CN102743941A - Desulphurizing dedusting cylinder structure regulated by liquid level - Google Patents
Desulphurizing dedusting cylinder structure regulated by liquid level Download PDFInfo
- Publication number
- CN102743941A CN102743941A CN201210198254XA CN201210198254A CN102743941A CN 102743941 A CN102743941 A CN 102743941A CN 201210198254X A CN201210198254X A CN 201210198254XA CN 201210198254 A CN201210198254 A CN 201210198254A CN 102743941 A CN102743941 A CN 102743941A
- Authority
- CN
- China
- Prior art keywords
- tube
- liquid level
- cylinder
- desulphurizing
- dedusting
- 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
Images
Landscapes
- Separating Particles In Gases By Inertia (AREA)
Abstract
The invention discloses a desulphurizing dedusting cylinder structure regulated by a liquid level. The structure is characterized by comprising a base cylinder (1) equipped with a desulfurizer cylinder (2) and a dehydrator cylinder (3). The upper end of the desulfurizer cylinder (2) is connected to an air inlet connection pipe (4), while the upper end of the dehydrator cylinder (3) is connected to an air outlet connection pipe (5). The air inlet connection pipe (4) and the air outlet connection pipe (5) both bend outward. The desulphurizing dedusting cylinder structure disclosed in the invention has the advantages of reasonable structural design, convenient liquid level regulation, strong load adaptability, and good desulphurizing and dedusting effects.
Description
Technical field
The present invention relates to the desulfurization and dedusting tube in a kind of desulphurization system.
Background technology
Desulfurizing dust-collector technological process at present generally is that flue gas gets into from the desulfurizing tower bottom, makes progress then, arranges that at desulfurization section shower nozzle sprays downwards.Flue gas contacts with doctor solution is reverse, though the application of this kind technology is comparatively extensive, and the running resistance that increase equipment is whole, the while has also increased the power of motor of blower fan.And existing desulfurizing dust-collector generally is that desulfurizing tower and dehydrating tower are to separate two independent parts, and equipment investment is big, and reasonable structure is bad.
Summary of the invention
The object of the invention is exactly the deficiency to above-mentioned prior art, provides a kind of simple and practical, reasonable in design, the desulfurization and dedusting barrel structure that liquid level is easy to adjust, load adaptability is strong.
The technical scheme that the present invention adopts is following:
A kind of desulfurization and dedusting barrel structure of regulating through liquid level; It is characterized in that it includes the basis tube, the basis tube is provided with devulcanizer tube and dehydrator tube, and devulcanizer tube upper end connects inlet pipe connection; Dehydrator tube upper end connects the tube connector of giving vent to anger, and inlet pipe connection is crooked laterally with the tube connector of giving vent to anger.
Be provided with demarcation strip in the tube of said basis.
Beneficial effect of the present invention has:
Reasonable in design, liquid level is easy to adjust, load adaptability is strong, and desulfurization and dedusting is effective.
Description of drawings
Fig. 1 is a structural representation of the present invention.
The specific embodiment
Below in conjunction with accompanying drawing the present invention is done explanation further:
Shown in accompanying drawing 1, it includes basis tube 1 the present invention, and basis tube 1 is a concrete tube, and inside is placed with doctor solution.Basis tube 1 is provided with devulcanizer tube 2 and dehydrator tube 3, and devulcanizer tube 2 upper ends connect inlet pipe connection 4, and dehydrator tube 3 upper ends connect the tube connector 5 of giving vent to anger, and inlet pipe connection 4 is crooked laterally with the tube connector 5 of giving vent to anger.
Be provided with demarcation strip 6 in the said basis tube 1.
The course of work of the present invention is following:
, leading edge moves from top to bottom after taking over 4 flue gases that get into and doctor solution mixes fully, in the process that entering devulcanizer tube 2 moves downward, owing to dilatation; Flue gas flow rate slows down to some extent, helps dust, impurity, water smoke and collides each other, form bigger material with flue gas to devulcanizer tube 2 bottom comers places; Because gravity and action of centrifugal force; Most of dust, impurity and drop directly fall in the desulfurizing tower base foundation tube, accomplish preliminary desulfurization and dedusting process.
Devulcanizer tube of the present invention 2 is open design with dehydrator tube 3 lower ends, and fuses with basis tube 1, and basis tube 1 communicates with circulatory pool; The liquid level scalable; When liquid level raise, the connection flue cross section between devulcanizer tube 2 and the dehydrator tube 3 respectively diminished, and flue gas flow rate increases; While impact liquid level, part dust and drop can fall into the water again and accomplish desulfurization and dedusting process for the second time.
Flue gas gets into dehydrator tube 3 bottoms; And then turn to and move upward, when connecting flue, because rising, the actual internal area of liquid level diminish, flue gas flow rate increases; Increase the centrifugal force of dust and drop simultaneously; When flue gas moves upward,, accomplish whole desulfurization and dedusting process because the dust of centrifugal action flue gas and drop fall into the dehydrating tower bottom again.
The undeclared part of other that the present invention relates to is identical with prior art.
Claims (2)
1. one kind is passed through the desulfurization and dedusting barrel structure that liquid level is regulated; It is characterized in that it includes basis tube (1); Basis tube (1) is provided with devulcanizer tube (2) and dehydrator tube (3); Devulcanizer tube (2) upper end connects inlet pipe connection (4), and dehydrator tube (3) upper end connects the tube connector (5) of giving vent to anger, and inlet pipe connection (4) and the tube connector of giving vent to anger (5) are crooked laterally.
2. the desulfurization and dedusting barrel structure of regulating through liquid level according to claim 1 is characterized in that being provided with demarcation strip (6) in the said basis tube (1).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201210198254XA CN102743941A (en) | 2012-06-15 | 2012-06-15 | Desulphurizing dedusting cylinder structure regulated by liquid level |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201210198254XA CN102743941A (en) | 2012-06-15 | 2012-06-15 | Desulphurizing dedusting cylinder structure regulated by liquid level |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN102743941A true CN102743941A (en) | 2012-10-24 |
Family
ID=47024645
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201210198254XA Pending CN102743941A (en) | 2012-06-15 | 2012-06-15 | Desulphurizing dedusting cylinder structure regulated by liquid level |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN102743941A (en) |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2220590Y (en) * | 1994-04-05 | 1996-02-21 | 武汉水利电力大学 | Tangential air intake dust removing desulfurization three-phase fluidized bed |
| CN2582731Y (en) * | 2002-12-09 | 2003-10-29 | 贾瑞彬 | Spraying self-excitation type desulfur dust collector |
| CN202638217U (en) * | 2012-06-15 | 2013-01-02 | 无锡翱翔环保机械有限公司 | Desulfuration and dedusting barrel structure through liquid level regulation |
-
2012
- 2012-06-15 CN CN201210198254XA patent/CN102743941A/en active Pending
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2220590Y (en) * | 1994-04-05 | 1996-02-21 | 武汉水利电力大学 | Tangential air intake dust removing desulfurization three-phase fluidized bed |
| CN2582731Y (en) * | 2002-12-09 | 2003-10-29 | 贾瑞彬 | Spraying self-excitation type desulfur dust collector |
| CN202638217U (en) * | 2012-06-15 | 2013-01-02 | 无锡翱翔环保机械有限公司 | Desulfuration and dedusting barrel structure through liquid level regulation |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN102743942A (en) | Wet-type desulfurizing deduster downstream spraying structure | |
| CN202638217U (en) | Desulfuration and dedusting barrel structure through liquid level regulation | |
| CN102743941A (en) | Desulphurizing dedusting cylinder structure regulated by liquid level | |
| CN205550020U (en) | Wet flue gas desulfurization dust collector | |
| CN204911221U (en) | Unequal venturi in convergent flaring angle restraints and CFB absorption tower thereof | |
| CN103908888B (en) | Spraying spray desulfurizing tower | |
| CN202638215U (en) | Compartment type desulfurizing structure | |
| CN207102129U (en) | A kind of dust treatment combination tower | |
| CN2642391Y (en) | Mixed-flow grid plate type water film dedusting desulfurizing equipment | |
| CN202263522U (en) | Flue gas desulfurization serial-column device | |
| CN205913885U (en) | But airflow flow velocity quick adjustment's defroster | |
| CN204147707U (en) | Drum type gas purifier | |
| CN202638216U (en) | Downstream spraying structure of wet type desulfurization precipitator | |
| CN209501336U (en) | A kind of desulfurizing tower single column double circulation structure | |
| CN201823446U (en) | High-efficiency energy-saving double-tower desulfurization deduster system | |
| CN202638214U (en) | High-order downstream spraying device | |
| CN209173730U (en) | A kind of fume desulfurating absorption tower with twin-stage airflow distribution device | |
| CN106731591A (en) | Two stage cycle subregion desulfurizing tower | |
| CN102743965A (en) | Direction-changing Venturi tube used for desulfurization system | |
| CN202237590U (en) | Novel folding-line type two-passage defogger | |
| CN202237591U (en) | Novel streamlined two-passage defogger | |
| CN205925405U (en) | Efficiency of desulfurization of wet desulfurization tower is improved device | |
| CN202289712U (en) | Novel broken line type three-channel demister | |
| CN102743967A (en) | Partitioned bin type desulfurization structure | |
| CN102743966A (en) | High downstream spraying device |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C02 | Deemed withdrawal of patent application after publication (patent law 2001) | ||
| WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20121024 |