CN201437720U - Proportional-control injecting system - Google Patents
Proportional-control injecting system Download PDFInfo
- Publication number
- CN201437720U CN201437720U CN2009201071297U CN200920107129U CN201437720U CN 201437720 U CN201437720 U CN 201437720U CN 2009201071297 U CN2009201071297 U CN 2009201071297U CN 200920107129 U CN200920107129 U CN 200920107129U CN 201437720 U CN201437720 U CN 201437720U
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- Prior art keywords
- chemical agent
- pump
- agent solution
- pipeline
- injection
- 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
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- 239000013043 chemical agent Substances 0.000 claims abstract description 64
- 239000000243 solution Substances 0.000 claims abstract description 53
- 238000002347 injection Methods 0.000 claims abstract description 52
- 239000007924 injection Substances 0.000 claims abstract description 52
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 19
- 238000009826 distribution Methods 0.000 claims abstract description 10
- 230000003068 static effect Effects 0.000 claims abstract description 9
- 238000012544 monitoring process Methods 0.000 claims abstract description 4
- 230000001105 regulatory effect Effects 0.000 claims description 23
- 239000007788 liquid Substances 0.000 claims description 8
- 238000010790 dilution Methods 0.000 claims description 4
- 239000012895 dilution Substances 0.000 claims description 4
- 238000000034 method Methods 0.000 abstract description 13
- 239000000126 substance Substances 0.000 abstract description 4
- 238000005516 engineering process Methods 0.000 description 37
- 229920002401 polyacrylamide Polymers 0.000 description 28
- 230000008569 process Effects 0.000 description 9
- 238000006073 displacement reaction Methods 0.000 description 6
- 238000005265 energy consumption Methods 0.000 description 4
- 230000008901 benefit Effects 0.000 description 3
- 230000009467 reduction Effects 0.000 description 3
- 230000033228 biological regulation Effects 0.000 description 2
- 238000010276 construction Methods 0.000 description 2
- 230000008878 coupling Effects 0.000 description 2
- 238000010168 coupling process Methods 0.000 description 2
- 238000005859 coupling reaction Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000002513 implantation Methods 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- 238000005070 sampling Methods 0.000 description 2
- 238000012360 testing method Methods 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 1
- 239000003085 diluting agent Substances 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 230000035800 maturation Effects 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000010355 oscillation Effects 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 238000003825 pressing Methods 0.000 description 1
- 238000010992 reflux Methods 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
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Abstract
The utility model discloses a proportional-control injecting system, which comprises a supercharge pump, wherein the supercharge pump is provided with a plurality of pump heads, and each pump head correspond one injection well; each pump head is provided with a flow-rate adjusting mechanism for controlling the flow rate of chemical agent solution, each pump head is independently communicated with a high-pressure valve assembly pipeline for conveying and monitoring the state of the chemical agent solution, the output end of the high-pressure valve assembly pipeline is connected with a high-pressure water pipeline, the output end port of the high-pressure valve assembly pipeline is communicated with a static mixer, the chemical agent solution is diluted by the water according to a setup proportion, and the diluted solution is injected into the injection well after being further and uniformly mixed inside the static mixer. The adjustment of the flow rate of the chemical agent solution is directly completed through the output of the supercharge pump, so the procedure of the original one-pump multi-well craftwork that the chemical agent solution is adjusted through a valve so as to realize the distribution of the flow rate can be canceled, the one-pump multi-well craftwork is simplified, the investment for the oil field chemical driving field can be saved, and the loss of the viscosity of the chemical agent solution at the injection link can be reduced.
Description
Technical field
The utility model relates to oil exploitation chemical displacement of reservoir oil field, especially a kind of proportion regulating and injecting system.
Background technology
In order to improve the oil production rate in oil field, chemical displacement of reservoir oil technology has become the key technology in the oil extraction process, Figure 1 shows that the chemical flooding injected system of present maturation, it adopts " the many wells of a pump " injection technology, inject underground chemical agent solution from storage tank to injecting well head, polyacrylamide generation to a certain degree the degraded of each link to containing in the chemical agent solution in the flow process, its total viscosity loss is about 20%, wherein in this system, after the chemical agent solution that contains polyacrylamide boosts by booster pump, discharging port by one discharges, again respectively by header and each by-pass line each individual well that leads, because there is difference in the actual injection pressure of each individual well, can effectively inject each individual well in order to satisfy the chemical agent solution that contains polyacrylamide like this, the output pressure of booster pump just must be not less than the highest individual well pressure, and for the individual well of pressing than The Small Well, excessive pressure reduces will cause the chemical agent solution viscosity loss that contains polyacrylamide, the chemical agent solution viscosity loss that contains polyacrylamide that wherein the Flow-rate adjustment link causes in " the many wells of a pump " is maximum, its viscosity loss can reach 10%-15%, for the big individual well of indivedual pressure reduction, contain the chemical agent solution viscosity loss of polyacrylamide even substantially exceed the oil field and inject index, bigger to the implantation quality influence.This injected system, owing to interfere mutually between many wells, its complex technical process, control system complexity, inconvenient operation, big, the chemical agent solution adjusting complexity of investment, in the course of the work, the fluctuation of chemical agent solution is big, thereby makes system's fluctuation of service.
The utility model content
At the problem that prior art exists, the purpose of this utility model is to provide a kind of chemical agent solution viscosity loss proportion regulating and injecting system little, simple in structure, simple to operate that injects link.
For achieving the above object, the utility model proportion regulating and injecting system comprises booster pump, and this booster pump is provided with several pump heads, and each pump head is corresponding to injecting well flatly; Each pump head is provided with the flow control device of control chemical agent liquid inventory, each pump head all independently is communicated with carries the also high pressure valve group pipeline of monitoring chemical agent solution state, be connected with high-pressure water pipeline on the output of high pressure valve group pipeline, be communicated with static mixer on the output port of high pressure valve group pipeline, chemical agent solution is diluted according to the ratio of setting by water, and dilution carries out further being injected into the injection well after the evenly mixing in static mixer.
Further, described high pressure valve group pipeline is provided with flap valve, ball valve and electromagnetic flowmeter.
Further, also be provided with the sampler valve that is used to take a sample on the described high pressure valve group pipeline.
Further, described high-pressure water pipeline is provided with the automatic distribution water device, and the automatic distribution water device comprises flow meter, motor operated valve and controller, and its ratio that is used to control according to setting is carried out the water distribution dilution to chemical agent solution.
The utility model proportion regulating and injecting system, directly finish the adjusting of chemical agent liquid inventory by the output of booster pump, thereby cancelled chemical agent solution in original " the many wells of a pump " technology is realized assignment of traffic by valve regulated link, simplified " the many wells of a pump " technology, save oilfield chemistry and driven the ground investment, greatly reduced the viscosity loss of the chemical agent solution that injects link.
Description of drawings
Fig. 1 is the injected system schematic diagram of prior art;
Fig. 2 is an injected system schematic diagram of the present utility model.
The specific embodiment
As shown in Figure 2, the utility model proportion regulating and injecting system, comprise booster pump 1, it is used for providing the chemical agent solution that contains polyacrylamide to inject runner to the supercharging of chemical agent solution, the process duct 3 that contains polyacrylamide, booster pump 1 is provided with several pump heads 2, regulates the chemical agent solution that output contains polyacrylamide as required, is provided with 3 pump heads 2 in the present embodiment, can increase and decrease the quantity of pump head in the practical application according to demand, its general quantity is 3～7; Each pump head 2 is corresponding to injecting well flatly, and the follow-up pipeline that pump head connected is used to provide the chemical agent solution injection process that contains polyacrylamide of injecting well flatly; Each pump head 2 is provided with the flow control device that control contains the chemical agent liquid inventory of polyacrylamide, this flow control device comprises pilot plunger, by the linear regulation that how much realizes discharge capacity in the pilot plunger embedding pump cylinder, the flow adjustable extent is 30-100%, this flow control device can be locked, and guarantees that discharge capacity has advantages of higher stability, and operation separately, do not disturb mutually each other, easy to operate.
Each pump head 2 all independently is communicated with the high pressure valve group pipeline 4 of carrying and monitoring the chemical agent solution state that contains polyacrylamide, high pressure valve group pipeline 4 comprises flap valve 42, ball valve 43 electromagnetic flowmeters 41 and sampler valve 44, flap valve 42 is used to prevent that the chemical agent solution of exporting that contains polyacrylamide from refluxing, when being used for corrective maintenance, ball valve 43 is convenient to the dismounting of miscellaneous part, electromagnetic flowmeter 41 is used for injection is contained the metering of the chemical agent solution of polyacrylamide, and sampler valve 44 is used for sampling.Be connected with high-pressure water pipeline 5 near on the output of high pressure valve group pipeline 4, be communicated with static mixer 6 on the output port of high pressure valve group pipeline 4, chemical agent solution in-line is diluted according to the ratio of setting by water earlier, diluent stream will be carried out further evenly mixing after going into static blender 6, evenly mix the back and be injected into the injection well by injecting pipeline 7.
High-pressure water pipeline 5 is provided with automatic distribution water device 51; Automatic distribution water device 51 comprises flow meter, motor operated valve and controller, and it has compact conformation, and is easy and simple to handle, and intuitive display is manually controlled characteristics such as flow or automatic control flow, and its ratio that is used to control according to setting is carried out the water distribution dilution to chemical agent solution.
Advantage of the present utility model:
1, simplifies oilfield chemistry and drive the injection technology flow process, reduce the ground investment
Cancel oilfield chemistry and driven the link that contains the chemical agent liquid inventory adjusting of polyacrylamide in former " the many wells of a pump " technique by the realization of valve group, cancelled simultaneously complicated robot control system(RCS), greatly reduced the ground surface works investment;
2, it is little to contain the chemical agent solution viscosity loss of polyacrylamide, saves the consumption of polyacrylamide;
Cancel oilfield chemistry and driven the link that realizes the adjusting of chemical agent liquid inventory in former " the many wells of a pump " technique by the valve group, greatly reduce the chemical agent solution that contains polyacrylamide at the viscosity loss that injects link, save the polyacrylamide consumption, Effective Raise oilfield chemistry oil displacement efficiency;
3, individual well injection pressure coupling reduces operation energy consumption
The corresponding individual well of the booster pump list pump head of this injection technology, therefore output pressure and individual well subsurface pressure mate fully, there is not pressure reduction, eliminate oilfield chemistry fully and driven the individual well difference pressuring loss that former " the many wells of a pump " technique causes, can significantly reduce the real output of booster pump, have good energy-saving effect;
4, stable continuously, the chemical agent solution injection fluctuation that contains polyacrylamide is very little
This injection technology individual well coupling does not have to disturb between well, the supercharging pump delivery good stability of employing, and the chemical agent solution injection fluctuation that contains polyacrylamide is very little;
5, the chemical agent liquid inventory is regulated simply, and the workman is easy to operate
This injection technology realizes that by regulating the flow control device of single pump head individual well contains the chemical agent solution injection rate requirement of polyacrylamide, satisfies the linearity adjustment of the chemical agent solution injection rate that contains polyacrylamide, makes things convenient for the workman to operate.
The utility model experimentation:
1, stable, the momentary fluctuation of chemical agent solution is little
Technology operating condition is stable in the test, and it is easy to adjust that this injection technology contains the chemical agent solution discharge capacity of polyacrylamide, has substituted the function of " former many wells of a pump skid injection device and a flow regulator ".Three mouthfuls of injection wells that field trial is chosen, two mouthfuls of instantaneous injection rate 0.6m of well chemical agent solution
3/ h, a bite well 0.42m in addition
3/ h by regulating the flow regulator of single pump head, has realized that the single well chemical agent solution of three mouthfuls of different flows injects requirement.
As shown in table 1, to regulate in the on-the-spot running of injection technology in ratio, the instantaneous injection rate fluctuation of each pump head outlet pressure and chemical agent solution is very little, and maximum pressure fluctuates less than 0.3MPa, injects the fluctuation of chemical agent solution instantaneous delivery at 0.07m
3About/h, less than scheme require ± 5% deviation.As shown in table 2, many wells of pump process chemistry agent solution momentary fluctuation is on average at 0.013m
3/ h, the part well reaches behind the decimal point one, ratio is regulated the fluctuation that the fluctuation of injection technology chemical agent solution instantaneous displacement is lower than flow regulator in original technology by contrast, the ratio that illustrated is regulated injection technology discharge capacity stability better, the flow regulator of single pump head has higher degree of regulation, can satisfy the linearity adjustment of chemical agent solution injection rate.
