CN106194658B - A kind of gas-liquid exchanger structure and the gas-liquid switch type gas compressor with the mechanism - Google Patents

A kind of gas-liquid exchanger structure and the gas-liquid switch type gas compressor with the mechanism Download PDF

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Publication number
CN106194658B
CN106194658B CN201610781582.0A CN201610781582A CN106194658B CN 106194658 B CN106194658 B CN 106194658B CN 201610781582 A CN201610781582 A CN 201610781582A CN 106194658 B CN106194658 B CN 106194658B
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China
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gas
liquid
seal
pressure vessel
sealing
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CN106194658A (en
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吴礼智
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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
    • F04BPOSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS
    • F04B39/00Component parts, details, or accessories, of pumps or pumping systems specially adapted for elastic fluids, not otherwise provided for in, or of interest apart from, groups F04B25/00 - F04B37/00
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B43/00Arrangements for separating or purifying gases or liquids; Arrangements for vaporising the residuum of liquid refrigerant, e.g. by heat
    • F25B43/003Filters

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  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Analytical Chemistry (AREA)
  • Power Engineering (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Filling Or Discharging Of Gas Storage Vessels (AREA)

Abstract

The present invention provides a kind of gas-liquid exchanger structure, part is exchanged including gas-liquid, seal boss, supporting arrangement, side seal assembly and end seals assembly, the wherein described gas-liquid exchanges part and is mounted in the seal boss by supporting arrangement, the both ends that the gas-liquid exchanges part are connected by end seals assembly with seal boss, the both sides that the gas-liquid exchanges part are connected by side seal assembly with seal boss, it includes that gas-liquid exchanges part support interconnecting piece that the gas-liquid, which exchanges part, cylindrical gas-liquid exchanges part ontology and several gas-liquids exchange groove for exchanging part ontology outer ring in gas-liquid is arranged.The gas-liquid switch type gas compressor of the present invention has better seal effect, quantity of gas leakage less;Gas-liquid switch type gas compressor is simple in structure, few easy workout part, repair simplicity, long lifespan, easy to manufacture, final assembly is convenient, cheap, reliable for operation, sturdy and durable.

Description

A kind of gas-liquid exchanger structure and the gas-liquid switch type gas compressor with the mechanism
Technical field
The present invention relates to machinery fields, specifically, being related to a kind of gas-liquid exchanger structure and the gas-liquid friendship with the mechanism Change formula gas compressor.
Background technology
Gas compressor is a kind of universal machine that purposes is very extensive, in compressed air, natural gas compressing and transport, is changed It is essential production equipment in the fields such as work, refrigeration, it may be said that be related to compressed gas all and pass through compressed gas Body all be unable to do without gas compressor in the field that produces and run.Currently, being widely used in the gas pressure in each gas field Contracting owner will have reciprocating compressor and rotary compressor two major classes, wherein reciprocating compressor includes various piston type pressures Contracting machine and reciprocating hydraulic formula compressor etc., rotary compressor include various screw compressors, centrifugal compressor, axial-flow type Compressor, liquid-piston compressor, sliding-vane compressor, scroll compressor etc..
When above-mentioned gas compressor normal operation, there is a common technological deficiencies always --- and above-mentioned gas compresses Machine always has quite a few gas to need repeated compression that could finally be pressed into high-pressure area in compressed gas.Such as reciprocal In formula compressor, reciprocating member (piston) between cylinder head must there are certain gaps, just can guarantee reciprocating member just in this way Often operation and normal compressed gas will lead to reciprocating member and cylinder top if very close to each other between reciprocating member and cylinder head The generation of phenomena such as portion's collision or liquid hammer, and then reciprocating compressor is damaged, therefore in reciprocating compressor, reciprocating member and gas Between at the top of cylinder must there are certain gaps, however, between reciprocating member and cylinder head must there are gap result in again Some total gas is detained in this gap and cannot disposably be pressed into high-pressure area, and which results in reciprocating pressures Contracting machine some total gas during compressed gas needs repeated compression that can finally be pressed into high-pressure area;In another example It is necessary between revolving part (screw rod, blade, slide plate, rotor, scroll etc.) and fixed cylinder block in various rotary compressors There are certain gaps, just can guarantee revolving part normal operation and normal compressed gas in this way, if revolving part and fixed gas It is very close to each other between cylinder body, phase mutual friction between revolving part and fixed cylinder block or generation phenomena such as mutually shock will be caused, And then rotary compressor is damaged, it must there are certain therefore in rotary compressor, between revolving part and fixed cylinder block Gap, however, between revolving part and fixed cylinder block must there are gap result in again always some compressed High pressure gas leaks into area of low pressure by these gaps from high-pressure area, then repeats indentation higher-pressure region further through revolving part Domain, which results in rotary compressors during compressed gas, and some total gas needs repeated compression can Final indentation high-pressure area.In conclusion existing various common gas compressors are in compressed gas, gas is repeated pressure Contracting is the shared technological deficiency present in them, and this technological deficiency results in existing various common gas compressor fortune It needs to consume and waste a large amount of energy when row that compressed gas could be produced.
Another common technological deficiency is existing for above-mentioned gas compressor:By low-pressure gas be compressed into high pressure and When extra-high, it is necessary to can be only achieved purpose using the mode of multi-stage compression.Such as in various reciprocating compressors, back and forth Maximum distance of the reciprocating member (piston) between cylinder head determines the reciprocating compression when part (piston) compression travel starts The highest compression ratio of machine, the compression ratio to improve reciprocating compressor must must just increase reciprocating member (piston) compression travel and open Maximum distance of the reciprocating member (piston) between cylinder head when the beginning, it is clear that in reciprocating compressor, reciprocating member (piston) pressure The elongation that maximum distance of the reciprocating member (piston) between cylinder head can not possibly be unlimited when indention journey starts, it is so, past Twin compressor will become very huge, while be limited by factors such as mechanical strength, stability, lubrication, coolings, reciprocating The single stage compress of compressor is limited than always, and therefore, low-pressure gas is being compressed into high pressure and surpassed by reciprocating compressor When high pressure gas, it is necessary to can be only achieved purpose using the mode of multi-stage compression.In another example in various rotary compressors, rotation Between part (screw rod, blade, slide plate, rotor, scroll etc.) and fixed cylinder block must there are certain gaps, could protect in this way Demonstrate,prove revolving part normal operation and normal compressed gas, and between revolving part and fixed cylinder block must there are gap cause Some total high pressure gas compressed leaks into area of low pressure by these gaps from high-pressure area, and rotary Number of compression stages in compressor is fewer, and high pressure gas leaks into the resistance of area of low pressure with regard to smaller from high-pressure area, high pressure gas Also easier to leak into area of low pressure from high-pressure area, therefore, in actual production, rotary compressor always needs multistage Low-pressure gas could be compressed into high pressure or extra-high by compression, even in many rotary compressors (such as screw Compressor, sliding-vane compressor, scroll compressor etc.) in, between revolving part and fixed cylinder block must there are gap, make Low-pressure gas can not be compressed into increasing number of compression stages high pressure or extra-high by obtaining them.
Invention content
The present invention provides a kind of gas-liquid exchanger structure, and a kind of gas-liquid exchange is provided on the basis of the gas-liquid exchanger structure Formula gas compressor, the technical problem to be solved is that a part of gas needs repeated compression that could press in traditional gas compressor Need multi-stage compression that could give birth to when producing high pressure and extra-high in the problem of entering high pressure field and traditional gas compressor The problem of production.
The technical solution that the present invention solves above-mentioned technical problem is as follows:
The present invention provides a kind of gas-liquid exchanger structure, including gas-liquid exchanges part, supporting arrangement, seal boss, side sealing Assembly and end seals assembly, the gas-liquid exchange part and are supported in the seal boss by the supporting arrangement, the gas The both ends that liquid exchanges part are connected by end seals assembly with seal boss, and the gas-liquid exchanges part by being set in its both sides Side seal assembly be connected on seal boss.
Further, the seal boss includes seal boss bottom plate and is arranged on seal boss bottom plate hollow convex Playscript with stage directions body, is provided with multiple seal boss interconnecting pieces on the seal boss bottom plate, and the top of the boss ontology is provided with close Boss openings are sealed, the both ends and both sides of the seal boss opening all have smooth outer surface, and the gas-liquid exchanges part set It is connected in seal boss opening.
In gas-liquid exchanger structure, the effect of seal boss is:Part, side seal assembly, end seals are exchanged with gas-liquid The collective effects such as assembly to which high-pressure bottle and low pressure vessel to be spaced from each other, and seal against each other;Ensure in high-pressure bottle simultaneously The liquid in portion can exchange part by gas-liquid with the gas inside low pressure vessel and swap.In assembly, in the seal boss Empty position is connected with low-pressure gas chamber.
Further, the gas-liquid exchange part includes:
Gas-liquid exchanges part ontology, and the gas-liquid, which exchanges the cylinder that part ontology is cylindrical and is socketed in seal boss opening, to be worked as In;
Gas-liquid exchanges groove, and it is at least one outside for being distributed in the gas-liquid and exchanging part ontology that the gas-liquid, which exchanges groove, Groove on face, the gas-liquid exchanges groove can be completely covered by the sealing cambered surface.
Gas-liquid exchanges part and interconnecting piece, the gas-liquid exchange part support interconnecting piece is supported to exchange part ontology with the gas-liquid and be linked as One, the gas-liquid exchange part support interconnecting piece and are connected with supporting arrangement;
Be located by connecting hole, and the both ends that part ontology is exchanged in the gas-liquid are arranged in the hole that is located by connecting, and the gas-liquid exchanges Part ontology is connected by the hole that is located by connecting with end seals assembly.
Further, the end seals assembly includes:
End seals part, the end seals part include the cylindric inner cylinder and sealing veneer for having smooth outer surface, The inner cylinder is socketed in the gas-liquid and exchanges on part ontology and seal against each other, and the sealing veneer is the axis phase with the inner cylinder Vertical smooth plane, the sealing veneer mutually join with the inner cylinder;
End seals assembly preload piece, the end seals assembly preload piece is connected with the end seals part, and makees For the end seals part so that the end seals part under the action of pretightning force always with the seal boss and The side seal assembly fits closely;
End seals part locating piece:The end seals part locating piece includes being fixed for exchanging part ontology with the gas-liquid The end of connection is fixedly connected with portion and the end active connection part for being flexibly connected with the end seals part, the end Sealing element locating piece is fixedly installed in the both ends of the gas-liquid exchange part ontology by the end portion of being fixedly connected and is lived by end Rotation connection is flexibly connected with the end seals part.
Further, the side seal assembly includes:
Side seal, is provided with smooth sealing cambered surface in the side seal, the radian of the sealing cambered surface with The radian that the gas-liquid exchanges part ontology matches, and the side seal is provided at both ends with the side with smooth outer surface End seals face, side end sealing surface mutually join with the sealing cambered surface, and tool is provided in the side seal There are the sealing bottom surface of smooth outer surface, the sealing bottom surface mutually to join with side end sealing surface, the sealing bottom surface It is fitted closely with the smooth outer surface of seal boss opening both sides, flexible connection is additionally provided in the side seal Portion;
Side seal assembly preload piece:The side seal preload piece is connected and acts on the side seal The side seal, so that with the gas-liquid to exchange part ontology always under the action of pretightning force tight for the side seal Closely connected conjunction;
Side locating piece:The side locating piece is fixedly installed in by connector on the seal boss, the side The side active connection part for being flexibly connected with the side seal, the side active connection part are provided in locating piece It is flexibly connected with the active connection part being arranged in the side seal.
Further, the length of the sealing cambered surface is more than the length that each gas-liquid exchanges part groove, the sealing cambered surface Radian be more than the radian that each gas-liquid exchanges groove so that the sealing cambered surface can cover each gas-liquid exchange groove, The side seal assembly preload piece be spring or magnet, the end seals assembly preload piece be spring or magnet, it is described The length of side seal is consistent with the length for the seal boss opening being arranged on the boss ontology.
In gas-liquid exchanger structure, the effect of side seal assembly is that sealing gas-liquid exchanges part ontology outer circle and seal boss Gap between opening both sides.During gas-liquid exchanger structure is run, when the sealing cambered surface in side seal is to some gas When liquid exchange groove is completely covered, the fluid that part inside grooves are exchanged in the gas-liquid is in sealing state, that is, is in the gas-liquid Exchange part inside grooves fluid at this time can neither be connected inside high-pressure bottle, can not with low pressure vessel inside be connected It is logical, it can not be connected with the external world.When side, seal assembly uses magnet as side seal assembly preload piece, side sealing Sealing cambered surface and gas-liquid in part, which exchange the gas-liquid exchange part main body in part, to select magnetic material to be made.
In gas-liquid exchanger structure, the effect of end seals assembly is that sealing gas-liquid exchanges part and seal boss opening both ends Between gap.Wherein, when end seals assembly preload piece is big spring, it is close that big spring by big spring seat is installed on end Between sealing and end seals part locating piece;When end seals assembly preload piece is little spring, little spring passes through little spring seat It is installed between end seals part and end seals part locating piece;When end seals assembly uses magnet as end seals assembly When preload piece, the both ends of sealing veneer, the both ends of side seal, seal boss in end seals part need to select magnetic material It is made.In assembly, which is flexibly connected with end seals part locating piece, so that end seals part can held Part synchronous rotary is exchanged with gas-liquid under the drive of head sealing element locating piece.
Further, the junction between the seal boss is open both ends and seal boss opening both sides is also It is provided with sealing strip;Junction between the sealing veneer and the inner cylinder of the end seals part of the end seals part is also set up There is sealing strip;Junction between the side end sealing surface of the side seal and the sealing cambered surface of the side seal It is additionally provided with sealing strip;Between sealing bottom surface and the side end sealing surface of the side seal of the side seal Junction is additionally provided with sealing strip;The effect of each sealing strip be further enhance it is close between each parts in gas-liquid exchanger structure Seal effect.
The invention further relates to a kind of gas-liquid switch type gas compressors, including low pressure vessel, high-pressure bottle, above-mentioned gas-liquid Exchange mechanism, hydraulic system, tank level control system, it is characterised in that:The high-pressure bottle is installed on the upper of the low pressure vessel Side;The gas-liquid exchanger structure is respectively as the component part of the high-pressure bottle and the low pressure vessel and is installed on the height Between pressure vessel and the low pressure vessel;Hydraulic pump is housed, the hydraulic pump is by the low pressure vessel in the hydraulic system It draws low pressure liquid and is pressed into inside the high-pressure bottle after being pressurized low pressure liquid in portion;The tank level control system is for controlling The liquid level of the high-pressure bottle internal liquid.
Further, the low pressure vessel includes low pressure vessel shell, and the low pressure vessel shell is in upper end opening Empty capsid, the open end of the low pressure vessel shell is fixed by the seal boss bottom plate of connector and the seal boss to be connected It connects;It is hollow chamber inside the low pressure vessel, the lower part of chamber is the low pressure liquid chamber for loading liquid, and top is Low-pressure gas chamber for loading gas;The shell of the low-pressure gas chamber is equipped with low-pressure gas entrance.
Further, the high-pressure bottle includes high pressure vessel, and the high pressure vessel is in lower ending opening Empty capsid, the open end of the high pressure vessel is fixed by the seal boss bottom plate of connector and the seal boss to be connected It connects;It is hollow chamber inside the high-pressure bottle, the lower part of chamber is the highly pressurised liquid chamber for loading liquid, and top is High pressure gas chamber for loading gas;The shell of the high pressure gas chamber is exported equipped with high pressure gas.
Further, the junction between the gas-liquid exchanger structure and high pressure vessel is equipped with the sealing for sealing Part, the gas-liquid exchanger structure pass through sealing element airtight connection with high pressure vessel;The gas-liquid exchanger structure holds with low pressure Junction between device shell is equipped with the sealing element for sealing, and the gas-liquid exchanger structure passes through sealing with low pressure vessel shell Part airtight connection.
The working mechanism of gas-liquid switch type gas compressor:
Referring to Figure 11 and Figure 12, the process of gas-liquid switch type gas compressor normal operation, actually sealing, gas-liquid The process of exchange, gas compression and Liquid level mutual cooperation operation.So as to produce compressed gas.
Sealing --- in gas-liquid switch type gas compressor, the collective effect of each parts makes in gas-liquid exchanger structure Obtaining gas-liquid exchange mechanism has good sealing function, can be spaced from each other high-pressure bottle and low pressure vessel;Gas-liquid exchanger Sealing element between structure and high pressure vessel can will be spaced from each other between inside the high-pressure bottle and external world;Gas-liquid exchanger structure Sealing element between low pressure vessel shell can will be spaced from each other between inside the low pressure vessel and external world.
