CN207347530U - A kind of biogas desulfurization decarburization device for adding odor - Google Patents
A kind of biogas desulfurization decarburization device for adding odor Download PDFInfo
- Publication number
- CN207347530U CN207347530U CN201720479609.0U CN201720479609U CN207347530U CN 207347530 U CN207347530 U CN 207347530U CN 201720479609 U CN201720479609 U CN 201720479609U CN 207347530 U CN207347530 U CN 207347530U
- Authority
- CN
- China
- Prior art keywords
- decarburization
- adding odor
- biogas
- container
- naoh
- 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.)
- Expired - Fee Related
Links
Abstract
The utility model proposes a kind of biogas desulfurization decarburization device for adding odor,From left to right include the air inlet pipe connected by connecting pipe successively,Desulphurisation vessel,Decarburization container,Dewatering container,Compressor and air accumulator,Desulphurization reaction plate is equipped with desulphurisation vessel,Desulphurisation vessel one end is equipped with the first NaOH solution tank NaOH,The opposite other end is equipped with the first liquid waste collector,Decarburizing reaction plate is equipped with decarburization container,Decarburization one end is equipped with the second NaOH solution tank NaOH,The opposite other end is equipped with the second liquid waste collector,The device for adding odor is provided between air accumulator and compressor,Dehydrating agent plate is equipped with dewatering container,Semiconductor heater is equipped with dehydrating agent plate,A kind of biogas desulfurization decarburization device for adding odor of the utility model makes biogas and desulfuration solution,Decarbonizing solution comprehensive engagement,The sulphur removed in biogas in maximum magnitude,The impurity such as carbon,By semiconductor heat booster heating dehydrating agent plate internal desiccant can be enable to reuse,The biogas after purification is carried out by device for adding odor plus smelly.
Description
Technical field
The utility model belongs to field of renewable energy technology, particularly relates to a kind of desulfurization and decarburization device for adding odor.
Background technology
The energy and environmental problem have become two big outstanding problem of today's society, non-renewable energy resources increasingly reduce and into
In the case of this is increasingly elevated, large and medium-sized biogas engineering is one of important means for solving the energy and environmental problem.Biogas into
Dividing generally has methane (CH4), carbon dioxide (CO2), oxygen (O2), nitrogen (N2), carbon monoxide (CO), hydrogen (H2), water (H2O)
With hydrogen sulfide (H2Other gases compositions such as S).The purifying process of biogas mainly retains its flammable and combustion-supporting components methane (CH4), oxygen
Gas (O2), carbon monoxide (CO) and hydrogen (H2), to the H in biogas2S, H2O, CO2It is removed with other impurity.
Desulfurization is in order to avoid hydrogen sulfide (H2S) etching apparatus and pipeline, hydrogen sulfide is in methane fuelled engine and internal combustion engine
It can corrode bearing and some matching surfaces, make the deterioration of lubricant of engine, so as to accelerate engine scuffing;And leakage
H2S can cause poisoning, its product SO released that burns2、SO3It is the arch-criminal for causing acid rain, compares H2To be endangered caused by S also
Greatly.It is more traditional in biogas desulfurization method to have two class of dry desulfurization and wet desulphurization, the dry desulfurization in industrial applications
Easy to operate, equipment investment is small, its outstanding advantages is degree of purification height, and can remove a variety of organic sulfur compounds, is suitable for scale
Small, biogas desulfurization when sulfur content is relatively low application, otherwise desulfurizing agent replace frequent, it is difficult to solve that sulphur, which cannot effectively recycle problem,
Such as iron oxide process, activated carbon method, sieve method.Wet desulphurization is therein with specific solvent and feed gas, removing
Hydrogen sulfide, the method are generally used for that treatment scale is big, the high thick desulfurization of sulfur content, but it is low there is also Sulfur capacity, purifies low precision
Shortcoming, does not remove organic sulfur generally, applicable to have pressurization WATER-WASHING METHOD, Alkali absorption method, ferrous solution absorption process, tannin extract (tannin)
Method etc..In addition, new biogas desulfurization technique also has the methods of UF membrane desulfurization and biological desulphurization, but operation and maintenance cost
Height, difficulty are big, not yet industrially universal extensive use.And in large-sized biogas industrial applications also without a kind of big ability,
Precision is high, cost is low and can recycle the technique for applying of Sulphur ressource to greatest extent.
Decarbonization method in biogas is mainly liquid absorption method and solid absorption method, and liquid absorption method is divided into two major classes:One
Class is Physical Absorption method, i.e., can be dissolved in this characteristics of some liquid using CO2 separates from mixture it, different
The ability of solvent absorption CO2 is different, and the purification degrees being finally reached are also different, but general all lower than the purification degrees of chemical absorbing.
Another kind of is chemical absorption method, is the characteristic of sour gas according to CO2, using alkaline absorbent and CO2 chemically reacted come
Remove.CO2 in gas can be refined to very high degree by chemical absorption method under less high pressure.But inhaled when with chemistry
In the time receiving, just no longer have the characteristic for absorbing CO2, so the absorbability of chemical absorbent after chemical absorbent has reacted completely
It is limited.
Biogas from anaerobic ferment devices output when, carry substantial amounts of moisture, particularly in medium temperature or hot fermentation, biogas
With higher humidity.When the biogas of higher levels of humidity flows in pipeline, since the change dew point of temperature, pressure reduces, water steams
Air cooling is solidifying to add the resistance that biogas flows in pipeline, and the presence of vapor also reduces the calorific value of biogas, therefore needs
Condensed water in biogas is removed, at present, common biogas dewatering is dehydrated for gravitational method, cold partition method, solvent
Absorption process and solid-state physics water suction method, gravitational method dehydration are removed the part vapor in biogas with biogas gas-water separator,
This biogas gas-water separator mainly installs horizontal strainer and vertical strainer respectively up and down in tower, promotes the water in biogas to steam
Gas and biogas separation, but this device cannot simply and easily collect condensed water, need to additionally increase water collector equipment, add into
This;Cold partition method is to cause temperature change using pressure energy change, the method for making vapor be condensed out from gas phase, such a dress
Putting need to be pressurizeed or decompression processing, complicated and consume energy;Solvent absorption be using dehydrated solvent such as calcium chloride, lithium chloride and
Glycols absorb vapor, this method brings the possibility of other impurities into having while vapor is absorbed to biogas, at the same time
Regularly replace dehydrated solvent;Solid-state physics water suction method absorption produces under the effect of surface of solids power, and adsorbent exists de-
It is the problem of cannot regenerating and need to regularly replacing after water, complicated while of high cost.
Utility model content
The utility model proposes a kind of desulfurization and decarburization device for adding odor, solve in the prior art can not to comprehensively to biogas into
Row desulfurization, decarburization, dehydration plus it is smelly the defects of, by biogas and desulfuration solution, decarbonizing solution comprehensive engagement, in maximum magnitude
The impurity such as sulphur, carbon in removing biogas, can enable dehydrating agent plate internal desiccant reuse by semiconductor heat booster heating,
The characteristics of being carried out by device for adding odor to the biogas after purification plus smelly, preventing biogas from can not discover after leaking.
In order to solve the above-mentioned technical problem, the technical solution of the utility model is:
A kind of biogas desulfurization decarburization device for adding odor, the air inlet pipe for from left to right including connecting by connecting pipe successively, take off
Sulfur capacity device, decarburization container, dewatering container, compressor and air accumulator, the desulphurisation vessel is interior to be equipped with desulphurization reaction plate, the desulfurization
One end is equipped with the first NaOH solution tank NaOH, and the opposite other end is equipped with the first liquid waste collector, decarburization is equipped with the decarburization container
Reaction plate, the decarburization one end are equipped with the second NaOH solution tank NaOH, and the opposite other end is equipped with the second liquid waste collector, the gas storage
The device for adding odor is provided between tank and compressor, dehydrating agent plate is equipped with the dewatering container, is set in the dehydrating agent plate
There is semiconductor heater.
Containing desulfuration reagents such as sodium carbonate in first NaOH solution tank NaOH, the second NaOH solution tank NaOH is interior to contain the decarburizations such as organic amine examination
Agent.
First NaOH solution tank NaOH and the second NaOH solution tank NaOH are equipped with solution float.
Protective cover is equipped with above the air inlet pipe.
The junction of first NaOH solution tank NaOH and desulphurisation vessel is provided with the first spray port, second NaOH solution tank NaOH and decarburization
The junction of container is provided with the second spray port.
The desulphurisation vessel, decarburization tank atmosphere exit are equipped with solid particulate filters net.
Drier is additionally provided with the dehydrating agent plate.
Electronic valve is equipped with the device for adding odor.
In conclusion the utility model has the advantage of:Desulfuration solution, decarbonizing solution pass through spray port and gas in container
Comprehensive engagement, for the interior float that is equipped with of container easy to observation solution level, desulphurisation vessel, decarburization tank atmosphere exit are equipped with solid
Grain filter screen, may filter that the solid particle in gas, and be connected with semiconductor heat booster between gas-guide tube is dehydrated, and work as drier
After water suction, heating drier by semiconductor heat booster can reuse, and device for adding odor can be supervised by electronic valve flow
Control uniformly carries out plus smelly biogas after purification, prevents biogas from can not discover after leaking.
Brief description of the drawings
In order to illustrate the embodiment of the utility model or the technical proposal in the existing technology more clearly, below will be to embodiment
Or attached drawing needed to be used in the description of the prior art is briefly described, it should be apparent that, drawings in the following description are only
It is some embodiments of the utility model, for those of ordinary skill in the art, before not making the creative labor property
Put, other attached drawings can also be obtained according to these attached drawings.
Fig. 1 is a kind of biogas desulfurization decarburization device for adding odor structure diagram of the utility model.
In figure, 1- air inlet pipe;2- desulphurization reaction plates;3- desulphurisation vessels;The first NaOH solution tank NaOHs of 4-;The first liquid waste collectors of 5-;
6- decarburizing reaction plates;The second NaOH solution tank NaOHs of 7-;8- decarburization containers;The second liquid waste collectors of 9-;10- dewatering containers;11- dehydrating agents
Plate;12- compressors;13- device for adding odor;14- air accumulators.
Embodiment
The following is a combination of the drawings in the embodiments of the present utility model, and the technical scheme in the embodiment of the utility model is carried out
Clearly and completely describe, it is clear that the described embodiments are only a part of the embodiments of the utility model, rather than whole
Embodiment.Based on the embodiment in the utility model, those of ordinary skill in the art are without creative efforts
All other embodiments obtained, shall fall within the protection scope of the present invention.
As shown in Figure 1, a kind of biogas desulfurization decarburization device for adding odor, a kind of biogas desulfurization decarburization device for adding odor, including air inlet
Pipe 1, desulphurisation vessel 3, decarburization container 8, dewatering container 10, compressor 12, device for adding odor 13, air accumulator 14, in the air inlet pipe 1
Side is equipped with protective cover, and desulphurization reaction plate 2 is equipped with the desulphurisation vessel 3, and the top of desulphurisation vessel 3 is equipped with the first NaOH solution tank NaOH 4,
Lower section is equipped with the first liquid waste collector 5, and the decarburization container 8 connects desulphurisation vessel 3, and it is anti-to be equipped with decarburization in the decarburization container 3
Plate 6 is answered, the top of decarburization container 8 is equipped with the second NaOH solution tank NaOH 7, and lower section is equipped with the second liquid waste collector 9, the dewatering container 10
Decarburization container 8 is connected to, the dewatering container 10 is equipped with dehydrating agent plate 11, and semiconductor heating dress is equipped with the dehydrating agent plate 11
Put, the compressor 12, device for adding odor 13, air accumulator 14 are connected with dehydration device 10 successively.First NaOH solution tank NaOH 4 includes
There are the desulfuration reagents such as sodium carbonate, contain the decarburization reagents such as organic amine in the second NaOH solution tank NaOH 7.First NaOH solution tank NaOH 4 and second molten
Flow container 7 is equipped with solution float.The top of air inlet pipe 1 is equipped with protective cover.The desulphurisation vessel 3, decarburization container 8 spray for fountain
Liquid.The desulphurisation vessel 3,4 gas outlet of decarburization container are equipped with solid particulate filters net.Half is equipped with the dewatering container 10
Conductor heating unit.Drier is equipped with the dewatering container.Electronic valve is equipped with the device for adding odor 13.
The above is only the preferred embodiment of the utility model only, is not intended to limit the utility model, all at this
Within the spirit and principle of utility model, any modification, equivalent replacement, improvement and so on, should be included in the utility model
Protection domain within.
Claims (8)
- A kind of 1. biogas desulfurization decarburization device for adding odor, it is characterised in that:From left to right include what is connected by connecting pipe successively Air inlet pipe, desulphurisation vessel, decarburization container, dewatering container, compressor and air accumulator, the desulphurisation vessel is interior to be equipped with desulphurization reaction Plate, described desulphurisation vessel one end are equipped with the first NaOH solution tank NaOH, and the opposite other end is equipped with the first liquid waste collector, the decarburization container Interior to be equipped with decarburizing reaction plate, the decarburization one end is equipped with the second NaOH solution tank NaOH, and the opposite other end is equipped with the second waste collection Device, is provided with the device for adding odor between the air accumulator and compressor, dehydrating agent plate is equipped with the dewatering container, described de- Semiconductor heater is equipped with aqua plate.
- A kind of 2. biogas desulfurization decarburization device for adding odor according to claim 1, it is characterised in that:In first NaOH solution tank NaOH Containing desulfuration reagents such as sodium carbonate, contain the decarburization reagents such as organic amine in the second NaOH solution tank NaOH.
- A kind of 3. biogas desulfurization decarburization device for adding odor according to claim 1, it is characterised in that:First NaOH solution tank NaOH with Second NaOH solution tank NaOH is equipped with solution float.
- A kind of 4. biogas desulfurization decarburization device for adding odor according to claim 1, it is characterised in that:Set above the air inlet pipe There is protective cover.
- A kind of 5. biogas desulfurization decarburization device for adding odor according to claim 1 or 2 or 3, it is characterised in that:Described first is molten The junction of flow container and desulphurisation vessel is provided with the first spray port, and the junction of second NaOH solution tank NaOH and decarburization container is provided with Second spray port.
- A kind of 6. biogas desulfurization decarburization device for adding odor according to claim 1, it is characterised in that:The desulphurisation vessel, take off The gas outlet of carbon vessel is equipped with solid particulate filters net.
- A kind of 7. biogas desulfurization decarburization device for adding odor according to claim 1, it is characterised in that:In the dehydrating agent plate also Equipped with drier.
- A kind of 8. biogas desulfurization decarburization device for adding odor according to claim 1, it is characterised in that:Set in the device for adding odor There is electronic valve.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201720479609.0U CN207347530U (en) | 2017-05-02 | 2017-05-02 | A kind of biogas desulfurization decarburization device for adding odor |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201720479609.0U CN207347530U (en) | 2017-05-02 | 2017-05-02 | A kind of biogas desulfurization decarburization device for adding odor |
Publications (1)
Publication Number | Publication Date |
---|---|
CN207347530U true CN207347530U (en) | 2018-05-11 |
Family
ID=62361249
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201720479609.0U Expired - Fee Related CN207347530U (en) | 2017-05-02 | 2017-05-02 | A kind of biogas desulfurization decarburization device for adding odor |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN207347530U (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110172368A (en) * | 2019-06-26 | 2019-08-27 | 毅康科技有限公司 | A kind of integrated apparatus purified and remove pernicious gas in biogas |
-
2017
- 2017-05-02 CN CN201720479609.0U patent/CN207347530U/en not_active Expired - Fee Related
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110172368A (en) * | 2019-06-26 | 2019-08-27 | 毅康科技有限公司 | A kind of integrated apparatus purified and remove pernicious gas in biogas |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN102559316B (en) | Methane purifying method and equipment thereof | |
CN102154046B (en) | Method for processing and utilizing methane in refuse landfill | |
CN101274203B (en) | Method for removing carbon disulfide gas in production process of viscose fiber | |
CN103111177B (en) | Method and device for removing hydrogen sulfide in gas phase through oxidation | |
CN203820739U (en) | Biogas treatment system | |
KR20110117809A (en) | Purification system of high purity biogas for fuel cell and purification method thereof | |
CN103013600A (en) | Biogas desulfurization method in series of wet method with dry method | |
CN102120134A (en) | Electrochemical treatment device and method for removing hydrogen sulfide in methane | |
CN206902139U (en) | A kind of biogas Preparation equipment | |
CN104804790A (en) | Resourceful treatment system adopting straw to produce biogas and having efficient desulphurization and decarbonization functions | |
CN207347530U (en) | A kind of biogas desulfurization decarburization device for adding odor | |
CN202036906U (en) | NHD (polyethylene glycol dimethyl ether) desulfuration and decarburization condensate recycling system | |
CN214528878U (en) | Biogas filtering and purifying system in co-production of biogas and organic fertilizer by straw, livestock and poultry manure | |
CN202015580U (en) | Hydrogen sulfide gas absorption system | |
CN206375869U (en) | Wet desulphurization device | |
CN102451608A (en) | Tail gas treatment process applicable to natural gas with high sulfur | |
CN102453566A (en) | Purified gas dehydration technology applied in natural gas with high sulfur content | |
CN210814652U (en) | Deep hydrogen sulfide removal device for sulfur recovery tail gas | |
Deng et al. | Biogas cleaning and upgrading | |
CN208814962U (en) | Rear-mounted natural gas dry desulfurization device before a kind of | |
CN207899230U (en) | A kind of novel Complexing Iron desulphurization system | |
CN206955972U (en) | A kind of biogas desulfurization dehydration device | |
CN202595070U (en) | Device for purifying methane | |
CN104830365B (en) | High sulfur crude oil oil-gas recovery technology and oil-gas recovery system | |
CN205821273U (en) | A kind of hydramine method natural-gas desulfurizer |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
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: 20180511 Termination date: 20200502 |