CN205294904U - Oil -water separator is used in organic matter production - Google Patents
Oil -water separator is used in organic matter production Download PDFInfo
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- CN205294904U CN205294904U CN201521019840.9U CN201521019840U CN205294904U CN 205294904 U CN205294904 U CN 205294904U CN 201521019840 U CN201521019840 U CN 201521019840U CN 205294904 U CN205294904 U CN 205294904U
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- mass flowmenter
- waste oil
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Abstract
The utility model discloses an oil -water separator is used in organic matter production, including reation kettle, its characterized in that still includes mass flow meter and control system, mass flow meter and reation kettle pass through the pipeline intercommunication, mass flow meter on still be connected with wastewater collection jar and waste oil collecting jar respectively through the pipeline, mass flow meter and wastewater collection jar between install first valve, mass flow meter and waste oil collecting jar between install the second valve, thereby the control system signal of receiving mass flow meter control first valve and second valve opening with the closure. The utility model discloses control system receives mass flow meter's signal, thereby controls opening of first valve and second valve and retrieve waste water and waste oil with closed making respectively in wastewater collection jar and the waste oil collecting jar, automatic control, and simply convenient, the recovery efficiency height is just distinguished effectually.
Description
Technical field
This utility model relates to a kind of Organic substance production oily-water seperating equipment.
Background technology
In existing production and processing, the oil water mixture of process units output, is often carelessly discharge, and so not only causes huge cost to waste, and oil water mixture also becomes industrial refuse contaminated environment, and environment causes permanent destruction. More existing enterprises are having tried to collection oil water mixture thus recycling, adopt collecting tank by after oil water mixture sufficient standing, density variation due to waste water and thick oil, water layer can rest on lower floor, thick oil is on upper strata, and then manually range estimation fluid and water discharge respectively, and this method does not simply fail to accurately difference fluid and water, and inefficiency, it is easy to maloperation causes reclaiming difficulty.
Utility model content
The purpose of this utility model is to overcome the deficiencies in the prior art, it is provided that a kind of oil water separator being automatically separated profit.
For realizing object above, this utility model is achieved through the following technical solutions:
Organic substance production oily-water seperating equipment, including reactor, it is characterized in that, also include mass flowmenter and control system, described mass flowmenter and reactor pass through pipeline communication, described mass flowmenter is connected to wastewater collection tank and waste oil collecting tank also by pipeline, first valve is installed between described mass flowmenter and wastewater collection tank, second valve is installed between described mass flowmenter and waste oil collecting tank, the signal of described control system quality of reception effusion meter is thus controlling unlatching and the Guan Bi of the first valve and the second valve.
In above-mentioned Organic substance production oily-water seperating equipment, described reactor being connected to liquidometer, described liquidometer is for monitoring the liquid level change in reactor.
In above-mentioned Organic substance production oily-water seperating equipment, described liquid level is calculated as glass plate liquidometer.
In above-mentioned Organic substance production oily-water seperating equipment, between described reactor and mass flowmenter, it is provided with discharging pump.
In above-mentioned Organic substance production oily-water seperating equipment, being provided with discharging pipeline visor between described reactor and discharging pump, described discharging pipeline visor is used for observing profit situation.
In above-mentioned Organic substance production oily-water seperating equipment, between described discharging pump and mass flowmenter, it is connected to Pressure gauge.
This utility model controls the signal of system quality of reception effusion meter, control the unlatching of the first valve and the second valve with Guan Bi so that wastewater collection tank and waste oil collecting tank are separately recovered waste water and waste oil, automatically controlling, simple and convenient, organic efficiency is high and distinguishes effective.
This utility model liquidometer is for monitoring the liquid level change in reactor, it is to avoid liquid level too high the causing in reactor, the accidents such as spilling occurred; Discharging pipeline visor is used for observing profit situation, it is possible to understand the material actual state in pipeline, switches at any time, make separating effect better between the collection of waste water and waste oil collecting.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
Number in the figure illustrates:
1, reactor; 2, mass flowmenter; 3, system is controlled; 4, wastewater collection tank; 5, waste oil collecting tank; 6, the first valve; 7, the second valve; 8, liquidometer; 9, discharging pump; 10, discharging pipeline visor; 11, Pressure gauge.
Detailed description of the invention
Below in conjunction with accompanying drawing, this utility model is described in detail.
As shown in Figure 1, Organic substance production oily-water seperating equipment includes reactor 1, including mass flowmenter 2 and control system 3, described mass flowmenter 2 passes through pipeline communication with reactor 1, described mass flowmenter 2 is connected to wastewater collection tank 4 and waste oil collecting tank 5 also by pipeline, first valve 6 is installed between described mass flowmenter 2 and wastewater collection tank 4, second valve 7 is installed between described mass flowmenter 2 and waste oil collecting tank 5, the signal of described control system 3 quality of reception effusion meter 2 is thus controlling unlatching and the Guan Bi of the first valve 6 and the second valve 7.
