CN103615442A - Liquid transferring method through vortex valves - Google Patents
Liquid transferring method through vortex valves Download PDFInfo
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- CN103615442A CN103615442A CN201310634561.2A CN201310634561A CN103615442A CN 103615442 A CN103615442 A CN 103615442A CN 201310634561 A CN201310634561 A CN 201310634561A CN 103615442 A CN103615442 A CN 103615442A
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Abstract
A liquid transferring method through vortex valves comprises the following steps that the vortex valves are assembled to form chrysanthemum-type vortex valves, particularly, axial pipes of the vortex valves are communicated with the outer lateral surface of an axial pipe bundle, tangential pipes are communicated with the outer lateral surface of a tangential pipe bundle, and then one chrysanthemum-type vortex valve is obtained; a waste liquid pool is connected with the axial pipe bundle of one chrysanthemum-type vortex valve, and the tangential pipe bundle of the chrysanthemum-type vortex valve is connected with a three-way joint; a target pool is connected with the tangential pipe bundle of the other chrysanthemum-type vortex valve, and the axial pipe bundle of the chrysanthemum-type vortex valve is connected with the three-way joint; the three-way joint is connected with a cavity under a piston of an air-liquid transduction tank; high-pressure fluid is used for driving the piston to move back and forth and then waste liquid is transferred to the target pool. The liquid transferring method through the vortex valves can achieve the liquid transferring process driven through high-pressure air and liquid, the process does not need a rotary device, operation for a long time is achieved, maintenance is not needed, long-distance conveying of liquid can be carried out, conveying fluid amount within the unit time is stable, and radioactive industrial waste water or industrial waste water harmful to the human body can be conveyed. Non-Newtonian fluid with solid particles such as mud and coal slurry can be conveyed.
Description
Technical field
The present invention relates to a kind of method that liquid shifts, be specifically related to a kind of method of utilizing swirl valve to carry out liquid transfer, belong to high pressure-temperature fluid energy recovery and utilization technology field.
Background technique
In large-scale industrial activity in production; conventionally the situation that existence need to be discharged high temperature high pressure liquid or gas; and these high-temperature, high pressure fluids contain huge energy; if directly discharge; so not only can produce waste gas, waste liquid and befouling environment; also can cause the wasting of resources, not meet the trend of requirement and the energy-saving and emission-reduction of low-carbon environment-friendly.
Tradition drives turbo machine rotation to do manual work by high pressure exhaust gas, the overbottom pressure of tail gas can be converted to the mechanical energy of rotation, this gas overbottom pressure energy recovery technology is due to energy multiple conversions, its energy recovery efficiency lower (a kind of turbine booster group CN 102373305 A that reclaim for energy of blast furnace tail gas).
Liquid excess pressure energy recover utilizes drive motor rotor driven to realize the exchange of high low pressure fluid energy, its energy recovery efficiency is higher, but this reclaiming system often needs motor to drive, and whole system is controlled comparatively complicated, core apparatus in callback course is higher to seal request, in reality is used, once design of Sealing Structure is unreasonable or using process was lost efficacy, will directly cause reuse efficiency significantly to reduce (a kind of liquid excess pressure energy recovery device CN 101865191 A).
In a word, traditional overbottom pressure only often can reclaim for Single Medium fluid, as the overbottom pressure that is only applicable to gas or liquid can reclaim, and system exists rotary component, and rate of fault is higher, and the while, reuse efficiency was lower because energy passes through secondary conversion.Therefore need to design a kind of efficient method of can high pressure-temperature fluid carrying out liquid transfer.
Summary of the invention
The object of this invention is to provide a kind of method of utilizing swirl valve to carry out liquid transfer, to overcome the deficiencies in the prior art.
A method of utilizing swirl valve to carry out liquid transfer, is characterized in that comprising the following steps:
(1) utilize swirl valve assembling chrysanthemum formula swirl valve:
Described swirl valve comprises the disc structure body of a hollow, and the excircle of this disc structure body is provided with a tangential pipe communicating with its inner chamber, is provided with an axial pipe communicating with its inner chamber on the axis of disc structure body one side; Described chrysanthemum formula swirl valve also comprises the tangential tube bank of one end sealing, and the axial tube bank of one end sealing, described tangential tube bank and axially tube bank arranged in co-axial alignment, and closed end arranges in opposite directions; The axial pipe of above-mentioned three or three above swirl valves is all communicated with to the outer side surface of restraining axially, and the opening direction of tangential pipe is consistent with the opening direction of tangential tube bank; The tangential pipe of described swirl valve is all communicated with the outer side surface in tangential tube bank; Thereby obtain a chrysanthemum formula swirl valve monomer;
(2) waste liquid pool is connected to the axial tube bank of a chrysanthemum formula swirl valve, the tangential tube bank of this chrysanthemum formula swirl valve is connected with a mouth of pipe of threeway;
Object pool is connected to the tangential tube bank of another chrysanthemum formula swirl valve, the axial tube bank of this chrysanthemum formula swirl valve is connected with another mouth of pipe of threeway;
(3) the 3rd mouth of pipe of above-mentioned threeway is connected in to the chamber of the piston below of gas-liquid transducing tank;
(4) then utilize high-pressure liquid to drive the piston in above-mentioned gas-liquid transducing tank to move back and forth, thereby the liquid rotating in waste liquid pool is moved on in target pond.
Above-mentioned steps 4), in, the concrete grammar that utilizes high-pressure liquid to drive the piston in above-mentioned gas-liquid transducing tank to move back and forth is as follows:
4.1) a driving transducing tank that includes driven plunger is set above above-mentioned gas-liquid transducing tank, and driven plunger is connected with the piston in gas-liquid transducing tank via connecting rod;
4.2) utilize high-pressure liquid energy storage canister stores high pressure fluid, by bilateral switching valve, control high-pressure liquid and alternately enter in the upper chamber and lower chambers that drives transducing tank;
When carrying out imbibition process, bilateral switching valve turns to the lower floor's chamber that drives transducing tank, high-pressure liquid enters, the exhaust-valve of upper chamber is opened simultaneously, driven plunger is under lower floor's high-pressure liquid drives, and drivening rod moves upward, and in gas-liquid transducing tank, gas-liquid piston moves upward simultaneously, gas-liquid transducing tank lower floor forms vacuum, and liquid is inhaled in gas-liquid transducing tank;
When pressing while breaking through journey, bilateral switching valve turns to the upper strata chamber that drives transducing tank, and high-pressure liquid enters, and the exhaust-valve of lower chambers is opened simultaneously, and driven plunger is ordered about gas-liquid piston in gas-liquid transducing tank and moved downward under the drive of connecting rod; Liquid in gas-liquid transducing tank is imported in object pool.
Above-mentioned steps 4.2) in, also comprise a control cabinet, and drive high level meter and low level meter in transducing tank;
Described control cabinet is controlled described bilateral switching valve, exhaust-valve, exhaust-valve and level meter;
When the liquid in gas-liquid transducing tank reaches the height of high level meter setting, control cabinet is controlled bilateral switching valve and is turned to the upper strata chamber that drives transducing tank, and opens exhaust-valve;
During height that the liquid in gas-liquid transducing tank is set lower than low level meter, control cabinet is controlled bilateral switching valve and is turned to the lower floor's chamber that drives transducing tank, and opens exhaust-valve.
The axial pipe of above-mentioned swirl valve comprises canalis spinalis section, and the stub end of this canalis spinalis section is connected in disc structure body, microcephaly holds and connects a gradient tube, and the other end of this gradient tube connects straight length, and the diameter of the (i) little head end of canalis spinalis section is less than the diameter of straight length.
The disc structure body of above-mentioned swirl valve by ante-chamber plate, back cavity plate and connect front/back cavity plate ring-type circular arc plate, form, and the curvature of ring-type circular arc plate is identical with the curvature of tangential pipe.
The inner side surface of the front/back cavity plate of above-mentioned swirl valve is also provided with the distributing fin of circular arc.
Above-mentioned distributing fin comprises short distributing fin and long distributing fin, and short distributing fin is arranged alternately the inner side surface at front/back cavity plate with long distributing fin centered by the axis of disc structure body.
