CN203890080U - Device for separating volatile matters in wastewater - Google Patents
Device for separating volatile matters in wastewater Download PDFInfo
- Publication number
- CN203890080U CN203890080U CN201420291901.6U CN201420291901U CN203890080U CN 203890080 U CN203890080 U CN 203890080U CN 201420291901 U CN201420291901 U CN 201420291901U CN 203890080 U CN203890080 U CN 203890080U
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- China
- Prior art keywords
- separating barrel
- tube
- pipe
- waste water
- separation bucket
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- 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
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- Heat Treatment Of Water, Waste Water Or Sewage (AREA)
- Degasification And Air Bubble Elimination (AREA)
- Physical Water Treatments (AREA)
Abstract
The utility model discloses a device for separating volatile matters in wastewater. The device comprises a separation bucket of a sealed structure, wherein an air outlet tube which is internally communicated with the inside of the separation bucket is connected with the outer side of the top of the separation bucket; a feeding liquid tube, a discharge liquid tube, a steam inlet tube, a steam outlet tube and an air inlet tube which are internally communicated with the inside of the separation bucket are respectively connected with the outer side wall of the separation bucket; a blower is connected to one end far away from the separation bucket, of the air inlet tube; a draft fan is connected to one end far away from the separation bucket, of the air outlet tube; a gas-liquid separator which is in sealed connection with the inner side of the separation bucket is arranged inside the separation bucket; the gas-liquid separator is positioned above the feeding liquid tube and the air inlet tube; an aeration tube and a heating coil tube are further arranged inside the separation bucket; one end of the aeration tube is connected with the air inlet tube; one end of the heating coil tube is connected with the steam inlet tube; the other end of the heating coil tube is connected with the steam outlet tube. With the combination of two techniques, namely, hot method separation and blow-off separation, the device for separating volatile matters in wastewater is capable of relatively thoroughly separating volatile matters such as COD and hydrogen sulfide in wastewater.
Description
Technical field
The utility model relates to field of waste water treatment, relates in particular to volatile matter tripping device in a kind of waste water.
Background technology
The industries such as Sweet natural gas, Coal Chemical Industry and medicine, can produce a large amount of waste water in production process, these waste water mostly contain inorganics and a small amount of organism of high density, can adopt evaporative crystallization isolation technique to process and reclaim resource.But when evaporation concentration, volatile organic matter can evaporate together with water, not only can affect the quality that separates water, and may cause equipment corrosion, even causes life danger to operator.
Utility model content
Based on this, for the existing problem that volatile organic matter can evaporate together with water when the evaporation concentration, be necessary to propose the separated two kind technology separated with stripping of the hot method of a kind of combination, more thoroughly volatile matter tripping device in the waste water of the volatile matter such as the COD in separated waste water and hydrogen sulfide.
The technical solution of the utility model is: volatile matter tripping device in a kind of waste water, the separating barrel that comprises sealed structure, described separating barrel top outer is connected with the air outlet tube with its internal communication, the outer side wall of described separating barrel is connected with respectively the feeding liquid pipe with its internal communication, out-feed liquid pipe, enter vapour pipe, go out vapour pipe and blast pipe, described blast pipe is connected with gas blower away from one end of described separating barrel, described air outlet tube is connected with induced draft fan away from one end of described separating barrel, described separating barrel inside is provided with the gas-liquid separator being tightly connected with its inner side-wall, this gas-liquid separator is positioned at the top of feeding liquid pipe and blast pipe, described separating barrel inside is also provided with aeration tube and heating coil, wherein one end of described aeration tube is connected with blast pipe, one end of described heating coil with enter vapour pipe and be connected, the other end with go out vapour pipe and be connected.
Combination by the separated two kind technology separated with stripping of hot method, adds the use of gas-liquid separator, first by steam, waste water is heated, and isolates the volatile matter such as lightweight oil-containing, COD and hydrogen sulfide; Then by rousing as the mode of air, these materials are taken out of from air outlet tube.
Therein in an embodiment, described in enter vapour pipe and be provided with the first variable valve, described separating barrel outer side wall is also provided with the thermometer that detects separating barrel internal temperature, described the first variable valve is interlocked with described thermometer.The first variable valve and thermometer are used in conjunction with, and can effectively control the temperature of heating.
