CN203906206U - Carbon dioxide booster pump skid - Google Patents
Carbon dioxide booster pump skid Download PDFInfo
- Publication number
- CN203906206U CN203906206U CN201420324307.2U CN201420324307U CN203906206U CN 203906206 U CN203906206 U CN 203906206U CN 201420324307 U CN201420324307 U CN 201420324307U CN 203906206 U CN203906206 U CN 203906206U
- Authority
- CN
- China
- Prior art keywords
- carbon dioxide
- liquid
- booster pump
- sledge
- gas
- Prior art date
- 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 - Lifetime
Links
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 title claims abstract description 139
- 229910002092 carbon dioxide Inorganic materials 0.000 title claims abstract description 69
- 239000001569 carbon dioxide Substances 0.000 title claims abstract description 69
- 239000007791 liquid phase Substances 0.000 claims abstract description 41
- 239000007788 liquid Substances 0.000 claims abstract description 40
- 239000012071 phase Substances 0.000 claims abstract description 22
- 239000007789 gas Substances 0.000 claims description 21
- 238000010992 reflux Methods 0.000 claims description 15
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 12
- 238000001816 cooling Methods 0.000 claims description 9
- 230000008676 import Effects 0.000 claims description 7
- 239000007792 gaseous phase Substances 0.000 claims description 6
- 238000007664 blowing Methods 0.000 claims description 3
- 238000006073 displacement reaction Methods 0.000 claims description 3
- 230000008901 benefit Effects 0.000 abstract description 2
- 238000005516 engineering process Methods 0.000 description 4
- 230000006378 damage Effects 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 2
- 241000790917 Dioxys <bee> Species 0.000 description 1
- 208000027418 Wounds and injury Diseases 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- 235000011089 carbon dioxide Nutrition 0.000 description 1
- 239000013043 chemical agent Substances 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 239000005431 greenhouse gas Substances 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 208000014674 injury Diseases 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 239000003129 oil well Substances 0.000 description 1
- 230000035699 permeability Effects 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000009834 vaporization Methods 0.000 description 1
- 230000008016 vaporization Effects 0.000 description 1
Landscapes
- Details Of Reciprocating Pumps (AREA)
Abstract
The utility model relates to a carbon dioxide booster pump skid which comprises a bottom skid body, a gas and liquid separator, a carbon dioxide booster pump, a liquid phase inlet end, a gas phase inlet end, a liquid phase outlet end and a gas phase outlet end. The gas and liquid separator and the carbon dioxide booster pump are arranged on the upper portion of the bottom skid body and are fixedly connected with the bottom skid body, the liquid phase inlet end and the gas phase inlet end are arranged at the front end of the bottom skid body, and the liquid phase outlet end and the gas phase outlet end are arranged at the rear end of the bottom skid body. The carbon dioxide booster pump skid has the advantages that carbon dioxide can be pressurized, the probability that liquid carbon dioxide is gasified after pressure is reduced is greatly reduced, a large amount of liquid carbon dioxide can be provided for a fracturing truck, and needs of the fracturing truck are met.
Description
Technical field
The utility model relates to the anhydrous pressure break oil field of carbon dioxide, relates in particular to a kind of carbon dioxide booster pump sledge.
Background technique
So-called hydrofracturing method refers to that the high pressure water that is mixed with sandstone and chemical substance is injected to oil well breaks through rammell, discharges shale gas.For being low-permeability oilfield, unconventional oil-gas reservoir volume increase, the effect of hydraulic fracturing technology is obvious to all.But the harm of fracturing also should not be underestimated.
Each hydraulic crushing needs millions of tons water, and for China such Yi Ge lack of water big country, the great lot of water resources expending in its fracturing process is quite surprising.Although what a large amount of chemical agents that add in fracturing fluid injected is deep formation, can not cause direct pollution to underground water, in the long run, still has potential hazard.After fracturing finishes, return discharge opeing processing bad, also can cause rugged environment to pollute.At present, fracturing is controversial in a plurality of countries, and French Government has even been promulgated ban to it.