Gas-liquid exchanges --- when gas-liquid switch type gas compressor is run, under the drive of external force, and gas-liquid exchanger structure In gas-liquid exchange part and end seals assembly and will rotate, now exchanging the first groove of groove with one of gas-liquid is Example, makes an explanation to the operation principle of gas-liquid exchanger structure:If gas-liquid exchanges part and rotates clockwise, the first groove also revolves clockwise Turn, during the first groove rotates to B points by A points, the first groove gradually with the low-pressure gas chamber inside low pressure vessel 63 are connected and are finally connected completely with low-pressure gas chamber 63, under liquid dead weight and the double action of centrifugal force, originally Liquid in the first inside grooves is thrown out of the first groove and finally flows into the low pressure liquid chamber 62 inside low pressure vessel, together When low-pressure gas the first inside grooves are charged under the action of negative pressure, to realize liquids and gases inside low pressure vessel Exchange;During the first groove rotates to C points by B points, the first groove is gradually covered and final by side seal 21 It is completely covered by side seal 21, when the first groove is completely covered by side seal 21, in the first inside grooves Gas is in sealing state, can neither be connected with the low-pressure gas chamber 63 inside low pressure vessel, can not be with high pressure-volume Highly pressurised liquid chamber 72 inside device is connected, and can not be connected with external environment, ensures that in this way in the first groove The gas in portion can be transported to by the first groove inside high-pressure bottle;During the first groove rotates to D points by C points, First groove be gradually connected with the highly pressurised liquid chamber 72 inside high-pressure bottle and it is final completely with 72 phase of highly pressurised liquid chamber Connection, low-pressure gas of the first inside grooves is totally submerged inside in highly pressurised liquid chamber 72 during this, due to gas Density is small more than the density of liquid, thus the gas of the first inside grooves the first groove can be progressively disengaged under the action of buoyancy and It floats in the high pressure gas chamber 73 inside high-pressure bottle, and the space of the first inside grooves is then filled by liquid, from And realize exchange of the liquids and gases inside high-pressure bottle;During the first groove rotates to A points by D points, first Groove is gradually covered by side seal 21 and is finally completely covered by side seal 21, when the first groove is by side seal 21 it is completely covered when, be in sealing state in the liquid of the first inside grooves, can neither be with the height inside high-pressure bottle Hydraulic fluid fluid chamber 72 is connected, and can not be connected with the low-pressure gas chamber 63 inside low pressure vessel, can not be with the external world Environment is connected, and ensures that the liquid of the first inside grooves can be transported to by the first groove inside low pressure vessel in this way. It will be evident that when the first groove re-rotates to A points by A points, a working cycle process is completed, when gas-liquid exchanges part not When rotating disconnectedly, gas continuously will flow into the low-pressure gas chamber 63 inside low pressure vessel by low-pressure gas source, then pass through Each groove that gas-liquid exchanges in part is transported to inside high-pressure bottle, while the liquid inside high-pressure bottle is exchanged also by gas-liquid Each groove in part is transported to inside low pressure vessel, so that the gas inside the liquid and low pressure vessel inside high-pressure bottle Body can be swapped constantly.
Gas compression --- when gas-liquid switch type gas compressor is run, under the drive of external force, in hydraulic system Constantly by inside the liquid indentation high-pressure bottle in low pressure vessel, the liquid being pressed into inside high-pressure bottle acts on hydraulic pump There are two main:When the liquid that supplement gas-liquid exchanger structure is taken away inside high-pressure bottle, in gas-liquid switch type gas compression In machine, inside high-pressure bottle cannot not no liquid, if liquid not enough inside high-pressure bottle, then, by low pressure Gas inside container delivered inside to high-pressure bottle will be by each trough return current to low pressure vessel inside, it is so low Gas inside pressure vessel can be not transported to inside high-pressure bottle, needless to say be had compressed;Second is that compressed gas, In gas-liquid switch type gas compressor, since the volume inside high-pressure bottle is fixed and limited, liquid is in high-pressure bottle The volume in portion is also dynamic stability, in this case, when compressible gas and incompressible liquid are all constantly defeated When being sent to inside the high-pressure bottle of finite volume, compressible gas will necessarily be compressed by incompressible liquid, to produce Raw compressed gas.
Liquid level --- when gas-liquid switch type gas compressor is run, due to the influence of various factors, hydraulic pressure pump pressure Gas-liquid exchanger structure liquid of discharge inside high-pressure bottle can not be consistently equal to by entering the flow of the liquid inside high-pressure bottle Flow.If the flow that hydraulic pressure is pumped into the liquid inside high-pressure bottle is frequently larger than gas-liquid exchanger structure inside high-pressure bottle The flow of the liquid of discharge, then the liquid level inside high-pressure bottle will constantly rise, is finally led without being controlled Liquid is caused to be discharged into gas equipment by the high pressure gas outlet being equipped in high pressure gas chamber, due to gas-liquid switch type gas pressure Liquid in contracting machine is limited, will result in that liquid stock inside low pressure vessel is reduced in the course of time and cannot recycle makes With in turn resulting in entire gas-liquid switch type gas compressor and be unable to operate normally;If hydraulic pressure is pumped into inside high-pressure bottle The flow of liquid is frequently less than the flow for the liquid that gas-liquid exchanger structure is discharged inside high-pressure bottle without being controlled, then Liquid level inside high-pressure bottle will constantly decline, and eventually lead to the high pressure gas inside high-pressure bottle and handed over each gas-liquid It changes groove to be in direct contact, then high pressure gas will exchange groove by each gas-liquid and leak into low pressure vessel, in turn result in entire Gas-liquid switch type gas compressor is unable to operate normally.Therefore in order to ensure that gas-liquid switch type gas compressor can be transported normally Row, must be configured with tank level control system in gas-liquid switch type gas compressor.Tank level control system is the prior art in gas Application in liquid switch type gas compressor, effect be control high-pressure bottle inside liquid level, be allowed to always be in set In fixed effective range, and then ensure the normal operation of gas-liquid switch type gas compressor, tank level control system is to pass through adjusting Hydraulic pressure is pumped into the stream of the flow and gas-liquid exchanger structure liquid of discharge inside high-pressure bottle of the liquid inside high-pressure bottle Difference between amount controls the liquid level inside high-pressure bottle.
When gas-liquid exchanger structure is run, the low-pressure gas inside low pressure vessel is constantly transported in high-pressure bottle Portion then will appear negative pressure inside low pressure vessel, and under the action of negative pressure, the gas of extraneous low-pressure gas source can be pressed into low automatically Inside pressure vessel, to constantly provide low-pressure gas for low pressure vessel.
The beneficial effects of the present invention are:First, gas-liquid switch type gas compressor of the invention has good sealing Property.Without mechanical clearance in gas-liquid switch type gas compressor, across thickness thickness between high pressure gas and low-pressure gas Liquid, therefore area of low pressure, and gas-liquid switch type gas compressor can be leaked into from high-pressure area almost without gas Low-pressure gas can be disposably transported to high-pressure area, the degree of gas repeated compression can be preferably minimized, Jin Erda Energy-efficient effect is arrived.Secondly, gas-liquid switch type gas compressor of the invention has good cooling effect, in gas-liquid In switch type gas compressor, compressed gas needs just be transported in high-pressure area across one layer of liquid, compressed gas Good cooling is obtained during across liquid level, therefore closer when gas-liquid switch type gas compressor compressed gas In isotherm compression, and then achieve the effect that energy-efficient.Again, gas-liquid switch type gas compressor of the invention has high Single stage compress ratio, in gas-liquid switch type gas compressor, the output pressure of compressed gas is not limited by mechanical dimension. Theoretically, the output pressure of compressed gas is the not no upper limit in gas-liquid switch type gas compressor, as long as gas-liquid switch type gas The mechanical strength of gas compressor is sufficiently strong, then it only needs one stage of compression that can export the gas of enough pressure, rather than Existing various gas compressors need multi-stage compression that could export the gas of enough pressure like that, this technical characteristic is existing Any type gas compressor not available for, this feature can make gas-liquid switch type gas compressor structure simpler List, cost is less expensive, manufacture is more convenient, repair is easier.
Description of the drawings
Fig. 1 is the structural schematic diagram of the gas-liquid exchanger structure of the present invention;
Fig. 2 is the A-A cross-sectional views of the gas-liquid exchanger structure of the present invention;
Fig. 3 is the structural schematic diagram of the seal boss of the gas-liquid exchanger structure of the present invention;
Fig. 4 is that the gas-liquid of the gas-liquid exchanger structure of the present invention exchanges the structural schematic diagram of part;
Fig. 5 is a kind of structural schematic diagram of end seals assembly of the gas-liquid exchanger structure of the present invention;
Fig. 6 is a kind of structural schematic diagram of end seals assembly of the gas-liquid exchanger structure of the present invention;
Fig. 7 is a kind of structural schematic diagram of side seal assembly of the gas-liquid exchanger structure of the present invention;
Fig. 8 is a kind of structural schematic diagram of side seal assembly of the gas-liquid exchanger structure of the present invention;
Fig. 9 is the structural schematic diagram of the low pressure vessel of the gas-liquid switch type gas compressor of the present invention;
Figure 10 is the structural schematic diagram of the high-pressure bottle of the gas-liquid switch type gas compressor of the present invention;
Figure 11 is the structural schematic diagram of the gas-liquid switch type gas compressor of the present invention;
Figure 12 is the sectional view of Figure 11 of the present invention;
Figure 13 is a kind of structure chart of gas-liquid switch type gas compressor of the present invention;
Figure 14 is a kind of structure chart of gas-liquid exchanger structure of the present invention;
Figure 15 is the z-z sectional views of Figure 14 of the present invention;
Figure 16 is a kind of structure chart of gas-liquid switch type gas compressor of the present invention;
Figure 17 is the X-X sectional views of Figure 16 of the present invention;
Figure 18 is the Y-Y sectional views of Figure 16 of the present invention
Figure 19 is a kind of structure chart of gas-liquid switch type gas compressor of the present invention;
Figure 20 is the O-O sectional views of Figure 19 of the present invention;
Figure 21 is the Q-Q sectional views of Figure 19 of the present invention;
Figure 22 is the P-P sectional views of Figure 19 of the present invention.
Reference sign:
1, gas-liquid exchanges part, and 2, side seal assembly, 3, end seals assembly, 4 seal bosses, 5 supporting arrangements, 11, gas Liquid exchanges part ontology, 12, gas-liquid exchange groove, 13, be located by connecting hole, 14, gas-liquid exchange part and support interconnecting piece, 21, side it is close Sealing, 211, sealing cambered surface, 212, side seal active connection part, 22, side seal assembly preload piece, 23, side positioning Part, 232, side active connection part, 31, end seals part, 311, inner cylinder, 312, sealing veneer, 313, end seals side, 32, End seals assembly preload piece, 33, end seals part locating piece, 331, end be fixedly connected with portion, 332, end active connection part, 41, seal boss bottom plate, 42, boss ontology, 44, seal boss opening, 43, seal boss interconnecting piece, 6, low pressure vessel, 7, high Pressure vessel, 61, low pressure vessel shell, 62, low pressure liquid chamber, 63, low-pressure gas chamber, 64, low-pressure gas entrance, 71, high Pressure vessel shell, 72, highly pressurised liquid chamber, 73, high pressure gas chamber, 74, high pressure gas outlet, 8, exchange in groove from gas-liquid It is discharged and flows to the gas of heavy pressure gas chamber room, 9, the liquid for being discharged and flowing to low pressure liquid chamber in groove is exchanged from gas-liquid, 10, gas-liquid exchanger structure, 111, power supply, 112, controller, 113, liquid level measurer, 114, linker, 115, electric wire, 116, even Connect device, 117, engine, 118, auxiliary sealing member, 119, connector, 120, liquid non-return valve, the 121, first groove, 122, liquid Body pipeline, 1231, hydraulic pump, 124, sedimeter, 131, mechanical seal, 132, cooling device, 133, heat exchanger: 134, high pressure gas pipeline, 135, gas-liquid separator, 136, barostat, 137, cooling gas check valve, 138, gas-liquid cushion pad, 139, power lug, 140, one word nozzle, 141, change-over switch, 142, intermediate receptacle shell, 143, intermediate receptacle gas chamber, 144, intermediate receptacle liquid chamber, 145, conversion gas circuit, 1232, volume adjustable hydraulic pump.
Specific implementation mode
The principle and features of the present invention will be described below with reference to the accompanying drawings, and the given examples are served only to explain the present invention, and It is non-to be used to limit the scope of the present invention.
Specific embodiment 1
As shown in figures 1-8, the present invention relates to a kind of gas-liquid exchanger structures, including gas-liquid to exchange part 1, supporting arrangement 5, sealing Boss 4, side seal assembly 2 and end seals assembly 3, the gas-liquid exchange part 1 are supported on described by the supporting arrangement 5 In seal boss 4, the both ends that the gas-liquid exchanges part 1 are connected by end seals assembly 3 with seal boss 4, the gas-liquid Part 1 is exchanged to be connected on seal boss 4 by the side seal assembly 2 for being arranged on the outside.
The seal boss 4 includes seal boss bottom plate 41 and the hollow boss sheet being arranged on seal boss bottom plate 41 Body 42 is provided with multiple seal boss interconnecting pieces 43 on the seal boss bottom plate 41, and the top of the boss ontology 42 is equipped with Seal boss opening 44, the gas-liquid exchange part 1 and are socketed in seal boss opening 44.Seal boss bottom plate 41 is hollow , it is provided with boss ontology 42 on hollow seal boss bottom plate 41, boss ontology 42 is also hollow, and seal boss The hollow position of bottom plate 41 position hollow with boss ontology 42 is connected;It is provided at the top of hollow boss ontology 42 close Boss openings 44 are sealed, the both ends of seal boss opening 44 are also respectively provided with the smooth end part seal plane being mutually parallel;It should The both sides of seal boss opening 44 are also respectively arranged with smooth side sealing surface;The end part seal plane respectively with it is corresponding Side sealing surface is connected, and junction is also respectively provided with sealing strip.
The gas-liquid exchanges part:
Gas-liquid exchanges part ontology 11, and the gas-liquid exchanges the cylinder that part ontology 11 is cylindrical and is socketed in seal boss and opens In mouth 44;
Gas-liquid exchanges groove 12, and the gas-liquid exchanges groove 12 and is distributed in the gas-liquid exchange part ontology 11 to be at least one Lateral surface on groove;
Gas-liquid exchanges part and interconnecting piece 14, the gas-liquid is supported to exchange part support interconnecting piece 14 and exchange part ontology with the gas-liquid 11 are linked together, and the gas-liquid exchanges part support interconnecting piece 14 and is connected with supporting arrangement 5;
Be located by connecting hole 13, and the both ends that part ontology 11 is exchanged in the gas-liquid, the gas is arranged in the hole 13 that is located by connecting Liquid exchanges part ontology 11 and is connected with end seals assembly 3 by the hole 13 that is located by connecting.
The end seals assembly includes:
End seals part 31, the end seals part 31 include having the cylindric inner cylinder 311 of smooth outer surface and close Sealing label face 312, the inner cylinder 311 are socketed in the gas-liquid and exchange on part ontology 11 and seal against each other, and the sealing veneer 312 is With the smooth plane of the axis perpendicular of the inner cylinder 311, the sealing veneer 312 mutually joins with the inner cylinder 311;
End seals assembly preload piece 32, the end seals assembly preload piece 32 are connected with the end seals part 31 Connect, and act on the end seals part 31 so that the end seals part 31 under the action of pretightning force always with it is described Seal boss 4 and the side seal assembly 2 fit closely;
End seals part locating piece 33:The end seals part locating piece 33 includes for exchanging part ontology with the gas-liquid 11 ends being fixedly connected are fixedly connected with portion 331 and the end flexible connection for being flexibly connected with the end seals part 31 Portion 332, the end seals part locating piece 33 are fixedly connected with portion 331 by end and are fixedly installed in the gas-liquid exchange part ontology Both ends and be flexibly connected with the end seals part 31 by end active connection part 332.
The side seal assembly includes:
Side seal 21 is provided with smooth sealing cambered surface 211, the sealing cambered surface in the side seal 21 The radian that 211 radian exchanges part ontology 11 with the gas-liquid matches, and being provided at both ends with for the side seal 21 has The side end sealing surface of smooth outer surface, side end sealing surface mutually join with the sealing cambered surface 211, the side The sealing bottom surface with smooth outer surface, the sealing bottom surface and the side end sealing surface phase are provided in face seal 21 The smooth outer surface of mutually handing-over, the sealing bottom surface and 44 both sides of seal boss opening fits closely, and the side is close Active connection part 212 is additionally provided on sealing 21;
Side seal assembly preload piece 22:The side seal preload piece 22 is connected simultaneously with the side seal 21 The side seal 21 is acted on, so that the side seal 21 is handed over the gas-liquid always under the action of pretightning force Part ontology 11 is changed to fit closely;
Side locating piece 23, the side locating piece 23 is fixedly installed in by connector on the seal boss 4, described The side active connection part 232 for being flexibly connected with the side seal 21, the side are provided in side locating piece 23 Face active connection part 232 is flexibly connected with the active connection part 212 being arranged in the side seal 21.
The length of the sealing cambered surface 211 is more than the length that each gas-liquid exchanges part groove 12, the sealing cambered surface 211 Radian is more than the radian that each gas-liquid exchanges groove 12, so that can to cover the exchange of each gas-liquid recessed for the sealing cambered surface 211 Slot 12, the side seal assembly preload piece 22 be spring or magnet, the end seals assembly preload piece 32 be spring or Magnet, the length phase one of the length of the side seal 21 and the seal boss opening 44 being arranged on the boss ontology 42 It causes.
Embodiment 2
The present invention also provides a kind of gas-liquid switch type gas compressors:
As is illustrated by figs. 11 and 12, the gas-liquid switch type gas compressor is mainly held by gas-liquid exchanger structure 10, low pressure The compositions such as device 6, high-pressure bottle 7, hydraulic system, tank level control system, wherein gas-liquid exchanger structure 10 are located at low pressure vessel 6 and height It is spaced from each other between pressure vessel 7 and by low pressure vessel 6 and high-pressure bottle 7;
Gas-liquid exchanger structure 10 is connected by connector 1161 with the first engine 1171, the gas-liquid exchanger structure 10 As described in example 1 above;
Low pressure vessel 6 is mainly made of gas-liquid exchanger structure 10 and low pressure vessel shell 61, wherein gas-liquid exchanger structure 10 It is fixedly connected above low pressure vessel shell 61 and by connector 119;Gas-liquid exchanger structure 10 and low pressure vessel shell 61 Auxiliary sealing member 118 is also equipped between junction;Gas-liquid exchanger structure 10 and low pressure vessel shell 61 collectively constitute in one The top of empty sealing cavity, cavity loads low-pressure gas, and lower section loads low pressure liquid;It is additionally provided in low pressure vessel shell 61 Low-pressure gas entrance 64 for introducing low-pressure gas;
High-pressure bottle 7 is mainly made of gas-liquid exchanger structure 10 and high pressure vessel 71, wherein gas-liquid exchanger structure 10 It is fixedly connected positioned at 71 lower section of high pressure vessel and by connector 119;Gas-liquid exchanger structure 10 and high pressure vessel 71 Auxiliary sealing member 118 is also equipped between junction;Gas-liquid exchanger structure 10 and high pressure vessel 71 collectively constitute in one The top of empty sealing cavity, cavity loads high pressure gas, and lower section loads highly pressurised liquid;It is additionally provided in high pressure vessel 71 High pressure gas for high pressure gas to be discharged exports 74;
Hydraulic system is mainly made of hydraulic pump 1231, the second engine 1172, fluid pipeline 122 etc., wherein hydraulic pump 1231 are connected with the second engine 1172 by connector 1162 and are installed on jointly inside low pressure vessel 6;Hydraulic pump 1231 It is installed in fluid pipeline 122,122 one end of fluid pipeline is connected with sedimeter 124, the other end and high pressure-volume It is connected inside device 7;
Tank level control system is mainly by controller 112, liquid level measurer 113, linker 114, the first engine 1171, Two engines 1172 etc. form, wherein controller 112 by electric wire 115 respectively with liquid level measurer 113, the first engine 1171, the second engine 1172 is electrically connected, and liquid level measurer 113 is used to measure the liquid level of linker 114, and measurement data is passed It is defeated by controller 112;Controller 112 controls the first engine 1171 and the second engine according to the liquid level of linker 114 1172 operation, and then control and the liquid level inside stable high voltage container 7.
In actual production and application, in order to increase the effect of compressed gas, in the gas-liquid switch type gas compressor It further include scheme further below:
As the further scheme of the present invention, the gas-liquid switch type gas compressor in this specific embodiment has added connection Device 114, the linker 114 be set to high pressure vessel 71 side and be connected inside high-pressure bottle 7;
As the further scheme of the present invention, the gas-liquid switch type gas compressor in this specific embodiment has added electric wire Connector 139, power lug 139 is respectively arranged in low pressure vessel shell 61 and high pressure vessel 71, so that electric wire 115 It through between inside and outside gas-liquid switch type gas compressor and can be interconnected;
As the further scheme of the present invention, the gas-liquid switch type gas compressor in this specific embodiment has added liquid One end of filter device 124, the sedimeter 124 is connected with low pressure liquid, and the other end is connected with hydraulic pump 1231, To improve the cleannes of liquid;
As the further scheme of the present invention, the gas-liquid switch type gas compressor in this specific embodiment has added liquid Check valve 120, which is set in fluid pipeline 122, to prevent the liquid in high-pressure bottle 7 from passing through liquid Body pipeline 122 flows back to inside low pressure vessel 6.
Specific embodiment 3
As shown in figure 13, a kind of transformation embodiment as the present invention, additionally provides a kind of gas-liquid switch type gas compression Machine, the gas-liquid switch type gas compressor is mainly by gas-liquid exchanger structure 10, low pressure vessel 6, high-pressure bottle 7, hydraulic system, liquid The compositions such as level controlling system, wherein gas-liquid exchanger structure 10 are between low pressure vessel 6 and high-pressure bottle 7 and by low pressure vessel 6 It is spaced from each other with high-pressure bottle 7;
The both ends that gas-liquid in gas-liquid exchanger structure 10 exchanges part 1 extend respectively into high-pressure bottle 7 by mechanical seal 131 Outside, gas-liquid exchange part 1 one end be connected with engine 117 by connector 116, the other end then by connector respectively with Hydraulic pump 1231 and volume adjustable hydraulic pump 1232 are connected, and the gas-liquid exchanger structure 10 is as described in example 1 above;
Low pressure vessel 6 is mainly made of gas-liquid exchanger structure 10 and low pressure vessel shell 61, wherein gas-liquid exchanger structure 10 It is fixedly connected above low pressure vessel shell 61 and by connector 119;Gas-liquid exchanger structure 10 and low pressure vessel shell 61 Auxiliary sealing member 118 is also equipped between junction;Gas-liquid exchanger structure 10 and low pressure vessel shell 61 collectively constitute in one The top of empty sealing cavity, cavity loads low-pressure gas, and lower section loads low pressure liquid;It is additionally provided in low pressure vessel shell 61 Low-pressure gas entrance 64 for introducing low-pressure gas;
High-pressure bottle 7 is mainly made of gas-liquid exchanger structure 10 and high pressure vessel 71, wherein gas-liquid exchanger structure 10 It is fixedly connected positioned at 71 lower section of high pressure vessel and by connector 119;Gas-liquid exchanger structure 10 and high pressure vessel 71 Auxiliary sealing member 118 is also equipped between junction;Gas-liquid exchanger structure 10 and high pressure vessel 71 collectively constitute in one The top of empty sealing cavity, cavity loads high pressure gas, and lower section loads highly pressurised liquid;It is additionally provided in high pressure vessel 71 High pressure gas for high pressure gas to be discharged exports 74;
Hydraulic system is mainly made of hydraulic pump 1231, volume adjustable hydraulic pump 1232, engine 117, fluid pipeline 122 etc., Wherein, hydraulic pump 1231 and volume adjustable hydraulic pump 1232 exchange part 1 by connector 116 with the gas-liquid in gas-liquid exchanger structure 10 It is connected again with engine 117 by connector 116 after being connected;Hydraulic pump 1231 and volume adjustable hydraulic pump 1232 are installed respectively In fluid pipeline 122,122 one end of fluid pipeline is connected with the sedimeter 124 inside low pressure vessel 6, separately It is connected inside one end and high-pressure bottle 7
Tank level control system is mainly by controller 112, liquid level measurer 113, linker 114, engine 117, hydraulic pump 1231, the compositions such as volume adjustable hydraulic pump 1232, wherein controller 112 by electric wire 115 respectively with liquid level measurer 113, engine 117, volume adjustable hydraulic pump 1232 is electrically connected, and liquid level measurer 113 is used to measure the liquid level of linker 114, and measurement data is passed It is defeated by controller 112;Controller 112 controls engine 117, hydraulic pump 1231, variable delivery hydraulic according to the liquid level of linker 114 The operation of pump 1232, and then control and the liquid level inside stable high voltage container 7.
In actual production and application, in order to increase the effect of compressed gas, in the gas-liquid switch type gas compressor It further include scheme further below:
Gas-liquid switch type gas compressor in this specific embodiment has added gas-liquid separator 135, the gas-liquid separator 135 are set in high-pressure air pipe 134, in order to the gas-liquid separation inside high-pressure bottle 7;Gas-liquid in this specific embodiment exchanges Formula gas compressor has added barostat 136, which is set in high-pressure air pipe 134, and passes through electric wire 115 are electrically connected with controller 112, in order to adjust the pressure of output gas;Gas-liquid switch type gas in this specific embodiment Compressor has added linker 114, the linker 114 be set to high pressure vessel 71 one side and with 7 inside phase of high-pressure bottle Connection;Gas-liquid switch type gas compressor in this specific embodiment has added mechanical seal 131, which is set to Between gas-liquid in high pressure vessel 71 and gas-liquid exchange mechanism 10 exchanges part 1, in order to by engine 117, hydraulic pump 1231, volume adjustable hydraulic pump 1232 etc. is installed on the outside of gas-liquid switch type gas compressor;Gas-liquid in this specific embodiment is handed over The formula gas compressor of changing has added cooling system, which is formed by cooling down equipment 132 and heat exchanger 133, wherein cold But equipment 132 is respectively arranged on the outside of gas-liquid switch type gas compressor, heat exchanger 133 extend through in high-pressure bottle 7 with And low pressure vessel 6 is inside and outside, and be connected respectively with corresponding cooling equipment, in order to preferably cooling gas-liquid switch type gas The body of compressor;Gas-liquid switch type gas compressor in this specific embodiment has added cooling gas check valve 137, the gas list It is set in high-pressure air pipe to valve 137, in order to prevent the high pressure gas in high-pressure air equipment from flowing back into high-pressure bottle 7 Portion;Gas-liquid switch type gas compressor in this specific embodiment has added gas-liquid cushion pad 138, and gas-liquid cushion pad 138 is distinguished Set on the inside of high-pressure bottle 7 and low pressure vessel 6, in order to reduce noise, reduce liquid to gas-liquid switch type gas compression The impact of machine body;Gas-liquid switch type gas compressor in this specific embodiment has added liquid non-return valve 120, the liquid list It is set in fluid pipeline 122 to valve 120, to prevent the liquid in high-pressure bottle 7 from flowing back to low pressure by fluid pipeline 122 Inside container 6.
