CN203123780U - Novel ammonia absorption pot - Google Patents
Novel ammonia absorption pot Download PDFInfo
- Publication number
- CN203123780U CN203123780U CN 201320152032 CN201320152032U CN203123780U CN 203123780 U CN203123780 U CN 203123780U CN 201320152032 CN201320152032 CN 201320152032 CN 201320152032 U CN201320152032 U CN 201320152032U CN 203123780 U CN203123780 U CN 203123780U
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- China
- Prior art keywords
- tank body
- ammonia
- pipeline section
- heat exchanger
- exchanger tube
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Abstract
The utility model discloses a novel ammonia absorption pot, and relates to the technical field of gas absorbers. The novel ammonia absorption pot comprises a horizontal elliptical sealed pot body, an ammonia distribution pipe and heat exchange pipes, wherein gas outlet of the ammonia distribution pipe is inserted into the horizontal elliptical sealed pot body; air holes are uniformly formed in the pipe wall of the horizontal elliptical sealed pot body in which the ammonia distribution pipe is inserted; and the heat exchange pipes are positioned in the pot body, internally provided with cooling media, connected with external refrigerating equipment, and arranged in the transverse direction of the horizontal elliptical sealed pot body. The absorption pot has a relatively good ammonia absorbing effect, and can enable ammonia water to be high in concentration and be recyclable.
Description
Technical field
The utility model relates to the gas absorbing device technical field, relates in particular to a kind of novel ammonia tourie.
Background technology
Ammonia is a kind of inorganic compound, is the colourless gas that penetrating odor is arranged under the normal temperature, and is soluble in water, when ammonia is water-soluble, the amino molecule formation ammoniacal liquor that combines with hydrone, ammoniacal liquor can become ammonium ion and hydroxide ion by fraction electric power, so the existing alkalescent of ammoniacal liquor can make phenolphthalein solution redden.The main effect of ammonia is to make ammonium salt and nitrogenous fertilizer.In fields such as chemical industry and the desulfurization of non-ferrous metal metallurgy industry, denitration, dechlorinations, contain a large amount of ammonias in the exhaust gas discharged, if it is not effectively handled, will cause severe contamination to environment.Existing ammonia absorption plant adopts tank body to put into water mostly, the direct insertion of ammonia pipeline wherein absorbs, because ammonia is dissolved in a large amount of heat releases of water meeting, ammonia solubility diminished after the ammonia spirit temperature rose, the gained ammonia concn is lower, can not reclaim use, as the sewage disposal difficulty, also increase production cost.
The utility model content
Technical problem to be solved in the utility model provides a kind of novel ammonia tourie, and it is effective that described tourie has the ammonia of absorption, the characteristics that ammonia concn is high.
For solving the problems of the technologies described above, technical solution adopted in the utility model is: a kind of novel ammonia tourie, it is characterized in that comprising horizontal ellipse head tank body, ammonia distributor pipe and heat exchanger tube, described horizontal ellipse head tank body is inserted in the gas outlet of described ammonia distributor pipe, insert at the ammonia distributor pipe on the tube wall of described horizontal ellipse head tank body part and be furnished with air-vent uniformly, described heat exchanger tube is positioned at described tank body, be provided with cooling medium in the heat exchanger tube, heat exchanger tube is connected with the peripheral hardware refrigeration plant, and heat exchanger tube is arranged along the horizontal direction of described horizontal ellipse head tank body.
Preferably: described ammonia distributor pipe comprises first pipeline section and second pipeline section, described first pipeline section is fixedlyed connected with second pipeline section, the jar dolly of described first pipeline section and described horizontal ellipse head tank body is straight, described second pipeline section is parallel with the jar end of described horizontal ellipse head tank body, described second pipeline section is positioned at the bottom of described tank body, described second pipeline section is arranged along the horizontal direction of described tank body, and described second pipeline section is positioned at the centre of described tank body fore-and-aft direction.
Preferably: described heat exchanger tube is arranged in the both sides, front and back of described second pipeline section, and described heat exchanger tube is arranged along the horizontal direction of described tank body, and described heat exchanger tube is parallel with described tank body.
Preferably: the heat exchanger tube of both sides is respectively equipped with 8 before and after described second pipeline section.
The beneficial effect that adopts technique scheme to produce is: when using described tourie, in tourie, add absorption liquid, feed cooling medium in the heat exchanger tube, ammonia is fed in the ammonia distributor pipe, ammonia enters absorption liquid by the air-vent on the distributor pipe and is absorbed, and the absorption reaction liberated heat is passed to cooling medium by heat exchanger tube, has reduced the absorption liquid temperature, also further accelerate flowing of absorption liquid when ammonia enters absorption liquid from distributor pipe simultaneously, strengthened the heat exchange effect of heat exchanger tube.Therefore, use described tourie to absorb ammonia and have assimilation effect preferably, make that the concentration of ammoniacal liquor is higher, recyclable.
Description of drawings
Below in conjunction with the drawings and specific embodiments the utility model is described in further detail.
Fig. 1 is structural representation of the present utility model;
Fig. 2 be among Fig. 1 A-A to the sectional structure schematic diagram;
Wherein: 1, horizontal ellipse head tank body 2, heat exchanger tube 3, ammonia distributor pipe 31, first pipeline section 32, second pipeline section.
The specific embodiment
Shown in Fig. 1-2, a kind of novel ammonia tourie comprises horizontal ellipse head tank body 1, ammonia distributor pipe 3 and heat exchanger tube 2.Described horizontal ellipse head tank body 1 is inserted in the gas outlet of described ammonia distributor pipe 3, is furnished with air-vent uniformly on the tube wall of described horizontal ellipse head tank body 1 part of ammonia distributor pipe 3 insertions.Described heat exchanger tube 2 is positioned at described tank body, is provided with cooling medium in the heat exchanger tube, and heat exchanger tube is connected with the peripheral hardware refrigeration plant, and heat exchanger tube 2 is arranged along the horizontal direction of described horizontal ellipse head tank body 1.
Described ammonia distributor pipe 3 comprises first pipeline section 31 and second pipeline section 32, described first pipeline section 31 is fixedlyed connected with second pipeline section 32, described first pipeline section 31 is straight with the jar dolly of described horizontal ellipse head tank body 1, described second pipeline section 32 is parallel with the jar end of described horizontal ellipse head tank body 1, described second pipeline section is positioned at the bottom of described tank body, described second pipeline section 32 is arranged along the horizontal direction of described tank body, and described second pipeline section 32 is positioned at the centre of described tank body fore-and-aft direction.
In order to increase the ability that described tourie absorbs ammonia, described heat exchanger tube 2 is arranged in the both sides, front and back of described second pipeline section 32, and described heat exchanger tube 2 is arranged along the horizontal direction of described tank body, and described heat exchanger tube 2 is parallel with described tank body.The heat exchanger tube 2 of both sides, described second pipeline section, 32 front and back is respectively equipped with 8, and the radical of heat exchanger tube is not limited to above number, can arrange according to actual needs.
Horizontal oval tank body adopts alkali resistance corrosion steel to make, and at its two ellipsoidal head a considerable amount of heat exchanger tubes is installed, and two heat exchanger tubes adopt flange to be connected with the arc connecting pipe, are convenient to exchange inside heat pipe like this and clean.The quantity of heat exchanger tube and caliber can be selected as required.At the bottom of being parallel to after at the bottom of the ammonia distributor pipe is gone into jar by the pipe tip cutting jar, be with the corrosion resistant metal pipe of a great deal of aperture on the tube wall, ammonia enters absorption liquid via aperture and absorbs, and can promote flowing of absorption liquid simultaneously, strengthens the heat exchange between liquid and the heat exchanger tube.
When this tourie uses, absorption liquid will be added in the tourie, then ammonia is fed in the tourie by the ammonia distributor pipe, cooling medium carries out the energy transmission by heat exchanger tube inside with absorption liquid, absorption liquid in the jar is lowered the temperature, the flange exchange heat pipe that can open heat exchanger tube two when overhaul of the equipments cleans, to improve heat exchange efficiency.The utility model has the advantages that, easy to use, ammonia absorption efficiency height, easy access can obtain high concentration ammoniacal liquor, and is recyclable.
Used specific case herein principle of the present utility model and embodiment thereof are set forth, the explanation of above embodiment is just with helping understand method of the present utility model and core concept thereof.Should be pointed out that for the person of ordinary skill of the art, can also carry out some improvement and modification to the utility model under the prerequisite that does not break away from the utility model principle, these improvement and modification also fall in the protection domain of the utility model claim.
Claims (4)
1. novel ammonia tourie, it is characterized in that comprising horizontal ellipse head tank body (1), ammonia distributor pipe (3) and heat exchanger tube (2), described horizontal ellipse head tank body (1) is inserted in the gas outlet of described ammonia distributor pipe (3), on the tube wall of ammonia distributor pipe (3) the described horizontal ellipse head tank body of insertion (1) part, be furnished with air-vent uniformly, described heat exchanger tube (2) is positioned at described tank body, be provided with cooling medium in the heat exchanger tube, heat exchanger tube is connected with the peripheral hardware refrigeration plant, and heat exchanger tube (2) is arranged along the horizontal direction of described horizontal ellipse head tank body (1).
2. a kind of novel ammonia tourie according to claim 1, it is characterized in that described ammonia distributor pipe (3) comprises first pipeline section (31) and second pipeline section (32), described first pipeline section (31) is fixedlyed connected with second pipeline section (32), described first pipeline section (31) is straight with the jar dolly of described horizontal ellipse head tank body (1), described second pipeline section (32) is parallel with the jar end of described horizontal ellipse head tank body (1), described second pipeline section is positioned at the bottom of described tank body, described second pipeline section (32) is arranged along the horizontal direction of described tank body, and described second pipeline section (32) is positioned at the centre of described tank body fore-and-aft direction.
3. a kind of novel ammonia tourie according to claim 2, it is characterized in that described heat exchanger tube (2) is arranged in the both sides, front and back of described second pipeline section (32), described heat exchanger tube (2) is arranged along the horizontal direction of described tank body, and described heat exchanger tube (2) is parallel with described tank body.
4. a kind of novel ammonia tourie according to claim 3 is characterized in that the heat exchanger tube (2) of both sides, described second pipeline section (32) front and back is respectively equipped with 8.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201320152032 CN203123780U (en) | 2013-03-29 | 2013-03-29 | Novel ammonia absorption pot |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201320152032 CN203123780U (en) | 2013-03-29 | 2013-03-29 | Novel ammonia absorption pot |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203123780U true CN203123780U (en) | 2013-08-14 |
Family
ID=48931808
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201320152032 Expired - Lifetime CN203123780U (en) | 2013-03-29 | 2013-03-29 | Novel ammonia absorption pot |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203123780U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104190214A (en) * | 2014-09-17 | 2014-12-10 | 南京凯盛国际工程有限公司 | Ammonia gas absorbing device |
-
2013
- 2013-03-29 CN CN 201320152032 patent/CN203123780U/en not_active Expired - Lifetime
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104190214A (en) * | 2014-09-17 | 2014-12-10 | 南京凯盛国际工程有限公司 | Ammonia gas absorbing device |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CX01 | Expiry of patent term |
Granted publication date: 20130814 |
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| CX01 | Expiry of patent term |