CN205323240U - Dispose adjustable evaporation plant who charges machine - Google Patents
Dispose adjustable evaporation plant who charges machine Download PDFInfo
- Publication number
- CN205323240U CN205323240U CN201521144045.2U CN201521144045U CN205323240U CN 205323240 U CN205323240 U CN 205323240U CN 201521144045 U CN201521144045 U CN 201521144045U CN 205323240 U CN205323240 U CN 205323240U
- Authority
- CN
- China
- Prior art keywords
- ammonia
- chamber
- evaporating
- evaporating column
- electrodialysis
- 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 discloses a dispose adjustable evaporation plant who charges machine, including ammonia evaporating column, ammonia collection device, steam boiler, there are two reacting chambers the inside of ammonia evaporating column, and the left side reacting chamber is the electrodialysis reacting chamber, and the reacting chamber on right side is the evaporating chamber, pass through the pipe connection between electrodialysis reacting chamber and the evaporating chamber, evaporating chamber left and right sides lower extreme is equipped with the agitator, and the steam conduit is installed to the right side upper end inside the evaporating chamber, installs the toper collection chamber in the middle of the ammonia evaporating column, the air exhauster that links to each other with drying device is installed to the positive centre of collection chamber, installs the pipeline at the evaporating column top and is connected with ammonia collection device's lower extreme. The utility model discloses simple structure, convenient and practical utilizes vapor to provide the heat to the ammonia evaporating column, can improve the availability factor of water, sets up the agitator inside the evaporating chamber, can mix the aqueous ammonia, is favorable to the evaporation of ammonia, and drying device's use has reduced the vapor in the ammonia, has improved the purity of ammonia.
Description
Technical field
This utility model relates to ammonia evaporation technique field, is specially a kind of vaporising device configuring adjustable charger。
Background technology
It is that ammonia is warming up to 130～150 DEG C that traditional ammonia prepares the method for ammonia, thus the ammonia component in ammonia and water component together being evaporated。This system is owing to having evaporated the substantial amounts of moisture that system is useless, thus causing that operation energy consumption is very high, econmics comparison is poor, and the ammonia purity collected is relatively low。
Utility model content
The purpose of this utility model is in that to provide a kind of vaporising device configuring adjustable charger, with the problem solving to propose in above-mentioned background technology。
For achieving the above object, this utility model provides following technical scheme: a kind of vaporising device configuring adjustable charger, including ammonia evaporating column, device for collecting ammonia gas, steam boiler, there are two reative cells the inside of described ammonia evaporating column, left side reative cell is electrodialysis reative cell, the reative cell on right side is vaporization chamber, connected by pipeline between described electrodialysis reative cell and vaporization chamber, inlet valve is had in the upper right side of electrodialysis reative cell, lower end, the described vaporization chamber left and right sides is provided with agitator, in vaporization chamber lower end, part is provided with drainage arrangement on the right side, and upper end is provided with jet chimney on the right side of evaporation chamber, one end of described jet chimney is connected to the upper end of steam boiler, on the right side of other end traverse ammonia evaporating column, bottom is connected with the upper end, left side of water purification retracting device, taper collection chamber is installed in the middle of ammonia evaporating column, the upper end, middle of described collection chamber is provided with the air exhauster being connected with drying device, the pipeline having the lower end with device for collecting ammonia gas to be connected in the middle of evaporating column top is installed。
Preferably, the place that described jet chimney is connected with steam boiler is provided with control valve。
Preferably, it is provided with water pump in the centre of pipeline。
Compared with prior art, the beneficial effects of the utility model are: this utility model simple in construction, convenient and practical, utilize electrolysis can remove other impurity in ammonia, steam is utilized to provide heat to ammonia evaporating column, the service efficiency of water can be improved, agitator is set in evaporating column bottom, it is possible to stir ammonia, ammonia is made to be heated evenly, be conducive to the evaporation of ammonia, drying device be set in a device and can remove the steam in ammonia, it is possible to improve the purity of ammonia。
