CN205295260U - Coal gas sweetener - Google Patents
Coal gas sweetener Download PDFInfo
- Publication number
- CN205295260U CN205295260U CN201620058114.6U CN201620058114U CN205295260U CN 205295260 U CN205295260 U CN 205295260U CN 201620058114 U CN201620058114 U CN 201620058114U CN 205295260 U CN205295260 U CN 205295260U
- Authority
- CN
- China
- Prior art keywords
- layer
- coal gas
- rectification
- sweetener
- gas
- 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.)
- Active
Links
Landscapes
- Gas Separation By Absorption (AREA)
Abstract
The utility model belongs to the technical field of the coal gas desulfurization and a coal gas sweetener is disclosed, spray layer, defroster, gas outlet, pump line, water pump and circulation tank including gas inlet, rectification layer, the first layer, hollow layer packing layer, casing, second of spraying, the casing bottom is equipped with circulation tank, casing bottom one side is equipped with gas inlet, inside being equipped with of casing sets up parallel arrangement's a plurality of root circles shape or the rectification layer that square pipeline constitutes by the level, rectification layer top is equipped with the first layer that sprays. The utility model discloses a first layer that sprays the layer with the second, can effectual improvements desulfurization efficiency, improved the inside gas distribution state of sweetener greatly through the rectification layer, and owing to disposed the rectification layer structure, can optimize the coal gas evenly distributed on the whole cross section of sweetener, optimize flow field in the sweetener greatly, can fully break the crude gas simultaneously, coal gas and fluid contact are shunted to the formation stranded, have increased the desulfurization degree of sweetener.
Description
Technical field
The utility model relates to a kind of sweetener, is specifically related to a kind of coal gas desulfurization equipment, belongs to coal gas desulfurization technical field.
Background technology
The raw materials such as coal gas Sweet natural gas, fuel gas has a wide range of applications mode, mainly contain: produce other Chemicals as unstripped gas, produce special rolling-mill section, it is used for the generating of coal gas steam turbine as fuel, MAGNESIUM METAL gas making, coal tar processing, lime kilning, machine brick, building block, solid caustic soda, gas turbines for power generation, oil engine generates electricity, methyl alcohol processed, city air feed etc., the raising again and again of national environmental standard, require coal gas, Sweet natural gas, coking industry need to optimize technique further, improve level of purification, concentration of hydrogen sulfide requires to bring up to 20mg/m3 by original 200mg/m3, future may require higher, it is less than 5mg/m3. if adopting the process technology of high-temperature coking gas purification process, emission request can not be reached.
Practical novel content
The technical problems to be solved in the utility model overcomes existing defect, a kind of coal gas desulfurization equipment is provided, adopt the first spraying layer and the 2nd spraying layer, can effectively improve desulfuration efficiency, the gas distribution state of sweetener inside is substantially improved by rectification layer, owing to being configured with rectification Rotating fields, the coal gas can optimized on the whole cross section of sweetener is uniformly distributed, greatly optimize sweetener flow field, crude gas fully can be broken simultaneously, form multiply shunting coal gas and liquid comes into contact, add the desulfurization degree of sweetener, can effectively solve the problem in background technology.
In order to solve the problems of the technologies described above, the utility model provides following technical scheme:
The utility model provides a kind of coal gas desulfurization equipment, comprise gas inlet, rectification layer, first spraying layer, voided layer packing layer, housing, 2nd spraying layer, mist eliminator, air outlet, pump line, water pump and cyclic water tank, described housing bottom is provided with cyclic water tank, described housing bottom side is provided with gas inlet, described enclosure interior is provided with by the rectification layer being horizontally disposed with some circles arranged in parallel or square pipe is formed, described rectification layer top is provided with the first spraying layer, described first spraying layer top is provided with voided layer packing layer, described voided layer packing layer top is provided with the 2nd spraying layer, described 2nd spraying layer top is provided with mist eliminator, described case top is provided with air outlet, described first spraying layer and the 2nd spraying layer side are all connected with water pump by pump line, described water pump is arranged on cyclic water tank and one end is connected by pump line.
As a kind of optimal technical scheme of the present utility model, bottom described first spraying layer and the 2nd spraying layer, it is equipped with some spray headers.
As a kind of optimal technical scheme of the present utility model, described rectification layer, spraying layer, voided layer packing layer, the 2nd spraying layer are fixedly connected with inner walls with mist eliminator.
As a kind of optimal technical scheme of the present utility model, described rectification layer circle or square pipe are nonuniform mutation operator.
As a kind of optimal technical scheme of the present utility model, described mist eliminator is at least side.
The useful effect that the utility model reaches is: a kind of coal gas desulfurization equipment, adopt the first spraying layer and the 2nd spraying layer, can effectively improve desulfuration efficiency, the gas distribution state of sweetener inside is substantially improved by rectification layer, owing to being configured with rectification Rotating fields, the coal gas can optimized on the whole cross section of sweetener is uniformly distributed, greatly optimize sweetener flow field, crude gas fully can be broken simultaneously, form multiply shunting coal gas and liquid comes into contact, add the desulfurization degree of sweetener.
Accompanying drawing explanation
Accompanying drawing be used to provide to of the present utility model it is further understood that and form the part of specification sheets, be used from explanation the utility model with embodiment one of the present utility model, do not form restriction of the present utility model.
In the accompanying drawings:
Fig. 1 is a kind of coal gas desulfurization equipment overall structure schematic diagram described in the utility model embodiment;
Fig. 2 is a kind of coal gas desulfurization equipment rectification Rotating fields schematic diagram described in the utility model embodiment;
Number in the figure: 1, gas inlet; 2, rectification layer; 3, the first spraying layer; 4, voided layer packing layer; 5, housing; 6, the 2nd spraying layer; 7, mist eliminator; 8, air outlet; 9, pump line; 10, water pump; 11, cyclic water tank.
Embodiment
Below in conjunction with accompanying drawing, preferred embodiment of the present utility model is described, it will be appreciated that preferred embodiment described herein is only for instruction and explanation of the utility model, and is not used in restriction the utility model.
Embodiment: refer to Fig. 1-2, a kind of coal gas desulfurization equipment of the utility model, comprise gas inlet 1, rectification layer 2, first spraying layer 3, voided layer packing layer 4, housing 5, 2nd spraying layer 6, mist eliminator 7, air outlet 8, pump line 9, water pump 10 and cyclic water tank 11, it is provided with cyclic water tank 11 bottom described housing 5, bottom described housing 5, side is provided with gas inlet 1, described housing 5 inside is provided with by the rectification layer 2 being horizontally disposed with some circles arranged in parallel or square pipe is formed, described rectification layer 2 top is provided with the first spraying layer 3, described first spraying layer 3 top is provided with voided layer packing layer 4, described voided layer packing layer 4 top is provided with the 2nd spraying layer 6, described 2nd spraying layer 6 top is provided with mist eliminator 7, described housing 5 top is provided with air outlet 8, described first spraying layer 3 and the 2nd spraying layer 6 side are all connected with water pump 10 by pump line 9, described water pump 10 is arranged on cyclic water tank 11 and one end is connected by pump line 9.
It is equipped with some spray headers bottom described first spraying layer 3 and the 2nd spraying layer 6, can effectively improve desulfuration efficiency, described rectification layer 2, spraying layer 3, voided layer packing layer 4, the 2nd spraying layer 6 are fixedly connected with housing 5 inwall with mist eliminator 7, described rectification layer 2 circle or square pipe are nonuniform mutation operator, described mist eliminator 7 is at least one layer, it is possible to filtered by the fog carried in gas.
It should be noted that, the utility model is a kind of coal gas desulfurization equipment, during work, adopt the first spraying layer and the 2nd spraying layer, can effectively improve desulfuration efficiency, the gas distribution state of sweetener inside is substantially improved by rectification layer, owing to being configured with rectification Rotating fields, the coal gas can optimized on the whole cross section of sweetener is uniformly distributed, greatly optimize sweetener flow field, crude gas fully can be broken simultaneously, form multiply shunting coal gas and liquid comes into contact, add the desulfurization degree of sweetener.
Finally it is noted that the foregoing is only preferred embodiment of the present utility model, it is not limited to the utility model, although the utility model being described in detail with reference to previous embodiment, for a person skilled in the art, technical scheme described in foregoing embodiments still can be modified by it, or wherein part technology feature carries out equivalent replacement. All within spirit of the present utility model and principle, any amendment of doing, equivalent replacement, improvement etc., all should be included within protection domain of the present utility model.
