CN101245779A - Oil balancing system of reciprocating oil isolation membrane pump fluid end - Google Patents
Oil balancing system of reciprocating oil isolation membrane pump fluid end Download PDFInfo
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- CN101245779A CN101245779A CNA2008100343839A CN200810034383A CN101245779A CN 101245779 A CN101245779 A CN 101245779A CN A2008100343839 A CNA2008100343839 A CN A2008100343839A CN 200810034383 A CN200810034383 A CN 200810034383A CN 101245779 A CN101245779 A CN 101245779A
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Abstract
The invention relates to an oil balance system of a reciprocating oil separation diaphragm pump hydraulic end, in particular to the oil balance system of the reciprocating oil separation diaphragm pump which is suitable for delivering a high temperature and high pressure slurry with solid grains. The oil balance system comprises a cylinder body, a diaphragm, a deflation valve which is arranged on the upper end of the cylinder body and an oil supplementary valve which is arranged at the lower end of the cylinder body, and an oil separation tank. The oil balance system is characterized in that the oil separation diaphragm structure is adopted and the deflation system cooperates with the oil supplementary system so as to control the oil level in the separation tank to change within a safe range. The oil balance system of the invention has the beneficial effects of sensitive response, effectively controlling the oil level of the separation tank in the safe range when the oil supplementary pump supplements oil, preventing over-high or over-low oil level which causes the pump not to run normally, reducing the working temperature of the diaphragm and prolonging the service life of the diaphragm.
Description
Technical field
The present invention relates to the oil balancing system of reciprocating oil isolation membrane pump fluid end, particularly be applicable to the oil balancing system of the reciprocating oil isolation membrane pump of carrying the High Temperature High Pressure slurry that contains solid particle.
Background technique
General employing plunger pump when carrying the medium of High Temperature High Pressure, but certain leakage is all arranged, and adopt diaphragm pump just can effectively address the leakage concern.But barrier film can't proper functioning under high temperature condition, therefore must solve high temperature problem.Can the residual fraction air in the pump chamber before the pump startup, and generally contain a small amount of gas in the oil of pump chamber, in the pump work process, these gases can overflow gradually and accumulate in the pump chamber top, if untimely discharge will influence the work and the volumetric efficiency of pump.
Untimely replenishing can constantly consume at pump oil in running, if will cause in the pump pressure unbalance and make the pump cisco unity malfunction.The High Temperature High Pressure reciprocating oil isolation membrane pump fluid end often adopts the constant repairing both at home and abroad at present.When repairing amount during less than requirement, slurries can cause the wearing and tearing of fluid end, and during serious wear, pump is with cisco unity malfunction; When repairing amount during greater than requirement, the oil that has more will improve operating cost with carrying liquid drain.
Summary of the invention
The object of the present invention is to provide a kind of oil balancing system, to satisfy the normal use of the reciprocating oil isolation membrane pump of carrying the High Temperature High Pressure slurry.
The objective of the invention is to be achieved through the following technical solutions: a kind of oil balancing system of reciprocating oil isolation membrane pump fluid end, comprise cylinder body, barrier film, be positioned at the bleed valve of cylinder body upper end and be positioned at the Fill valve of cylinder body lower end, oily isolation tank, it is characterized in that: adopt oily isolation diaphragm type structure, blow-off system and oil-supplementing system acting in conjunction, the oil level in the control isolation tank moves in safety range.
Oil isolation diaphragm type structure adopts oily isolation tank to connect cylinder body and flow passage components, and the isolation tank middle and upper part is an oil, and its underpart is the high temperature slurry, so just barrier film and slurry are kept apart with oil, the heat transfer property of oil is relatively poor, has reduced the operating temperature of barrier film, the working life of having improved barrier film.
Blow-off system is a bleed valve, and bleed valve is made up of the opposite one-way valve of both direction.
Oil-supplementing system is an electric control system, Fill valve links to each other with slippage pump by pipeline, communicate with system oil-way simultaneously, the high-low limit position of oil level is established the contact respectively in oily isolation tank, electric control signal is sent in the contact, the control slippage pump begins or stops repairing, and oil level is moved between the high-low limit position.
Bleed valve is positioned at the cylinder body top, can be considered two one-way valves, first one-way valve opens under the normal state, second one-way valve closure.Gas in the pump in the residual empty G﹠O can overflow and accumulate in the cylinder body top gradually in the pump operation process, gather to a certain degree and produce certain pressure, make first closed check valve, simultaneously a small amount of gas overflows, second one-way valve opens, gas release is gone out, and can take away a small amount of oil simultaneously.Fill valve is positioned at the cylinder body lower end, can be considered an one-way valve, communicates by pipeline with slippage pump, and is closed under the normal state, when slippage pump begins repairing, and one-way valve opens.
In the pump work process, oil is constantly discharged along with slurry, a spot of oil of taking away when adding the bleed valve venting, and the oil in the active chamber constantly reduces, and the oil level in the oily isolation tank constantly rises.When rising to certain altitude, slurry flows into cylinder body and causes wearing and tearing.During the slippage pump repairing, oil level descends gradually in the oily isolation tank, drops to certain altitude, and oil enters the loss that the flow passage components runner causes oil.Therefore, must be within the specific limits with oil level control.The high-low limit position of oil level is established upper contact and lower contact respectively in oily isolation tank.When the oil level in the oily isolation tank arrives upper contact, send electric control signal, make the automatic repairing of slippage pump; When the oil level in the oily isolation tank drops to lower contact, send electric control signal, slippage pump stops repairing.Through the continuous circulation of above-mentioned working state, promptly reach the oily balance of fluid end system.
Blow-off system of the present invention is to carry out at the pump work state, and oil-supplementing system carries out under the pump off working state, promptly carries out repairing when the plunger backhaul, and the phase difference of slippage pump and pump is 180 °.
The invention has the beneficial effects as follows: be quick on the draw, can control oil level in the isolation tank during slippage pump repairing effectively in safety range, prevent that oil level is too high or too low and cause the pump can't proper functioning, reduced the operating temperature of barrier film, the working life of having improved barrier film.
Description of drawings
Fig. 1 is a structure diagram of the present invention.
1 is bleed valve, and 2 is cylinder body, and 3 is barrier film, and 4 is Fill valve, and 5 is oily isolation tank, and 6 is slippage pump, and 7 is fuel tank, and a is a upper contact, and b is a lower contact, and A is an one-way valve, and B is an one-way valve.
Specific embodiment
As shown in Figure 1, bleed valve 1 is positioned at cylinder body 2 upper ends, barrier film 3 is positioned at cylinder body 2 left sides, and Fill valve 4 is positioned at cylinder body 2 lower ends, is connected by pipeline with slippage pump, communicate with oil circuit in the cylinder body simultaneously, cylinder body 2 is connected by oily isolation tank 5 with flow passage components, and oily isolation tank 5 middle and upper parts are oil, and the bottom is a slurry, oil level constantly moves up and down, and establishes upper and lower contact a, b in oil level high-low limit position.When the cylinder body top produced gas, a small amount of gas overflowed from one-way valve A, one-way valve A closure, and one-way valve B opens, and gas is emitted in bleed valve.Oil in the oil isolation tank 5 is constantly along with slurry flows away, and the oil in the system constantly reduces, and the oil level in the oily isolation tank constantly raises.When oil level is elevated to upper contact a, send electric control signal, slippage pump begins repairing, and Fill valve 4 is opened, and the oil level in the oily isolation tank 5 constantly descends, and when dropping to lower contact b, sends electric control signal, and slippage pump stops repairing, and slippage pump 4 cuts out.Repeat said process.
Oil-supplementing system among the present invention is an electric control system, and upper contact a, lower contact b all link to each other with sensor, has insulation rubber to separate between sensor and the oily isolation tank.This system can receive and dispatch electric control signal fast, in time begins repairing and stops repairing, has guaranteed the safe operation of pump.
Claims (4)
1. the oil balancing system of a reciprocating oil isolation membrane pump fluid end, comprise cylinder body, barrier film, be positioned at the bleed valve of cylinder body upper end and be positioned at the Fill valve of cylinder body lower end, oily isolation tank, it is characterized in that: adopt oily isolation diaphragm type structure, blow-off system and oil-supplementing system acting in conjunction, the oil level in the control isolation tank moves in safety range.
2. according to the oil balancing system of right 1 described reciprocating oil isolation membrane pump fluid end, it is characterized in that: oily isolation diaphragm type structure adopts oily isolation tank to connect cylinder body and flow passage components, the isolation tank middle and upper part is an oil, and its underpart is the high temperature slurry, with oil barrier film and high temperature slurry is kept apart.
3. according to the oil balancing system of right 1 described reciprocating oil isolation membrane pump fluid end, it is characterized in that: blow-off system is a bleed valve, and bleed valve is made up of the opposite one-way valve of both direction.
4. according to the oil balancing system of right 1 described reciprocating oil isolation membrane pump fluid end, it is characterized in that: oil-supplementing system is an electric control system, Fill valve links to each other with slippage pump by pipeline, communicate with system oil-way simultaneously, the high-low limit position of oil level is established the contact respectively in oily isolation tank, electric control signal is sent in the contact, and the control slippage pump begins or stop repairing, and oil level is moved between the high-low limit position.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200810034383 CN101245779B (en) | 2008-03-07 | 2008-03-07 | Oil balancing system of reciprocating oil isolation membrane pump fluid end |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200810034383 CN101245779B (en) | 2008-03-07 | 2008-03-07 | Oil balancing system of reciprocating oil isolation membrane pump fluid end |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN101245779A true CN101245779A (en) | 2008-08-20 |
| CN101245779B CN101245779B (en) | 2010-04-21 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 200810034383 Expired - Fee Related CN101245779B (en) | 2008-03-07 | 2008-03-07 | Oil balancing system of reciprocating oil isolation membrane pump fluid end |
Country Status (1)
| Country | Link |
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| CN (1) | CN101245779B (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103410708A (en) * | 2013-08-27 | 2013-11-27 | 成都添益天然气压缩机制造有限公司 | Automatic lubricating oil compensation device with automatic decompression valve |
| CN105889056A (en) * | 2015-01-20 | 2016-08-24 | 于长和 | Diaphragm floating ball type oil isolating device |
| CN105889036A (en) * | 2015-01-20 | 2016-08-24 | 于长和 | Diaphragm type oil isolating device |
| CN109653998A (en) * | 2018-11-28 | 2019-04-19 | 西安交通大学 | A kind of hydrogenation stations autoclave diaphragm compressor flow structure and overflow method and hydrogenation stations autoclave diaphragm compressor |
Family Cites Families (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2292919Y (en) * | 1996-10-25 | 1998-09-30 | 胜利石油管理局采油工艺研究院 | Automatic oil supplementing device of diaphragm pump |
| IT1297087B1 (en) * | 1997-11-28 | 1999-08-03 | Enea Ente Nuove Tec | DEVICE FOR PUMPING LIQUIDS OR AERIFORMS, WITH DOUBLE ACTING ALTERNATIVE MOTION OBTAINED BY HYDRAULIC SYSTEM. |
| TW511316B (en) * | 2001-08-15 | 2002-11-21 | Asia Pacific Fuel Cell Tech | Diaphragm pump and anode stream recirculation system using such pump for a fuel cell |
| CN2685607Y (en) * | 2003-12-26 | 2005-03-16 | 重庆水泵厂有限责任公司 | Uniform pressure oil supply device for diaphragm pump |
-
2008
- 2008-03-07 CN CN 200810034383 patent/CN101245779B/en not_active Expired - Fee Related
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103410708A (en) * | 2013-08-27 | 2013-11-27 | 成都添益天然气压缩机制造有限公司 | Automatic lubricating oil compensation device with automatic decompression valve |
| CN103410708B (en) * | 2013-08-27 | 2016-01-20 | 成都添益天然气压缩机制造有限公司 | Be provided with the lubricant oil automatic compensator of automatic decompression valve |
| CN105889056A (en) * | 2015-01-20 | 2016-08-24 | 于长和 | Diaphragm floating ball type oil isolating device |
| CN105889036A (en) * | 2015-01-20 | 2016-08-24 | 于长和 | Diaphragm type oil isolating device |
| CN109653998A (en) * | 2018-11-28 | 2019-04-19 | 西安交通大学 | A kind of hydrogenation stations autoclave diaphragm compressor flow structure and overflow method and hydrogenation stations autoclave diaphragm compressor |
Also Published As
| Publication number | Publication date |
|---|---|
| CN101245779B (en) | 2010-04-21 |
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Granted publication date: 20100421 Termination date: 20120307 |