CN205055802U - Advection is compound desulfurization absorption tower against current - Google Patents

Advection is compound desulfurization absorption tower against current Download PDF

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Publication number
CN205055802U
CN205055802U CN201520663531.9U CN201520663531U CN205055802U CN 205055802 U CN205055802 U CN 205055802U CN 201520663531 U CN201520663531 U CN 201520663531U CN 205055802 U CN205055802 U CN 205055802U
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China
Prior art keywords
tower body
advection
flue gas
pipeline
spraying layer
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CN201520663531.9U
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Chinese (zh)
Inventor
孙长年
周万云
徐忠俊
刘船
周广东
聂岸亮
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Jiangsu selon energy saving technology Engineering Co., Ltd
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YANCHENG SAILONG ENERGY-SAVING TECHNOLOGY ENGINEERING Co Ltd
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Abstract

The utility model relates to an advection is compound desulfurization absorption tower against current, it includes: the tower body, the tower body lower part is equipped with holds the dressing trough, seted up on the lateral wall of tower body with hold the corresponding air duct that is used for leading -in flue gas of dressing trough, an at least a set of spray assembly, a spray assembly is including installing just be located in the tower body the first layer that sprays of air duct top, first spray the layer to spray the direction opposite with flue gas flow direction, at least two a set of spray assembly, the 2nd spray assembly includes vertical the installation the air duct is interior just dorsad the second of tower body sprays the layer. Flue gas leading -in like this can contact with the liquid phase of holding in the dressing trough, is favorable to reduceing the velocity of flow of flue gas, plays the effect of stationary flow, cooling, improvement desulfurization efficiency, still the enough feasible liquid that sprays fully contacts with the flue gas, can reduce the liquid -gas ratio when guaranteeing desulfurization efficiency, practices thrift desulfurization system's the working costs and the investment of equipment.

Description

Advection adverse current composite desulfate absorption tower
Technical field
The utility model relates to a kind of absorption tower, is specifically related to a kind of advection adverse current composite desulfate absorption tower.
Background technology
Coal-burning boiler is exactly fuel is coal-fired boiler, refers to through fire coal combustion heat release amount in burner hearth, heat medium water or other organic heat carrier (as heat conduction wet goods) is heated to the thermal powerplant of uniform temperature (or pressure).In coal-burning boiler, the heat of coal is after transforming, and produce steam or become hot water, but not all heat all effectively transforms, some reactive power consumption, so just exists efficiency, and general larger boiler efficiency is high, between 60% ~ 80%.
During boiler operatiopn; sometimes higher, load becomes large to exit gas temperature, exhaust gas volumn is higher, fire coal species changes, the more high factor of sulfur content in coal rate usually can cause flue gas flow rate very fast; the time of staying of flue gas in tower is shorter, sulfur dioxide concentration discharge beyond standards in exiting flue gas.At present, conventional desulfur technology is exhaust gas desulfurization, is about to the sulfur-containing smoke gas of discharge or waste gas passes into absorbent and adsorbent removes oxysulfide, therefore needs the absorption tower can carrying out desulfurization.
Summary of the invention
The utility model object provides a kind of advection adverse current composite desulfate absorption tower to overcome the deficiencies in the prior art.
For achieving the above object, the technical solution adopted in the utility model is: a kind of advection adverse current composite desulfate absorption tower, and it comprises:
Tower body, described tower body bottom is provided with holds stock tank, the sidewall of described tower body offers and holds the corresponding wireway for importing flue gas of stock tank with described;
At least one group of the first spray assemblies, described first spray assemblies comprises and being arranged in described tower body and the first spraying layer be positioned at above described wireway, and the spray direction of described first spraying layer is contrary with flow of flue gas direction;
At least one group of the second spray assemblies, described second spray assemblies comprises and being vertically arranged in described wireway and the second spraying layer of described tower body dorsad.
Optimally, described wireway comprises and being arranged on described tower body sidewall and coupled the first logical pipeline and be arranged on described first pipeline outer end and coupled logical second pipe, described second spraying layer is arranged in described first pipeline, and the upper wall of described first pipeline and all downward-sloping and slope of its upper wall of lower wall are less than the slope of its lower wall.
Further, the junction of described first pipeline lower wall and described second pipe is fixed with the deflector extended to described tower body direction, and described deflector is inclined upwardly setting.
Optimally, described tower body top is provided with coupledly logical leads smoke pipe, described in lead smoke pipe cross-sectional area be less than the cross-sectional area of described tower body; Described leading between smoke pipe and described tower body is connected with cone.
Optimally, described first spray assemblies also comprises and described the first serum recycle pipeline held the first elevator pump that stock tank is connected, be connected with described first spraying layer with described first elevator pump.
Optimally: described second spray assemblies also comprises and described the second serum recycle pipeline held the second elevator pump that stock tank is connected, be connected with described second spraying layer with described second elevator pump.
Optimally, described tower body inwall is provided with the guide ring being positioned at and matching below described first spraying layer and with it.
Because technique scheme is used, the utility model compared with prior art has following advantages: the utility model advection adverse current composite desulfate absorption tower, arrange in tower body bottom on the one hand and hold stock tank, and on the sidewall of tower body, offer the wireway corresponding with holding stock tank, the flue gas of such importing can contact with the liquid held in stock tank, be conducive to the flow velocity lowering flue gas, play the effect of current stabilization, cooling, raising desulfuration efficiency; The spray direction of the first spraying layer is contrary with flow of flue gas direction on the other hand, and the second spraying layer of tower body is dorsad set in wireway, spray liquid can be made so fully to contact with flue gas, can liquid-gas ratio be reduced while guarantee desulfuration efficiency, save the operating cost of desulphurization system and the investment of equipment.
Accompanying drawing explanation
Accompanying drawing 1 is the structural representation on the utility model advection adverse current composite desulfate absorption tower;
Wherein, 1, tower body; 11, stock tank is held; 12, wireway; 121, the first pipeline; 1211, upper wall; 1212, lower wall; 122, second pipe; 2, the first spray assemblies; 21, the first elevator pump; 22, the first serum recycle pipeline; 23, the first spraying layer; 3, the second spray assemblies; 31, the second elevator pump; 32, the second serum recycle pipeline; 33, the second spraying layer; 4, deflector; 5, cone; 6, smoke pipe is led; 7, guide ring.
Detailed description of the invention
Below in conjunction with embodiment shown in the drawings, the utility model is further described.
Below about in the definition in direction, all defined according to direction viewed in Fig. 1.
Advection adverse current composite desulfate absorption tower as shown in Figure 1, mainly comprises tower body 1, first spray assemblies 2 and the second spray assemblies 3.
