CN205199269U - High -efficient sulphur removal device - Google Patents
High -efficient sulphur removal device Download PDFInfo
- Publication number
- CN205199269U CN205199269U CN201521006328.0U CN201521006328U CN205199269U CN 205199269 U CN205199269 U CN 205199269U CN 201521006328 U CN201521006328 U CN 201521006328U CN 205199269 U CN205199269 U CN 205199269U
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- burner
- desulfurizing tower
- displacement pump
- combustor
- pipe
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Abstract
The utility model relates to a high -efficient sulphur removal device, it includes flue, pipeline, constant delivery pump A, constant delivery pump B, ammonifying device, chimney, draught fan, desulfurizing tower, defroster, dust remover, the flue be connected with the combustor, the combustor be connected with cooling device, the inside of combustor be provided with the pipe, the top of combustor be provided with the intake pipe, the bottom of combustor be provided with the outlet duct, the combustor on be provided with the methyl alcohol storage tank, methyl alcohol storage tank and combustor between be provided with constant delivery pump A, the combustor be connected with the cooler, the flue gas passes through dust remover, defroster, desulfurizing tower in proper order, the top of intake pipe and desulfurizing tower be connected, the outlet duct be connected with the chimney, outlet duct and chimney between be provided with the draught fan, total, this utility model has can reduce the reaction destabilizing factor, the sulphur removal rate is high, smoke diffusing is fast, the reaction is easily controlled, futuramic advantage.
Description
Technical field
The utility model belongs to field of Environment Protection, particularly the efficient desulfurizing device of one.
Background technology
At present, along with the development of science and technology, the energy needs consumption to increase, a large amount of coal-fired place such as thermal power plant, easily there is smoke pollution, containing pollution gas such as sulfur dioxide in flue gas, can to health, environment works the mischief, therefore be protection human-body safety, safeguard environment, a large amount of coal-fired place such as present thermal power plant needs to install desulfurizing device, most desulfurizing device is after desulfurization, need heat flue gas, then chimney is entered, ensure flue gas diffusion rapidly, do not affect surrounding environment, flue gas adds the cost of enterprise, energy consumption is high, and in sulphur removal process, the content of oxygen can affect except reaction of Salmon-Saxl, add destabilizing factor, I makes a thorough investigation of many years of experience and proposes a kind of efficient desulfurizing device, install combustion device, adopt methyl alcohol combustion product gases again, and can heat neat stress, decrease the destabilizing factor except reaction of Salmon-Saxl, improve desulphurizing ratio, have can reduce that reaction destabilizing factor, desulphurizing ratio are high, flue gas diffusion is fast, reaction is easy to control, futuramic advantage.
Summary of the invention
The purpose of this utility model is to overcome the deficiencies in the prior art, and reaction destabilizing factor, desulphurizing ratio are high, flue gas diffusion is fast, reaction is easy to control, futuramic efficient desulfurizing device to provide one to reduce.
The purpose of this utility model is achieved in that a kind of efficient desulfurizing device, it comprises flue, pipeline, constant displacement pump A, constant displacement pump B, ammonifying device, chimney, air-introduced machine, desulfurizing tower, demister, deduster, described flue is connected with burner, pipeline is provided with between described flue and burner, described burner is connected with cooling device, the inside of described burner is provided with pipe, the top of described burner is provided with air inlet pipe, the bottom of described burner is provided with escape pipe, described burner is provided with methanol tank, constant displacement pump A is provided with between described methanol tank and burner, described burner is connected with cooler, described cooler is connected with deduster, the bottom of described deduster is provided with lets out dirt mouth, described deduster is connected with demister, silk screen is provided with in described demister, described demister is connected with desulfurizing tower, described air inlet pipe is connected with the top of desulfurizing tower, described desulfurizing tower is provided with ammonifying device, constant displacement pump B is provided with between described ammonifying device and desulfurizing tower, the bottom of described desulfurizing tower is provided with outlet, described escape pipe is connected with chimney, air-introduced machine is provided with between described escape pipe and chimney.
Described pipe is arranged between air inlet pipe and escape pipe.
Described silk screen is two-layer.
Described air inlet pipe and the connected mode at the top of desulfurizing tower are that bolt is connected.
Described air-introduced machine is Y type.
Described constant displacement pump B is AF40 type.
The beneficial effects of the utility model: the utility model adopts flue, pipeline, constant displacement pump A, constant displacement pump B, ammonifying device, chimney, air-introduced machine, desulfurizing tower, demister, a kind of efficient desulfurizing device of deduster composition, have can reduce reaction destabilizing factor, desulphurizing ratio is high, flue gas diffusion is fast, reaction is easy to control, novel in design, the convenient advantage regulated, the inside of the burner that the utility model adopts is provided with pipe, the top of burner is provided with air inlet pipe, the bottom of burner is provided with escape pipe, burner is provided with methanol tank, constant displacement pump A is provided with between methanol tank and burner, burner is transported to through air inlet pipe by from desulfurizing tower neat stress out, constant displacement pump A quantitatively extracts the methyl alcohol in methanol tank, burn to from flue flue gas out, combustion heat heating neat stress, can while deoxygenation, neat stress is heated, it is made to spread rapidly, away from ground, there is deoxygenation, reduce reaction destabilizing factor, desulphurizing ratio is high, flue gas spreads fast advantage, be provided with silk screen in demister, there is the advantage that demist rate is high, be provided with constant displacement pump B between ammonifying device and desulfurizing tower, the content of ammonia in adjustable desulfurizing tower, there is the advantage that convenience regulates, desulphurizing ratio is high, be easy to control, total, this utility model have measure accurately, information transmission is convenient, reference convenient, Real-Time Monitoring, can and alarm improve the advantage of monitoring dynamics.
Accompanying drawing explanation
Fig. 1 is the structural representation of a kind of efficient desulfurizing device of the present utility model.
In figure: 1, flue 2, pipeline 3, methanol tank 4, constant displacement pump A5, burner 6, air inlet pipe 7, silk screen 8, constant displacement pump B9, ammonifying device 10, chimney 11, outlet 12, air-introduced machine 13, desulfurizing tower 14, demister 15, deduster 16, let out dirt mouth 17, cooler 18, escape pipe 19, pipe.
Detailed description of the invention
Below in conjunction with accompanying drawing, the utility model is described further.
Embodiment 1
As shown in Figure 1, a kind of efficient desulfurizing device, it comprises flue 1, pipeline 2, constant displacement pump B84A, constant displacement pump B84B, ammonifying device 9, chimney 10, air-introduced machine 12, desulfurizing tower 13, demister 14, deduster 15, described flue 1 is connected with burner 5, pipeline 2 is provided with between described flue 1 and burner 5, described burner 5 is connected with cooler 17, the inside of described burner 5 is provided with pipe 19, the top of described burner 5 is provided with air inlet pipe 6, the bottom of described burner 5 is provided with escape pipe 18, described burner 5 is provided with methanol tank 3, constant displacement pump B84A is provided with between described methanol tank 3 and burner 5, described burner 5 is connected with cooler, described cooler is connected with deduster 15, the bottom of described deduster 15 is provided with lets out dirt mouth 16, described deduster 15 is connected with demister 14, silk screen 7 is provided with in described demister 14, described demister 14 is connected with desulfurizing tower 13, described air inlet pipe 6 is connected with the top of desulfurizing tower 13, described desulfurizing tower 13 is provided with ammonifying device 9, constant displacement pump B84B is provided with between described ammonifying device 9 and desulfurizing tower 13, the bottom of described desulfurizing tower 13 is provided with outlet 11, described escape pipe 18 is connected with chimney 10, air-introduced machine 12 is provided with between described escape pipe 18 and chimney 10.
