heat exchanger, and outlet is communicated with nozzle.
The outlet of pipe is communicated with the afterbody of nozzle in the described main heat exchanger, and the outlet of pipe is communicated with the middle part of nozzle in the described supplementary heat exchanger.
Described nozzle is a steam two-phase nozzle, and nozzle is towards consistent with the flow of flue gas direction.
The present invention is made up of energy conversion system, the doctor solution circulatory system, desulfurization and dedusting tower three parts, and energy conversion system enters nozzle after utilizing the waste heat of flue gas that water is heated into steam; The doctor solution circulatory system recycles the desulfurization and dedusting liquid part that the desulfurization and dedusting tower uses, enter nozzle after the waste heat heating of another part by flue gas, the high velocity vapor jet of nozzle ejection provides and has made the power of flue gas by device, and do not need powerful blower fan that energy is provided, overcome the weakness of Venturi tube again when the advantage of Venturi tube is given full play to, and improved the efficiency of dust collection of whole device.
The waste heat that device of the present invention makes full use of flue gas carries out power conversion, and the desulfurization and dedusting liquid that the steam jet that is sprayed at a high speed by nozzle is being carried fully atomizing secretly produces flue gas in Venturi tube highly turbulent, dust in flue gas and SO
2Being desulfurized dedusting liquid fully absorbs and enters follow-up desulfurization and dedusting tower after the after-purification and carry out further desulfurization and dedusting and demist.This device efficiency of dust collection can reach 99.5%, and the capture particle diameter of dust is 1 micron, and desulfuration efficiency can reach 90%.
Description of drawings
Fig. 1 is a structural representation of the present invention.
The specific embodiment
As figure, a kind of energy-saving desulfation dust-extraction device of UTILIZATION OF VESIDUAL HEAT IN, comprise Venturi tube and desulfurization and dedusting tower 1, described Venturi tube is made up of contraction section 6, mixer 5, diffuser 4, be provided with main heat exchanger 7, supplementary heat exchanger 8 and nozzle 9 in the contraction section 5, tube inlet is communicated with clear water reserviors 3 by water pump 2 in the main heat exchanger 7, and outlet is communicated with the afterbody of nozzle 9; The inlet of pipe is connected with the circulating water pool 11 of desulfurization and dedusting tower 1 by water circulating pump 10 in the supplementary heat exchanger 8, and outlet is communicated with the middle part of nozzle 9.
Nozzle 9 is a steam two-phase nozzle, and nozzle is towards consistent with the flow of flue gas direction.
Desulfurization and dedusting tower 1 can be towers such as moisture film, spray column, packed tower, sieve-plate tower, rotating stream tray scrubber.
Clarified water pump 2 is squeezed into the clear water in the clear water reserviors in the main heat exchanger 7, and high-temperature flue gas (200-500 ℃) carries out exchange heat with clear water, evaporates the water, and produces 1-2kg/cm
2The steam of pressure.Steam is transported to the tail end of two-phase nozzle 9 by pipeline, and desulfurization and dedusting liquid is squeezed into the middle part of two-phase nozzle 9 by circulating pump 10 with certain pressure, and steam is by the form ejection of two-phase nozzle 9 with high-speed jet, and meanwhile, nozzle 9 is with desulfurization and dedusting liquid high atomisation.Desulfurization and dedusting liquid and the flue gas of being carried secretly fully atomizing by the steam jet of nozzle 9 high speed ejections enter mixer section 5, and gas speed is the 30-50 meter per second.Reduced jet velocity by a large amount of condensations when preventing that steam from contacting with desulfurization and dedusting liquid in nozzle 9, desulfurization and dedusting liquid earlier heats (80-90 ℃) through auxiliary heater 8 before entering nozzle 9, flue gas with desulfurization and dedusting liquid during at a high speed by mixer section 5 the cross-flow effect of generation flue gas and highly turbulent flow make dust in flue gas and SO
2Being desulfurized dedusting liquid fully absorbs.The flue gas that fully mixes with desulfurization and dedusting liquid and be purified slows down by diffuser 4 and enters follow-up desulfurization and dedusting tower 1 after recovering energy and carry out further desulfurization and dedusting and demist, clean flue gas is discharged by cat head, desulfurization and dedusting liquid is back to circulatory pool 11 at the bottom of by tower, through adding alkali, clarification back reuse, desulfurization and dedusting liquid is realized closed cycle, and desulfurization slag and dust deposit the back and be used to repair the roads and brickmaking with grabbing bucket to grab out in circulatory pool 11.
For smoke evacuation tolerance is 50000M
3The down-draft kiln flue gas of/H, flue-gas temperature is 500 ℃, handles the blower fan that needs to be equipped with 55KW with common venturi and can make the dust-removing desulfurizing device operation normal, and flue gas reaches discharge standard, outfit apparatus of the present invention only need be equipped with the 22KW blower fan and just can reach desulfurization and dedusting effect preferably, flue gas qualified discharge.
The present invention can be widely used in exhaust gas temperature and be higher than 250 ℃ various industrial furnaces as down-draft kiln, tunnel cave, glass-melting furnace, Metal Melting furnace etc.
Claims (7)
1. the energy-saving and high efficient desulfurization and dust-removal method of a UTILIZATION OF VESIDUAL HEAT IN, flue gas carries out desulfurization and dedusting by Venturi scrubbing device, the desulfurization and dedusting tower of serial connection, the Venturi scrubbing device is made up of Venturi tube and nozzle, desulfurization and dedusting liquid sprays by nozzle, it is characterized in that: flue gas is heated into steam by heat-exchange system with water before entering the Venturi scrubbing device; Steam enters the nozzle of Venturi scrubbing device, after flue gas carries out preliminary desulfurization and dedusting by the high velocity vapor of nozzle ejection and the desulfurization and dedusting liquid jet turbulence effect by Venturi tube, is driven by steam and to discharge after entering the further desulfurization and dedusting of desulfurization and dedusting tower.