And than traditional hydraulic fracturing technology, there are not the problems referred to above in the anhydrous pressure break of carbon dioxide.It has following advantage:
Without water, can not cause water-sensitive, water blocking damage to reservoir, side by side alleviated the pressure to environment and water resources;
Without residue, can not cause residue injury to reservoir and supporting crack permeability;
Energy increasing function, after earth pressure release, dioxy carbon gas expansion, can realize the row of returning rapidly;
Carbon injects reservoir, realizes greenhouse gases recycling.
Carbon dioxide supercharging equipment is the nucleus equipment of the anhydrous fracturing work of carbon dioxide.In the anhydrous fracturing work of carbon dioxide, carbon dioxide supercharging equipment can carry out pressurize and pressurization to liquid carbon dioxide, reduce pressure surge feed flow not enough, avoid pressure drop to produce dry ice, carbon dioxide that can separation of vaporization is also discharged, for fracturing unit truck provides the liquid carbon dioxide of large discharge capacity, meet the needs of fracturing unit truck.
In sum, the future develop of carbon dioxide supercharging equipment is boundless.But current carbon dioxide supercharging equipment is main dependence on import also, and its core technology is grasped and monopolized by offshore company, and price is high, delivery date is long.
Model utility content
Technical problem to be solved in the utility model is to provide a kind of carbon dioxide booster pump sledge, solves the deficiencies in the prior art.
The technological scheme that the utility model solves the problems of the technologies described above is as follows: a kind of carbon dioxide booster pump sledge, comprises end sledge, gas-liquid separator, carbon dioxide booster pump, liquid phase entrance point, gas phase entrance point, liquid-phase outlet end, gaseous phase outlet end; Described gas-liquid separator is all arranged at the top of sledge of the described end and is all fixedly connected with sledge of the described end with carbon dioxide booster pump; Described liquid phase entrance point and gas phase entrance point are arranged at the front end of sledge of the described end, and described liquid-phase outlet end and gas phase outlet end are arranged at the rear end of sledge of the described end; Between the import on described liquid phase entrance point and described gas-liquid separator top, by collector, be connected; Between the liquid outlet of described gas-liquid separator and the suction side of described carbon dioxide booster pump, by the first pipeline, be connected; Between the liquid outlet of described carbon dioxide booster pump and described liquid-phase outlet end, by the second pipeline, be connected and on described the second pipeline, be provided with successively flowmeter, one-way valve, liquid phase expulsion valve; Between described gas phase entrance point and described gaseous phase outlet end, by gas phase pipeline, be connected, and be provided with ball valve on described gas phase pipeline; Also be included as described carbon dioxide booster pump the power system of power is provided, described power system is arranged at the rear end of sledge of the described end; Described power system comprises motor, transfer case, engine-cooling system; Described engine-cooling system adopts blowing type vertical water loose, and described engine-cooling system is arranged at the front end of described motor; Described transfer case is connected with the output terminal of described motor, and described transfer case drives described carbon dioxide booster pump.
The beneficial effects of the utility model are: can pressurize to carbon dioxide, the possibility that reduces to gasify because of pressure greatly to reduce liquid carbon dioxide can be the liquid carbon dioxide that fracturing unit truck provides large discharge capacity simultaneously, meets the needs of fracturing unit truck.
Further: also to comprise reflux pipeline; One end of described reflux pipeline is connected with the liquid outlet of described carbon dioxide booster pump, and the other end of described reflux pipeline is connected with the import of described gas-liquid separator; On described reflux pipeline, series connection is provided with hand-driven return-flow valve, automatic reflux valve.
Further: also to comprise suction booster bypass line; One end of described suction booster bypass line is connected with the suction side of described carbon dioxide booster pump, and the other end of described suction booster bypass line is connected with the exhaust end of described carbon dioxide booster pump; Described suction booster bypass line is provided with puts system displacement valve.
Further: described liquid-phase outlet end is made as two groups, and described in two groups, liquid-phase outlet end is arranged at the both sides of sledge of the described end; Described carbon dioxide booster pump is made as two groups; A described liquid-phase outlet end is connected with the exhaust port of described gas-liquid separator by a described carbon dioxide booster pump; Described in another, liquid-phase outlet end is connected with the exhaust port of described gas-liquid separator by carbon dioxide booster pump described in another.
Accompanying drawing explanation
Fig. 1 is the structural representation that the utility model is faced;
Fig. 2 is the structural representation that the utility model is overlooked.
Embodiment
Below in conjunction with accompanying drawing, principle of the present utility model and feature are described, example, only for explaining the utility model, is not intended to limit scope of the present utility model.
As shown in Figure 1 and Figure 2, a kind of carbon dioxide booster pump sledge, comprises end sledge 1, gas-liquid separator 2, carbon dioxide booster pump 3, liquid phase entrance point 4, gas phase entrance point 5, liquid-phase outlet end 6, gaseous phase outlet end 7; Described gas-liquid separator 2 is all arranged at the top of sledge of the described end 1 and is all fixedly connected with sledge of the described end 1 with carbon dioxide booster pump 3; Described liquid phase entrance point 4 and gas phase entrance point 5 are arranged at the front end of sledge of the described end 1, and described liquid-phase outlet end 6 and gas phase outlet end 7 are arranged at the rear end of sledge of the described end 1; Between the import on described liquid phase entrance point 4 and described gas-liquid separator 2 tops, by collector, be connected; Between the suction side of the liquid outlet of described gas-liquid separator 2 and described carbon dioxide booster pump 3, by the first pipeline, be connected; Between the liquid outlet of described carbon dioxide booster pump 3 and described liquid-phase outlet end 6, by the second pipeline, be connected and on described the second pipeline, be provided with successively flowmeter, one-way valve, liquid phase expulsion valve; Between described gas phase entrance point 5 and described gaseous phase outlet end 7, by gas phase pipeline, be connected, and be provided with ball valve on described gas phase pipeline.
This example is also included as the power system 8 that described carbon dioxide booster pump 3 provides power, and described power system 8 is arranged at the rear end of sledge of the described end 1; Described power system 8 comprises motor, transfer case, engine-cooling system; Described engine-cooling system adopts blowing type vertical water loose, and described engine-cooling system is arranged at the front end of described motor; Described transfer case is connected with the output terminal of described motor, and described transfer case drives described carbon dioxide booster pump 3.
This example also comprises reflux pipeline 9; One end of described reflux pipeline 9 is connected with the liquid outlet of described carbon dioxide booster pump 3, and the other end of described reflux pipeline 9 is connected with the import of described gas-liquid separator 2; On described reflux pipeline 9, series connection is provided with hand-driven return-flow valve, automatic reflux valve.
This example also comprises suction booster bypass line 10; One end of described suction booster bypass line 10 is connected with the suction side of described carbon dioxide booster pump 3, and the other end of described suction booster bypass line 10 is connected with the exhaust end of described carbon dioxide booster pump 3; Described suction booster bypass line 10 is provided with puts system displacement valve.
Described liquid-phase outlet end 6 is made as two groups, and described in two groups, liquid-phase outlet end 6 is arranged at the both sides of sledge of the described end 1; Described carbon dioxide booster pump 3 is made as two; A described liquid-phase outlet end 6 is connected with the exhaust port of described gas-liquid separator 2 by a described carbon dioxide booster pump 3; Described in another, liquid-phase outlet end 6 is connected with the exhaust port of described gas-liquid separator 2 by carbon dioxide booster pump described in another 3.
Described end sledge 1 be directly positioned on chassis vehicle or make auxiliary girder after be positioned over and on chassis vehicle, form vehicle carried type structure.Described power system 8, liquid-phase outlet end 6 are placed in chassis vehicle headstock one side, and described gas-liquid separator 2, liquid phase entrance point 4 are placed in the tailstock one side.
The foregoing is only preferred embodiment of the present utility model, not in order to limit the utility model, all within spirit of the present utility model and principle, any modification of doing, be equal to replacement, improvement etc., within all should being included in protection domain of the present utility model.
Claims (6)
1. a carbon dioxide booster pump sledge, is characterized in that: comprise end sledge (1), gas-liquid separator (2), carbon dioxide booster pump (3), liquid phase entrance point (4), gas phase entrance point (5), liquid-phase outlet end (6), gaseous phase outlet end (7); Described gas-liquid separator (2) is all arranged at the upper of sledge of the described end (1) and is all fixedly connected with sledge of the described end (1) with carbon dioxide booster pump (3); Described liquid phase entrance point (4) and gas phase entrance point (5) are arranged at the front end of sledge of the described end (1), and described liquid-phase outlet end (6) and gas phase outlet end (7) are arranged at the rear end of sledge of the described end (1);
Between the import on described liquid phase entrance point (4) and described gas-liquid separator (2) top, by collector, be connected; Between the liquid outlet of described gas-liquid separator (2) and the suction side of described carbon dioxide booster pump (3), by the first pipeline, be connected; Between the liquid outlet of described carbon dioxide booster pump (3) and described liquid-phase outlet end (6), by the second pipeline, be connected and on described the second pipeline, be provided with successively flowmeter, one-way valve, liquid phase expulsion valve;
Between described gas phase entrance point (5) and described gaseous phase outlet end (7), by gas phase pipeline, be connected, and be provided with ball valve on described gas phase pipeline;
Also being included as described carbon dioxide booster pump (3) provides the power system (8) of power, and described power system (8) is arranged at the rear end of sledge of the described end (1); Described power system (8) comprises motor, transfer case, engine-cooling system; Described engine-cooling system adopts blowing type vertical water loose, and described engine-cooling system is arranged at the front end of described motor; Described transfer case is connected with the output terminal of described motor, and described transfer case drives described carbon dioxide booster pump (3).
2. a kind of carbon dioxide booster pump sledge according to claim 1, is characterized in that: also comprise reflux pipeline (9); One end of described reflux pipeline (9) is connected with the liquid outlet of described carbon dioxide booster pump (3), and the other end of described reflux pipeline (9) is connected with the import of described gas-liquid separator (2); The upper series connection of described reflux pipeline (9) is provided with hand-driven return-flow valve and automatic reflux valve.
3. a kind of carbon dioxide booster pump sledge according to claim 2, is characterized in that: also comprise suction booster bypass line (10); One end of described suction booster bypass line (10) is connected with the suction side of described carbon dioxide booster pump (3), and the other end of described suction booster bypass line (10) is connected with the exhaust end of described carbon dioxide booster pump (3); Described suction booster bypass line (10) is provided with puts system displacement valve.
4. according to the arbitrary described a kind of carbon dioxide booster pump sledge of claims 1 to 3, it is characterized in that: described liquid-phase outlet end (6) is made as two groups, described in two groups, liquid-phase outlet end (6) is arranged at the both sides of sledge of the described end (1); Described carbon dioxide booster pump (3) is made as two; A described liquid-phase outlet end (6) is connected with the exhaust port of described gas-liquid separator (2) by a described carbon dioxide booster pump (3); Described in another, liquid-phase outlet end (6) is connected with the exhaust port of described gas-liquid separator (2) by carbon dioxide booster pump described in another (3).
5. a kind of carbon dioxide booster pump sledge according to claim 4, is characterized in that: described end sledge (1) be directly positioned on chassis vehicle or make auxiliary girder after be positioned over and on chassis vehicle, form vehicle carried type structure.
6. a kind of carbon dioxide booster pump sledge according to claim 5, it is characterized in that: described power system (8), liquid-phase outlet end (6) are placed in chassis vehicle headstock one side, described gas-liquid separator (2), liquid phase entrance point (4) are placed in the tailstock one side.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN201420324307.2U CN203906206U (en) | 2014-06-17 | 2014-06-17 | Carbon dioxide booster pump skid |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
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CN201420324307.2U CN203906206U (en) | 2014-06-17 | 2014-06-17 | Carbon dioxide booster pump skid |
Publications (1)
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CN203906206U true CN203906206U (en) | 2014-10-29 |
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Family Applications (1)
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CN201420324307.2U Expired - Lifetime CN203906206U (en) | 2014-06-17 | 2014-06-17 | Carbon dioxide booster pump skid |
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