The curvature of above-mentioned short distributing fin is greater than the curvature of long distributing fin, and the length of long distributing fin is not less than the twice of short-range missile stream finned length.
Above-mentionedly for connecting the axial tube bank of the chrysanthemum formula swirl valve of waste liquid pool, be greater than it and tangentially restrain; The axial tube bank that is used for the chrysanthemum formula swirl valve in linking objective pond is less than it and tangentially restrains.
The concrete structure that above-mentioned tangential pipe is connected to tangential tube bank is as follows: first tangential pipe connects one 90 degree elbows, and the axial direction of another port and the parallel to an axis of disc structure body of this 90 degree elbow; The another port of this 90 degree elbow connects second 90 degree elbow by a rectilinear tubes; And the axial direction of the another port of second 90 degree elbow is axial vertical with tangential tube bank, and this another port is connected to the side of tangential tube bank.
In said method, a plurality of chrysanthemum formula swirl valves are connected in parallel and form swirl valve group, then described waste liquid pool is connected to the axial tube bank of each chrysanthemum formula swirl valve of one of them swirl valve group, described object pool is connected to the tangential tube bank of each chrysanthemum formula swirl valve of another swirl valve group, can significantly improve working efficiency.
Utilize method of the present invention, can realize the liquid transfer process by pressurized gas, liquid driven, this process is without slewing gear, can long-play, and without keeping in repair.The present invention utilizes high-pressure liquid energy drives piston, can carry out the remote conveying of liquid, and in the unit time, feed flow is stable.Because conveying liquid body in whole system divides device without spin, adopt all-welded structure, therefore can carry with emissivity or harmful industrial wastewater; Except can be used for carrying, have toxicity, emanative Newtonian fluid, also can slurry conveyed, coal slurry etc. is with the non-Newtonian fluid of solid particle.Through overtesting, confirm, after gas-liquid piston moves upward and then moves downward, enter the liquid of gas-liquid transducing tank lower chambers, the volume that is input to object pool is 49:1 with the ratio of recharging waste liquid pool, and visible native system has extremely significant effect.
Accompanying drawing explanation
Fig. 1 is the structural representation of swirl valve of the present invention.
Fig. 2 is the front view of swirl valve of the present invention.
Fig. 3 is the AA sectional view of Fig. 5.
Fig. 4 is the BB sectional view of Fig. 5.
Fig. 5 is the structural representation of chrysanthemum formula swirl valve of the present invention.
Fig. 5 A is that liquid is restrained to the mobile schematic diagram of tangential tube bank from axial, and Fig. 5 B is that liquid is tangentially restrained to the moving schematic diagram of axial pipe line certainly.
Fig. 6 is general structure block diagram of the present invention.
Fig. 7 is bilateral switching valve arrangement schematic diagram of the present invention.
Wherein, 1, energy storage canister, 2, bilateral switching valve, 3, driven plunger, 4, drive transducing tank, 5, connecting rod, 6, gas-liquid piston, 7, gas-liquid transducing tank, 8, object pool, 9, front chrysanthemum formula eddy current group, 10, rear chrysanthemum formula eddy current group, 11, waste liquid pool, 12, control cabinet, 13, exhaust-valve, 14, exhaust-valve, 15, threeway, 16, exhaust-valve, 17, high level meter, 18, low level meter;
J, chrysanthemum formula swirl valve, W, swirl valve, X, disc structure body, Y, tangentially pipe, Z, axial pipe, P, tangentially tube bank, Q, axially tube bank;
13-a, supervisor, 13-b, spool, 13-c, side branch, 13-d, primary branch;
A, straight length, b, gradient tube, c, short distributing fin, d, long distributing fin, e, ante-chamber plate, f, the tangential mouth of pipe, g, circular arc plate, h, back cavity plate, i, canalis spinalis section.
Embodiment
As shown in Fig. 1,5,6, a kind of method of utilizing swirl valve to carry out liquid transfer, is characterized in that comprising the following steps:
(1) utilize swirl valve W assembling chrysanthemum formula swirl valve:
Described swirl valve W comprises the disc structure body X of a hollow, and the excircle of this disc structure body X is provided with a tangential pipe Y who communicates with its inner chamber, is provided with an axial pipe Z who communicates with its inner chamber on the axis of disc structure body Y mono-side; Described chrysanthemum formula swirl valve J also comprises the tangential tube bank P of one end sealing, and the axial tube bank Q of one end sealing, described tangential tube bank P and axially tube bank Q arranged in co-axial alignment, and closed end arranges in opposite directions; The axial pipe Z of the above swirl valve W of above-mentioned three or three is all communicated with at the axial outer side surface of tube bank Q, and it is consistent with the opening direction of tangentially restraining P tangentially to manage the opening direction of Y; The tangential pipe X of described swirl valve W is all communicated with the outer side surface at tangential tube bank P; Thereby obtain a chrysanthemum formula swirl valve monomer;
(2) waste liquid pool 11 is connected to the axial tube bank Q of a chrysanthemum formula swirl valve J, the tangential tube bank P of this chrysanthemum formula swirl valve J is connected with a mouth of pipe of threeway 15;
The tangential tube bank P that object pool 8 is connected to another chrysanthemum formula swirl valve J, the axial tube bank Q of this chrysanthemum formula swirl valve J is connected with another mouth of pipe of threeway 15;
(3) the 3rd mouth of pipe of above-mentioned threeway 15 is connected in to the chamber of the piston below of gas-liquid transducing tank 7;
(4) then utilize high-pressure liquid to drive the piston in above-mentioned gas-liquid transducing tank 7 to move back and forth, thereby the liquid rotating in waste liquid pool 11 is moved on in target pond 8.
Above-mentioned steps 4), in, the concrete grammar that utilizes high-pressure liquid to drive the piston in above-mentioned gas-liquid transducing tank 7 to move back and forth is as follows:
4.1) a driving transducing tank 4 that includes driven plunger 3 is set above above-mentioned gas-liquid transducing tank 7, and driven plunger 3 is connected with the piston in gas-liquid transducing tank 7 via connecting rod 5;
4.2) utilize high-pressure liquid energy storage canister 1 stores high pressure fluid, by bilateral switching valve 2, control high-pressure liquid and alternately enter in the upper chamber and lower chambers that drives transducing tank 4;
When carrying out imbibition process, bilateral switching valve 2 turns to the lower floor's chamber that drives transducing tank 4, high-pressure liquid enters, the exhaust-valve 13 of upper chamber is opened simultaneously, driven plunger 3 is under lower floor's high-pressure liquid drives, and drivening rod 5 moves upward, and in gas-liquid transducing tank 7, gas-liquid piston 6 moves upward simultaneously, gas-liquid transducing tank (7) lower floor forms vacuum, and liquid is inhaled in gas-liquid transducing tank (7);
When pressing while breaking through journey, bilateral switching valve 2 turns to the upper strata chamber that drives transducing tank 4, and high-pressure liquid enters, and the exhaust-valve 14 of lower chambers is opened simultaneously, and driven plunger 3 is ordered about gas-liquid piston 6 in gas-liquid transducing tank 7 and moved downward under the drive of connecting rod 5; Liquid in gas-liquid transducing tank 7 is imported in object pool 8.
Above-mentioned steps 4.2) in, also comprise a control cabinet 12, and drive high level meter and low level meter in transducing tank 4;
Described control cabinet 12 pairs of described bilateral switching valves 2, exhaust-valve 13, exhaust-valve 14 and level meters are controlled;
When the liquid in gas-liquid transducing tank 7 reaches the height of high level meter setting, control cabinet 12 is controlled bilateral switching valves 2 and is turned to the upper strata chamber that drives transducing tank 4, and opens exhaust-valve 14;
During height that the liquid in gas-liquid transducing tank 7 is set lower than low level meter, control cabinet 12 is controlled bilateral switching valves 2 and is turned to the lower floor's chamber that drives transducing tank 4, and opens exhaust-valve 13.