2. the energy-saving and high efficient desulfurization and dust-removal method of a kind of UTILIZATION OF VESIDUAL HEAT IN according to claim 1, it is characterized in that: described heat-exchange system is made up of clear water reserviors, water pump, main heat exchanger, secondary unit; Main heat exchanger and secondary unit are located in the exhaust gases passes, and main heat exchanger enters nozzle after clear water is heated into steam; Secondary unit enters nozzle after desulfurization and dedusting liquid is heated.
3. the energy-saving and high efficient desulfurization and dust-removal method of a kind of UTILIZATION OF VESIDUAL HEAT IN according to claim 1, it is characterized in that: described desulfurization and dedusting liquid is carried by the circulatory system, and the circulatory system is made up of circulating pump, circulating water pool; Circulating water pool is handled using back desulfurization and dedusting liquid in the desulfurization and dedusting tower, and the desulfurization and dedusting liquid of circulating pump after with the processing in the circulating water pool is transported to the desulfurization and dedusting tower and recycles, and another part is transported to nozzle.
4. the energy-saving and high efficient desulfation dust-extraction device of a UTILIZATION OF VESIDUAL HEAT IN, form by Venturi scrubbing device, desulfurization and dedusting tower, the Venturi scrubbing device is made up of Venturi tube and nozzle (9), Venturi tube is made up of contraction section (6), mixer (5) and diffuser (4), it is characterized in that: be provided with main heat exchanger (7) and nozzle (9) in the contraction section of described Venturi tube (6), the interior tube inlet of described main heat exchanger (7) is communicated with clear water reserviors (3) by water pump (2), and outlet is communicated with nozzle (9); Nozzle (9) also is provided with pipeline and is communicated with the circulating water pool (11) of desulfurization and dedusting tower (1) by circulating pump (10).
5. the energy-saving and high efficient desulfation dust-extraction device of a kind of UTILIZATION OF VESIDUAL HEAT IN according to claim 4, it is characterized in that: be provided with supplementary heat exchanger (8) in the contraction section of described Venturi tube (6), the inlet of the interior pipe of supplementary heat exchanger (8) links to each other with water circulating pump (10), and outlet is communicated with nozzle (9).
6. the energy-saving and high efficient desulfation dust-extraction device of a kind of UTILIZATION OF VESIDUAL HEAT IN according to claim 4, it is characterized in that: the outlet of the interior pipe of described main heat exchanger (7) and nozzle (9)) afterbody be communicated with, the outlet of the interior pipe of described supplementary heat exchanger (8) is communicated with the middle part of nozzle (9).
7. the energy-saving and high efficient desulfation dust-extraction device of a kind of UTILIZATION OF VESIDUAL HEAT IN according to claim 4, it is characterized in that: described nozzle (9) is a steam two-phase nozzle, and nozzle (9) is towards consistent with the flow of flue gas direction.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 02159347 CN1218771C (en) | 2002-12-23 | 2002-12-23 | Energy-saving high effective desulfurizing and dust control method and equipment using remaining heat |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 02159347 CN1218771C (en) | 2002-12-23 | 2002-12-23 | Energy-saving high effective desulfurizing and dust control method and equipment using remaining heat |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1467015A true CN1467015A (en) | 2004-01-14 |
| CN1218771C CN1218771C (en) | 2005-09-14 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 02159347 Expired - Fee Related CN1218771C (en) | 2002-12-23 | 2002-12-23 | Energy-saving high effective desulfurizing and dust control method and equipment using remaining heat |
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| CN (1) | CN1218771C (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100398185C (en) * | 2005-10-24 | 2008-07-02 | 温州市双屿防腐设备制造公司 | Wet fume purifier |
| CN108479273A (en) * | 2018-06-11 | 2018-09-04 | 兰州大学 | Cleaner and dust pelletizing system |
| CN109908730A (en) * | 2019-03-22 | 2019-06-21 | 刘振 | A kind of glass reinforced plastic desulfurization tower to be removed the gred using waste heat power |
| CN109985499A (en) * | 2019-04-16 | 2019-07-09 | 程琛 | A kind of desulfurization oxidized input air intelligent Matching method and system |
| CN111151106A (en) * | 2018-11-07 | 2020-05-15 | 洛阳德明石化设备有限公司 | System for improving gas-liquid separation effect of WGS (WGS) desulfurizing tower and application of system |
-
2002
- 2002-12-23 CN CN 02159347 patent/CN1218771C/en not_active Expired - Fee Related
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100398185C (en) * | 2005-10-24 | 2008-07-02 | 温州市双屿防腐设备制造公司 | Wet fume purifier |
| CN108479273A (en) * | 2018-06-11 | 2018-09-04 | 兰州大学 | Cleaner and dust pelletizing system |
| CN111151106A (en) * | 2018-11-07 | 2020-05-15 | 洛阳德明石化设备有限公司 | System for improving gas-liquid separation effect of WGS (WGS) desulfurizing tower and application of system |
| CN109908730A (en) * | 2019-03-22 | 2019-06-21 | 刘振 | A kind of glass reinforced plastic desulfurization tower to be removed the gred using waste heat power |
| CN109985499A (en) * | 2019-04-16 | 2019-07-09 | 程琛 | A kind of desulfurization oxidized input air intelligent Matching method and system |
| CN109985499B (en) * | 2019-04-16 | 2024-02-23 | 程琛 | Intelligent matching method and system for desulfurization and oxidation air quantity |
Also Published As
| Publication number | Publication date |
|---|---|
| CN1218771C (en) | 2005-09-14 |
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