Table 1: ratio is regulated technology outlet pressure and flowed fluctuation situation
| And number | 9-PS1312 | 10-PS1302 | 10-PS1234 |
| Pressure oscillation (MPa) | ＜0.15 | ＜0.30 | ＜0.20 |
| Instantaneous (the m of scheme chemical agent 3/h) | 0.42 | 0.6 | 0.6 |
| Chemical agent momentary fluctuation (m 3/h) | ＜0.007 | ＜0.01 | ＜0.006 |
Table 2: many wells of pump technology is injected situation
| Header | Header pressure (MPa) | Average injection pressure (MPa) | Difference (MPa) | Average chemical agent momentary fluctuation (m3/h) |
| 1# | 11.06 | 9.7 | 1.36 | 0.015 |
| 2# | 14.47 | 11.5 | 2.97 | 0.014 |
| 3# | 10.88 | 9.3 | 1.58 | 0.011 |
2, ratio regulate injection technology to the viscosity loss of the chemical agent solution that contains polyacrylamide less than former many wells of pump technology
As shown in table 3, detect by the scene, the dense viscosity of sampling was more stable after ratio was regulated the injection technology static mixer, and concentration is that two mouthfuls of well viscosity of 1200mg/L remain on more than the 50mPa.s, concentration is that the 1000mg/L well also remains on about 36mPa.s, and viscosity loss is less than 10%.Be lost in about 20% in many wells of pump technology medium viscosity, it is less that ratio is regulated the injection technology viscosity loss, with regard to its main cause is flow regulator and the header of having cancelled many wells of pump technology, has avoided owing to reasons such as the card of flow regulator is stifled seriously, front and back pressure reduction is big cause the sticking greatly of chemical agent solution to containing polyacrylamide to decrease.Booster pump belongs to positive displacement pump, viscosity loss is in 4%, suitable with common three-throw ram pump, so ratio regulates the loss of injection technology overall viscosity and reduced about 10% than the pump well of a manying technology of employing flow regulator, helps further improving the chemical agent implantation quality.
Table 3: ratio is regulated the dense viscosity measurements data of injection technology
3, ratio adjusting injection technology can reduce operation energy consumption 15%
The main energy consumption of driving in the chemical agent injection technology process at oilfield chemistry is to be used for chemical agent solution to boost, original many wells of pump injection technology, the injection well of a corresponding 5-10 mouth of header, because the injection pressure of each individual well is inequality, in order to guarantee the normal injection of minority high pressure well, just must make whole header all keep higher pressure, thereby improve the pump pressure of injection pump, cause the loss of well head cutoff pressure big.Though adopt three headers, carry out the pressure marshalling, because the restriction of injection rate and the existence of individual well injection pressure difference can not be eliminated difference pressuring loss fully, the energy loss that therefore dams still exists.
Two kinds of injection technology pressure loss contrasts of table 4
As can be seen from Table 4,1# chemical agent solution header pressure average loss 1.36MPa, 2# header pressure average loss 2.97MPa, 3# header pressure average loss 1.58MPa, wherein the injection pump pressure loss of 2# header correspondence is bigger, accounts for 20% of gross pressure, whole average loss about 15%.And ratio is regulated injection technology, owing to cancelled header and flow regulator, does not have the link of damming, and the pressure loss is very little, and visible ratio is regulated the pressure loss that injection technology can reduce system 15%, reduces system's operation energy consumption.
4, simplify the injection technology flow process, reduce the surface construction investment
The booster pump that test is adopted is ripe homemade pump, pump can corresponding many mouthfuls of injection wells, compare with the technology pattern of " the many wells of a pump "+" flow regulator ", ratio is regulated the automatic control system that injection technology has been saved frequency-changing control system, flow regulator and control chemical agent liquid inventory, not only simplify technological process, can also save the ground construction investment.Confirm by the scene operation, ratio adjusting injection technology is practical, reach every injection index preferably, the viscosity loss that can reduce the chemical agent solution that contains polyacrylamide reaches about 10%, not only reduced the consumption of polyacrylamide dry powder, also help further raising oil displacement efficiency, economic benefit is considerable, has good popularization value.
Claims (4)
1. proportion regulating and injecting system is characterized in that, this system comprises booster pump, and this booster pump is provided with several pump heads, and each pump head is corresponding to injecting well flatly; Each pump head is provided with the flow control device of control chemical agent liquid inventory, each pump head all independently is communicated with carries the also high pressure valve group pipeline of monitoring chemical agent solution state, be connected with high-pressure water pipeline on the output of high pressure valve group pipeline, be communicated with static mixer on the output port of high pressure valve group pipeline, the outlet of static mixer is connected with the injection well by injecting pipeline.
2. proportion regulating and injecting system as claimed in claim 1 is characterized in that, described high pressure valve group pipeline is provided with flap valve, ball valve and electromagnetic flowmeter.
3. proportion regulating and injecting system as claimed in claim 2 is characterized in that, also is provided with the sampler valve that is used to take a sample on the described high pressure valve group pipeline.
4. proportion regulating and injecting system as claimed in claim 1, it is characterized in that, described high-pressure water pipeline is provided with the automatic distribution water device, and the automatic distribution water device comprises flow meter, motor operated valve and controller, and its ratio that is used to control according to setting is carried out the water distribution dilution to chemical agent solution.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2009201071297U CN201437720U (en) | 2009-04-07 | 2009-04-07 | Proportional-control injecting system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2009201071297U CN201437720U (en) | 2009-04-07 | 2009-04-07 | Proportional-control injecting system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201437720U true CN201437720U (en) | 2010-04-14 |
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ID=42399696
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2009201071297U Expired - Lifetime CN201437720U (en) | 2009-04-07 | 2009-04-07 | Proportional-control injecting system |
Country Status (1)
| Country | Link |
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| CN (1) | CN201437720U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102162347A (en) * | 2011-02-28 | 2011-08-24 | 西南石油大学 | Injection device capable of adapting to low-temperature environment in foam drainage gas recovery |
| CN104709926A (en) * | 2015-03-05 | 2015-06-17 | 卜明 | Multi-well brine differentiated-treatment device and method thereof |
-
2009
- 2009-04-07 CN CN2009201071297U patent/CN201437720U/en not_active Expired - Lifetime
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102162347A (en) * | 2011-02-28 | 2011-08-24 | 西南石油大学 | Injection device capable of adapting to low-temperature environment in foam drainage gas recovery |
| CN104709926A (en) * | 2015-03-05 | 2015-06-17 | 卜明 | Multi-well brine differentiated-treatment device and method thereof |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| EE01 | Entry into force of recordation of patent licensing contract |
Assignee: Dafeng Oil Field Tech Co., Ltd., Daqing Assignor: Wanaopu (Beijing) Petroleum Engineering Technology Development Research Institute Co., Ltd. Contract record no.: 2011230000077 Denomination of utility model: Proportion regulating and injecting system Granted publication date: 20100414 License type: Exclusive License Record date: 20110808 |
|
| ASS | Succession or assignment of patent right |
Owner name: DAFENG OIL FIELD TECH CO LTD, DAQING Free format text: FORMER OWNER: WAN'AOPU (BEIJING) PETROLEUM ENGINEERING TECHNOLOGY DEVELOPMENT INSTITUTE CO., LTD. Effective date: 20120215 Owner name: NUOXINWEI (BEIJING) SCIENCE AND TECHNOLOGY DEVELOP Effective date: 20120215 |
|
| C41 | Transfer of patent application or patent right or utility model | ||
| COR | Change of bibliographic data |
Free format text: CORRECT: ADDRESS; FROM: 100085 HAIDIAN, BEIJING TO: 163316 DAQING, HEILONGJIANG PROVINCE |
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| TR01 | Transfer of patent right |
Effective date of registration: 20120215 Address after: 163316 Daqing hi tech Zone, Heilongjiang, Jianshe Road Co-patentee after: North Winner (Beijing) Technology Development Co., Ltd. Patentee after: Dafeng Oil Field Tech Co., Ltd., Daqing Address before: 100085, A406, Haidian District, Beijing, 5 Patentee before: Wanaopu (Beijing) Petroleum Engineering Technology Development Research Institute Co., Ltd. |
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| C41 | Transfer of patent application or patent right or utility model | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20160229 Address after: 163316 No. 28 Xinfa street, hi tech Development Zone, Heilongjiang, Daqing Patentee after: Daqing Dafeng Energy Technology Service Co., Ltd. Address before: 163316 Daqing hi tech Zone, Heilongjiang, Jianshe Road Patentee before: Dafeng Oil Field Tech Co., Ltd., Daqing Patentee before: North Winner (Beijing) Technology Development Co., Ltd. |
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| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20170822 Address after: No. 28-4 Xinfa street, Daqing Development Zone, Heilongjiang Patentee after: Daqing demeitel Technology Co., Ltd. Address before: 163316 No. 28 Xinfa street, hi tech Development Zone, Heilongjiang, Daqing Patentee before: Daqing Dafeng Energy Technology Service Co., Ltd. |
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| CX01 | Expiry of patent term | ||
| CX01 | Expiry of patent term |
Granted publication date: 20100414 |