Claims (5)
1. a coal gas desulfurization equipment, comprise gas inlet (1), rectification layer (2), first spraying layer (3), voided layer packing layer (4), housing (5), 2nd spraying layer (6), mist eliminator (7), air outlet (8), pump line (9), water pump (10) and cyclic water tank (11), it is characterized in that, described housing (5) bottom is provided with cyclic water tank (11), side, described housing (5) bottom is provided with gas inlet (1), described housing (5) inside is provided with by the rectification layer (2) being horizontally disposed with some circles arranged in parallel or square pipe is formed, described rectification layer (2) top is provided with the first spraying layer (3), described first spraying layer (3) top is provided with voided layer packing layer (4), described voided layer packing layer (4) top is provided with the 2nd spraying layer (6), described 2nd spraying layer (6) top is provided with mist eliminator (7), described housing (5) top is provided with air outlet (8), described first spraying layer (3) and the 2nd spraying layer (6) side are all connected with water pump (10) by pump line (9), described water pump (10) is arranged on cyclic water tank (11) and one end is connected by pump line (9).
2. a kind of coal gas desulfurization equipment according to claim 1, it is characterised in that, described first spraying layer (3) and the 2nd spraying layer (6) bottom are equipped with some spray headers.
3. a kind of coal gas desulfurization equipment according to claim 1, it is characterized in that, described rectification layer (2), spraying layer (3), voided layer packing layer (4), the 2nd spraying layer (6) are fixedly connected with housing (5) inwall with mist eliminator (7).
4. a kind of coal gas desulfurization equipment according to claim 1, it is characterised in that, described rectification layer (2) circle or square pipe are nonuniform mutation operator.
5. a kind of coal gas desulfurization equipment according to claim 1, it is characterised in that, described mist eliminator (7) is at least one layer.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620058114.6U CN205295260U (en) | 2016-01-21 | 2016-01-21 | Coal gas sweetener |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620058114.6U CN205295260U (en) | 2016-01-21 | 2016-01-21 | Coal gas sweetener |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205295260U true CN205295260U (en) | 2016-06-08 |
Family
ID=56429204
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620058114.6U Active CN205295260U (en) | 2016-01-21 | 2016-01-21 | Coal gas sweetener |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205295260U (en) |
-
2016
- 2016-01-21 CN CN201620058114.6U patent/CN205295260U/en active Active
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN107899394B (en) | Desulfurization dust collector based on rotatory spraying and spiral gas-liquid separation principle | |
| CN105289246A (en) | Method and device for washing and purifying ocean engineering power tail gas only through seawater | |
| CN104289095A (en) | Pre-washing absorption tower | |
| CN205295260U (en) | Coal gas sweetener | |
| CN104307314A (en) | Energy-saving washing tower | |
| CN209052641U (en) | For purifying the wash mill of biogas | |
| CN206688457U (en) | A kind of chemical emission processing unit | |
| CN205886545U (en) | Horizontal acid mist purification device | |
| CN205461706U (en) | Take exhaust treatment device of waste heat recovery function | |
| CN206355763U (en) | Funnel-cap type exhaust gas washing tower | |
| CN204853524U (en) | Desulfurizing dust remover | |
| CN107537268A (en) | A kind of new energy air cleaning unit | |
| CN106978218A (en) | A kind of flammable gas purifier for rice husk gasifying electricity generation | |
| CN205340541U (en) | Area sprays desulfurization cigarette tower of distributor | |
| CN208678681U (en) | A kind of flue gas condensing and dust removal integrated plant | |
| CN104874277A (en) | Environmental blade type tail gas treatment device | |
| CN206014781U (en) | A kind of petroleum sweetening device | |
| CN104857792A (en) | Tube array type tail gas environmental protection treatment device | |
| CN109233929A (en) | It is a kind of for purifying the wash mill and washing methods of biogas | |
| CN212068301U (en) | Waste gas desulfurization equipment for thermal power plant | |
| CN204051320U (en) | A kind of desulfurating dust-removing equipment | |
| CN213895423U (en) | Recycling device for smoke de-whitening condensed water | |
| CN205313080U (en) | Circulation hydrogen controlling means who uses in crude benzene hydrogenation production technology | |
| CN203382532U (en) | Novel horizontal tower injection type deoxidization device | |
| CN219603370U (en) | Novel stripping deamination tower combined with ultrasonic technology |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant |