CN206111162U - Dense system falls in clear water that brine was adopted to machine - Google Patents
Dense system falls in clear water that brine was adopted to machine Download PDFInfo
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- CN206111162U CN206111162U CN201621146252.6U CN201621146252U CN206111162U CN 206111162 U CN206111162 U CN 206111162U CN 201621146252 U CN201621146252 U CN 201621146252U CN 206111162 U CN206111162 U CN 206111162U
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- pipeline
- valve
- salt well
- connection
- clear water
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Abstract
The utility model discloses a dense system falls in clear water that brine was adopted to machine, including salt well A and salt well B, be equipped with the center tube in the salt well B, salt well B intercommunication is equipped with inlet channel B, is equipped with the electrical submersible pump pump in the center tube, and the discharge end of electrical submersible pump pump passes through pipeline D and goes out steamed pipeline intercommunication, still include salt well A's water injection pipe, the water injection pipe passes through inlet channel A and salt well A intercommunication, the water injection pipe before the inlet channel A who lies in salt well A, loop through pipeline A, pipeline B and pipeline C and salt well B intercommunication, pipeline C passes through inlet channel B and salt well B intercommunication, pipeline A goes up the intercommunication and is equipped with valve A, on the pipeline B in proper order serial connectivity be equipped with flowmeter, manometer A and valve B, on the pipeline D in proper order serial connectivity be equipped with valve C and manometer B. By the utility model discloses the structure can know, through the utility model discloses a pipe -line system can realize falling densely to salt well B's clear water to make salt well B's the continuous production time to prolong greatly, improved production efficiency.
Description
Technical field
The utility model is related to salt well and adopts halogen field, and in particular to a kind of machine adopts the clear water of bittern and drops dense system.
Background technology
In well mine salt exploitation, level connection well group water soluble method is current main mining type, when well group is normally produced, halogen
Sodium chloride average content in water is easy for salt pipe plugging by crystallization phenomenon if it exceeds 300g/l, and exchange water filling side is usually taken
To solution.It is to adopt enter under halogen end electric submersible pump in connection well group that machine adopts bittern, improves lift-off pressures, and it is low to be mainly used in production-injection ratio, raw
Produce the well group of inefficiency.When pump adopts halogen initial design, do not design clear water and drop dense system, if adopted during halogen, send out
Raw salt crystallization, shutdown clear water is rinsed and reruned after pump.After the completion of Soviet Union's down-hole pump of salt 15, in test run, owing repeatedly occurs in electric pump
Carry and shut down the problem that cannot realize continuous operation, with clear water backwashing pump after, restarting to run again, and the longest run time is 10
Hour, most short 3 hours, although illustrating to be adopted in bittern using electric submersible pump to drain out, are because crystallizing quick plugging problem
But cannot continuously run, cause the operability for adopting halogen using electric submersible pump to be merely limited, will be unable to put into production use.
The content of the invention
The purpose of this utility model is：Overcome the deficiencies in the prior art, there is provided a kind of machine adopts the clear water of bittern and drops dense system
System, by pipe-line system of the present utility model, it is possible to achieve dense to the clear water drop of salt well B, so that the continuous production of salt well B
Time can greatly prolong, and improve production efficiency；Not only can by the use of other salt wells of such as salt well A as water injection well when
Wait, clear water is carried out with the water injection pipe of the salt well and drops dense, and when other salt wells of such as salt well A are as halogen well is gone out, also
Clear water drop can be carried out with clear water well dense, it is ensured that the system can be with continuous service；By the effect of pipeline F and pipeline G, can be with
This two pipelines are used alternatingly, such that it is able to pipeline wherein carry out clear water drop it is dense while, another pipeline is carried out
Repair and maintenance, it is ensured that the service life of system, nor affect production；By the effect of pipeline H, it is possible to achieve to salt well
B circulation flushings, protect electric submersible pump, also beneficial to the continuous production of salt well B.
Technical solution adopted in the utility model is：
Machine adopts the clear water of bittern and drops dense system, including salt well A and salt well B, is provided with central tube in the salt well B, it is described in
The bottom of heart pipe connects with the bottom of salt well B, and the salt well B connections are provided with inlet channel B, electric submersible pump are provided with central tube, institute
The discharge end for stating electric submersible pump passes through pipeline D and goes out halogen pipeline communication；Also including salt well A water injection pipe, the water injection pipe pass through into
Waterpipe A is connected with salt well A, the water injection pipe positioned at salt well A inlet channel A before, pass sequentially through pipeline A, pipeline B and
Pipeline C is connected with salt well B, and the pipeline C is connected by inlet channel B with salt well B；Connection on the pipeline A is provided with valve A,
Connection is sequentially connected in series on the pipeline B and is provided with flowmeter, pressure Table A and valve B, be sequentially connected in series connection on the pipeline D and be provided with
Valve C and pressure gauge B.
The further improvement project of the utility model is that the pipeline C is located at connection between valve B and inlet channel B and is provided with
Outlet conduit, connection on the outlet conduit is provided with valve J.
The utility model further improvement project is, between the pipeline A and pipeline B parallel communication be provided with pipeline F and
Pipeline G, connection on the pipeline F is provided with valve G, and connection on the pipeline G is provided with valve H.
The utility model further improvement project is that the rear side on the pipeline G positioned at valve H is also connected and is provided with valve
I, the pipeline G are located at the position between valve H and valve I and are connected with clear water well by pipeline E, on the pipeline E successively
Serial communication is provided with self priming pump and valve F.
The utility model further improvement project is, it is described go out halogen pipeline on connection be provided with valve E, the pipeline D positions
Connected with inlet channel B by pipeline H in the rear side of pressure gauge B, connection on the pipeline H is provided with valve K.
The utility model further improvement project is to be located to be connected between pressure gauge B and pipeline H on the pipeline D to set
There is valve D.
The beneficial effects of the utility model are：
Firstth, machine of the present utility model adopts the clear water of bittern and drops dense system, by pipe-line system of the present utility model, can be with
Realize that the clear water drop to salt well B is dense, so that the continuous production time of salt well B can greatly prolong, from original continuous life
Product extends to continuous production 15 days for 3 hours, improves production efficiency.
Secondth, machine of the present utility model adopts the clear water of bittern and drops dense system, not only can utilize other salt of such as salt well A
When well is as water injection well, clear water is carried out with the water injection pipe of the salt well and drops dense, and in other salt well conducts of such as salt well A
When going out halogen well, clear water drop can also be carried out with clear water well dense, it is ensured that the system can be with continuous service.
3rd, machine of the present utility model adopts the dense system of clear water drop of bittern, by the effect of pipeline F and pipeline G, Ke Yijiao
For using this two pipelines, such that it is able to pipeline wherein carry out clear water drop it is dense while, another pipeline is examined
Repair maintenance, it is ensured that the service life of system, nor affect production.
4th, machine of the present utility model adopts the dense system of clear water drop of bittern, by the effect of pipeline H, it is possible to achieve to salt
Well B circulation flushings, protect electric submersible pump, also beneficial to the continuous production of salt well B.
5th, machine of the present utility model adopts the clear water of bittern and drops dense system, clear water into the flow velocity in salt well B should be greater than from
Central tube A extracts the flow velocity of bittern out, so as to ensure that into the clear water in salt well B shaft bottom can be poured.
Description of the drawings
Fig. 1 is pipeline structure schematic diagram of the present utility model.
Specific embodiment
As shown in figure 1, the utility model includes salt well A13 and salt well B10, central tube 11 is provided with the salt well B10,
The bottom of the central tube 11 connects with the bottom of salt well B10, and the salt well B10 connections are provided with inlet channel B5 central tubes 11
Electric submersible pump is provided with, the discharge end of the electric submersible pump is connected by pipeline D6 with halogen pipeline 7 is gone out；Also including the water injection pipe of salt well A13
1, the water injection pipe 1 is connected by inlet channel A with salt well A13, the water injection pipe 1 positioned at salt well A13 inlet channel A it
Before, pass sequentially through pipeline A2, pipeline B3 and pipeline C4 and connect with salt well B10, the pipeline C4 is by inlet channel B5 and salt well
B10 is connected；Connection on the pipeline A2 is provided with valve A14, is sequentially connected in series connection on the pipeline B3 and is provided with flowmeter 8, pressure
Table A 9 and valve B15, are sequentially connected in series connection and are provided with valve C16 and pressure gauge B12 on the pipeline D6；The pipeline C4 is located at valve
Connection between door B15 and inlet channel B5 is provided with outlet conduit 28, and connection on the outlet conduit 28 is provided with valve J29；It is described
Parallel communication is provided with pipeline F23 and pipeline G25 between pipeline A2 and pipeline B3, and connection on the pipeline F23 is provided with valve G24,
Connection on the pipeline G25 is provided with valve H26；Rear side on the pipeline G25 positioned at valve H26 is also connected and is provided with valve I27,
The pipeline G25 is located at the position between valve H26 and valve I27 and is connected with clear water well 19 by pipeline E20, the pipeline
Connection is sequentially connected in series on E20 and is provided with self priming pump 21 and valve F22；It is described go out halogen pipeline 7 on connection be provided with valve E18, the pipe
Road D6 is located at the rear side of pressure gauge B12 and is connected with inlet channel B5 by pipeline H30, and connection on the pipeline H30 is provided with valve
K31；It is located to be connected between pressure gauge B12 and pipeline H30 on the pipeline D6 and is provided with valve D17.
When the excessive concentration of sodium chloride in bittern in salt well B10, if salt well A13 is as water injection well,
Valve A14, valve G24, valve B15, valve C16, valve D17 and valve E18 are opened simultaneously（Now can be with service conduits
G25）, and close remaining valve；Or while open valve A14, valve H26, valve I27, valve B15, valve C16, valve
D17 and valve E18（Now can be with service conduits F23）, and close remaining valve；The water injection pipe 1 that salt well A13 can be passed through will
In clear water injection salt well B10, so as to reduce the concentration of sodium chloride in bittern in salt well B10, it is to avoid sodium chloride concentration mistake in bittern
It is high and crystallize, cause damage to electric submersible pump, and then so that the continuous production time of salt well B10 greatly prolong；
If salt well A13 is as halogen well is gone out, at the same open valve F22, valve I27, valve B15, valve C16,
Valve D17 and valve E18（Now can be with service conduits F23）, and remaining valve is closed, clear water can be injected by clear water well
In salt well B10, so as to reduce the concentration of sodium chloride in bittern in salt well B10.
In above process, valve J29 can be opened, hydrodynamic is carried out to salt well B10 so as to pass through outlet conduit 28
Face is tested.
After the concentration of sodium chloride in bittern in salt well B10 is reduced, when electric submersible pump is by the operation of halogen amount is designed, during operation
Between extended to 15 days from initial 3 hours, effectively extend continuous operating time.But because machine adopts the monolateral exploitation of bittern
Feature, adopts halogen end pit shaft salt crust problem and yet suffers from, it is necessary to is rinsed by clear water and is solved, when flushing by clear water, salt well
Liquid level in B10 is improved constantly, and is accomplished by discharging in the bittern in salt well B when liquid level is too high, but in view of electric submersible pump
The characteristics of not supporting frequent start-stop, so needing to be circulated flushing.When operation, at the same open valve F22, valve I27,
Valve B15, valve C16, valve D17 and valve K31（Now can be with service conduits F23）, and remaining valve is closed, work as salt well
When liquid level in B10 is increased to certain altitude, valve F22, valve I27 and valve B15 are closed, make the halogen in salt well B10
Water passes sequentially through pipeline D6, pipeline H30 and inlet channel B5 and turns again to salt well by electric submersible pump from after the extraction of central tube 11
In B10, the function of the circulation flushing of salt well B10 is realized.In order to ensure that clear water pours shaft bottom, clear water is entered in salt well B10
Flow velocity should be greater than from central tube A11 extracting the flow velocity of bittern out.
