CN203925622U - Incoagulable gas releasing system for ammoniacal liquor power generation system - Google Patents
Incoagulable gas releasing system for ammoniacal liquor power generation system Download PDFInfo
- Publication number
- CN203925622U CN203925622U CN201420259450.8U CN201420259450U CN203925622U CN 203925622 U CN203925622 U CN 203925622U CN 201420259450 U CN201420259450 U CN 201420259450U CN 203925622 U CN203925622 U CN 203925622U
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- CN
- China
- Prior art keywords
- ammonia
- tourie
- hot well
- water mixture
- incoagulable gas
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- Withdrawn - After Issue
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Abstract
The utility model discloses a kind of incoagulable gas releasing system for ammoniacal liquor power generation system, comprise vapour condenser, hot well, ammonia-water mixture liquid container and tourie, described hot well is arranged on the below of vapour condenser, described hot well comprises the gas phase zone on top and the liquid phase region of bottom, the liquid phase region of described hot well is connected with ammonia-water mixture liquid container by Drainage pipe, the gas phase zone of described hot well is communicated with the absorbing medium of tourie by exhaust duct, the top of described tourie is provided with outlet valve, the bottom of described tourie is connected with ammonia-water mixture liquid container by liquid-transport pipe-line.The utility model can be isolated the ammonia-water mixture in incoagulable gas thoroughly, and the safety and stability of safeguards system operation, meanwhile, can discharge safely incoagulable gas thoroughly, greatly reduces the pollution to environment.
Description
Technical field
The utility model belongs to ammoniacal liquor technical field of power generation, is specifically related to a kind of incoagulable gas releasing system for ammoniacal liquor power generation system.
Background technique
Along with going deep into of manufacturing enterprise's middle-low temperature heat utilization, organic working medium generating will be promoted gradually, and the generating that ammoniacal liquor is working medium of take that is adapted to middle low-temperature heat source also will extensively be utilized.Ammoniacal liquor generator set is in operation, having partial ammonia water decomposes, and other factors, cause existing in system incoagulable gas, in these incoagulable gas with a large amount of ammonia-water mixtures, if be directly discharged in atmosphere, certainly will cause the loss of ammonia-water mixture, affect stability and the efficiency of system operation, also can cause environmental pollution simultaneously, therefore need to take effective measures the ammonia-water mixture reclaiming in incoagulable gas, with the normal operation of safeguards system.
Model utility content
The purpose of this utility model is to provide a kind of incoagulable gas releasing system for ammoniacal liquor power generation system, its ammonia-water mixture in can effective separated incoagulable gas, the safety and stability of safeguards system operation.
The utility model solves the technological scheme that its technical problem adopts:
A kind of incoagulable gas releasing system for ammoniacal liquor power generation system is provided, comprise vapour condenser, hot well, ammonia-water mixture liquid container and tourie, described hot well is arranged on the below of vapour condenser, described hot well comprises the gas phase zone on top and the liquid phase region of bottom, the liquid phase region of described hot well is connected with ammonia-water mixture liquid container by Drainage pipe, the gas phase zone of described hot well is communicated with the absorbing medium of tourie by exhaust duct, the top of described tourie is provided with outlet valve, and the bottom of described tourie is connected with ammonia-water mixture liquid container by liquid-transport pipe-line.
By technique scheme, the absorbing medium in described tourie is water.
By technique scheme, described exhaust duct is arranged on the 50mm place, top, liquid phase region of hot well.
By technique scheme, on described outlet valve, be provided with can absorbing ammonia steam filler.
By technique scheme, on described tourie, intake pipe is installed.
The utility model, there is following beneficial effect: this system is passed through vapour condenser, liquid ammonia-water mixture first congeals into the ammonia gas vapor of the most of coercibility in incoagulable gas, and collect by hot well, through Drainage pipe, enter ammonia-water mixture liquid container again, remaining incoagulable gas enters tourie by exhaust duct after entering hot well, absorbing medium in tourie is converted into remaining a small amount of ammonia gas vapor into ammonia-water mixture, and entering ammonia-water mixture liquid container through liquid-transport pipe-line, remaining incoagulable gas is discharged by outlet valve.This system can be isolated the ammonia-water mixture in incoagulable gas thoroughly, and the safety and stability of safeguards system operation, meanwhile, can discharge safely incoagulable gas thoroughly, greatly reduces the pollution to environment.
Accompanying drawing explanation
Below in conjunction with drawings and Examples, the utility model is described in further detail, in accompanying drawing:
Fig. 1 is the utility model embodiment's structural representation.
Wherein: 1-vapour condenser; 2-hot well; 3-ammonia-water mixture liquid container; 4-outlet valve; 5-tourie; 6-exhaust duct; 7-liquid-transport pipe-line; 8-Drainage pipe; 9-intake pipe.
Embodiment
In order to make the purpose of this utility model, technological scheme and advantage clearer, below in conjunction with drawings and Examples, the utility model is further elaborated.Should be appreciated that specific embodiment described herein is only in order to explain the utility model, and be not used in restriction the utility model.
