CN204637929U - A kind of compound lector desulphurization plant - Google Patents
A kind of compound lector desulphurization plant Download PDFInfo
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- CN204637929U CN204637929U CN201520309834.0U CN201520309834U CN204637929U CN 204637929 U CN204637929 U CN 204637929U CN 201520309834 U CN201520309834 U CN 201520309834U CN 204637929 U CN204637929 U CN 204637929U
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- ring
- impact head
- desulphurization plant
- lector
- admission line
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Abstract
The utility model relates to a kind of compound lector desulphurization plant, is distributed ring, packing layer, shower, dehydrator, gas-distribution pipe of giving vent to anger, gas outlet and admission line formed by air inlet, anti-clogging water inlet pipe, impact head, secondary pulse ring, ascending air.Described air inlet and anti-clogging water inlet pipe are placed in the top on impact head top respectively, impact head is located at the lower end of admission line, secondary pulse is located on the periphery of impact head, ascending air distributes the top that ring is positioned at impact head and secondary pulse ring, packing layer, shower and dehydrator is provided with successively above ascending air distribution ring, gas-distribution pipe of giving vent to anger is connected with gas outlet, and admission line is that vertical direction is placed.This equipment runnability is stable and cost is low, simple to operate, long service life, has good economic results in society.
Description
Technical field
The utility model relates to a kind of compound lector desulphurization plant, belongs to dust, fume purification techniques field.
Background technology
China's State of Air pollution is on the rise, and be with in Jing-jin-ji region, the Yangtze River Delta, Pearl River Delta one especially, haze pollution problem is especially outstanding, and atmosphere polluting problem has become the key factor of restriction socio-economic development.SO
2, NO
x, VOCs, NH
3, fine particle etc. is the priority pollutant causing haze to pollute, and SO
2it is the Main Factors causing Acid Rain Pollution phenomenon.The industries such as metallurgy, oil, chemical industry, iron and steel, building materials, electric power are the important sources of dust, flue dust and smoke pollution, research and develop novel dust removing desulphurization plant, contribute to from Sources controlling atmosphere pollution, reduce the discharge capacity of industrial pollutants.
Flue gas desulfurization technique has wet method, dry method, half wet process three kinds, and wet desulphurization makes flue gas and chemical liquid react or utilizes physical support to absorb flue gas, reaches reduce SO with this
2object.Wet desulphurization equipment develops into the various new equipment such as packed tower, spray Sieve plates, spray high speed tower, liquid column tower, bubble tower from initial spray column.Ammonia type flue gas desulfurizing technology is the flue gas desulfurization technique of comparative maturity, and lime stone-gypsum sulfur removal technology is Application comparison technique early in desulfur technology.Wet desulphurization reaction speed is fast, absorption efficiency is high, therefore becomes the sulfur removal technology be most widely used.
Dedusting technology comprises mechanical type dedusting, inertial dust collection, electric precipitation, wet dust removal, filtering type dedusting etc.Sack cleaner is subject to the impact of flue-gas temperature, humidity etc., needs to regularly replace cloth bag, adds cost.Once have a cloth bag to damage will shut down replacing in hundreds and thousands of cloth bags, and the cloth bag will finding out damage in numerous cloth bags neither an easy thing.In addition, due to the difference of the situation such as temperature, water content of flue gas, higher requirement is proposed to the material of filter cloth.Although there is the filter cloth of some New Type Material, filtrate in recent years, bring no small financial burden because operating cost is high to enterprise.The dry dedusting technology such as bag-type dust, electric precipitation can not solve the desulphurization problem of flue gas, also must install wet type desulfurizing equipment in rear end.
Current dedusting technology is just towards following future development: (1) is studied more adding system to traditional dedusting technology and goed deep into; (2) high efficiency of dedusting technology, global function, low cost and stable operation is required; (3) focus on the coupling of various dedusting technology, make dedusting and desulphurization integrated.Day by day tightening up of discharge standard requires that the development of dedusting technology is more strict to equipment, researches and develops novel integration dust-removing desulphurization plant for raising efficiency of dust collection, reduces discharging SO
2be even more important.
Chinese patent CN2796810Y discloses a kind of wet dust desulfurization equipment, this equipment has spray column and catches a tower formation, by boiling-house, two towers are connected, the techniques such as spray, impact, flue gas even distribution, bubble absorption are completely newly combined, reaches the object of dust-removal and desulfurizing.
