CN205973860U - Waste liquid evaporating treatment system - Google Patents
Waste liquid evaporating treatment system Download PDFInfo
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- CN205973860U CN205973860U CN201620920681.8U CN201620920681U CN205973860U CN 205973860 U CN205973860 U CN 205973860U CN 201620920681 U CN201620920681 U CN 201620920681U CN 205973860 U CN205973860 U CN 205973860U
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Abstract
The utility model discloses a waste liquid evaporating treatment system, its structure is waste liquid inlet pipe connection waste liquid box, establish a magnetic level gauge and cooling water inner tube in the waste liquid box, cooling water inlet pipe connects the cooling water inner tube, union coupling cooling water outlet pipe in the cooling water, waste liquid pump is connected to waste liquid box's drain pipe, waste liquid pump's play water piping connection waste liquid evaporimeter, establish the 2nd magnetic level gauge on the waste liquid evaporimeter, establish the electroplax heat facility in the waste liquid evaporimeter, the bottom on carbon fiber absorption tower is connected to the outlet duct at waste liquid evaporimeter top, the bottom of solid recombination reaction tower is connected to the outlet duct at carbon fiber absorption tower top, the evacuation pipe is established at the top of solid recombination reaction tower. The utility model discloses an advantage: simple structure is effective, simple process, and convenient operation, safe and reliable, is economy suitable for, easily promotes, does not produce secondary pollution, HCFC in the gas that discharged the processing back 141b's concentration less than or equal to 500ppm, nitrogen dioxide's concentration less than or equal to 0.5ppm.
Description
Technical field
The utility model relates to waste liquid evaporation process system is and in particular to a kind of dinitrogen tetroxide spent liquor evaporation process
System.
Background technology
Dinitrogen tetroxide is one of most important propellant.Because being easier to be maintained at liquid, it is mainly used in
Composition can storing liquid propellant.(intercontinental missile allows at any time the liquid fuel intercontinental missile in early stage for the dinitrogen tetroxide
Transmitting, its propellant requires to store for a long time rather than fills temporarily) in be widely used, god of unusual strength's formula of the such as U.S. is intercontinental
Guided missile.Dinitrogen tetroxide can form double elements hypergolic propellants with many rocket fuels：Dinitrogen tetroxide/aerozine, four oxidations
Phenodiazine/uns-dimethylhydrazine, dinitrogen tetroxide/MMH etc..Modal combination is dinitrogen tetroxide/uns-dimethylhydrazine, the Soviet Union
The Long March 2 application of Proton Carrier Rocket and China is exactly this combination.U.S. god of unusual strength -3 carrier rocket
Use dinitrogen tetroxide/aerozine 50.
But dinitrogen tetroxide has very strong toxicity, major determinant respiratory tract.The suction initial stage only have slight eye and on exhale
Inhale road irritation, such as pharyngeal discomfort, dry cough etc..Constant hour Late-onset to more than ten hours or incubation period longer time
, uncomfortable in chest, respiratory distress, cough, cough up frothy sputum, cyanosis etc. in pulmonary edema, adult respiratory distress syndrome.Can complicated with pneumothorax and
Mediastinal emphysema.Pulmonary edema disappears and may occur in which Delayed onset bronchiolitis about two weeks after.And dinitrogen tetroxide spent liquor
Impact to environment is very big, has corrosivity, and corrosiveness increases with moisture and aggravates, and dinitrogen tetroxide can part point
Solve as nitrogen dioxide, the nitrogen oxides such as nitrogen dioxide can consumingly damage the ozone layer in the presence of ultraviolet, and destructive power is not low
In fluorine alkyl chloride.
Existing dinitrogen tetroxide spent liquor processing method is usually Production by Catalytic Combustion Process, and this method is difficult to control due to temperature
System, once temperature runaway, can cause catalyst life to shorten and inactivate, catalyst periodic replacement causes operating cost to improve, due to useless
The concentration of liquid is unstable, leads to catalysis burning very wayward, in addition reactor material is required strict, increases on the whole
The cost that disposes waste liquid.
Utility model content
The utility model proposes waste liquid evaporation process system, its purpose be intended to overcome prior art exists above-mentioned not
Foot, realizes processing the dinitrogen tetroxide spent liquor of variable concentrations, and does not form secondary pollution.