In preferred embodiment of the present utility model, as shown in Figure 1, a kind of incoagulable gas releasing system for ammoniacal liquor power generation system, comprise vapour condenser 1, hot well 2, ammonia-water mixture liquid container 3 and tourie 5, hot well 2 is arranged on the below of vapour condenser 1, hot well 2 comprises the gas phase zone on top and the liquid phase region of bottom, the liquid phase region of hot well 2 is connected with ammonia-water mixture liquid container 3 by Drainage pipe 8, the gas phase zone of hot well 2 is communicated with the absorbing medium of tourie 5 by exhaust duct 6, gas in hot well 2 rely on and tourie 5 between pressure reduction enter in tank, be absorbed Absorption of Medium, exhaust duct 6 is arranged on the 50mm place, top, liquid phase region of hot well 2, absorbing medium in tourie 5 is water, the top of tourie 5 is provided with outlet valve 4, on outlet valve 4, be provided with can absorbing ammonia steam filler, avoid the ammonia vapor not being completely absorbed to enter atmosphere, befouling environment, the bottom of tourie 5 is connected with ammonia-water mixture liquid container 3 by liquid-transport pipe-line 7, intake pipe 9 is installed with irregular moisturizing on tourie 5, the one, the normal liquid level of assurance tourie 5 interior absorbing mediums, the 2nd, guarantee that the ammonia concn of tourie 5 interior liquid is no more than limit, to guarantee that liquid has the ability of enough absorption ammoniacal liquor.
Working principle of the present utility model is: first by vapour condenser, the condensable gas in incoagulable gas is separated, be about to most of ammonia gas vapor liquid ammonia-water mixture that congeals into, and collect ammonia-water mixture by hot well, through Drainage pipe, enter ammonia-water mixture liquid container again, enter incoagulable gas in hot well because of the pressure reduction between hot well and tourie, by exhaust duct, enter tourie, absorbing medium water in tourie is converted into remaining condensable gas into ammonia-water mixture, liquid in tourie reaches after certain liquid level, by liquid-transport pipe-line, be transported in ammonia-water mixture liquid container, remaining incoagulable gas passes through outlet valve safety dumping in atmosphere, if the incoagulable gas of getting rid of is also remaining, there is an ammonia vapor, the filler being deflated on valve during to outside drain absorbs, avoid the discharge of ammoniacal liquor.This system can be isolated the ammonia-water mixture in incoagulable gas thoroughly, and the safety and stability of safeguards system operation, meanwhile, can discharge safely incoagulable gas thoroughly, greatly reduces the pollution to environment.
Should be understood that, for those of ordinary skills, can be improved according to the above description or convert, and all these improvement and conversion all should belong to the protection domain of the utility model claims.
Claims (5)
1. the incoagulable gas releasing system for ammoniacal liquor power generation system, it is characterized in that: comprise vapour condenser, hot well, ammonia-water mixture liquid container and tourie, described hot well is arranged on the below of vapour condenser, described hot well comprises the gas phase zone on top and the liquid phase region of bottom, the liquid phase region of described hot well is connected with ammonia-water mixture liquid container by Drainage pipe, the gas phase zone of described hot well is communicated with the absorbing medium of tourie by exhaust duct, the top of described tourie is provided with outlet valve, and the bottom of described tourie is connected with ammonia-water mixture liquid container by liquid-transport pipe-line.
2. system according to claim 1, is characterized in that: the absorbing medium in described tourie is water.
3. system according to claim 1, is characterized in that: described exhaust duct is arranged on the 50mm place, top, liquid phase region of hot well.
4. system according to claim 1, is characterized in that: on described outlet valve, be provided with can absorbing ammonia steam filler.
5. system according to claim 1, is characterized in that: on described tourie, intake pipe is installed.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420259450.8U CN203925622U (en) | 2014-05-21 | 2014-05-21 | Incoagulable gas releasing system for ammoniacal liquor power generation system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420259450.8U CN203925622U (en) | 2014-05-21 | 2014-05-21 | Incoagulable gas releasing system for ammoniacal liquor power generation system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203925622U true CN203925622U (en) | 2014-11-05 |
Family
ID=51821451
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420259450.8U Withdrawn - After Issue CN203925622U (en) | 2014-05-21 | 2014-05-21 | Incoagulable gas releasing system for ammoniacal liquor power generation system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203925622U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103982254A (en) * | 2014-05-21 | 2014-08-13 | 中冶南方工程技术有限公司 | Foul gas exhaust system for ammonia water power generation system |
-
2014
- 2014-05-21 CN CN201420259450.8U patent/CN203925622U/en not_active Withdrawn - After Issue
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103982254A (en) * | 2014-05-21 | 2014-08-13 | 中冶南方工程技术有限公司 | Foul gas exhaust system for ammonia water power generation system |
| CN103982254B (en) * | 2014-05-21 | 2016-09-21 | 中冶南方工程技术有限公司 | Incoagulable gas exhaust system for ammonia electricity generation system |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20141105 Effective date of abandoning: 20160921 |
|
| AV01 | Patent right actively abandoned |
Granted publication date: 20141105 Effective date of abandoning: 20160921 |
|
| C25 | Abandonment of patent right or utility model to avoid double patenting |