As Figure 1-5, the axial pipe Z of above-mentioned swirl valve W comprises canalis spinalis section i, the stub end of this canalis spinalis section i is connected in disc structure body X, microcephaly holds and connects a gradient tube b, and the other end of this gradient tube b connects straight length a, and the diameter of the little head end of canalis spinalis section i is less than the diameter of straight length a.
The disc structure body X of above-mentioned swirl valve W by ante-chamber plate e, back cavity plate h and connect front/back cavity plate ring-type circular arc plate g, form, and the curvature of ring-type circular arc plate g is identical with the curvature of tangentially managing Y.
The inner side surface of front/back cavity plate e, the h of above-mentioned swirl valve W is also provided with the distributing fin of circular arc.
Above-mentioned distributing fin comprises short distributing fin c and long distributing fin d, and short distributing fin c is arranged alternately the inner side surface at front/back cavity plate e, h with long distributing fin d centered by the axis of disc structure body X.
The curvature of above-mentioned short distributing fin c is greater than the curvature of long distributing fin d, and the length of long distributing fin d is not less than the twice of short distributing fin c length.
Above-mentionedly for connecting the axial tube bank Q of the chrysanthemum formula swirl valve J of waste liquid pool 11, be greater than its tangential tube bank (P); The axial tube bank Q that is used for the chrysanthemum formula swirl valve J in linking objective pond 8 is less than its tangential tube bank P.
It is as follows that above-mentioned tangential pipe Y is connected to the concrete structure of tangential tube bank P: tangentially manage Y and first connect one 90 degree elbows, and the axial direction of another port and the parallel to an axis of disc structure body of this 90 degree elbow; The another port of this 90 degree elbow connects second 90 degree elbow by a rectilinear tubes; And the axial direction of the another port of second 90 degree elbow is axial vertical with tangential tube bank P's, and this another port is connected to the side of tangential tube bank P.
Swirl valve W of the present invention as Figure 1-5,
Straight length a is connected by gradient tube b with canalis spinalis section i, 4 short distributing fin c and 4 length of a film distributing fin d are all installed on ante-chamber plate e and back cavity plate h, short distributing fin c and long distributing fin d axially lay every 45 ° of intervals around center tube, between long distributing fin d on the plate of chamber, front and back, have space, interval, this gap lengths is not less than 50% chamber, front and back distance between plates; Tangential pipe Y end is tangential pipe mouth of pipe f.
When fluid is by tangentially managing after Y inflow, in vortex cavity, form eddy flow, by center, radially with this, form forced vortex and free vortex, its reverse resistance is mainly determined by the intensity of forced vortex, general forced vortex radius is not more than 30% of vortex cavity radius, in order to strengthen intensity and the scope of forced vortex in vortex cavity, increase the short distributing fin c of structure and long distributing fin d, after tangential influent stream, at the circular arc plate g place near vortex cavity, form eddy flow, when eddy flow is after short distributing fin c and long distributing fin d, form segmentation eddy flow, cause being subject in fluid rotary process the driving from fluid between short distributing fin c and long distributing fin d septal pathways, swirl strength constantly strengthens, increase the group six of reverse flow,
When the fluid center tube of flowing through enters after vortex cavity, fluid is divided into stereotyped writing tributary and radially flow to after annular circular arc plate g under the shunting action of short distributing fin c and long distributing fin d, and through tangential pipe outflow, fluid resistance is less.
As shown in Figure 7, bilateral switching valve 2 of the present invention comprises that supervisor 13-a, supervisor 13-a connect respectively side branch 13-c and primary branch 13-d by spool 13-b; By rotational valve core, 13-b commutates.
Working principle of the present invention is as follows:
In order to make full use of the overbottom pressure energy of high pressure gas waste gas, utilize pressurized gas energy storage tank 1 to store pressurized gas, by bilateral switching valve 2, control pressurized gas and enter in driving transducing tank 4;
When pressing while breaking through journey, bilateral switching valve 2 turns to the upper strata chamber that drives transducing tank 4, and pressurized gas enter, and exhaust-valve 14 is opened simultaneously, and driven plunger 3 is ordered about gas-liquid piston 6 in gas-liquid transducing tank 7 and moved downward under the drive of connecting rod 5;
Front chrysanthemum formula eddy current group 9, rear chrysanthemum formula eddy current group 10 at least comprises a chrysanthemum formula swirl valve, described chrysanthemum formula swirl valve has two import and export, is respectively tangentially to restrain P, axially restrain Q, as shown in Figure 3.In Fig. 3 a, when liquid flows to B by A, liquid is divided into six strands at each swirl valve tangential entry, enters in vortex cavity and flows out through center tube, converges to outlet line.Due to after fluid tangentially enters, in chamber, form strong rotational flow, fluid resistance is larger; In Fig. 3 b, when liquid flows to B by A, liquid is divided into six strands in each swirl valve center tube import, enters in vortex cavity and flows out through tangential pipe, converges to outlet line.Due to after fluid center tube enters, in chamber, forming distributes flows, and fluid is less.It is larger that fluid imports and exports through two of (9) (10) chrysanthemum formula swirl valves the flow resistance difference forming;
The axial tube bank Q of chrysanthemum formula swirl valve W in front chrysanthemum formula eddy current group 9 connects waste liquid pool 11, tangentially restrains P connecting tee 15;
The axle of chrysanthemum formula swirl valve W in rear chrysanthemum formula eddy current group 10 is tangentially restrained Q connecting tee 15, tangentially restrains P linking objective pond 8.
When liquid by gas-liquid transducing tank 7 in gas-liquid piston 6 to pressing down while rushing, liquid goes out to form shunting in threeway 15, because front chrysanthemum formula swirl valve group 9 now flows to as tangentially to center, so present high-drag characteristic; Then chrysanthemum formula swirl valve group 10 is extremely tangential centered by now flowing to, so present lower resistance characteristic; The trend lower resistance that flows fluid flows, and therefore, when gas-liquid piston 6 is to pressing down while rushing, the waste liquid in gas-liquid transducing tank 7 flows to object pool 8 via rear chrysanthemum formula swirl valve group;
When carrying out imbibition process, bilateral switching valve 2 turns to the lower floor's chamber that drives transducing tank 4, pressurized gas enter, exhaust-valve 13 is opened simultaneously, driven plunger 3 is under lower floor's drive of high-pressure gas, drivening rod 5 moves upward, in gas-liquid transducing tank 7, gas-liquid piston 6 moves upward simultaneously, gas-liquid transducing tank 7 lower floors form certain vacuum, liquid is inhaled in gas-liquid transducing tank 7, and in this process, liquid goes out to form shunting in threeway 15, due to front chrysanthemum formula swirl valve group 9 now flow to centered by tangential, so present lower resistance characteristic; Then chrysanthemum formula swirl valve group 10 now flows to as tangentially to center, so present high-drag characteristic; The mobile trend of fluid lower resistance flows, and therefore, when gas-liquid piston 6 makes progress imbibition, the waste liquid of waste liquid pool 11 flows as in gas-liquid transducing tank 7 via front chrysanthemum formula swirl valve group 9; Whole process can accurately be controlled each valve according to the signal of two level meters by control cabinet 12.
Above process moves in circles, and realizes the conveying of liquid, carry movement-less part in core apparatus, and transfer efficiency efficiency is high, and good stability can long time continuous working, without safeguarding, can be used for carrying having danger, radioactive waste liquid.