China CN201543367U discloses a kind of Wet smoke dust-removing desulfurating apparatus, this device integrates eddy flow water film dedusting, impacts dedusting, foam absorbing, hollow-spraying-tower technology, be combined the technical scheme forming complex control system by absorption tower with outer cylinder body, reach good dust-removal and desulfurizing effect equally.
China CN201719948U discloses a kind of smoke dust-removing equipment, this equipment is made up of the smoke-intake pipe connected in turn, numb stone cylindrical shell and smoke exhaust pipe, spray equipment is provided with at the air inlet of smoke-intake pipe, this device effectively can reduce particle in boiler emission flue gas and content of sulfur dioxide, makes fume emission up to standard.
More than the equipment described in invention all can effectively to clarifying smoke, but complex structure, the improvement in the textural shortage details of equipment, the complementary energy of the impact process related to is not fully used, and causes the loss of energy.This external equipment runs, the cost of management process lacks estimation, has no utilization example.
Summary of the invention
The utility model object is to provide a kind of compound lector desulphurization plant.
In order to solve the problem, this utility model is achieved through the following technical solutions.
Compound lector desulphurization plant, it is characterized in that: compound lector desulphurization plant is distributed ring (5), packing layer (6), shower (7), dehydrator (8), gas-distribution pipe of giving vent to anger (9), gas outlet (10) and admission line (11) formed by dedusting and desulfurizing tower, air inlet (1), anti-clogging water inlet pipe (2), impact head (3), secondary pulse ring (4), ascending air, and wherein admission line (11) vertical direction is placed in dust removing desulphurization plant, the outlet of admission line (11) is positioned under the liquid level of dust removing desulphurization plant inside, anti-clogging water inlet pipe (2) is positioned at admission line (11) bosom position, impact head (3) is contained in the inside in admission line (11) exit, the top of impact head (3) is the water outlet of admission line (11), secondary pulse ring (4) is located at the outside that admission line (11) exports, ascending air distributes the top that ring (5) is positioned at impact head (3) and secondary pulse ring (4), ascending air distributes ring (5) top and is provided with packing layer (6) successively, shower (7) and dehydrator (8), gas-distribution pipe (9) of giving vent to anger is positioned at shower (7) top, be connected with gas outlet (10), gas outlet (10) is positioned at the sidepiece of lector desulphurization plant.
Described impact head (3) flare, the port of export of anti-clogging water inlet pipe (2) is positioned at the center position on impact head (3) top.
Described secondary pulse ring (4) is arranged on dust removing desulphurization plant inner wall lower, and secondary pulse ring (4) entirety is in coniform, then have a large circle and small circle ring, the outlet of impact head (3) is placed on secondary pulse ring (4) small circle ring bottom.
Described shower (7) is evenly distributed with several spray nozzle.
Under described packing layer (6) is arranged on shower (7), place with the form spreading heap at random.
It is multiple up big and down small loudspeaker circle permutation that described ascending air distributes ring (5), is arranged on the top of secondary pulse ring (4).
operation principle: admission line (11) to be placed in dust removing desulphurization plant and to place in vertical, waste gas is introduced into admission line (11) from air inlet (1), impact head (3) ejection under liquid level is positioned at again from admission line (11) bottom, waste gas is blocked by tubaeform impact head (3) in admission line (11) exit, move downward along periphery, because the bottom of impact head (3) is horn-like, so the bottom of impact head (3) and admission line (11) exit inwall are in the state of gradually shrinking, waste gas movement velocity is accelerated, finally be sprayed onto the water that compound lector desulphurization plant inner lower is equipped with (or in absorbing liquid) equably from admission line (11) outlet surrounding, form strong turbulent flow after the fast waste gas of jet velocity contacts with water to impact, by in waste gas with dust (flue dust), the materials such as sulfur dioxide carry out first time and catch, absorb.
Owing to being provided with the secondary pulse ring (4) of ring-type at compound lector desulphurization plant inner wall lower, secondary pulse ring (4) is positioned at again the outside that admission line (11) exports, and on the water surface, off-gas flows after first time impacts rises on liquid (water) face, again blocked by secondary pulse ring (4), in the space left between liquid (water) face and secondary pulse ring (4), off-gas flows again forms secondary rotating and impacts, carry out second time to catch, absorb the dust (flue dust) in waste gas and sulfur dioxide, obtain the technique effect of twice composite impact.
What off-gas flows flow to top through tubaeform impact head (3) and secondary pulse ring (4) small circle ring indentation, there again rises distribution of air flow ring (5) parts place, ascending air distributes ring (5) and is uniformly distributed by the off-gas flows flowed through, liquid film on rising off-gas flows and packing layer (6) collides, be again captured and absorption after CONTACT WITH FRICTION, absorb the dust (flue dust) in waste gas and sulfur dioxide further, last waste gas flows out equipment from gas outlet (10) after the guiding of gas-distribution pipe of giving vent to anger (9), completes dust-removal and desulfurizing process.
The water that anti-clogging water inlet pipe (2) flows out flows directly to impact head (3) top, water flows down from impact head (3) top to surrounding equably, allow the dust (flue dust) sticking to impact head (3) wall flow into equipment bottom liquid (water) face with water, thus the opening part that the bottom of guarantee impact head (3) and admission line (11) outlet inside wall are collapsed shape gradually can not be blocked by dust (flue dust).
The utility model equipment runnability is stable, cost is low, simple to operate, long service life, has good economic results in society.
Accompanying drawing explanation
Fig. 1 is the structural representation of compound lector desulphurization plant.
Number in the figure: 1-air inlet; 2-anti-clogging water inlet pipe; 3-impact head; 4-secondary pulse ring; 5-ascending air distributes ring; 6-packing layer; 7-shower; 8-dehydrator; 9-gas-distribution pipe of giving vent to anger; 10-gas outlet; 11-admission line.
Detailed description of the invention
The compound lector desulphurization plant of the utility model is by air inlet 1, anti-clogging water inlet pipe 2, impact head 3, secondary pulse ring 4, ascending air distributes ring 5, packing layer 6, shower 7, dehydrator 8, to give vent to anger gas-distribution pipe 9, gas outlet 10 and admission line 11 form, described air inlet 1 and anti-clogging water inlet pipe 2 are placed in the left and right sides on impact head 3 top respectively, impact head 3 is located at the lower end of pipeline 11, secondary pulse ring 4 is located at the periphery of impact head 3, ascending air distributes the top that ring 5 is positioned at impact head 3 and secondary pulse ring 4, packing layer 6 is provided with successively above ascending air distribution ring 5, shower 7 and dehydrator 8, to give vent to anger gas-distribution pipe 9 and gas outlet 10, admission line 11 is placed in the middle part of compound lector desulphurization plant, and be vertical direction placement.
Further, the port of export of described anti-clogging water inlet pipe 2 is positioned at the center position at impact head 3 top, and impact head 3 is tubaeform.
Concrete, described shower 7 is evenly distributed with spray nozzle.
Be illustrated in figure 1 whole compound lector desulphurization plant.Waste gas is from being positioned at the ejection of tubaeform impact head 3 exit, spout is positioned under liquid level water, the waste gas of spurting and liquid level water form strong first time turbulent flow and impact, by waste gas with dust (flue dust) and flue gas in sulfur dioxide carry out first time seizure, absorption; The air-flow impacted forms second time rotary impact again at secondary pulse ring 4 place, carry out the dust (flue dust) in second time seizure, absorption waste gas and sulfur dioxide; Catch and from top to bottom form liquid film on packing layer 6 surface with absorbing liquid, the rising off-gas flows of leading the way through ascending air distribution ring 5 and the filler of packing layer 6 collide, rub, again catch, absorb the dust (flue dust) in waste gas and sulfur dioxide, complete dust-removal and desulfurizing work.
This equipment runnability is stable and cost is low, simple to operate, long service life, has good economic results in society.
Claims (6)
1. a compound lector desulphurization plant, it is characterized in that: compound lector desulphurization plant is distributed ring (5), packing layer (6), shower (7), dehydrator (8), gas-distribution pipe of giving vent to anger (9), gas outlet (10) and admission line (11) formed by dedusting and desulfurizing tower, air inlet (1), anti-clogging water inlet pipe (2), impact head (3), secondary pulse ring (4), ascending air, and wherein admission line (11) vertical direction is placed in dust removing desulphurization plant, the outlet of admission line (11) is positioned under the liquid level of dust removing desulphurization plant inside, anti-clogging water inlet pipe (2) is positioned at admission line (11) bosom position, impact head (3) is contained in the inside in admission line (11) exit, the top of impact head (3) is the water outlet of admission line (11), secondary pulse ring (4) is located at the outside that admission line (11) exports, ascending air distributes the top that ring (5) is positioned at impact head (3) and secondary pulse ring (4), ascending air distributes ring (5) top and is provided with packing layer (6) successively, shower (7) and dehydrator (8), gas-distribution pipe (9) of giving vent to anger is positioned at shower (7) top, be connected with gas outlet (10), gas outlet (10) is positioned at the sidepiece of lector desulphurization plant.
2. compound lector desulphurization plant according to claim 1, is characterized in that: described impact head (3) flare, the port of export of anti-clogging water inlet pipe (2) is positioned at the center position on impact head (3) top.
3. compound lector desulphurization plant according to claim 1, it is characterized in that: described secondary pulse ring (4) is arranged on dust removing desulphurization plant inner wall lower, secondary pulse ring (4) entirety is in coniform, then have a large circle and small circle ring, the outlet of impact head (3) is placed on secondary pulse ring (4) small circle ring bottom.
4. compound lector desulphurization plant according to claim 1, is characterized in that: described shower (7) is evenly distributed with several spray nozzle.
5. compound lector desulphurization plant according to claim 1, is characterized in that: under described packing layer (6) is arranged on shower (7), places with the form spreading heap at random.
6. compound lector desulphurization plant according to claim 1, is characterized in that: it is multiple up big and down small loudspeaker circle permutation that described ascending air distributes ring (5), is arranged on the top of secondary pulse ring (4).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520309834.0U CN204637929U (en) | 2015-05-14 | 2015-05-14 | A kind of compound lector desulphurization plant |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520309834.0U CN204637929U (en) | 2015-05-14 | 2015-05-14 | A kind of compound lector desulphurization plant |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204637929U true CN204637929U (en) | 2015-09-16 |
Family
ID=54090706
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520309834.0U Expired - Fee Related CN204637929U (en) | 2015-05-14 | 2015-05-14 | A kind of compound lector desulphurization plant |
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| CN (1) | CN204637929U (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107308813A (en) * | 2017-08-09 | 2017-11-03 | 成都中祥天宇环保科技有限公司 | A kind of desulfurizing tower of radial direction circulation flue gas |
| TWI622736B (en) * | 2016-10-25 | 2018-05-01 | Lin Cheng Wu | Unpowered oil smoke dust odor separator |
| TWI623714B (en) * | 2016-07-14 | 2018-05-11 | 林成武 | System structure of laminated injection and filtering |
| CN108709654A (en) * | 2018-07-26 | 2018-10-26 | 深圳市亚派光电器件有限公司 | Temperature testing device |
| CN114504915A (en) * | 2022-02-07 | 2022-05-17 | 山东瑞龙环保科技有限公司 | Ultralow-emission efficient wet dust removal system and process |
-
2015
- 2015-05-14 CN CN201520309834.0U patent/CN204637929U/en not_active Expired - Fee Related
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| TWI623714B (en) * | 2016-07-14 | 2018-05-11 | 林成武 | System structure of laminated injection and filtering |
| TWI622736B (en) * | 2016-10-25 | 2018-05-01 | Lin Cheng Wu | Unpowered oil smoke dust odor separator |
| CN107308813A (en) * | 2017-08-09 | 2017-11-03 | 成都中祥天宇环保科技有限公司 | A kind of desulfurizing tower of radial direction circulation flue gas |
| CN108709654A (en) * | 2018-07-26 | 2018-10-26 | 深圳市亚派光电器件有限公司 | Temperature testing device |
| CN108709654B (en) * | 2018-07-26 | 2024-01-16 | 深圳市亚派光电器件有限公司 | Temperature testing device |
| CN114504915A (en) * | 2022-02-07 | 2022-05-17 | 山东瑞龙环保科技有限公司 | Ultralow-emission efficient wet dust removal system and process |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20150916 Termination date: 20210514 |