CN204607791U - A kind of enthalpy difference compensation purification dilatation vaporizer - Google Patents
A kind of enthalpy difference compensation purification dilatation vaporizer Download PDFInfo
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- CN204607791U CN204607791U CN201520272996.1U CN201520272996U CN204607791U CN 204607791 U CN204607791 U CN 204607791U CN 201520272996 U CN201520272996 U CN 201520272996U CN 204607791 U CN204607791 U CN 204607791U
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- dilatation
- tank
- purification
- compensation
- static pressure
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Abstract
A kind of enthalpy difference described in the utility model compensation purification dilatation vaporizer, the adsorption filtration tank comprising dilatation static pressure tank and be connected with dilatation static pressure tank, the sidewall of described dilatation static pressure tank is provided with high temperature water inlet, compensates steam-in, air outlet and leakage fluid dram; The sidewall of described adsorption filtration tank is provided with the inlet mouth that arrange corresponding to described air outlet, and for discharging the vapour outlet of the rear gas of purification, the air outlet of described dilatation static pressure tank is connected with the inlet mouth of described adsorption filtration tank.The utility model carries out collection filtration treatment by dilatation static pressure tank and adsorption filtration tank to hot industry waste water, and by the compensation steam-in be arranged on dilatation static pressure tank, further temperature compensation is carried out to trade effluent, all to be vaporized by hot wastewater and to reach pressure and the quality requirements of use.
Description
Technical field
The utility model relates to carburettor technology field, is specifically related to a kind of enthalpy difference compensation purification dilatation vaporizer.
Background technology
Along with developing rapidly of industry, kind and the quantity of waste water rapidly increase, also increasingly extensive and serious to the pollution of water body, threaten the health and safety of the mankind.Therefore, for protection of the environment, the process of trade effluent is more even more important than the process of municipal effluent.Trade effluent is in the technological process of iron and steel, chemical industry and generating, and its water temperature is higher, most of boiler wastewater at about 200 degree, as waste water directly discharged the pollution that not only can cause the waste of the energy but also environment can be caused.In order to the recycling of waste water, in wastewater discharge process, the normal retrieving arrangement that adopts reclaims at present, this device just reclaims waste water mainly through tank body, prevents the evaporation of hot wastewater from causing waste, and the steam formed by the heat of waste water self carries out filtration recycling to waste water.Adopt the equipment that this device reclaims waste water residual heat, in waste heat recovery operation, not only cost recovery is higher for it, and waste heat recovery rate is lower, and heat taste is not enough and cannot utilize, and its foreign matter content of waste water after collection and treatment is higher, can not directly use.
Utility model content
The technical problems to be solved in the utility model is to provide a kind of enthalpy difference compensation purification dilatation vaporizer, this melting tank can carry out enthalpy difference compensation to trade effluent, realize waste water all to reclaim, gaseous state separation is carried out to the impurity in waste water simultaneously, improve steam quality and heat taste.
For solving the problems of the technologies described above, the utility model by the following technical solutions:
A kind of enthalpy difference compensation purification dilatation vaporizer, the adsorption filtration tank comprising dilatation static pressure tank and be connected with dilatation static pressure tank, the sidewall of described dilatation static pressure tank is provided with high temperature water inlet, compensates steam-in, air outlet and leakage fluid dram; The sidewall of described adsorption filtration tank is provided with the inlet mouth that arrange corresponding to described air outlet, and for discharging the vapour outlet of the rear gas of purification, the air outlet of described dilatation static pressure tank is connected with the inlet mouth of described adsorption filtration tank.
Described dilatation static pressure tank is the tank body of arranged transversely, feet is provided with in the bottom of tank body, described leakage fluid dram is positioned at the downside of tank body, and described high temperature water inlet and compensation steam-in are positioned at left surface or the right flank of tank body, and described air outlet is positioned at the upper side of tank body.
Described adsorption filtration tank is the tank body of arranged transversely, and this tank body is positioned at the top of described dilatation static pressure tank, and described inlet mouth is positioned at the downside of tank body, and described vapour outlet is positioned at the upper side of tank body.
Horizontally disposed absorption filter element is along its length provided with in described adsorption filtration tank, outer shape and the tank body inner shape of described absorption filter element match, described absorption filter element and adsorption filtration tank are formed fit closely, the length of described absorption filter element is less than the length of described adsorption filtration tank inner chamber, described inlet mouth is positioned on the tank wall of absorption filter element overlay area, and described vapour outlet is positioned on the tank wall outside absorption filter element overlay area.
Described inlet mouth is at least two.
Described absorption filter element is that amino nano composite material is made.
The inside of described dilatation static pressure tank is provided with multiplely blocks filtering net.
The described filtering net that blocks along the distribution of tank body inner side-wall length direction indention, described in block the edge of filtering net and tank body inner side-wall fits tightly.
Also comprise monitoring device, described monitoring device comprises automatic monitoring instrument, and is connected with automatic monitoring instrument and is arranged on the flow transmitter of the upper side of adsorption filtration tank, temperature sensor and pressure and send depressor.
The end of described water inlet is also provided with strainer.
The beneficial effects of the utility model are: enthalpy difference described in the utility model compensation purification dilatation vaporizer, by dilatation static pressure tank and adsorption filtration tank, collection filtration treatment is carried out to hot industry water, and by the compensation steam-in be arranged on dilatation static pressure tank, further temperature compensation is carried out to process water, make it whole vaporization, improve the utilization taste of waste heat and the quality of steam.This vaporizer by the strainer on dilatation static pressure tank, block filtering net, and the filtration core arranged in adsorption filtration tank carries out three grades of purification filterings to process water, can remove to greatest extent solid impurity contained in water and salinity and filter and absorption, further increase the quality of steam water.
Accompanying drawing explanation
Fig. 1 is the structural representation of the utility model enthalpy difference compensation purification dilatation vaporizer;
Fig. 2 is the skeleton view of the utility model enthalpy difference compensation purification dilatation vaporizer.
Embodiment
Below in conjunction with accompanying drawing, the utility model will be further described.
As shown in Figure 1 and Figure 2, enthalpy difference described in the present embodiment compensation purification dilatation vaporizer, the adsorption filtration tank 2 comprising dilatation static pressure tank 1 and be connected with dilatation static pressure tank 1, dilatation static pressure tank 1 and adsorption filtration tank 2 are the tank body of arranged transversely, this tank body is by the cylindrical shell of both ends open, and being arranged on the cover composition at housing two ends, cover and housing to be interfixed the space that formation one seals by flange, and the tank body of this structure detachably facilitates and cleans dirt in tank.Adsorption filtration tank 2 is arranged on the top of dilatation static tube 1, is provided with high temperature water inlet 11, compensates steam-in 12, be provided with air outlet 13, be provided with leakage fluid dram 14 on the downside of it in the upside of dilatation static tube 1 at the right flank of dilatation static tube 1.The lower wall of adsorption filtration tank 2 is provided with the inlet mouth 21 that arrange corresponding to air outlet 13, its upper side wall is provided with vapour outlet 22, this vapour outlet 22 is for discharging the rear gas of purification, and the air outlet 13 of dilatation static pressure tank 1 is connected with the inlet mouth 21 of adsorption filtration tank 2.
Be provided with strainer 6 at high temperature water inlet 11 place of dilatation static pressure tank 1 end, this strainer 6 first can carry out single filter to high-temperature water, and in the impurity inflow dilatation static pressure tank 1 preventing high-temperature water Middle molecule larger, filtering net 15 is blocked in betting contest.Have in the inside of dilatation static pressure tank 1 and multiplely block filtering net 15, this blocks filtering net 15 along the distribution of tank body inner side-wall length direction indention, and the edge and the tank body inner side-wall that block filtering net 15 fit tightly, the good secondary filter of formation stopping property.
Horizontally disposed absorption filter element 23 is along its length provided with in adsorption filtration tank 2, outer shape and adsorption filtration tank 2 cavity shape of this absorption filter element 23 match, can be formed with adsorption filtration tank 2 to make absorption filter element 23 and fit closely, the length of absorption filter element 23 is less than the length of adsorption filtration tank 2 tank inner chamber, make that there is in adsorption filtration tank 2 space holding and filter rear gas, in order to reach good filter effect, this inlet mouth 21 is positioned on the tank wall of absorption filter element 23 overlay area, vapour outlet 22 is positioned on the tank wall outside absorption filter element 23 overlay area, absorption filter element 23 can carry out three-stage filtration to hot industry water.Make for amino nanometer conforms to material at the present embodiment absorption filter element 23, this filter core can bring up to 97% to Phosphate Adsorption rate.In order to enable the gas in dilatation static pressure tank 1 enter absorption filter element 23 inner filtration faster, the effect supporting adsorption filtration tank 23 can be played again simultaneously, this inlet mouth 21 can be set to two, three or more, have precedence over two in the present embodiment.Conveniently adsorption filtration tank 2 is connected with other devices, is also provided with Link Port 25 for subsequent use at adsorption filtration tank 2 upper side.
Conveniently detect the vaporization situation of high-temperature water in tank body, vaporizer described in the utility model is also provided with monitoring device, monitoring device is automatic monitoring instrument 41, flow transmitter 42 is provided with at the upper side of adsorption filtration tank 2, temperature sensor 43 and pressure send depressor 44, this flow transmitter 42, temperature sensor 43 and pressure send depressor 44 to be connected with automatic monitoring instrument 41, by flow and the temperature of gas in automatic monitoring instrument 41 regulating tank, to ensure that in tank, high-temperature water vaporization completely, flow transmitter 42 in the present embodiment, temperature sensor 43 and pressure send depressor 44 to be two.
Treating processes: hot industry water enters in dilatation static pressure tank 1 after carrying out single filter by high temperature water inlet 11, compensation steam is entered in tank body by compensation steam-in 12 and carries out temperature compensation to hot industry water simultaneously, liquid in dilatation static pressure tank 1 by after high-temperature evaporation and through in tank two-stage filter filter after enter in adsorption filtration tank 2, steam in adsorption filtration tank 2 carries out three-stage filtration through absorption filter element 23, and the steam after filtration is flowed out by vapour outlet 22.Regulated by the flow of the steam in automatic monitoring instrument 44 pairs of adsorption filtration tanks 2 and temperature, to ensure the complete of vaporescence in this process.
Above-described embodiment is only be described preferred implementation of the present utility model; not scope of the present utility model is limited; under the prerequisite not departing from the utility model design spirit; the various distortion that those of ordinary skill in the art make the technical solution of the utility model and improvement, all should fall in protection domain that the utility model claims determine.
Claims (10)
1. enthalpy difference compensation purification dilatation vaporizer, it is characterized in that: the adsorption filtration tank (2) comprising dilatation static pressure tank (1) and be connected with dilatation static pressure tank (1), the sidewall of described dilatation static pressure tank (1) is provided with high temperature water inlet (11), compensates steam-in (12), air outlet (13) and leakage fluid dram (14); The sidewall of described adsorption filtration tank (2) is provided with the inlet mouth (21) that arrange corresponding to described air outlet (13), and for discharging the vapour outlet (22) of the rear gas of purification, the air outlet (13) of described dilatation static pressure tank (1) is connected with the inlet mouth (21) of described adsorption filtration tank (2).
2. enthalpy difference according to claim 1 compensation purification dilatation vaporizer, it is characterized in that: the tank body that described dilatation static pressure tank (1) is arranged transversely, feet (3) is provided with in the bottom of tank body, described leakage fluid dram (14) is positioned at the downside of tank body, described high temperature water inlet (11) and compensation steam-in (12) are positioned at left surface or the right flank of tank body, and described air outlet (13) are positioned at the upper side of tank body.
3. enthalpy difference according to claim 1 compensation purification dilatation vaporizer, it is characterized in that: the tank body that described adsorption filtration tank (2) is arranged transversely, this tank body is positioned at the top of described dilatation static pressure tank (1), described inlet mouth (21) is positioned at the downside of tank body, and described vapour outlet (22) is positioned at the upper side of tank body.
4. enthalpy difference according to claim 1 compensation purification dilatation vaporizer, it is characterized in that: in described adsorption filtration tank (2), be provided with horizontally disposed absorption filter element (23) along its length, outer shape and the tank body inner shape of described absorption filter element (23) match, described absorption filter element (23) and adsorption filtration tank (2) are formed fit closely, the length of described absorption filter element (23) is less than the length of described adsorption filtration tank (2) tank inner chamber, described inlet mouth (21) is positioned on the tank wall of absorption filter element (23) overlay area, described vapour outlet (22) is positioned on the tank wall outside absorption filter element (23) overlay area.
5. enthalpy difference according to claim 4 compensation purification dilatation vaporizer, is characterized in that: described inlet mouth (21) is at least two.
6. enthalpy difference according to claim 4 compensation purification dilatation vaporizer, is characterized in that: described absorption filter element (23) is made for amino nano composite material.
7. enthalpy difference according to claim 1 compensation purification dilatation vaporizer, is characterized in that: the inside of described dilatation static pressure tank (1) is provided with multiplely blocks filtering net (15).
8. enthalpy difference according to claim 7 compensation purification dilatation vaporizer, is characterized in that: described in block filtering net (15) along the distribution of tank body inner side-wall length direction indention, described in block the edge of filtering net (15) and tank body inner side-wall fits tightly.
9. enthalpy difference according to claim 1 compensation purification dilatation vaporizer, it is characterized in that: also comprise monitoring device, described monitoring device comprises automatic monitoring instrument (41), and is connected with automatic monitoring instrument (41) and is arranged on the flow transmitter (42) of the upper side of adsorption filtration tank (2), temperature sensor (43) and pressure and send depressor (44).
10. enthalpy difference according to claim 1 compensation purification dilatation vaporizer, is characterized in that: the end of described water inlet (11) is also provided with strainer (6).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520272996.1U CN204607791U (en) | 2015-04-30 | 2015-04-30 | A kind of enthalpy difference compensation purification dilatation vaporizer |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520272996.1U CN204607791U (en) | 2015-04-30 | 2015-04-30 | A kind of enthalpy difference compensation purification dilatation vaporizer |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204607791U true CN204607791U (en) | 2015-09-02 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520272996.1U Expired - Fee Related CN204607791U (en) | 2015-04-30 | 2015-04-30 | A kind of enthalpy difference compensation purification dilatation vaporizer |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204607791U (en) |
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2015
- 2015-04-30 CN CN201520272996.1U patent/CN204607791U/en not_active Expired - Fee Related
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| Date | Code | Title | Description |
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| 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: 20150902 Termination date: 20210430 |
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| CF01 | Termination of patent right due to non-payment of annual fee |