Wherein, tower body 1 is divided into bottom, middle part and top from bottom to top, and its bottom is provided with holds stock tank 11, for depositing and storing spray liquid; Its middle part or/and bottom sidewall on offer wireway 12, for introducing the flue gas containing sulfur dioxide in tower body 1; It is also corresponding with holding stock tank 11, and the flue gas imported like this can import to be held in stock tank 11, and flue gas can be contacted with the liquid held in stock tank 11, is conducive to the flow velocity lowering flue gas, plays the effect of current stabilization, cooling, raising desulfuration efficiency.First spray assemblies 2 has one group at least, often organizes the first spray assemblies 2 and comprises and to be arranged in tower body 1 and to be positioned at the spray direction of the first spraying layer 23, first spraying layer 23 above wireway 12 contrary with flow of flue gas direction; Same, the second spray assemblies 3 also has one group at least, often organizes the second spray assemblies 3 and comprises and being vertically arranged in wireway 12 and the second spraying layer 33 of tower body 1 dorsad; Second spray assemblies 3 is first to flue gas cool-down, and wash with the sulfur dioxide haptoreaction in flue gas, scrubbing CO_2, the desulphurization reaction time of this second spray assemblies 3 prolong smoke is about 1s, and flue-gas temperature drops to about 80 DEG C, desulfuration efficiency about 40 ~ 50% simultaneously; Reacted low temperature and containing the flue gas of low-concentration sulfur dioxide enter tower body 1 and the first spraying layer 23 spray under the further haptoreaction of slurries, remove the sulfur dioxide in flue gas, final qualified discharge, achieve the object of advection and the absorption of adverse current composite desulfate like this, its desulfuration efficiency reaches more than 99.9%, lower liquid-gas ratio can be adopted while guarantee desulfuration efficiency, the investment of operating cost and equipment can be reduced.
In the present embodiment, wireway 12 comprises the first pipeline 121 and second pipe 122 that are connected; First pipeline 121 is arranged on tower body 1 sidewall, and is connected with tower body 1; Second pipe 122 correspondences are arranged on the outer end of the first pipeline 121, and are connected with the first pipeline 121, and now the second spraying layer 33 is arranged in the first pipeline 121.The cross sectional shape of the first pipeline 121 generally adopts circular or square regular shape, now can define its partial sidewall be positioned at above is upper wall 1211, and the partial sidewall be positioned at above is lower wall 1212, upper wall 1211 and all downward-sloping setting of lower wall 1212, the end that the end that namely they contact with second pipe 122 contacts with tower body 1 higher than it; And the slope of upper wall 1211 is less than the slope of lower wall 1212, and (namely the smoke inlet area of section of the first pipeline 121 is less than its exhanst gas outlet area of section, or first the area that contacts with second pipe 122 of pipeline 121 be less than its area contacted with tower body 1), the flue gas imported through wireway 12 like this forms the trend of carrying down under the stop of upper wall 1211, and hold the slurries liquid level stored in stock tank 11 and extend to and do not have part lower wall 1212, thus make flue gas and slurry liquid contacts more abundant, reduce further the temperature of flue gas, improve desulfuration efficiency.The cross sectional shape of second pipe 122 is also circular or square regular shape, and in the present embodiment, it is horizontally disposed with and bore is even.
In the present embodiment, the lower wall 1212 of the first pipeline 121 and the junction of second pipe 122 are fixed with the deflector 4 extended to tower body 1 direction, this deflector 4 is inclined upwardly setting, namely deflector 4 is tilted to extend by the direction of its upper wall 1211 on the lower wall 1212 of the first pipeline 121, thus flue gas is guided to the second spraying layer 33 place, make flue gas and the abundant haptoreaction of spray liquid, improve the efficiency of desulfurization.The top of tower body 1 is provided with coupledly logical leads smoke pipe 6, the cross-sectional area of leading smoke pipe 6 is less than the cross-sectional area of tower body 1, lead the cone 5 that must be connected with between smoke pipe 6 and tower body 1 and play cushioning effect like this, make flue gas be trapped in tower body 1 to a certain extent, the spray liquid fully sprayed with the first spraying layer 23 reacts.
In the present embodiment, first spray assemblies 2 has three groups, they to be arranged in tower body 1 and to set gradually from bottom to top, often organize the first spray assemblies 2 also to comprise and the first serum recycle pipeline 22 holding the first elevator pump 21 that stock tank 11 is connected, be connected with the first spraying layer 23 with the first elevator pump 21, thus realize recycling of spray liquid, reduce costs.Second spray assemblies then has two groups, often organizes the second spray assemblies 3 and also comprises and the second serum recycle pipeline 32 holding the second elevator pump 31 that stock tank 11 is connected, be connected with the second spraying layer 33 with the second elevator pump 31, also achieve recycling of spray liquid.The inwall of tower body 1 is provided with many group guide rings 7, the quantity of its quantity and the first spraying layer 23 always, they respectively correspondence be arranged on the below of the first spraying layer 23 and match in it, improve desulfuration efficiency further.
Above-described embodiment, only for technical conceive of the present utility model and feature are described, its object is to person skilled in the art can be understood content of the present utility model and implement according to this, can not limit protection domain of the present utility model with this.All equivalences done according to the utility model Spirit Essence change or modify, and all should be encompassed within protection domain of the present utility model.

Claims (7)

1. an advection adverse current composite desulfate absorption tower, it is characterized in that, it comprises:
Tower body (1), described tower body (1) bottom is provided with holds stock tank (11), the sidewall of described tower body (1) offers and holds the corresponding wireway (12) for importing flue gas of stock tank (11) with described;
At least one group of the first spray assemblies (2), described first spray assemblies (2) comprises and is arranged in described tower body (1) and is positioned at first spraying layer (23) of described wireway (12) top, and the spray direction of described first spraying layer (23) is contrary with flow of flue gas direction;
At least one group of the second spray assemblies (3), described second spray assemblies (3) comprises and being vertically arranged in described wireway (12) and second spraying layer (33) of described tower body (1) dorsad.
2. advection adverse current composite desulfate absorption tower according to claim 1, it is characterized in that: described wireway (12) comprises and being arranged on described tower body (1) sidewall and coupled logical the first pipeline (121) and be arranged on described first pipeline (121) outer end and coupled logical second pipe (122), described second spraying layer (33) is arranged in described first pipeline (121), the upper wall (1211) of described first pipeline (121) and all downward-sloping and slope that is its upper wall (1211) of lower wall (1212) are less than the slope of its lower wall (1212).
3. advection adverse current composite desulfate absorption tower according to claim 2, it is characterized in that: the junction of described first pipeline (121) lower wall (1212) and described second pipe (122) is fixed with the deflector (4) extended to described tower body (1) direction, described deflector (4) is inclined upwardly setting.
4. advection adverse current composite desulfate absorption tower according to claim 1, it is characterized in that: described tower body (1) top is provided with coupledly logical leads smoke pipe (6), described in lead smoke pipe (6) cross-sectional area be less than the cross-sectional area of described tower body (1); Described leading between smoke pipe (6) and described tower body (1) is connected with cone (5).
5. advection adverse current composite desulfate absorption tower according to claim 1, is characterized in that: described first spray assemblies (2) also comprises and described the first serum recycle pipeline (22) held the first elevator pump (21) that stock tank (11) is connected, be connected with described first spraying layer (23) with described first elevator pump (21).
6. advection adverse current composite desulfate absorption tower according to claim 1, is characterized in that: described second spray assemblies (3) also comprises and described the second serum recycle pipeline (32) held the second elevator pump (31) that stock tank (11) is connected, be connected with described second spraying layer (33) with described second elevator pump (31).
7. advection adverse current composite desulfate absorption tower according to claim 1, is characterized in that: described tower body (1) inwall is provided with and is positioned at described first spraying layer (23) below and the guide ring (7) matched with it.
CN201520663531.9U 2015-08-31 2015-08-31 Advection is compound desulfurization absorption tower against current Active CN205055802U (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105214469A (en) * 2015-08-31 2016-01-06 盐城市赛隆节能技术工程有限公司 Advection adverse current composite desulfate absorption tower

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105214469A (en) * 2015-08-31 2016-01-06 盐城市赛隆节能技术工程有限公司 Advection adverse current composite desulfate absorption tower

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Address after: 224056, Jiangsu province Yancheng City Salt Lake District, Huang Street, Yang Xu Village

Patentee after: Jiangsu selon energy saving technology Engineering Co., Ltd

Address before: 224056, Jiangsu province Yancheng City Salt Lake District, Huang Street, Yang Xu Village

Patentee before: Yancheng Sailong Energy-Saving Technology Engineering Co., Ltd.