In addition, the gas-liquid switch type gas compressor in this specific embodiment has added sedimeter 124, the liquid One end of filter device 124 is connected with low pressure liquid, and the other end is connected with fluid pipeline 122, to improve the clear of liquid Cleanliness.
Specific embodiment 4
As shown in Figure 14 and Figure 15, a kind of transformation embodiment as the present invention, additionally provides a kind of gas-liquid exchanger structure, The gas-liquid exchanger structure is converted on the basis of gas-liquid exchanger structure as shown in figures 1-8, and specific implementation is as follows: There are two hollow positions for setting on one seal boss bottom plate, have corresponding gas-liquid exchanger on each hollow position Structure 10 is coupled, and the gas-liquid exchanger structure 10 is as described in example 1 above, further, in the gas-liquid exchanger structure One end of each gas-liquid exchange part 1 each extends to the outside of high-pressure bottle 7, and each gas-liquid exchanges part 1 and high-pressure bottle shell Mechanical seal 131 is mounted between body 71.
Specific embodiment 5
As shown in Figure 16, Figure 17, Figure 18, as a kind of transformation embodiment of the present invention, a kind of gas-liquid exchange is additionally provided Formula gas compressor, the gas-liquid switch type gas compressor are a kind of gas-liquid switch types of multiple gas-liquid exchanger structure parallel runnings Gas compressor, mainly by groups such as gas-liquid exchanger structure 10, low pressure vessel 6, high-pressure bottle 7, hydraulic system, tank level control systems At wherein gas-liquid exchanger structure 10 is between low pressure vessel 6 and high-pressure bottle 7 and mutual by low pressure vessel 6 and high-pressure bottle 7 It separates;
Gas-liquid exchanger structure 10 in the gas-liquid switch type gas compressor is as described in example 4 above, further, the gas Gas-liquid exchanger structure 10 in liquid switch type gas compressor includes two gas-liquid exchanger structures arranged side by side, is the first gas-liquid respectively Exchange mechanism 101 and the second gas-liquid exchanger structure 102;
Low pressure vessel 6 is mainly made of gas-liquid exchanger structure 10 and low pressure vessel shell 61, wherein gas-liquid exchanger structure 10 It is fixedly connected above low pressure vessel shell 61 and by connector 119;Gas-liquid exchanger structure 10 and low pressure vessel shell 61 Auxiliary sealing member 118 is also equipped between junction;Gas-liquid exchanger structure 10 and low pressure vessel shell 61 collectively constitute in one The top of empty sealing cavity, cavity loads low-pressure gas, and lower section loads low pressure liquid;It is additionally provided in low pressure vessel shell 61 Low-pressure gas entrance 64 for introducing low-pressure gas;
High-pressure bottle 7 is mainly made of gas-liquid exchanger structure 10 and high pressure vessel 71, wherein gas-liquid exchanger structure 10 It is fixedly connected positioned at 71 lower section of high pressure vessel and by connector 119;Gas-liquid exchanger structure 10 and high pressure vessel 71 Auxiliary sealing member 118 is also equipped between junction;Gas-liquid exchanger structure 10 and high pressure vessel 71 collectively constitute in one The top of empty sealing cavity, cavity loads high pressure gas, and lower section loads highly pressurised liquid;It is additionally provided in high pressure vessel 71 High pressure gas for high pressure gas to be discharged exports 74;
Hydraulic system is mainly by hydraulic pump 1231, volume adjustable hydraulic pump 1232, the first engine 1171, the second engine 1172, the compositions such as fluid pipeline 122, wherein one end of the first gas-liquid exchanger structure 101 passes through connector 1161 and the first power Machine 1171 is connected, and the other end is then connected by connector 1162 with hydraulic pump 1231, and the one of the second gas-liquid exchanger structure 102 End is connected by connector 1163 with the second engine 1172, and the other end then passes through connector 1164 and volume adjustable hydraulic pump 1232 It is connected;Hydraulic pump 1231 and volume adjustable hydraulic pump 1232 are respectively arranged in fluid pipeline 122,122 one of fluid pipeline End is connected with the sedimeter 124 inside low pressure vessel 6, is connected inside the other end and high-pressure bottle 7;
Tank level control system is mainly by controller 112, liquid level measurer 113, linker 114, hydraulic pump 1231, variable liquid The compositions such as press pump 1232, the first engine 1171, the second engine 1172, wherein controller 112 by electric wire 115 respectively with Liquid level measurer 113, volume adjustable hydraulic pump 1232, the first engine 1171, the electrical connection of the second engine 1172, liquid level measurer 113 liquid level for measuring linker 114, and by data transfer to controller 112;Controller 112 is according to linker 114 Liquid level control the operation of volume adjustable hydraulic pump 1232, the first engine 1171, the second engine 1172, and then control and stablize Liquid level inside high-pressure bottle 7.
In actual production and application, in order to increase the effect of compressed gas, in the gas-liquid switch type gas compressor It further include scheme further below:
Gas-liquid switch type gas compressor in this specific embodiment has added power lug 139, and power lug 139 is set to In high pressure vessel 71, so that electric wire 115 can be through between inside and outside gas-liquid switch type gas compressor and phase It is intercommunicated;Gas-liquid switch type gas compressor in this specific embodiment has added gas-liquid separator 135, the gas-liquid separator 135 are set in high-pressure air pipe, in order to the gas-liquid separation inside high-pressure bottle 7;Gas-liquid switch type in this specific embodiment Gas compressor has added barostat 136, the barostat 136 be set to high-pressure air pipe in, and by electric wire 115 with Controller 112 is electrically connected, in order to adjust the pressure of output gas;Gas-liquid switch type gas compressor in this specific embodiment Added linker 114, the linker 114 be set to high pressure vessel 71 one side and be connected inside high-pressure bottle 7;This Gas-liquid switch type gas compressor in specific embodiment has added mechanical seal 131, which is set to high-pressure bottle Between gas-liquid in shell 71 and gas-liquid exchange mechanism 10 exchanges part 1, in order to by the first engine 1171, the second engine 1172 etc. are installed on the outside of gas-liquid switch type gas compressor;Gas-liquid switch type gas compressor in this specific embodiment adds If cooling system, the cooling system are formed by cooling down equipment 132 and heat exchanger 133, wherein cooling equipment 132 is respectively arranged on The outside of gas-liquid switch type gas compressor, heat exchanger 133 extend through inside and outside high-pressure bottle 7 and low pressure vessel 6, And be connected respectively with corresponding cooling equipment, in order to the body of preferably cooling gas-liquid switch type gas compressor;This tool Gas-liquid switch type gas compressor in body embodiment has added cooling gas check valve 137, which is set to high pressure gas In pipe, in order to prevent the high pressure gas in high-pressure air equipment from flowing back into inside high-pressure bottle 7;In this specific embodiment Gas-liquid switch type gas compressor has added gas-liquid cushion pad 138, and gas-liquid cushion pad 138 is respectively arranged on high-pressure bottle 7 and low The inside of pressure vessel 6, in order to reduce noise, reduce impact of the liquid to gas-liquid switch type gas compressor body;This is specific Gas-liquid switch type gas compressor in embodiment has added liquid non-return valve 120, which is set to fluid pipeline In 122, to prevent the liquid in high-pressure bottle 7 from being flowed back to inside low pressure vessel 6 by fluid pipeline 122.
In addition, the gas-liquid switch type gas compressor in this specific embodiment has added sedimeter 124, the liquid One end of filter device 124 is connected with low pressure liquid, and the other end is connected with fluid pipeline 122, to improve the clear of liquid Cleanliness.
Gas-liquid switch type gas compressor in this specific embodiment has added a word nozzle 140, which divides It is not connected with fluid pipeline 122, the direction of spout is respectively directed to each gas-liquid and exchanges the rail that groove moves in high-pressure bottle 7 Mark, to improve the speed of gas-liquid exchange.
Specific embodiment 6
As shown in Figure 19, Figure 20, Figure 21, Figure 22, as a kind of transformation embodiment of the present invention, a kind of gas-liquid is additionally provided Switch type gas compressor, wherein:1, the gas-liquid switch type gas compressor in this specific embodiment is a kind of multi-stage compression type Gas-liquid switch type gas compressor, mainly by the first gas-liquid exchanger structure 101, the second gas-liquid exchanger structure 102, low pressure vessel 6, the compositions such as medium pressure vessel, high-pressure bottle 7, hydraulic system 1, hydraulic system 2, tank level control system, wherein the first gas-liquid exchanges Mechanism 101 is spaced from each other between low pressure vessel 6 and medium pressure vessel and by low pressure vessel 6 with medium pressure vessel, and the second gas-liquid is handed over Converting mechanism 102 is spaced from each other between medium pressure vessel and high-pressure bottle 7 and by medium pressure vessel and high-pressure bottle 7.