Accompanying drawing explanation
Fig. 1 is this utility model structural representation。
In figure: 1 steam boiler, 2 ammonia evaporating columns, 21 electrodialysis reative cells, 22 vaporization chambers, 3 drying devices, 4 device for collecting ammonia gas, 5 air exhausters, 6 agitators, 7 drainage arrangements, 8 jet chimneys, 9 control valve, 10 taper collection chambers, 11 water purification retracting devices, 12 pipelines。
Detailed description of the invention
Below in conjunction with the accompanying drawing in this utility model embodiment, the technical scheme in this utility model embodiment is clearly and completely described, it is clear that described embodiment is only a part of embodiment of this utility model, rather than whole embodiments。Based on the embodiment in this utility model, the every other embodiment that those of ordinary skill in the art obtain under not making creative work premise, broadly fall into the scope of this utility model protection。
Refer to Fig. 1, this utility model provides a kind of technical scheme: a kind of vaporising device configuring adjustable charger, including ammonia evaporating column 2, device for collecting ammonia gas 4, steam boiler 1, there are two reative cells the inside of described ammonia evaporating column 2, left side reative cell is electrodialysis reative cell 21, the reative cell on right side is vaporization chamber 22, connected by pipeline 12 between described electrodialysis reative cell 21 and vaporization chamber 22, the middle of described pipeline 12 is provided with water pump, water pump provides circulation power for the ammonia circulation in evaporating column 2, lower end, described vaporization chamber 22 left and right sides is provided with agitator 6, in vaporization chamber 22 lower end, part is provided with drainage arrangement 7 on the right side, and in vaporization chamber 22 inner right side upper end, jet chimney 8 is installed, one end of described jet chimney 8 is connected to the upper end of steam boiler 1, on the right side of other end traverse ammonia evaporating column 2, bottom is connected with the upper end, left side of water purification retracting device 11, and the place that jet chimney 8 steam boiler connects is provided with control valve 9, control valve 9 and can control the flow velocity of steam in pipeline, in the middle of ammonia evaporating column 2, taper collection chamber 10 is installed, taper collection chamber is conducive to the air exhauster extraction to ammonia, more ammonia can be made to enter in drying device 3, the middle of described collection chamber 10 is provided with the air exhauster 5 being connected with drying device 3, air exhauster 5 can improve the speed of the collection of ammonia, thus the time of economy system gas collection, evaporating column crown center is provided with the discharge duct that the lower end with device for collecting ammonia gas is connected。
Operation principle: mixing ammonia initially enters the electrodialysis reative cell 21 within evaporating column, electrodialysis reative cell 21 can remove the metal ion contained in mixed solution, thus the impurity reduced in ammonia, electrodialysis terminates to utilize water pump that the ammonia after electrodialysis is delivered to vaporization chamber 22 afterwards, vaporization chamber 22 utilizes steam to control the temperature of ammonia, so that ammonia evaporation, the ammonia of evaporation can enter in taper collection chamber 10, ammonia in taper collection chamber 10 is pumped in exsiccator 3 by air exhauster 5, drying through exsiccator 3, steam greatly reduces, ammonia pipeline on evaporating column 2 is directly entered in device for collecting ammonia gas 4。
While there has been shown and described that embodiment of the present utility model, for the ordinary skill in the art, being appreciated that when without departing from principle of the present utility model and spirit and these embodiments can be carried out multiple change, amendment, replacement and modification, scope of the present utility model is defined by the appended claims and the equivalents thereof。
Claims (3)
1. the vaporising device configuring adjustable charger, including ammonia evaporating column (2), device for collecting ammonia gas (4), steam boiler (1), it is characterized in that: there are two reative cells the inside of described ammonia evaporating column (2), left side reative cell is electrodialysis reative cell (21), the reative cell on right side is vaporization chamber (22), connected by pipeline (12) between described electrodialysis reative cell (21) and vaporization chamber (22), inlet valve is had in the upper right side of electrodialysis reative cell (21), vaporization chamber (22) lower end, the left and right sides is provided with agitator (6), in vaporization chamber (22) lower end, part is provided with drainage arrangement (7) on the right side, and in vaporization chamber (22) inner right side upper end, jet chimney (8) is installed, one end of described jet chimney (8) is connected to the upper end of steam boiler (1), the other end is connected through bottom, ammonia evaporating column (2) right side with the upper end, left side of water purification retracting device (11), in the middle of ammonia evaporating column (2), taper collection chamber (10) is installed, collection chamber (10) connects electrodialysis reative cell (21) and (22) two air chambers of vaporization chamber, the middle, upper end of described collection chamber (10) is provided with the air exhauster (5) being connected with drying device (3), the intermediate course of described drying device (3) is placed with soda lime, evaporating column (2) crown center is provided with the pipeline that the lower end with device for collecting ammonia gas (4) is connected。
2. a kind of vaporising device configuring adjustable charger according to claim 1, it is characterised in that: the place that described jet chimney (8) steam boiler connects is provided with control valve (9)。
3. a kind of vaporising device configuring adjustable charger according to claim 1, it is characterised in that: the centre of described pipeline (12) is provided with water pump。
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201521144045.2U CN205323240U (en) | 2015-12-31 | 2015-12-31 | Dispose adjustable evaporation plant who charges machine |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201521144045.2U CN205323240U (en) | 2015-12-31 | 2015-12-31 | Dispose adjustable evaporation plant who charges machine |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205323240U true CN205323240U (en) | 2016-06-22 |
Family
ID=56209844
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201521144045.2U Expired - Fee Related CN205323240U (en) | 2015-12-31 | 2015-12-31 | Dispose adjustable evaporation plant who charges machine |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205323240U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111356879A (en) * | 2017-09-20 | 2020-06-30 | 德隆奇电器单一股东有限责任公司 | Boiler |
-
2015
- 2015-12-31 CN CN201521144045.2U patent/CN205323240U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111356879A (en) * | 2017-09-20 | 2020-06-30 | 德隆奇电器单一股东有限责任公司 | Boiler |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN107792909A (en) | A kind of dope drying system that desulfurization wastewater is concentrated using fume afterheat | |
| CN107098414A (en) | A kind of the low-temperature evaporation device and its discharge technology of the discharge for the treatment of of Power desulfurization wastewater | |
| CN105967253A (en) | Evaporation process and device of desulfurized wastewater cooling tower | |
| CN205323240U (en) | Dispose adjustable evaporation plant who charges machine | |
| CN201473332U (en) | Ammonium sulfate concentration device | |
| CN207468238U (en) | A kind of high efficiency refractory wastewater vaporising device | |
| CN205002365U (en) | Energy -saving and environment -friendly boiler | |
| CN103523763B (en) | A kind of energy saver and method of rapid concentration of dilute phosphoric acid | |
| CN110272082A (en) | Desulfurization wastewater evaporative crystallization couples flue gas reheat integral system | |
| CN202116399U (en) | Sewage disposal facility for production of rare earth materials | |
| CN205527834U (en) | Hybrid desulfurization waste water flue gas evaporative concentration device | |
| CN210796075U (en) | Desulfurization wastewater treatment system | |
| CN202961916U (en) | Calcium lactate concentration device | |
| CN204063983U (en) | The retracting device of a kind of fume afterheat and water | |
| CN103341274B (en) | In heat-engine plant wet desulfurization fume, moisture reclaims and gypsum rain controlling device and method | |
| CN204434413U (en) | Desulphurization system is containing sodium salt wastewater treatment equipment | |
| CN203017787U (en) | Combined type single-effect concentrator | |
| CN202595101U (en) | Swill grease primary refining device | |
| CN102491285A (en) | Waste sulphuric acid concentrating and recycling equipment | |
| CN205940201U (en) | High -efficient power steam hot water apparatus for producing | |
| CN207142871U (en) | Wet desulphurization wastewater zero discharge evaporation and crystallization system | |
| CN205299478U (en) | General vapour condensate water waste heat recovery device | |
| CN205164181U (en) | Crystal system is evaporated in succession to multiple -effect | |
| CN206288996U (en) | A kind of multistage continuous aeration processing unit of dichloromethane waste water | |
| CN205856359U (en) | A kind of NMP in working procedure of coating lithium ion cell recycle device |
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: 20160622 Termination date: 20171231 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |