CN202927949U - Concentrated sulfuric acid and water heating device - Google Patents
Concentrated sulfuric acid and water heating device Download PDFInfo
- Publication number
- CN202927949U CN202927949U CN2012206049056U CN201220604905U CN202927949U CN 202927949 U CN202927949 U CN 202927949U CN 2012206049056 U CN2012206049056 U CN 2012206049056U CN 201220604905 U CN201220604905 U CN 201220604905U CN 202927949 U CN202927949 U CN 202927949U
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- CN
- China
- Prior art keywords
- water
- sulfuric acid
- concentrated sulfuric
- heat energy
- reative cell
- 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
- 238000010438 heat treatment Methods 0.000 title claims abstract description 35
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 34
- QAOWNCQODCNURD-UHFFFAOYSA-N sulfuric acid Substances OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 title abstract description 23
- 238000006243 chemical reaction Methods 0.000 claims abstract description 32
- 239000002253 acid Substances 0.000 claims abstract description 20
- 238000003860 storage Methods 0.000 claims abstract description 19
- 238000005183 dynamical system Methods 0.000 claims description 9
- FWFGVMYFCODZRD-UHFFFAOYSA-N oxidanium;hydrogen sulfate Chemical compound O.OS(O)(=O)=O FWFGVMYFCODZRD-UHFFFAOYSA-N 0.000 claims description 9
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims description 6
- 239000010453 quartz Substances 0.000 claims description 6
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N silicon dioxide Inorganic materials O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 6
- 239000000203 mixture Substances 0.000 claims description 4
- 229910052742 iron Inorganic materials 0.000 claims description 3
- 230000000694 effects Effects 0.000 abstract description 3
- 239000002912 waste gas Substances 0.000 abstract description 3
- 239000002994 raw material Substances 0.000 abstract description 2
- 238000000034 method Methods 0.000 description 6
- 239000000446 fuel Substances 0.000 description 5
- 239000012153 distilled water Substances 0.000 description 4
- 239000007789 gas Substances 0.000 description 4
- 230000005540 biological transmission Effects 0.000 description 3
- 239000008236 heating water Substances 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- 239000000853 adhesive Substances 0.000 description 2
- 230000001070 adhesive effect Effects 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 239000011521 glass Substances 0.000 description 2
- 230000006698 induction Effects 0.000 description 2
- 239000004570 mortar (masonry) Substances 0.000 description 2
- 150000004965 peroxy acids Chemical class 0.000 description 2
- 230000009466 transformation Effects 0.000 description 2
- 238000009835 boiling Methods 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 230000000069 prophylactic effect Effects 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 239000013535 sea water Substances 0.000 description 1
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- Heat Treatment Of Water, Waste Water Or Sewage (AREA)
Abstract
The utility model discloses a concentrated sulfuric acid and water heating device, which comprises a water storage room, an acid storage room, a solution storage room, a circulating system I, a reaction room, a heat energy conversion system, a power system, a steam output pipe, a circulating system II and a waste gas processor, wherein the water storage room and the acid storage room are connected with the reaction room through the circulating system I; the reaction room is arranged in the heat energy conversion system; the heat energy conversion system is connected with the power system and a heating device through the steam output pipe; the reactor room is communicated with the solution storage room through the circulating system II; the waste gas processor is arranged on the solution storage room; and the heat energy is conveyed into steam by heating mediums such as water by utilizing a large amount of heat generated when the water is added into the concentrated sulfuric acid, so that the heating effect is realized. The device is simple in structure, is easy to operate, is capable of realizing circulating utilization of raw materials, and the environmental-protection no-pollution heating effect is achieved.
Description
Technical field
The utility model relates to a kind of concentrated sulfuric acid-water heating equipment, utilizes water to add the media such as sulfuric acid heat production heating water and the Novel heating equipment made, belongs to the heating technology field.
Background technology
Along with the development of society, heating equipment has also had corresponding raising, but, the reason such as environmental high low due to the fuel thermal energy conversion efficiency, and heating system is in a kind of status of embarrassment always.And along with people for the pursuit of high-quality life and the day by day raising of environmental protection consciousness, the heating and environment between contradiction more outstanding, develop new heating system, find suitable alternate resources to become a hot issue.
Summary of the invention
The utility model purpose is to provide a kind of concentrated sulfuric acid-water heating equipment, this equipment is low take cost, distilled water and the concentrated sulfuric acid that easily obtain are " fuel ", the media such as heating water by the transmission of conveyance conduit, are realized the Novel heating equipment of environment friendly and pollution-free heating.
the utility model concentrated sulfuric acid-water heating equipment comprises reservoir chamber 1, acid store room 2, solution storage chamber 3, circulatory system I 4, reative cell 5, heat energy conversion system 6, dynamical system 7, steam output pipe 8, circulatory system II 9, exhaust processor 10, reservoir chamber 1 is connected with acid store room and is connected with reative cell 5 by circulatory system I 4, reative cell 5 is arranged in heat energy conversion system 6, heat energy conversion system 6 is connected with heating system with dynamical system 7 by steam output pipe 8 and is connected, reative cell 5 is communicated with solution storage chamber 3 by circulatory system II 9, exhaust processor 10 is arranged on solution storage chamber 3, exhaust processor 10 is to reveal contaminated environment for a little waste gas in solution after prophylactic response.
Described in the utility modelly wrap up iron on the outer wall of reative cell 5, to improve reative cell intensity.
Heat energy conversion system 6 described in the utility model is the high strength boiler, water is housed in boiler the heat energy of sour water reaction generation is converted into the heat energy of steam.
Be provided with water inlet 11, sour entrance 12, mixture export 13 on reative cell 5 described in the utility model, reactor wall is quartz layer 14.
Reative cell described in the utility model is mainly used in the heat release that contacts sour and water, the concentrated sulfuric acid has strong corrosivity, and emit a large amount of heat when reacting with water, therefore, reative cell should have corrosion-resistant, resistant to elevated temperatures resistance concurrently, consider to quantize to produce recommendation glass, quartz, acid resistant adhesive mortar, pottery etc.
The special container that acid store room 2 is comprised of acid-resistant and anti-high-temperature (glass, quartz, acid resistant adhesive mortar, pottery or other acid-resistant and anti-high-temperature materials).
Reative cell described in the utility model is base unit, several reative cells are placed in heat energy conversion system 6---high strength boiler, are water in boiler, and the heat that reative cell produces is through reaction chamber wall transmission feedwater, the water generation steam that is heated, most of steam is as heating.
The part steam that the utility model device produces is as the power resources of dynamical system, by the conversion of plant equipment, is the kinetic energy of machine with the kinetic transformation of water vapour, thereby provides power for the processes such as conveying of heating equipment fuel etc.
In the utility model, circulatory system I 4 is acid and the induction system of water before reaction, and the concentrated sulfuric acid and water arrive reative cell by deposit chamber separately through the conveying of peracid pump, water pump, and the concentrated sulfuric acid is in the reative cell bottom, and distilled water process injector is sprayed onto concentrated sulfuric acid surface; Circulatory system II 9 is in order to carry reacted solution, and reacted solution is transported to solution storage chamber (the passage in transit cooling is processed) through conduit, and apotheca is provided with exhaust-gas treatment facilities, can effectively absorb the harmful substances such as acid gas in hot acid solution.
The present invention is much bigger according to concentrated sulfuric acid density ratio water, directly adds the entry meeting in the concentrated sulfuric acid and makes water float over the sulfuric acid surface, a large amount of heat releases and make the mixed liquor boiling.For a long time, this operating process is listed in the taboo in chemical experiment always, and still very important is the huge heat that produces in this process.The heat that produces when the present invention utilizes and mixes, the steam that heating water is obtained etc. is carried by pipeline, transferring heat, thus reach heating effect.And mixed dilute sulfuric acid can utilize the clean energy resource such as solar energy again concentrated, thereby realizes the cleaning with the recycling of energy.
Advantage of the present utility model is as follows: for traditional heating system, the utlity model has simple in structure, easy to operate, do not need coal or the expensive electric power of high pollution to act as a fuel, but the distilled water (can utilize solar energy evaporation seawater to obtain) to be simple and easy to obtain, the concentrated sulfuric acid of relatively easily producing is raw material, and the most important be reacted dilute sulfuric acid can utilize solar energy to evaporate wherein moisture obtains the concentrated sulfuric acid again.
Description of drawings
Fig. 1 is the utility model heating equipment structural representation;
Fig. 2 is reaction chamber structure schematic diagram in the utility model heating equipment;
In figure: the 1st, reservoir chamber; The 2nd, acid store room; The 3rd, solution storage chamber; The 4th, circulatory system I; The 5th, reative cell; The 6th, heat energy conversion system; The 7th, dynamical system; The 8th, steam output pipe, the 9th, circulatory system II, the 10th, exhaust processor, the 11st, water inlet; The 12nd, sour entrance; The 13rd, mixture export, the 14th, quartz layer, the 15th, heating system.
The specific embodiment
Below by drawings and Examples, the utility model is described in further detail, but protection domain of the present utility model is not limited to described content.
the utility model concentrated sulfuric acid-water heating equipment comprises reservoir chamber 1, acid store room 2, solution storage chamber 3, circulatory system I4, reative cell 5, heat energy conversion system 6, dynamical system 7, steam output pipe 8, circulatory system II9, exhaust processor 10, reservoir chamber 1 is connected with acid store room and is connected with reative cell 5 by circulatory system I 4, heat energy conversion system 6 is arranged on outside reative cell 5, heat energy conversion system 6 is connected with heating system with dynamical system 7 by steam output pipe 8 and is connected, reative cell 5 is communicated with solution storage chamber 3 by circulatory system II 9, exhaust processor 10 is arranged on solution storage chamber 3, wherein be provided with water inlet 11, sour entrance 12, mixture export 13 on reative cell 5, reaction chamber wall is quartz layer 14, and heat energy conversion system 6 is the high strength boiler, wraps up iron on the outer wall of reative cell 5.
Reative cell described in the utility model is base unit, several reative cells are placed in heat energy conversion system 6---high strength boiler, are water in boiler, and the heat that reative cell produces is through reaction chamber wall transmission feedwater, the water generation steam that is heated, most of steam is as heating.
The part steam that the utility model device produces is as the power resources of dynamical system 7, by the conversion of plant equipment, is the kinetic energy of machine with the kinetic transformation of water vapour, thereby provides power for the processes such as conveying of heating equipment fuel etc.
In the utility model, circulatory system I 4 is acid and the induction system of water before reaction, and the concentrated sulfuric acid and water arrive reative cell by deposit chamber separately through the conveying of peracid pump, water pump, and the concentrated sulfuric acid is in the reative cell bottom, and distilled water process injector is sprayed onto concentrated sulfuric acid surface; Circulatory system II 9 is in order to react the conveying of rear solution, and reacted solution is transported to solution storage chamber (the passage in transit cooling is processed) through pump, and apotheca is provided with exhaust-gas treatment facilities, can effectively absorb the harmful substances such as acid gas in hot acid solution.
Claims (4)
1. the concentrated sulfuric acid-water heating equipment is characterized in that: it comprise reservoir chamber (1), acid store room (2), solution storage chamber (3),
circulatory system I(4), reative cell (5), heat energy conversion system (6), dynamical system (7), steam output pipe (8), circulatory system II(9), exhaust processor (10), reservoir chamber (1) is connected 2 with acid store room) by circulatory system I(4) be connected with reative cell (5), reative cell (5) is arranged in heat energy conversion system (6), heat energy conversion system (6) is connected with heating system with dynamical system (7) by steam output pipe (8), reative cell (5) is by circulatory system II(9) be communicated with solution storage chamber (3), exhaust processor (10) is arranged on solution storage chamber (3).
2. the concentrated sulfuric acid-water heating equipment according to claim 1, is characterized in that: wrap up iron on the outer wall of reative cell (5).
3. the concentrated sulfuric acid-water heating equipment according to claim 1, it is characterized in that: heat energy conversion system (6) is the high strength boiler, and water is housed in boiler.
4. the concentrated sulfuric acid-water heating equipment according to claim 1, it is characterized in that: be provided with water inlet (11), sour entrance (12), mixture export (13) on reative cell (5), reaction chamber wall is quartz layer (14).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2012206049056U CN202927949U (en) | 2012-11-16 | 2012-11-16 | Concentrated sulfuric acid and water heating device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2012206049056U CN202927949U (en) | 2012-11-16 | 2012-11-16 | Concentrated sulfuric acid and water heating device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202927949U true CN202927949U (en) | 2013-05-08 |
Family
ID=48217904
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2012206049056U Expired - Fee Related CN202927949U (en) | 2012-11-16 | 2012-11-16 | Concentrated sulfuric acid and water heating device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202927949U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN117403080A (en) * | 2023-12-14 | 2024-01-16 | 中核内蒙古矿业有限公司 | Multistage adjustable heating system used in tank |
-
2012
- 2012-11-16 CN CN2012206049056U patent/CN202927949U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN117403080A (en) * | 2023-12-14 | 2024-01-16 | 中核内蒙古矿业有限公司 | Multistage adjustable heating system used in tank |
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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 |
Granted publication date: 20130508 Termination date: 20141116 |
|
| EXPY | Termination of patent right or utility model |