Technical solution of the present utility model：Waste liquid evaporation process system, its structure includes exhausted bath box, waste liquid evaporation
Device, carbon fiber absorption tower and solid compound reaction tower, wherein waste liquid feed tube connect exhausted bath box, and waste liquid feed tube sets the first electricity
Dynamic valve, sets the first magnetic double level gauge in exhausted bath box, equipped with pressure gauge and thermometer on exhausted bath box, set in cooling water in exhausted bath box
Pipe, cooling water inlet pipe connects the water inlet of cooling water inner tube, and the outlet of cooling water inner tube connects cooling water outlet pipe, cooling
Second electrodynamic valve is set on water water inlet pipe, the drain pipe of exhausted bath box connects waste drains pump, and the outlet pipe of waste drains pump connects liquid waste evaporator,
3rd electrodynamic valve is set on the outlet pipe of waste drains pump, liquid waste evaporator sets the second magnetic double level gauge, in liquid waste evaporator, set electricity
Disk thermal, equipped with pressure gauge and thermometer on liquid waste evaporator, the escape pipe at liquid waste evaporator top connects carbon fiber and absorbs
The bottom of tower, the escape pipe at liquid waste evaporator top sets the 4th electrodynamic valve, and equipped with setting pressure gauge on carbon fiber absorption tower, carbon is fine
Dimension absorbs the bottom of the escape pipe connection solid compound reaction tower of top of tower, equipped with pressure gauge, solid on solid compound reaction tower
The top of compound reaction tower sets evacuated tube.
Preferably, the top of described exhausted bath box connects one end of relief tube, and the other end of relief tube connects waste liquid evaporation
The escape pipe at device top, relief tube sets automatic decompression valve.
Preferably, the range of the first described magnetic double level gauge is 1200mm.
Preferably, the range of the second described magnetic double level gauge is 1500mm.
Preferably, described electroplax hot charging is equipped with three sets.
Advantage of the present utility model：Structure is simply effective, process is simple, easy to operate, safe and reliable, economic and practical, easily
In popularization, do not produce secondary pollution, after process, the gas of discharge meets discharge standard of air pollutants《GB16297-
1996》, less than or equal to 500ppm, the concentration of nitrogen dioxide is less than or equal to 0.5ppm to the concentration of HC emissions FC-141b.
Brief description
Fig. 1 is the structural representation of waste liquid evaporation process system.
The 1 of in figure be waste liquid feed tube, 2 be exhausted bath box, 3 be waste drains pump, 4 be liquid waste evaporator, 5 be carbon fiber absorb
Tower, 6 be solid compound reaction tower, 7 be evacuated tube, 8 be the first magnetic double level gauge, 9 be cooling water inlet pipe, 10 be cooling water
Inner tube, 11 be cooling water outlet pipe, 12 be relief tube, 13 be automatic decompression valve, 14 be the first electrodynamic valve, 15 be second electronic
Valve, 16 be the 3rd electrodynamic valve, 17 be the 4th electrodynamic valve, 18 be electroplax thermal, 19 be the second magnetic double level gauge.
Specific embodiment
With reference to embodiment and specific embodiment, this utility model is described in further detail.
As shown in figure 1, waste liquid evaporation process system, its structure includes exhausted bath box 2, liquid waste evaporator 4, carbon fiber absorption tower
5 and solid compound reaction tower 6, wherein waste liquid feed tube 1 connects exhausted bath box 2, and waste liquid feed tube 1 sets the first electrodynamic valve 14, gives up
Set the first magnetic double level gauge 8 in liquid case 2, equipped with pressure gauge and thermometer on exhausted bath box 2, in exhausted bath box 2, set cooling water inner tube
10, cooling water inlet pipe 9 connects the water inlet of cooling water inner tube 10, and the outlet of cooling water inner tube 10 connects cooling water outlet pipe
11, cooling water inlet pipe 9 sets the second electrodynamic valve 15, the drain pipe of exhausted bath box 2 connects waste drains pump 3, and the outlet pipe of waste drains pump 3 is even
Connect liquid waste evaporator 4, the outlet pipe of waste drains pump 3 sets the 3rd electrodynamic valve 16, liquid waste evaporator 4 sets the second magnetic double level gauge
19, set electroplax thermal 18 in liquid waste evaporator 4, equipped with pressure gauge and thermometer on liquid waste evaporator 4, liquid waste evaporator 4 pushes up
The escape pipe in portion connects the bottom on carbon fiber absorption tower 5, and the escape pipe at liquid waste evaporator 4 top sets the 4th electrodynamic valve 17, carbon
Equipped with setting pressure gauge on fiber absorption tower 5, the escape pipe at carbon fiber absorption tower 5 top connects the bottom of solid compound reaction tower 6,
Equipped with pressure gauge on solid compound reaction tower 6, the top of solid compound reaction tower 6 sets evacuated tube 7.
The top of described exhausted bath box 2 connects one end of relief tube 12, and the other end of relief tube 12 connects liquid waste evaporator 4
The escape pipe at top, relief tube 12 sets automatic decompression valve 13.
The range of the first described magnetic double level gauge 8 is 1200mm.
The range of the second described magnetic double level gauge 19 is 1500mm.
Described electroplax thermal 18 has three sets.
Above-described is only preferred implementation of the present utility model it is noted that ordinary skill for this area
For personnel, on the premise of creating design without departing from this utility model, some deformation can also be made and improve, these all belong to
In protection domain of the present utility model.
Claims (5)
1. waste liquid evaporation process system, its feature includes exhausted bath box (2), liquid waste evaporator (4), carbon fiber absorption tower (5) and consolidates
Bluk recombination reaction tower (6), wherein waste liquid feed tube (1) connect exhausted bath box (2), and waste liquid feed tube sets the first electrodynamic valve on (1)
(14), the first magnetic double level gauge (8), equipped with pressure gauge and thermometer on exhausted bath box (2), exhausted bath box (2) are set in exhausted bath box (2)
Inside set cooling water inner tube (10), cooling water inlet pipe (9) connects the water inlet of cooling water inner tube (10), cooling water inner tube (10)
Outlet connects cooling water outlet pipe (11), and cooling water inlet pipe (9) sets the second electrodynamic valve (15), exhausted bath box (2) go out liquid
Pipe connects waste drains pump (3), and the outlet pipe of waste drains pump (3) connects liquid waste evaporator (4), the outlet pipe of waste drains pump (3) sets the 3rd
Electrodynamic valve (16), liquid waste evaporator (4) sets the second magnetic double level gauge (19), and liquid waste evaporator sets electroplax thermal in (4)
(18), equipped with pressure gauge and thermometer on liquid waste evaporator (4), the escape pipe at liquid waste evaporator (4) top connects absorbing carbon fiber
Receive the bottom of tower (5), the escape pipe at liquid waste evaporator (4) top sets the 4th electrodynamic valve (17), carbon fiber absorption tower (5) are upper to be filled
Set pressure gauge, the escape pipe at carbon fiber absorption tower (5) top connects the bottom of solid compound reaction tower (6), solid is combined anti-
Answer equipped with pressure gauge on tower (6), the top of solid compound reaction tower (6) sets evacuated tube (7).
2. waste liquid evaporation process system as claimed in claim 1, is characterized in that the top of described exhausted bath box (2) connects pressure release
One end of pipe (12), the other end of relief tube (12) connects the escape pipe at liquid waste evaporator (4) top, relief tube (12) sets certainly
Dynamic relief valve (13).
3. waste liquid evaporation process system as claimed in claim 1, is characterized in that the amount of described the first magnetic double level gauge (8)
Journey is 1200mm.
4. waste liquid evaporation process system as claimed in claim 1, is characterized in that described the second magnetic double level gauge (19)
Range is 1500mm.
5. waste liquid evaporation process system as claimed in claim 1, is characterized in that described electroplax thermal (18) has three sets.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620920681.8U CN205973860U (en) | 2016-08-22 | 2016-08-22 | Waste liquid evaporating treatment system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620920681.8U CN205973860U (en) | 2016-08-22 | 2016-08-22 | Waste liquid evaporating treatment system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205973860U true CN205973860U (en) | 2017-02-22 |
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ID=58033843
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620920681.8U Active CN205973860U (en) | 2016-08-22 | 2016-08-22 | Waste liquid evaporating treatment system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205973860U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106765209A (en) * | 2017-03-03 | 2017-05-31 | 中国人民解放军63729部队 | The processing unit and method of a kind of dinitrogen tetroxide spent liquor |
-
2016
- 2016-08-22 CN CN201620920681.8U patent/CN205973860U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106765209A (en) * | 2017-03-03 | 2017-05-31 | 中国人民解放军63729部队 | The processing unit and method of a kind of dinitrogen tetroxide spent liquor |
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| GR01 | Patent grant |