When the utility model is implemented, first from flue 1 flue gas out, enter into burner 5, constant displacement pump B84A extracts methyl alcohol, burning, neat stress from desulfurizing tower 13 out, the pipe 19 of burner 5 is entered into through air inlet pipe 6, while burner 5 deoxygenation, the neat stress in pipe 19 is heated, then flue gas is successively by way of cooler, deduster 15, demister 14 arrives desulfurizing tower 13, neat stress enters chimney 10 through escape pipe 18, discharge: the utility model adopts flue 1, pipeline 2, constant displacement pump B84A, constant displacement pump B84B, ammonifying device 9, chimney 10, air-introduced machine 12, desulfurizing tower 13, demister 14, deduster 15 forms a kind of efficient desulfurizing device, have and can reduce reaction destabilizing factor, desulphurizing ratio is high, flue gas diffusion is fast, reaction is easy to control, novel in design, the convenient advantage regulated, the inside of the burner 5 that the utility model adopts is provided with pipe 19, the top of burner 5 is provided with air inlet pipe 6, the bottom of burner 5 is provided with escape pipe 18, burner 5 is provided with methanol tank 3, constant displacement pump B84A is provided with between methanol tank 3 and burner 5, burner 5 is transported to through air inlet pipe 6 by from desulfurizing tower 13 neat stress out, constant displacement pump B84A quantitatively extracts the methyl alcohol of methanol tank 3 li, burn to from flue 1 flue gas out, combustion heat heating neat stress, can while deoxygenation, neat stress is heated, it is made to spread rapidly, away from ground, there is deoxygenation, reduce reaction destabilizing factor, desulphurizing ratio is high, flue gas spreads fast advantage, be provided with silk screen 7 in demister 14, there is the advantage that demist rate is high, be provided with constant displacement pump B84B between ammonifying device 9 and desulfurizing tower 13, the content of ammonia in adjustable desulfurizing tower 13, there is the advantage that convenience regulates, desulphurizing ratio is high, be easy to control, total, this utility model have measure accurately, information transmission is convenient, reference convenient, Real-Time Monitoring, can and alarm improve the advantage of monitoring dynamics.
Embodiment 2
As shown in Figure 1, a kind of efficient desulfurizing device, it comprises flue 1, pipeline 2, constant displacement pump B84A, constant displacement pump B84B, ammonifying device 9, chimney 10, air-introduced machine 12, desulfurizing tower 13, demister 14, deduster 15, described flue 1 is connected with burner 5, pipeline 2 is provided with between described flue 1 and burner 5, described burner 5 is connected with cooler 17, the inside of described burner 5 is provided with pipe 19, the top of described burner 5 is provided with air inlet pipe 6, the bottom of described burner 5 is provided with escape pipe 18, described burner 5 is provided with methanol tank 3, constant displacement pump B84A is provided with between described methanol tank 3 and burner 5, described burner 5 is connected with cooler, described cooler is connected with deduster 15, the bottom of described deduster 15 is provided with lets out dirt mouth 16, described deduster 15 is connected with demister 14, silk screen 7 is provided with in described demister 14, described demister 14 is connected with desulfurizing tower 13, described air inlet pipe 6 is connected with the top of desulfurizing tower 13, described desulfurizing tower 13 is provided with ammonifying device 9, constant displacement pump B84B is provided with between described ammonifying device 9 and desulfurizing tower 13, the bottom of described desulfurizing tower 13 is provided with outlet 11, described escape pipe 18 is connected with chimney 10, air-introduced machine 12 is provided with between described escape pipe 18 and chimney 10.
Described pipe 19 is arranged between air inlet pipe 6 and escape pipe 18.
Described silk screen 7 is two-layer.
Described air inlet pipe 6 and the connected mode at the top of desulfurizing tower 13 are that bolt is connected.
Described air-introduced machine 12 is Y type.
Described constant displacement pump B84B is AF40 type.
When the utility model is implemented, first from flue 1 flue gas out, enter into burner 5, constant displacement pump B84A extracts methyl alcohol, burning, neat stress from desulfurizing tower 13 out, the pipe 19 of burner 5 is entered into through air inlet pipe 6, while burner 5 deoxygenation, the neat stress in pipe 19 is heated, then flue gas is successively by way of cooler, deduster 15, demister 14 arrives desulfurizing tower 13, neat stress enters chimney 10 through escape pipe 18, discharge: the utility model adopts flue 1, pipeline 2, constant displacement pump B84A, constant displacement pump B84B, ammonifying device 9, chimney 10, air-introduced machine 12, desulfurizing tower 13, demister 14, deduster 15 forms a kind of efficient desulfurizing device, have and can reduce reaction destabilizing factor, desulphurizing ratio is high, flue gas diffusion is fast, reaction is easy to control, novel in design, the convenient advantage regulated, the inside of the burner 5 that the utility model adopts is provided with pipe 19, the top of burner 5 is provided with air inlet pipe 6, the bottom of burner 5 is provided with escape pipe 18, burner 5 is provided with methanol tank 3, constant displacement pump B84A is provided with between methanol tank 3 and burner 5, burner 5 is transported to through air inlet pipe 6 by from desulfurizing tower 13 neat stress out, constant displacement pump B84A quantitatively extracts the methyl alcohol of methanol tank 3 li, burn to from flue 1 flue gas out, combustion heat heating neat stress, can while deoxygenation, neat stress is heated, it is made to spread rapidly, away from ground, there is deoxygenation, reduce reaction destabilizing factor, desulphurizing ratio is high, flue gas spreads fast advantage, be provided with silk screen 7 in demister 14, there is the advantage that demist rate is high, be provided with constant displacement pump B84B between ammonifying device 9 and desulfurizing tower 13, the content of ammonia in adjustable desulfurizing tower 13, there is the advantage that convenience regulates, desulphurizing ratio is high, be easy to control, the pipe 19 that the utility model adopts is arranged between air inlet pipe 6 and escape pipe 18, has the advantage of convenient heating, silk screen 7 is two-layer, has the advantage that demist rate is high, air inlet pipe 6 and the connected mode at the top of desulfurizing tower 13 are that bolt is connected, and have advantage easy for installation, total, this utility model have measure accurately, information transmission is convenient, reference convenient, Real-Time Monitoring, can and alarm improve the advantage of monitoring dynamics.
The foregoing is only preferred embodiment of the present utility model, protection domain of the present utility model is not limited thereto, and anyly all belongs within the utility model protection domain based on the equivalent transformation in technical solutions of the utility model.
Claims (6)
1. an efficient desulfurizing device, it comprises flue, pipeline, constant displacement pump A, constant displacement pump B, ammonifying device, chimney, air-introduced machine, desulfurizing tower, demister, deduster, it is characterized in that: described flue is connected with burner, pipeline is provided with between described flue and burner, described burner is connected with cooling device, the inside of described burner is provided with pipe, the top of described burner is provided with air inlet pipe, the bottom of described burner is provided with escape pipe, described burner is provided with methanol tank, constant displacement pump A is provided with between described methanol tank and burner, described burner is connected with cooler, described cooler is connected with deduster, the bottom of described deduster is provided with lets out dirt mouth, described deduster is connected with demister, silk screen is provided with in described demister, described demister is connected with desulfurizing tower, described air inlet pipe is connected with the top of desulfurizing tower, described desulfurizing tower is provided with ammonifying device, constant displacement pump B is provided with between described ammonifying device and desulfurizing tower, the bottom of described desulfurizing tower is provided with outlet, described escape pipe is connected with chimney, air-introduced machine is provided with between described escape pipe and chimney.
2. the efficient desulfurizing device of one according to claim 1, is characterized in that: described pipe is arranged between air inlet pipe and escape pipe.
3. the efficient desulfurizing device of one according to claim 1, is characterized in that: described silk screen is two-layer.
4. the efficient desulfurizing device of one according to claim 1, is characterized in that: described air inlet pipe and the connected mode at the top of desulfurizing tower are that bolt is connected.
5. the efficient desulfurizing device of one according to claim 4, is characterized in that: described air-introduced machine is Y type.
6. the efficient desulfurizing device of one according to claim 1, is characterized in that: described constant displacement pump B is AF40 type.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201521006328.0U CN205199269U (en) | 2015-12-08 | 2015-12-08 | High -efficient sulphur removal device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201521006328.0U CN205199269U (en) | 2015-12-08 | 2015-12-08 | High -efficient sulphur removal device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205199269U true CN205199269U (en) | 2016-05-04 |
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ID=55837014
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201521006328.0U Expired - Fee Related CN205199269U (en) | 2015-12-08 | 2015-12-08 | High -efficient sulphur removal device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205199269U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106369623A (en) * | 2016-11-29 | 2017-02-01 | 冯伟忠 | System for removing smoke plumes through condensation, emission reduction, water collecting, heating and drying |
-
2015
- 2015-12-08 CN CN201521006328.0U patent/CN205199269U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106369623A (en) * | 2016-11-29 | 2017-02-01 | 冯伟忠 | System for removing smoke plumes through condensation, emission reduction, water collecting, heating and drying |
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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: 20160504 Termination date: 20161208 |