In an embodiment, described feeding liquid pipe is provided with the second variable valve therein, and described separating barrel outer side wall is also provided with the liquidometer that detects separating barrel inside liquid level, described the second variable valve and described liquidometer interlocking.Liquidometer and the second variable valve are used in conjunction with, and can effectively control liquid level.
In an embodiment, described separating barrel top outer is also provided with the tensimeter that detects separating barrel internal pressure therein.Manometric setting, can monitor the pressure in separating barrel.
In an embodiment, described separating barrel outer side wall is also provided with manhole therein.Arranging conveniently of manhole overhauled classification barrel inside.
The beneficial effects of the utility model are:
(1) utilize the combination of the separated two kind technology separated with stripping of hot method, effectively isolate the volatile matter in waste water, and can easily be discharged.
(2) by being used in conjunction with of thermometer, liquidometer and the first variable valve and the second variable valve, regulate easily the temperature of heating and the height of liquid level, guarantee separated effect.
Accompanying drawing explanation
Fig. 1 is the structural representation described in the utility model embodiment;
Description of reference numerals:
10, separating barrel, 20, air outlet tube, 30, feeding liquid pipe, 40, out-feed liquid pipe, 50, enter vapour pipe, 60, go out vapour pipe, 70, blast pipe, 80, gas blower, 90, induced draft fan, 100, gas-liquid separator, 110, aeration tube, 120, heating coil, 130, the first variable valve, 140, thermometer, the 150, second variable valve, 160, liquidometer, 170, tensimeter, 180, manhole.
Embodiment
Below in conjunction with accompanying drawing, embodiment of the present utility model is elaborated.
Embodiment:
As shown in Figure 1, volatile matter tripping device in a kind of waste water, the separating barrel 10 that comprises sealed structure, described separating barrel 10 top outer are connected with the air outlet tube 20 with its internal communication, the outer side wall of described separating barrel 10 is connected with respectively the feeding liquid pipe 30 with its internal communication, out-feed liquid pipe 40, enter vapour pipe 50, go out vapour pipe 60 and blast pipe 70, described blast pipe 70 is connected with gas blower 80 away from one end of described separating barrel 10, described air outlet tube 70 is connected with induced draft fan 90 away from one end of described separating barrel 10, described separating barrel 10 inside are provided with the gas-liquid separator 100 being tightly connected with its inner side-wall, this gas-liquid separator 100 is positioned at the top of feeding liquid pipe 30 and blast pipe 70, described separating barrel 10 inside are also provided with aeration tube 110 and heating coil 120, wherein one end of described aeration tube 110 is connected with blast pipe 70, one end of described heating coil 120 with enter vapour pipe 50 and be connected, the other end with go out vapour pipe 60 and be connected.
In the present embodiment, described in enter vapour pipe 50 and be provided with the first variable valve 130, described separating barrel 10 outer side walls are also provided with the thermometer 140 that detects separating barrel 10 internal temperatures, described the first variable valve 130 and described thermometer 140 interlockings.
In the present embodiment, described feeding liquid pipe 30 is provided with the second variable valve 150, and described separating barrel 10 outer side walls are also provided with the liquidometer 160 that detects separating barrel 10 inside liquid levels, described the second variable valve 150 and described liquidometer 160 interlockings.
In the present embodiment, described separating barrel 10 top outer are also provided with the tensimeter 170 that detects separating barrel 10 internal pressures.
In the present embodiment, described separating barrel 10 outer side walls are also provided with manhole 180.
When separated, waste water enters separating barrel 10 inside by feeding liquid pipe 30, and the liquid level of liquidometer 160 perception separating barrel 10 inside is controlled the second variable valve 150, thereby controls liquid level, makes it remain on the liquid level of standard.Then by entering vapour pipe 50, add steam, by steam, waste liquid is heated; In heat-processed, thermometer 140 perception separating barrel 10 internal temperatures, control temperature 90 ° of left and right by controlling the first variable valve 130, guarantee that waste water does not seethe with excitement.After waste water heating, isolate the volatile matter such as COD and hydrogen sulfide.By gas blower 80 and blast pipe 70, for separating barrel 10 inside, blast air, utilize the mode of air bubbling, allow bubble take volatile matter out of.Under the effect of induced draft fan 90, volatile matter flows towards the direction of air outlet tube 20, by gas-liquid separator 100, completely cuts off thoroughly the moisture in volatile matter, then by escape pipe 20, discharges.