Discharging pump 9 it is provided with between reactor 1 and mass flowmenter 2. Owing to waste water density is between 0.99-1.00kg/ml, thick oil density is about between 0.70-0.80kg/ml, utilizing waste water and the density variation of thick oil, water layer density is higher, in lower floor after stratification, discharging pump 9 is started working, control system 3 controls the first valve 6 and opens, and the discharging of water layer elder generation is to wastewater collection tank 4, when mass flowmenter 2 detects density < 0.92kg/ml, discharging pump 9 is out of service, it is prevented that oil reservoir is driven in waste water tank; When oil reservoir builds up to yield, and when mass flowmenter 2 detects density < 0.92kg/ml, discharging pump 9 works again, and control system 3 controls the second valve 7 and opens, and thick oil is beaten to waste oil collecting tank 5. So, while utilizing mass flowmenter 2 to realize water layer, oil reservoir flow measurement, it is achieved that the automatic identification of oil-water separation, it is to avoid the generation of maloperation, also mitigate labor intensity simultaneously.
Being connected to glass plate liquidometer 8 on reactor 1, described glass plate liquidometer 8 is for monitoring the liquid level change in reactor 1, it is to avoid liquid level too high the causing in reactor 1, the accidents such as spilling occurred; Discharging pipeline visor 10 is used for observing profit delamination, it is possible to understand the material actual state in pipeline, switches at any time, make separating effect better between the collection of waste water and waste oil collecting; Being connected to Pressure gauge 11 between discharging pump 9 and mass flowmenter 2, Pressure gauge 11, for monitoring the fluid pressure of discharging pump 9 discharging, is that the liquid of discharging pump 9 output maintains in stable scope all the time, thus ensureing that separating effect is better.
This utility model controls the signal of system 3 quality of reception effusion meter 2, control the unlatching of the first valve 6 and the second valve 7 with Guan Bi so that wastewater collection tank 4 and waste oil collecting tank 5 are separately recovered waste water and waste oil, automatically controlling, simple and convenient, organic efficiency is high and distinguishes effective.
Embodiment in this utility model, only for this utility model is illustrated, is not intended that the restriction to right, those skilled in that art it is contemplated that other replacements being substantially equal to, all in this utility model protection domain.
Claims (5)
1. Organic substance production oily-water seperating equipment, including reactor, it is characterized in that, also include mass flowmenter and control system, described mass flowmenter and reactor pass through pipeline communication, described mass flowmenter is connected to wastewater collection tank and waste oil collecting tank also by pipeline, first valve is installed between described mass flowmenter and wastewater collection tank, second valve is installed between described mass flowmenter and waste oil collecting tank, the signal of described control system quality of reception effusion meter is thus controlling unlatching and the Guan Bi of the first valve and the second valve.
2. Organic substance production oily-water seperating equipment according to claim 1, it is characterised in that be connected to liquidometer on described reactor.
3. Organic substance production oily-water seperating equipment according to claim 1, it is characterised in that be provided with discharging pump between described reactor and mass flowmenter.
4. Organic substance production oily-water seperating equipment according to claim 3, it is characterised in that be provided with discharging pipeline visor between described reactor and discharging pump.
5. Organic substance production oily-water seperating equipment according to claim 3, it is characterised in that be connected to Pressure gauge between described discharging pump and mass flowmenter.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201521019840.9U CN205294904U (en) | 2015-12-09 | 2015-12-09 | Oil -water separator is used in organic matter production |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201521019840.9U CN205294904U (en) | 2015-12-09 | 2015-12-09 | Oil -water separator is used in organic matter production |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205294904U true CN205294904U (en) | 2016-06-08 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201521019840.9U Active CN205294904U (en) | 2015-12-09 | 2015-12-09 | Oil -water separator is used in organic matter production |
Country Status (1)
| Country | Link |
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| CN (1) | CN205294904U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107473360A (en) * | 2017-08-08 | 2017-12-15 | 武汉市园林建筑工程公司 | A kind of sewage disposal system |
| CN110152581A (en) * | 2019-05-15 | 2019-08-23 | 巴斯夫新材料有限公司 | Spent acid separation and processing system |
-
2015
- 2015-12-09 CN CN201521019840.9U patent/CN205294904U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107473360A (en) * | 2017-08-08 | 2017-12-15 | 武汉市园林建筑工程公司 | A kind of sewage disposal system |
| CN110152581A (en) * | 2019-05-15 | 2019-08-23 | 巴斯夫新材料有限公司 | Spent acid separation and processing system |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant |