CN205155542U - Modified torch gas divides fluid reservoir to press liquid system - Google Patents
Modified torch gas divides fluid reservoir to press liquid system Download PDFInfo
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- CN205155542U CN205155542U CN201520830876.9U CN201520830876U CN205155542U CN 205155542 U CN205155542 U CN 205155542U CN 201520830876 U CN201520830876 U CN 201520830876U CN 205155542 U CN205155542 U CN 205155542U
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- oil pump
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Abstract
The utility model provides a modified torch gas divides fluid reservoir to press liquid system, belongs to the chemical industry field. It changes oil pump inlet pipe and secret sump oil jar export pipeline at the bottom of the fluid reservoir and installs hydraulic tubing additional to divide torch gas, with torch gas divide in the fluid reservoir lime set through the new hydraulic tubing of adding after flowing into secret sump oil jar, fill nitrogen gas to the 0.4Mpa after with the sump oil jar, then lean on nitrogen pressure to press and retrieve to the sump oil tank field, has saved the branch fluid reservoir and has opened the pump and change oil, change the oil pump and save and to press oil safely, can also reach the using electricity wisely, practice thrift the purpose of investing.
Description
Technical field
The utility model relates to a kind of torch gas separatory tank pressure liquid system of improvement, belongs to chemical field.
Background technique
Former technique torch gas will open after dividing lime set in flow container many and be pumped to sump oil tank field, but separatory hand-dipping is few, and it is short and easily find time to open the pump time, has both taken electricity and has also been inconvenient to operate.
Summary of the invention
In view of the defect that prior art scheme exists, the utility model provides a kind of torch gas separatory tank pressure liquid system of improvement, and realize hydraulic fluid and need not open pump operated at any time, not only power saving but also safety, not easily find time.
The technological scheme that the utility model adopts is:
A kind of torch gas separatory tank pressure liquid system of improvement, comprise torch gas and divide flow container, divide at the bottom of flow container and turn oil pump, underground slop tank, sump oil tank field, divide at the bottom of flow container and turn oil pump inlet pipeline, divide at the bottom of flow container and turn fuel pump outlet pipeline, underground slop tank outlet conduit, first torch gas separatory tank bottom valve and underground slop tank outlet valve, torch gas divides flow container to turn oil pump by turning at the bottom of point flow container at the bottom of oil pump inlet pipeline connection point flow container, turn oil pump inlet pipeline at the bottom of point flow container and be provided with the first torch gas separatory tank bottom valve, turn fuel pump outlet pipeline one end at the bottom of point flow container to connect at the bottom of point flow container and turn oil pump, the other end is joined mutually with one end of underground slop tank outlet conduit and is connected to sump oil tank field, the other end of underground slop tank outlet conduit connects underground slop tank, underground slop tank outlet conduit is arranged underground slop tank outlet valve, it is characterized in that: also comprise hydraulic fluid pipeline, second torch gas separatory tank bottom valve, nitrogen gas delivery-line, nitrogen generation device, oil pump inlet pipeline is turned at the bottom of described hydraulic fluid pipeline one end connection point flow container, the other end connects underground slop tank outlet conduit, second torch gas separatory tank bottom valve is arranged on hydraulic fluid pipeline divides flow container one end near torch gas, connection underground, nitrogen gas delivery-line one end slop tank, the other end connects nitrogen generation device, and nitrogen gas delivery-line is provided with nitrogen gas control valve.
When described nitrogen pressure is 0.4MPa, openly descend slop tank outlet valve.
The torch separatory tank pressure liquid method improved, newly add a hydraulic fluid pipeline squeeze pump arrival line is connected with underground slop tank egress line, lime set in flow container is first divided by torch gas to be certainly depressed into underground slop tank during hydraulic fluid, then nitrogen is adopted to reclaim being depressed into sump oil tank field after the slop tank pressurising of underground, turn oil without the need to a point flow container and open pump, reach using electricity wisely, reduce investment and the object of handling safety, only flare system need be divided and turn oil pump inlet line and underground slop tank egress line at the bottom of flow container and install cross-line additional and can realize.Described process modification is: divided by torch gas and turn oil pump inlet line at the bottom of flow container and underground slop tank egress line installs hydraulic tubing additional, lime set is divided by torch gas in flow container to flow automatically after the slop tank of underground by newly adding hydraulic tubing, after slop tank inflated with nitrogen to 0.4Mpa, be then depressed into sump oil tank field by nitrogen pressure and reclaim.
After adopting said method, there is following beneficial effect compared with art methods: divided by torch gas lime set in flow container to be certainly depressed into underground slop tank, then be depressed into slop tank after adopting nitrogen pressurising to reclaim, save a point flow container open pump turn oil, turn oil pump can save and do not design or existing another using of moving away, can safe force feed, the object of using electricity wisely, investment reduction can also be reached.
Accompanying drawing explanation
Fig. 1 is the flow chart of torch separatory tank pressure oil technique;
In figure: 1, the second torch gas separatory tank bottom valve, 2, hydraulic fluid pipeline, 3, underground slop tank outlet valve, 4, turn oil pump 5, underground slop tank, the 6, first torch gas separatory tank bottom valve at the bottom of point flow container, 7, nitrogen gas delivery-line, 8, underground slop tank outlet conduit, 9, turn oil pump inlet pipeline at the bottom of point flow container, 10, nitrogen gas control valve, 11, flow container is divided, 12, sump oil tank field.
Embodiment
In order to understand the force feed processing line of this improvement further, be described as follows below in conjunction with accompanying drawing.
A kind of torch gas separatory tank pressure liquid system of improvement, comprise torch gas and divide flow container, divide at the bottom of flow container and turn oil pump, underground slop tank, sump oil tank field, divide at the bottom of flow container and turn oil pump inlet pipeline, divide at the bottom of flow container and turn fuel pump outlet pipeline, underground slop tank outlet conduit, first torch gas separatory tank bottom valve and underground slop tank outlet valve, torch gas divides flow container to turn oil pump by turning at the bottom of point flow container at the bottom of oil pump inlet pipeline connection point flow container, turn oil pump inlet pipeline at the bottom of point flow container and be provided with the first torch gas separatory tank bottom valve, turn fuel pump outlet pipeline one end at the bottom of point flow container to connect at the bottom of point flow container and turn oil pump, the other end is joined mutually with one end of underground slop tank outlet conduit and is connected to sump oil tank field, the other end of underground slop tank outlet conduit connects underground slop tank, underground slop tank outlet conduit is arranged underground slop tank outlet valve, it is characterized in that: also comprise hydraulic fluid pipeline, second torch gas separatory tank bottom valve, nitrogen gas delivery-line, nitrogen generation device, oil pump inlet pipeline is turned at the bottom of described hydraulic fluid pipeline one end connection point flow container, the other end connects underground slop tank outlet conduit, second torch gas separatory tank bottom valve is arranged on hydraulic fluid pipeline divides flow container one end near torch gas, connection underground, nitrogen gas delivery-line one end slop tank, the other end connects nitrogen generation device, and nitrogen gas delivery-line is provided with nitrogen gas control valve.
Torch gas is divided and turns oil pump inlet pipeline at the bottom of flow container and underground slop tank outlet conduit installs hydraulic tubing additional, lime set is divided by torch gas in flow container to flow automatically after the slop tank of underground by newly adding hydraulic tubing, after slop tank inflated with nitrogen to 0.4Mpa, be then depressed into sump oil tank field by nitrogen pressure and reclaim.
During hydraulic fluid, torch gas is divided at the bottom of flow container pump, inlet valve closes, will divide in flow container lime set from being depressed into underground slop tank, and being depressed into slop tank recovery after then adopting nitrogen pressurising, the safe force feed of energy, can also reach the useful object opening using electricity wisely, investment reduction.
Claims (2)
1. the torch gas separatory tank pressure liquid system improved, comprise torch gas and divide flow container, divide at the bottom of flow container and turn oil pump, underground slop tank, sump oil tank field, divide at the bottom of flow container and turn oil pump inlet pipeline, divide at the bottom of flow container and turn fuel pump outlet pipeline, underground slop tank outlet conduit, first torch gas separatory tank bottom valve and underground slop tank outlet valve, torch gas divides flow container to turn oil pump by turning at the bottom of point flow container at the bottom of oil pump inlet pipeline connection point flow container, turn oil pump inlet pipeline at the bottom of point flow container and be provided with the first torch gas separatory tank bottom valve, turn fuel pump outlet pipeline one end at the bottom of point flow container to connect at the bottom of point flow container and turn oil pump, the other end is joined mutually with one end of underground slop tank outlet conduit and is connected to sump oil tank field, the other end of underground slop tank outlet conduit connects underground slop tank, underground slop tank outlet conduit is arranged underground slop tank outlet valve, it is characterized in that: also comprise hydraulic fluid pipeline, second torch gas separatory tank bottom valve, nitrogen gas delivery-line, nitrogen generation device, oil pump inlet pipeline is turned at the bottom of described hydraulic fluid pipeline one end connection point flow container, the other end connects underground slop tank outlet conduit, second torch gas separatory tank bottom valve is arranged on hydraulic fluid pipeline divides flow container one end near torch gas, connection underground, nitrogen gas delivery-line one end slop tank, the other end connects nitrogen generation device, and nitrogen gas delivery-line is provided with nitrogen gas control valve.
2. the torch gas separatory tank pressure liquid system of a kind of improvement according to claim 1, is characterized in that: when described nitrogen pressure is 0.4MPa, openly descends slop tank outlet valve.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520830876.9U CN205155542U (en) | 2015-10-26 | 2015-10-26 | Modified torch gas divides fluid reservoir to press liquid system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520830876.9U CN205155542U (en) | 2015-10-26 | 2015-10-26 | Modified torch gas divides fluid reservoir to press liquid system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205155542U true CN205155542U (en) | 2016-04-13 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201520830876.9U Active CN205155542U (en) | 2015-10-26 | 2015-10-26 | Modified torch gas divides fluid reservoir to press liquid system |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105732318A (en) * | 2016-04-25 | 2016-07-06 | 张家港市华昌新材料科技有限公司 | Method for treating condensate of flare gas accident liquid separation tank |
| CN113581669A (en) * | 2021-08-27 | 2021-11-02 | 陕煤集团榆林化学有限责任公司 | Underground solid heavy dirty oil tank and solid heavy dirty oil delivery method |
-
2015
- 2015-10-26 CN CN201520830876.9U patent/CN205155542U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105732318A (en) * | 2016-04-25 | 2016-07-06 | 张家港市华昌新材料科技有限公司 | Method for treating condensate of flare gas accident liquid separation tank |
| CN113581669A (en) * | 2021-08-27 | 2021-11-02 | 陕煤集团榆林化学有限责任公司 | Underground solid heavy dirty oil tank and solid heavy dirty oil delivery method |
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