The utility model utilizes the combination of the separated two kind technology separated with stripping of hot method, effectively isolates the volatile matter in waste water, and can easily be discharged; By being used in conjunction with of thermometer 140, liquidometer 160 and the first variable valve 130 and the second variable valve 150, regulate easily the temperature of heating and the height of liquid level, guarantee separated effect.
The above embodiment has only expressed embodiment of the present utility model, and it describes comparatively concrete and detailed, but can not therefore be interpreted as the restriction to the utility model the scope of the claims.It should be pointed out that for the person of ordinary skill of the art, without departing from the concept of the premise utility, can also make some distortion and improvement, these all belong to protection domain of the present utility model.
Claims (5)
1. volatile matter tripping device in a waste water, it is characterized in that, the separating barrel that comprises sealed structure, described separating barrel top outer is connected with the air outlet tube with its internal communication, the outer side wall of described separating barrel is connected with respectively the feeding liquid pipe with its internal communication, out-feed liquid pipe, enter vapour pipe, go out vapour pipe and blast pipe, described blast pipe is connected with gas blower away from one end of described separating barrel, described air outlet tube is connected with induced draft fan away from one end of described separating barrel, described separating barrel inside is provided with the gas-liquid separator being tightly connected with its inner side-wall, this gas-liquid separator is positioned at the top of feeding liquid pipe and blast pipe, described separating barrel inside is also provided with aeration tube and heating coil, wherein one end of described aeration tube is connected with blast pipe, one end of described heating coil with enter vapour pipe and be connected, the other end with go out vapour pipe and be connected.
2. volatile matter tripping device in waste water according to claim 1, it is characterized in that, describedly enter vapour pipe and be provided with the first variable valve, described separating barrel outer side wall is also provided with the thermometer that detects separating barrel internal temperature, and described the first variable valve is interlocked with described thermometer.
3. volatile matter tripping device in waste water according to claim 1 and 2, it is characterized in that, described feeding liquid pipe is provided with the second variable valve, and described separating barrel outer side wall is also provided with the liquidometer that detects separating barrel inside liquid level, described the second variable valve and described liquidometer interlocking.
4. volatile matter tripping device in waste water according to claim 1 and 2, is characterized in that, described separating barrel top outer is also provided with the tensimeter that detects separating barrel internal pressure.
5. volatile matter tripping device in waste water according to claim 1 and 2, is characterized in that, described separating barrel outer side wall is also provided with manhole.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420291901.6U CN203890080U (en) | 2014-06-04 | 2014-06-04 | Device for separating volatile matters in wastewater |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420291901.6U CN203890080U (en) | 2014-06-04 | 2014-06-04 | Device for separating volatile matters in wastewater |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203890080U true CN203890080U (en) | 2014-10-22 |
Family
ID=51716508
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420291901.6U Expired - Fee Related CN203890080U (en) | 2014-06-04 | 2014-06-04 | Device for separating volatile matters in wastewater |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203890080U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108217799A (en) * | 2018-01-24 | 2018-06-29 | 江苏新聚环保技术有限公司 | A kind of Toluene Wastewater hot blow desorption adsorption device |
| CN110937647A (en) * | 2019-12-04 | 2020-03-31 | 东莞市泰丰空调制冷设备有限公司 | Waste water recovery device for high-temperature gas condenser |
-
2014
- 2014-06-04 CN CN201420291901.6U patent/CN203890080U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108217799A (en) * | 2018-01-24 | 2018-06-29 | 江苏新聚环保技术有限公司 | A kind of Toluene Wastewater hot blow desorption adsorption device |
| CN110937647A (en) * | 2019-12-04 | 2020-03-31 | 东莞市泰丰空调制冷设备有限公司 | Waste water recovery device for high-temperature gas condenser |
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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 | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20141022 Termination date: 20200604 |