The first gas-liquid exchanger structure 101, the second gas-liquid exchanger structure 102 in this specific embodiment are the gas-liquid switch types Indispensable special mechanism, essential structure are as described in example 1 above in gas compressor;
Low pressure vessel 6 in this specific embodiment is mainly by 61 groups of the first gas-liquid exchanger structure 101 and low pressure vessel shell At, wherein the first gas-liquid exchanger structure 101 is located at 61 top of low pressure vessel shell and is fixedly connected by connector 119;First Gas-liquid exchanger structure 101 and low pressure vessel shell are also equipped with auxiliary sealing member 118 between 61 junction;First gas-liquid exchanger Structure 101 and low pressure vessel shell 61 collectively constitute a hollow sealing cavity, and the top of cavity loads low-pressure gas, lower section dress Carry low pressure liquid;The low-pressure gas entrance 64 for introducing low-pressure gas is additionally provided in low pressure vessel shell 61.
Medium pressure vessel in this specific embodiment be both the first order compression high-pressure bottle 7 and the second level compression it is low Pressure vessel 6 is mainly made of the first gas-liquid exchanger structure 101, medium pressure vessel shell 142, the second gas-liquid exchanger structure 102, In, the first gas-liquid exchanger structure 101 is located at 142 lower section of medium pressure vessel shell and is fixedly connected by connector 119;First gas-liquid Auxiliary sealing member 118 is also equipped between exchange mechanism 101 and medium pressure vessel housing junction;Second gas-liquid exchanger structure 102 It is fixedly connected above medium pressure vessel shell 142 and by connector 119;Second gas-liquid exchanger structure 102 and medium pressure vessel Auxiliary sealing member 118 is also equipped between housing junction;First gas-liquid exchanger structure 101, medium pressure vessel shell 142, second Gas-liquid exchanger structure 102 collectively constitutes a hollow sealing cavity, and the top of cavity loads medium pressure gas, and lower section is pressed in loading Liquid.
High-pressure bottle 7 in this specific embodiment is mainly by 71 groups of the second gas-liquid exchanger structure 102 and high pressure vessel At, wherein the second gas-liquid exchanger structure 102 is located at 71 lower section of high pressure vessel and is fixedly connected by connector 119;Second Gas-liquid exchanger structure 102 and high pressure vessel are also equipped with auxiliary sealing member 118 between 71 junction;Second gas-liquid exchanger Structure 102 and high pressure vessel 71 collectively constitute a hollow sealing cavity, and the top of cavity loads high pressure gas, lower section dress Carry highly pressurised liquid;It is additionally provided with the high pressure gas for high pressure gas to be discharged in high pressure vessel 71 and exports 74.
Hydraulic system 1 in this specific embodiment is mainly by the first engine 1171, hydraulic pump 1231, the first variable delivery hydraulic Pump the composition such as 1232 and fluid pipeline 122, wherein the first engine 1171 passes through connector 1161 and the first gas-liquid exchanger Structure 101 is connected, and the first gas-liquid exchanger structure 101 is connected by connector 1162 with hydraulic pump 1231, and hydraulic pump 1231 is logical It crosses connector 1163 with the first volume adjustable hydraulic pump 1232 to be connected, hydraulic pump 1231, the first volume adjustable hydraulic pump 1232 are installed respectively In fluid pipeline 122, its total end of fluid pipeline 122 is connected with the sedimeter 124 inside low pressure vessel 6, Corresponding one end is connected with medium pressure vessel in branch.
Hydraulic system 2 in this specific embodiment mainly by the second engine 1172, the second volume adjustable hydraulic pump 1233 and Fluid pipelines 122 etc. form, wherein the second engine 1172 is connected by connector 1164 with the second gas-liquid exchanger structure 102 It connects, the second gas-liquid exchanger structure 102 is connected by connector 1165 with the second volume adjustable hydraulic pump 1233, the second volume adjustable hydraulic pump 1233 are installed in fluid pipeline 122, its total end of fluid pipeline 122 is filtered with its total end with the liquid inside low pressure vessel 6 Device 124 is connected, corresponding one end is connected with high-pressure bottle 7 in branch.
Tank level control system in this specific embodiment is mainly by controller 112, the first liquid level measurer 1131, the second liquid Position measuring appliance 1132, the first linker 1141, the second linker 1142, the first engine 1171, the first volume adjustable hydraulic pump 1232, The compositions such as the second engine 1172, the second volume adjustable hydraulic pump 1233, wherein controller 112 by electric wire 115 respectively with the first liquid Position measuring appliance 1131, the second liquid level measurer 1132, the first engine 1171, the first volume adjustable hydraulic pump 1232, the second engine 1172, the electrical connections such as second volume adjustable hydraulic pump 1233, the first liquid level measurer 1131 are used to measure the liquid of the first linker 1141 Position, and by data transfer to controller 112;Second liquid level measurer 1232 is used to measure the liquid of the second linker 1142 Position, and by data transfer to controller 112, controller 112 is according to the first linker 1141 and the second linker 1142 Liquid level control the first engine 1171, the first volume adjustable hydraulic pump 1232, the second engine 1172, the second volume adjustable hydraulic pump 1233 Deng operation, and then control and stable high voltage container 7 and medium pressure vessel inside liquid level.
In actual production and application, in order to increase the effect of compressed gas, in the gas-liquid switch type gas compressor It can also be just like down conversion scheme:
Gas-liquid switch type gas compressor in this specific embodiment has added gas-liquid separator 135, the gas-liquid separator 135 are set in high-pressure air pipe 134, in order to the gas-liquid separation inside high-pressure bottle 7.
Gas-liquid switch type gas compressor in this specific embodiment has added barostat 136, the barostat 136 are set in high-pressure air pipe 134, and are electrically connected with controller 112 by electric wire 115, in order to adjust the pressure of output gas Power.
Gas-liquid switch type gas compressor in this specific embodiment has added power lug 139, which sets In high pressure vessel 71, so that electric wire 115 can be through between inside and outside gas-liquid switch type gas compressor simultaneously It is interconnected.
Gas-liquid switch type gas compressor in this specific embodiment has added the first linker 1141 and the second linker 1142, wherein the first linker 1141 be set to high pressure vessel 71 one side and be connected inside high-pressure bottle 7;Second Linker 1142 be set to medium pressure vessel shell 142 one side and be connected inside medium pressure vessel.
Gas-liquid switch type gas compressor in this specific embodiment has added change-over switch 141 and conversion gas circuit 145, In, change-over switch 141 is installed in conversion gas circuit 145, and conversion 145 one end of gas circuit is connected with high pressure gas chamber 73, Its other end is connected with medium pressure gas chamber 143.When change-over switch 141 is closed and the second engine 1172 is run, the gas Liquid switch type gas compressor is convertible into compound compressor;When change-over switch 141 is opened and the closing of the second engine 1172 When, which is convertible into single-stage compressor.
Gas-liquid switch type gas compressor in this specific embodiment has added mechanical seal 131, and mechanical seal 131 is distinguished Between high pressure vessel 71 exchanges part 1 with the gas-liquid in the second gas-liquid exchanger structure 102;And medium pressure vessel shell with Between gas-liquid in first gas-liquid exchanger structure 101 exchanges part 1, in order to by the first engine 1171, hydraulic pump 1231, first Volume adjustable hydraulic pump 1232, second engine 1172 etc. are installed on the outside of gas-liquid switch type gas compressor.
Gas-liquid switch type gas compressor in this specific embodiment has added cooling system, which is set by cooling It is formed for 132 and heat exchanger 133, wherein cooling equipment 132 is respectively arranged on the outside of gas-liquid switch type gas compressor;Heat is handed over Parallel operation 133 extends through inside and outside high-pressure bottle 7, medium pressure vessel and low pressure vessel 6, and cools down equipment with corresponding respectively 132 are connected, in order to the body of preferably cooling gas-liquid switch type gas compressor.
Gas-liquid switch type gas compressor in this specific embodiment has added gas-liquid cushion pad 138, gas-liquid cushion pad 138 It is respectively arranged on the inside of high-pressure bottle 7, medium pressure vessel and low pressure vessel 6, gas-liquid is handed in order to reduce noise, reduce liquid Change the impact of formula gas compressor body.
Gas-liquid switch type gas compressor in this specific embodiment has added liquid non-return valve 120, liquid non-return valve 120 It is respectively arranged in fluid pipeline 122, holds to prevent the liquid in high-pressure bottle 7 from flowing back to low pressure by fluid pipeline 122 Inside device 6, also prevent the liquid in medium pressure vessel from being flowed back to inside low pressure vessel 6 by fluid pipeline 122.
Gas-liquid switch type gas compressor in this specific embodiment has added sedimeter 124, liquid filtering One end of device 124 is connected with low pressure liquid, and the other end is connected with fluid pipeline 122, to improve the cleannes of liquid.
Gas-liquid switch type gas compressor in this specific embodiment has added a word nozzle 140, a word nozzle 140 difference Be connected with fluid pipeline 122, the direction of 140 spout of a word nozzle be respectively directed to each gas-liquid exchange groove high-pressure bottle 7 with And the track moved in medium pressure vessel, to improve the speed of gas-liquid exchange.
The foregoing is merely presently preferred embodiments of the present invention, is not intended to limit the invention, it is all the present invention spirit and Within principle, any modification, equivalent replacement, improvement and so on should all be included in the protection scope of the present invention.

Claims (10)

1. a kind of gas-liquid exchanger structure, it is characterised in that:Including gas-liquid exchange part (1), supporting arrangement (5), seal boss (4), Side seal assembly (2) and end seals assembly (3), the gas-liquid exchange part (1) and are supported on institute by the supporting arrangement (5) It states in seal boss (4), the both ends that the gas-liquid exchanges part (1) are connected by end seals assembly (3) with seal boss (4) It connects, the gas-liquid exchanges part (1) and is connected on seal boss (4) by being set in the side seal assembly (2) of its both sides.
2. gas-liquid exchanger structure according to claim 1, which is characterized in that the seal boss (4) includes seal boss Bottom plate (41) and hollow boss ontology (42) on seal boss bottom plate (41) is set, on the seal boss bottom plate (41) Multiple seal boss interconnecting pieces (43) are provided with, the top of the boss ontology (42) is provided with seal boss opening (44), institute It states the both ends of seal boss opening (44) and both sides and all has smooth outer surface, the gas-liquid exchange part (1) is socketed in close It seals in boss openings (44).
3. gas-liquid exchanger structure according to claim 2, which is characterized in that the gas-liquid exchanges part and includes:
Gas-liquid exchanges part ontology (11), and the gas-liquid exchanges the cylinder that part ontology (11) is cylindrical and is socketed in seal boss and opens In mouth (44);
Gas-liquid exchanges groove (12), and the gas-liquid exchanges groove (12) and is distributed in the gas-liquid exchange part ontology to be at least one (11) the groove on lateral surface;
Gas-liquid exchanges part support interconnecting piece (14), and the gas-liquid exchanges part support interconnecting piece (14) and exchanges part ontology with the gas-liquid (11) it is linked together, the gas-liquid exchanges part support interconnecting piece (14) and is connected with supporting arrangement (5);
Be located by connecting hole (13), and the hole that is located by connecting (13) setting exchanges the both ends of part ontology (11) in the gas-liquid, described Gas-liquid exchanges part ontology (11) and is connected with end seals assembly (3) by the hole that is located by connecting (13).
4. gas-liquid exchanger structure according to claim 3, which is characterized in that the end seals assembly includes:
End seals part (31), the end seals part (31) include have smooth outer surface cylindric inner cylinder (311) and Veneer (312) is sealed, the inner cylinder (311) is socketed in the gas-liquid and exchanges on part ontology (11) and seal against each other, the sealing Veneer (312) is smooth plane with the axis perpendicular of the inner cylinder (311), the sealing veneer (312) with it is described interior Cylinder (311) mutually joins;
End seals assembly preload piece (32), the end seals assembly preload piece (32) are connected with the end seals part (31) Connect, and act on the end seals part (31) so that the end seals part (31) under the action of pretightning force always with The seal boss (4) and the side seal assembly (2) fit closely;
End seals part locating piece (33), the end seals part locating piece (33) include for exchanging part ontology with the gas-liquid (11) end being fixedly connected is fixedly connected with portion (331) and the end for being flexibly connected with the end seals part (31) and lives Rotation connection (332), the end seals part locating piece are fixedly connected with portion (331) by end and are fixedly installed in the gas-liquid friendship It changes the both ends of part ontology and is flexibly connected with the end seals part (31) by end active connection part (332).
5. gas-liquid exchanger structure according to claim 4, which is characterized in that the side seal assembly includes:
Side seal (21) is provided with smooth sealing cambered surface (211), the sealing cambered surface in the side seal (21) (211) radian that radian exchanges part ontology 11 with the gas-liquid matches, and side seal (21) are provided at both ends with Side end sealing surface with smooth outer surface, side end sealing surface mutually join with the sealing cambered surface (211), The sealing bottom surface with smooth outer surface, the sealing bottom surface and the side end are provided in the side seal (21) Sealing surface mutually joins, and the be open smooth outer surface of (44) both sides of sealing bottom surface and the seal boss fits closely, It is additionally provided with active connection part (212) on the side seal (21);
Side seal assembly preload piece (22), the side seal preload piece (22) are connected with the side seal (21) And act on the side seal (21) so that the side seal (21) under the action of pretightning force always with it is described Gas-liquid exchanges part ontology 11 and fits closely;
Side locating piece (23), the side locating piece (23) are fixedly installed in by connector on the seal boss (4), institute State the side active connection part (232) being provided in the locating piece of side for being flexibly connected with the side seal (21), institute It states side active connection part (232) and is flexibly connected with the active connection part (212) being arranged in the side seal (21).
6. gas-liquid exchanger structure according to claim 5, which is characterized in that the length of the sealing cambered surface (211) is more than Each gas-liquid exchanges the length of part groove (12), and the radian of the sealing cambered surface (211) is more than each gas-liquid and exchanges groove (12) Radian so that the sealing cambered surface (211), which can cover each gas-liquid, exchanges groove (12), the side seal assembly is pre- Tight part (22) is spring or magnet, and the end seals assembly preload piece (32) is spring or magnet, the side seal (21) length is consistent with the seal boss opening length of (44) being arranged on the boss ontology (42).
7. a kind of gas-liquid switch type gas compressor, including low pressure vessel, high-pressure bottle, as described in claim 1-6 is any Gas-liquid exchanger structure, hydraulic system, tank level control system, it is characterised in that:The high-pressure bottle (7) is installed on the low pressure and holds The top of device (6);Composition portion of the gas-liquid exchanger structure respectively as the high-pressure bottle (7) and the low pressure vessel (6) Divide and is installed between the high-pressure bottle (7) and the low pressure vessel (6);Hydraulic pump is housed in the hydraulic system, it is described Hydraulic pump is pressed into the high-pressure bottle (7) after being pressurized by the low pressure vessel (6) internal suction low pressure liquid and by low pressure liquid It is internal;The tank level control system is used to control the liquid level of the high-pressure bottle (7) internal liquid.
8. gas-liquid switch type gas compressor according to claim 7, it is characterised in that:The low pressure vessel (6) includes Low pressure vessel shell (61), the low pressure vessel shell (61) are the hollow housing of upper end opening, the low pressure vessel shell (61) open end is fixedly connected by connector with the seal boss bottom plate (41) of seal boss;It is inside the low pressure vessel Hollow chamber, the lower part of chamber are the low pressure liquid chamber (62) for loading liquid, and top is for loading the low of gas Fluid chamber of calming the anger (63);The shell of the low-pressure gas chamber (63) is equipped with low-pressure gas entrance (64).
9. gas-liquid switch type gas compressor according to claim 8, which is characterized in that the high-pressure bottle includes high pressure Container casing (71), the high pressure vessel (71) are the hollow housing of lower ending opening, the high pressure vessel (71) Open end is fixedly connected by connector with the seal boss bottom plate (41) of the seal boss;In being inside the high-pressure bottle Empty chamber, the lower part of chamber are the highly pressurised liquid chamber (72) for loading liquid, and top is the high pressure for loading gas Gas chamber (73);The shell of the high pressure gas chamber is equipped with high pressure gas and exports (74).
10. gas-liquid switch type gas compressor according to claim 8 or claim 9, which is characterized in that the gas-liquid exchanger structure Junction between high pressure vessel is equipped with the sealing element for sealing, the gas-liquid exchanger structure and high pressure vessel Pass through sealing element airtight connection;Junction between the gas-liquid exchanger structure and low pressure vessel shell is equipped with for the close of sealing Sealing, the gas-liquid exchanger structure pass through sealing element airtight connection with low pressure vessel shell.
CN201610781582.0A 2016-08-31 2016-08-31 A kind of gas-liquid exchanger structure and the gas-liquid switch type gas compressor with the mechanism Expired - Fee Related CN106194658B (en)

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US4269570A (en) * 1979-04-23 1981-05-26 Ford Motor Company Elastomeric mounting for wave compressor supercharger
CN102996404A (en) * 2012-12-28 2013-03-27 深圳市力科气动科技有限公司 Gas compressor
CN206017098U (en) * 2016-08-31 2017-03-15 吴礼智 A kind of gas-liquid exchanger structure and the gas-liquid switch type gas compressor with the mechanism

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GB0523265D0 (en) * 2005-11-15 2005-12-21 Andrews William T Pressure exchanger
US20160146229A1 (en) * 2014-11-26 2016-05-26 Energy Recovery, Inc. System and method for rotors

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Publication number Priority date Publication date Assignee Title
US4269570A (en) * 1979-04-23 1981-05-26 Ford Motor Company Elastomeric mounting for wave compressor supercharger
CN102996404A (en) * 2012-12-28 2013-03-27 深圳市力科气动科技有限公司 Gas compressor
CN206017098U (en) * 2016-08-31 2017-03-15 吴礼智 A kind of gas-liquid exchanger structure and the gas-liquid switch type gas compressor with the mechanism

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