Claims (10)
1. a method of utilizing swirl valve to carry out liquid transfer, is characterized in that comprising the following steps:
(1) utilize swirl valve (W) assembling chrysanthemum formula swirl valve:
Described swirl valve (W) comprises the disc structure body (X) of a hollow, the excircle of this disc structure body (X) is provided with a tangential pipe (Y) communicating with its inner chamber, is provided with an axial pipe communicating with its inner chamber (Z) on the axis of disc structure body (Y) side; Described chrysanthemum formula swirl valve (J) also comprises the tangential tube bank (P) of one end sealing, and the axial tube bank (Q) of one end sealing, described tangential tube bank (P) and axially tube bank (Q) arranged in co-axial alignment, and closed end arranges in opposite directions; The axial pipe (Z) of above-mentioned three or three above swirl valves (W) is all communicated with and is axially restraining the outer side surface of (Q), and the opening direction of tangential pipe (Y) is consistent with the opening direction of tangential tube bank (P); The tangential pipe (X) of described swirl valve (W) is all communicated with the outer side surface in tangential tube bank (P); Thereby obtain a chrysanthemum formula swirl valve monomer;
(2) waste liquid pool (11) is connected to the axial tube bank (Q) of a chrysanthemum formula swirl valve (J), the tangential tube bank (P) of this chrysanthemum formula swirl valve (J) is connected with a mouth of pipe of threeway (15);
Object pool (8) is connected to the tangential tube bank (P) of another chrysanthemum formula swirl valve (J), the axial tube bank (Q) of this chrysanthemum formula swirl valve (J) is connected with another mouth of pipe of threeway (15);
(3) the 3rd mouth of pipe of above-mentioned threeway (15) is connected in to the chamber of the piston below of gas-liquid transducing tank (7);
(4) then utilize high-pressure liquid to drive the piston in above-mentioned gas-liquid transducing tank (7) to move back and forth, thereby the liquid rotating in waste liquid pool (11) is moved on in target pond (8).
2. the method for claim 1, is characterized in that above-mentioned steps 4) in, the concrete grammar that utilizes high-pressure liquid to drive the piston in above-mentioned gas-liquid transducing tank (7) to move back and forth is as follows:
4.1) in above-mentioned gas-liquid transducing tank (7) top, a driving transducing tank (4) that includes driven plunger (3) is set, and driven plunger (3) is connected with the piston in gas-liquid transducing tank (7) via connecting rod (5);
4.2) utilize high-pressure liquid energy storage canister (1) stores high pressure fluid, by bilateral switching valve (2), control high-pressure liquid and alternately enter in the upper chamber and lower chambers that drives transducing tank (4);
When carrying out imbibition process, bilateral switching valve (2) turns to the lower floor's chamber that drives transducing tank (4), high-pressure liquid enters, the exhaust-valve (13) of upper chamber is opened simultaneously, driven plunger (3) is under lower floor's high-pressure liquid drives, and drivening rod (5) moves upward, and in gas-liquid transducing tank (7), gas-liquid piston (6) moves upward simultaneously, gas-liquid transducing tank (7) lower floor forms vacuum, and liquid is inhaled in gas-liquid transducing tank (7);
When pressing while breaking through journey, bilateral switching valve (2) turns to the upper strata chamber that drives transducing tank (4), high-pressure liquid enters, the exhaust-valve (14) of lower chambers is opened simultaneously, and driven plunger (3) is ordered about gas-liquid piston (6) in gas-liquid transducing tank (7) and moved downward under the drive of connecting rod (5); Liquid in gas-liquid transducing tank (7) is imported in object pool (8).
3. method as claimed in claim 2, is characterized in that above-mentioned steps 4.2) in also comprise a control cabinet (12), and drive high level meter and low level meter in transducing tank (4);
Described control cabinet (12) is controlled described bilateral switching valve (2), exhaust-valve (13), exhaust-valve (14) and level meter;
When the liquid in gas-liquid transducing tank (7) reaches the height of high level meter setting, control cabinet (12) is controlled bilateral switching valve (2) and is turned to the upper strata chamber that drives transducing tank (4), and opens exhaust-valve (14);
During height that the liquid in gas-liquid transducing tank (7) is set lower than low level meter, control cabinet (12) is controlled bilateral switching valve (2) and is turned to the lower floor's chamber that drives transducing tank (4), and opens exhaust-valve (13).
4. the method for claim 1, the axial pipe (Z) that it is characterized in that above-mentioned swirl valve (W) comprises canalis spinalis section (i), this canalis spinalis section stub end is (i) connected in disc structure body (X), microcephaly holds and connects a gradient tube (b), the other end of this gradient tube (b) connects straight length (a), and the diameter of the (i) little head end of canalis spinalis section is less than the diameter of straight length (a).
5. the method for claim 1, the disc structure body (X) that it is characterized in that above-mentioned swirl valve (W) by ante-chamber plate (e), back cavity plate (h) and connect front/back cavity plate ring-type circular arc plate (g), forms, and the curvature of ring-type circular arc plate (g) is identical with the curvature of tangentially managing (Y).
6. method as claimed in claim 5, is characterized in that the inner side surface of the front/back cavity plate (e, h) of above-mentioned swirl valve (W) is also provided with the distributing fin of circular arc.
7. method as claimed in claim 6, it is characterized in that above-mentioned distributing fin comprises short distributing fin (c) and long distributing fin (d), and short distributing fin (c) and long distributing fin (d) are arranged alternately the inner side surface at front/back cavity plate (e, h) centered by the axis of disc structure body (X).
8. method as claimed in claim 7, it is characterized in that the curvature of above-mentioned short distributing fin (c) is greater than the curvature of long distributing fin (d), and the length of long distributing fin (d) is not less than the twice of short distributing fin (c) length.
9. the freedom from repairs transporting system that high-pressure liquid as claimed in claim 1 drives, is characterized in that above-mentionedly for connecting the axial tube bank (Q) of the chrysanthemum formula swirl valve (J) of waste liquid pool (11), being greater than its tangential tube bank (P); The axial tube bank (Q) that is used for the chrysanthemum formula swirl valve (J) in linking objective pond (8) is less than its tangential tube bank (P).
10. the method for claim 1, it is characterized in that above-mentioned tangential pipe (Y) is connected to the concrete structure of tangential tube bank (P) as follows: tangential pipe (Y) first connects one 90 degree elbows, and the axial direction of another port and the parallel to an axis of disc structure body of this 90 degree elbow; The another port of this 90 degree elbow connects second 90 degree elbow by a rectilinear tubes; And the axial direction of the another port of second 90 degree elbow is axial vertical with tangential tube bank (P), and this another port is connected to the side of tangential tube bank (P).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201310634561.2A CN103615442B (en) | 2013-12-01 | 2013-12-01 | A kind of method utilizing swirl valve to carry out liquid transfer |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201310634561.2A CN103615442B (en) | 2013-12-01 | 2013-12-01 | A kind of method utilizing swirl valve to carry out liquid transfer |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN103615442A true CN103615442A (en) | 2014-03-05 |
| CN103615442B CN103615442B (en) | 2016-01-13 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201310634561.2A Expired - Fee Related CN103615442B (en) | 2013-12-01 | 2013-12-01 | A kind of method utilizing swirl valve to carry out liquid transfer |
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| Country | Link |
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| CN (1) | CN103615442B (en) |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5465695A (en) * | 1991-08-30 | 1995-11-14 | Mazda Motor Corporation | Ignition system for internal combustion engine |
| CN1176338A (en) * | 1996-08-12 | 1998-03-18 | 马自达汽车株式会社 | Direct fuel injection engine |
| JP2000087791A (en) * | 1998-09-08 | 2000-03-28 | Toyota Motor Corp | Combustion control device for internal combustion engine |
| CN1257566A (en) * | 1997-05-26 | 2000-06-21 | 日产自动车株式会社 | Linkage device of internal combustion engine |
| GB2409537A (en) * | 2002-02-27 | 2005-06-29 | Hydro Int Plc | Vortex valve with adjustable inlet |
-
2013
- 2013-12-01 CN CN201310634561.2A patent/CN103615442B/en not_active Expired - Fee Related
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5465695A (en) * | 1991-08-30 | 1995-11-14 | Mazda Motor Corporation | Ignition system for internal combustion engine |
| CN1176338A (en) * | 1996-08-12 | 1998-03-18 | 马自达汽车株式会社 | Direct fuel injection engine |
| CN1257566A (en) * | 1997-05-26 | 2000-06-21 | 日产自动车株式会社 | Linkage device of internal combustion engine |
| JP2000087791A (en) * | 1998-09-08 | 2000-03-28 | Toyota Motor Corp | Combustion control device for internal combustion engine |
| GB2409537A (en) * | 2002-02-27 | 2005-06-29 | Hydro Int Plc | Vortex valve with adjustable inlet |
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| Publication number | Publication date |
|---|---|
| CN103615442B (en) | 2016-01-13 |
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