Claims (6)
1. machine adopts the dense system of clear water drop of bittern, including salt well A（13）With salt well B（10）, it is characterised in that：The salt well B
（10）Inside it is provided with central tube（11）, the central tube（11）Bottom and salt well B（10）Bottom connection, the salt well B（10）
Connection is provided with inlet channel B（5）, central tube（11）Electric submersible pump is inside provided with, the discharge end of the electric submersible pump passes through pipeline D（6）With
Go out halogen pipeline（7）Connection；Also include salt well A（13）Water injection pipe（1）, the water injection pipe（1）By inlet channel A and salt well A
（13）Connection, the water injection pipe（1）Positioned at salt well A（13）Inlet channel A before, pass sequentially through pipeline A（2）, pipeline B
（3）With pipeline C（4）With salt well B（10）Connection, the pipeline C（4）By inlet channel B（5）With salt well B（10）Connection；It is described
Pipeline A（2）Upper connection is provided with valve A（14）, the pipeline B（3）On be sequentially connected in series connection and be provided with flowmeter（8）, pressure Table A
（9）With valve B（15）, the pipeline D（6）On be sequentially connected in series connection and be provided with valve C（16）With pressure gauge B（12）.
2. machine as claimed in claim 1 adopts the dense system of clear water drop of bittern, it is characterised in that：The pipeline C（4）Positioned at valve
B（15）With inlet channel B（5）Between connection be provided with outlet conduit（28）, the outlet conduit（28）Upper connection is provided with valve J
（29）.
3. machine as claimed in claim 2 adopts the dense system of clear water drop of bittern, it is characterised in that：The pipeline A（2）With pipeline B
（3）Between parallel communication be provided with pipeline F（23）With pipeline G（25）, the pipeline F（23）Upper connection is provided with valve G（24）, it is described
Pipeline G（25）Upper connection is provided with valve H（26）.
4. machine as claimed in claim 3 adopts the dense system of clear water drop of bittern, it is characterised in that：The pipeline G（25）On be located at
Valve H（26）Rear side also connect and be provided with valve I（27）, the pipeline G（25）Positioned at valve H（26）With valve I（27）Between
Position at pass through pipeline E（20）With clear water well（19）Connection, the pipeline E（20）On be sequentially connected in series connection and be provided with self priming pump
（21）With valve F（22）.
5. machine as claimed in claim 4 adopts the dense system of clear water drop of bittern, it is characterised in that：It is described go out halogen pipeline（7）Upper company
It is logical to be provided with valve E（18）, the pipeline D（6）Positioned at pressure gauge B（12）Rear side pass through pipeline H（30）With inlet channel B（5）
Connection, the pipeline H（30）Upper connection is provided with valve K（31）.
6. machine as claimed in claim 5 adopts the dense system of clear water drop of bittern, it is characterised in that：The pipeline D（6）It is upper to be located at pressure
Power table B（12）With pipeline H（30）Between connection be provided with valve D（17）.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621146252.6U CN206111162U (en) | 2016-10-21 | 2016-10-21 | Dense system falls in clear water that brine was adopted to machine |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621146252.6U CN206111162U (en) | 2016-10-21 | 2016-10-21 | Dense system falls in clear water that brine was adopted to machine |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206111162U true CN206111162U (en) | 2017-04-19 |
Family
ID=58527446
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621146252.6U Withdrawn - After Issue CN206111162U (en) | 2016-10-21 | 2016-10-21 | Dense system falls in clear water that brine was adopted to machine |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206111162U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106437672A (en) * | 2016-10-21 | 2017-02-22 | 淮安信息职业技术学院 | Clear water concentration reducing system for machine-collected brine |
-
2016
- 2016-10-21 CN CN201621146252.6U patent/CN206111162U/en not_active Withdrawn - After Issue
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106437672A (en) * | 2016-10-21 | 2017-02-22 | 淮安信息职业技术学院 | Clear water concentration reducing system for machine-collected brine |
| CN106437672B (en) * | 2016-10-21 | 2018-10-26 | 淮安信息职业技术学院 | Dense system drops in the clear water that machine adopts brine |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20170419 Effective date of abandoning: 20181026 |
|
| AV01 | Patent right actively abandoned |