CN206350991U - A kind of desulphurization plant of novel energy-conserving - Google Patents
A kind of desulphurization plant of novel energy-conserving Download PDFInfo
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- CN206350991U CN206350991U CN201621476299.9U CN201621476299U CN206350991U CN 206350991 U CN206350991 U CN 206350991U CN 201621476299 U CN201621476299 U CN 201621476299U CN 206350991 U CN206350991 U CN 206350991U
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- absorption tower
- pipeline
- sack cleaner
- conserving
- novel energy
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Abstract
The utility model discloses a kind of desulphurization plant of novel energy-conserving, including stove, sack cleaner, absorption tower, lime precipitation pond and technique water tank, stove upper end side is connected by pipeline with sack cleaner, sack cleaner includes cloth bag and ash bucket, absorption tower is located at sack cleaner side, and absorption tower side is connected close to upper end by pipeline with sack cleaner, opposite side passes through water pipe Joining Technology water tank close to upper end, the pipeline of the water pipe is provided with technique water pump, lime precipitation pond is connected by corresponding pipeline with absorption tower bottom side, and the pipeline on lime precipitation pond and absorption tower is provided with regeneration pump.The desulphurization plant of the novel energy-conserving, desulfurization dust-removing efficiency is high, efficient demisting, reduce the supersaturated moisture in flue gas, it is to avoid liquid, slag are few simultaneously for fan belt water and Wet chimney phenomenon, easily separated, desulfurization wastewater is recycled, and is economized on resources, it is to avoid secondary pollution phenomenon occur.
Description
Technical field
The utility model is related to a kind of desulphurization plant of novel energy-conserving, belongs to chemical technology field.
Background technology
Whether current flue gas desulfurization technique species adds water the dry and wet form with desulfurization product up to tens kinds by sweetening process,
Flue gas desulfurization is divided into:Wet method, semidry method, dry method three major types sulfur removal technology.Wet Flue Gas Desulfurization Technique is more ripe, efficiency high, operation
Simply.Supersaturated moisture of the Wet Flue Gas Desulfurization Technique in actual production process in flue gas is higher, so as to cause air-introduced machine band water
Phenomenon, have impact on desulfurization quality and efficiency, while liquid, slag are more, be not readily separated, and waste water can not be recycled preferably.
To solve the above problems, therefore it is proposed that a kind of desulphurization plant of novel energy-conserving.
Utility model content
The technical problems to be solved in the utility model is to overcome the defect of prior art there is provided a kind of desulfurization of novel energy-conserving
Equipment, in order to solve the above-mentioned technical problem, the utility model provide following technical scheme:
A kind of desulphurization plant of novel energy-conserving of the utility model, including stove, sack cleaner, absorption tower, lime precipitation
Pond and technique water tank, stove upper end side are connected by pipeline with sack cleaner, and sack cleaner includes cloth bag and ash bucket, are inhaled
Receive tower and be located at sack cleaner side, and absorption tower side is connected close to upper end by pipeline with sack cleaner, opposite side is leaned on
Nearly upper end is provided with technique water pump by water pipe Joining Technology water tank, the pipeline of the water pipe, and lime precipitation pond passes through corresponding
Pipeline is connected with absorption tower bottom side, and the pipeline on lime precipitation pond and absorption tower is provided with regeneration pump.
As a kind of preferred embodiment of the present utility model, two sections are divided into inside the absorption tower, upper end is divided into two layers,
Respectively demisting layer and spraying layer, install on spraying layer and are provided with shower nozzle.
As a kind of preferred embodiment of the present utility model, the pipeline connected between the sack cleaner and absorption tower
Upper install is provided with air-introduced machine.
As a kind of preferred embodiment of the present utility model, absorption tower upper end side connects and installs carbonated drink point
From device, steam-water separator is exported including net gas.
As a kind of preferred embodiment of the present utility model, the side bottom of absorption tower one connection, which is installed, is provided with fluid infusion
Pump.
The beneficial effect that the utility model is reached is:Desulfurization dust-removing efficiency is high, passes through the demisting being provided with inside absorption tower
The efficient demisting of device, reduces the supersaturated moisture in flue gas, it is to avoid fan belt water and Wet chimney phenomenon, while liquid, slag are few, easily
Separation, desulfurization wastewater is recycled, economized on resources, it is to avoid secondary pollution phenomenon occur.
Brief description of the drawings
Accompanying drawing is used for providing further understanding to of the present utility model, and constitutes a part for specification, with this practicality
New embodiment is used to explain the utility model together, does not constitute to limitation of the present utility model.In the accompanying drawings:
Fig. 1 is a kind of structural representation of the desulphurization plant of novel energy-conserving of the utility model;
In figure:1- stoves, 2- sack cleaners, 3- absorption towers, 31- demistings layer, 32- spraying layers, 4- lime precipitations pond, 5-
Technique water tank, 6- steam-water separators, 7- air-introduced machines, 8- regeneration pumps, 9- fluid infusion pumps, 10- industrial water pumps.
Embodiment
Preferred embodiment of the present utility model is illustrated below in conjunction with accompanying drawing, it will be appreciated that described herein excellent
Select embodiment to be merely to illustrate and explain the utility model, be not used to limit the utility model.
Embodiment 1
As shown in figure 1, a kind of desulphurization plant of novel energy-conserving, including stove 1, sack cleaner 2, absorption tower 3, lime sink
Shallow lake pond 4 and technique water tank 5, the upper end side of stove 1 are connected by pipeline with sack cleaner 2, sack cleaner 2 include cloth bag and
Ash bucket, absorption tower 3 is located at the side of sack cleaner 2, and the side of absorption tower 3 is connected close to upper end by pipeline with sack cleaner 2
Logical, opposite side is close to upper end by water pipe Joining Technology water tank 5, and the pipeline of the water pipe is provided with technique water pump 10, and lime sinks
Shallow lake pond 4 is connected by corresponding pipeline with the bottom side of absorption tower 3, and the pipeline in lime precipitation pond 4 and absorption tower 3 is provided with again
Raw pump 8.
Advantage of the present utility model:It is divided into two sections inside the desulphurization plant of the novel energy-conserving, absorption tower 3, upper end is divided into two
Installed on layer, respectively demisting layer 31 and spraying layer 32, spraying layer 31 and be provided with shower nozzle, the sack cleaner 2 and absorption tower 3 it
Between install on the pipeline that connects and be provided with air-introduced machine 7, the upper end side of absorption tower 3 connects and installs steam-water separator 6, carbonated drink
Separator 6 is exported including net gas, and the side bottom of absorption tower 3 one connection, which is installed, is provided with fluid infusion pump 9.
Operation principle:The utility model is by using double alkali method desulfurizing technology, and the flue gas produced by stove 1 passes through prime cloth
Bag dust collector 2 carries out dedusting, and the flue gas after dedusting sends into absorption tower 3 by air-introduced machine 7 and carries out epimere arrangement in desulfurization, absorption tower 3
There are Multi-layer sprinkling layer 32 and demisting layer 31, the water smoke containing desulfurizing agent can be sprayed, then dividing for carbonated drink is carried out by steam-water separator 6
After carrying out fully reacting with absorbing liquid from, SO2 in flue gas, contact, bottom of towe is deposited to and by the feeding lime precipitation of regeneration pump 8
Concentrated, filtered in pond 4, obtaining gypsum.Flue gas after desulfurization and dedusting removes supersaturated moisture therein through high efficiency demister,
Both secondary pollution is prevented, alkali consumption and operation cost are reduced again.Flue gas after desulfurization and dedusting is gone out therein through high efficiency demister
Supersaturated moisture, reaches after discharge standard and to be discharged into air through chimney.
Finally it should be noted that:Preferred embodiment of the present utility model is the foregoing is only, this is not limited to
Utility model, although the utility model is described in detail with reference to the foregoing embodiments, for those skilled in the art
For, it can still modify to the technical scheme described in foregoing embodiments, or to which part technical characteristic
Carry out equivalent substitution.It is all it is of the present utility model spirit and principle within, any modification, equivalent substitution and improvements made etc.,
It should be included within protection domain of the present utility model.
Claims (5)
1. a kind of desulphurization plant of novel energy-conserving, including stove (1), sack cleaner (2), absorption tower (3), lime precipitation pond
(4) and technique water tank (5), it is characterised in that stove (1) upper end side is connected by pipeline with sack cleaner (2), and cloth bag is removed
Dirt device (2) includes cloth bag and ash bucket, and absorption tower (3) are located at sack cleaner (2) side, and absorption tower (3) side is close to upper end
Connected by pipeline with sack cleaner (2), opposite side close to upper end by water pipe Joining Technology water tank (5), the water pipe
Pipeline is provided with technique water pump (10), and lime precipitation pond (4) are connected by corresponding pipeline with absorption tower (3) bottom side, and
The pipeline in lime precipitation pond (4) and absorption tower (3) is provided with regeneration pump (8).
2. a kind of desulphurization plant of novel energy-conserving as claimed in claim 1, it is characterised in that be divided into two inside the absorption tower
Section, upper end is divided into two layers, respectively demisting layer (31) and spraying layer (32), is installed on spraying layer (32) provided with shower nozzle.
3. a kind of desulphurization plant of novel energy-conserving as claimed in claim 1, it is characterised in that the sack cleaner 2 is with inhaling
Receive to install on the pipeline connected between tower (3) and be provided with air-introduced machine (7).
4. a kind of desulphurization plant of novel energy-conserving as claimed in claim 1, it is characterised in that absorption tower (3) upper end one
Side is connected and installs steam-water separator (6), and steam-water separator (6) is exported including net gas.
5. a kind of desulphurization plant of novel energy-conserving as claimed in claim 1, it is characterised in that absorption tower (3) the side bottom
Portion's connection, which is installed, is provided with fluid infusion pump (9).
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN201621476299.9U CN206350991U (en) | 2016-12-30 | 2016-12-30 | A kind of desulphurization plant of novel energy-conserving |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
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CN201621476299.9U CN206350991U (en) | 2016-12-30 | 2016-12-30 | A kind of desulphurization plant of novel energy-conserving |
Publications (1)
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CN206350991U true CN206350991U (en) | 2017-07-25 |
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CN201621476299.9U Expired - Fee Related CN206350991U (en) | 2016-12-30 | 2016-12-30 | A kind of desulphurization plant of novel energy-conserving |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107694265A (en) * | 2017-11-08 | 2018-02-16 | 俞小林 | A kind of old metal smelting smoke dust processing system |
-
2016
- 2016-12-30 CN CN201621476299.9U patent/CN206350991U/en not_active Expired - Fee Related
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107694265A (en) * | 2017-11-08 | 2018-02-16 | 俞小林 | A kind of old metal smelting smoke dust processing system |
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Legal Events
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GR01 | Patent grant | ||
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: 20170725 Termination date: 20181230 |