CN104014442A - Rotating-in type dual-inlet medium ejector - Google Patents
Rotating-in type dual-inlet medium ejector Download PDFInfo
- Publication number
- CN104014442A CN104014442A CN201410262492.1A CN201410262492A CN104014442A CN 104014442 A CN104014442 A CN 104014442A CN 201410262492 A CN201410262492 A CN 201410262492A CN 104014442 A CN104014442 A CN 104014442A
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- China
- Prior art keywords
- vacuum chamber
- venturi tube
- nozzle
- screw
- tangential
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Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B05—SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
- B05B—SPRAYING APPARATUS; ATOMISING APPARATUS; NOZZLES
- B05B7/00—Spraying apparatus for discharge of liquids or other fluent materials from two or more sources, e.g. of liquid and air, of powder and gas
- B05B7/02—Spray pistols; Apparatus for discharge
- B05B7/04—Spray pistols; Apparatus for discharge with arrangements for mixing liquids or other fluent materials before discharge
- B05B7/0416—Spray pistols; Apparatus for discharge with arrangements for mixing liquids or other fluent materials before discharge with arrangements for mixing one gas and one liquid
- B05B7/0425—Spray pistols; Apparatus for discharge with arrangements for mixing liquids or other fluent materials before discharge with arrangements for mixing one gas and one liquid without any source of compressed gas, e.g. the air being sucked by the pressurised liquid
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- Jet Pumps And Other Pumps (AREA)
Abstract
The invention relates to a rotating-in type dual-inlet medium ejector which comprises a pipe body and a nozzle connected to the pipe body in a sleeved mode. The pipe body comprises a vacuum chamber, a nozzle hole, a venturi tube and two tangential branch tubes, wherein the nozzle hole, the venturi tube and the two tangential branch tubes are respectively communicated with the vacuum chamber in a sealed mode. The nozzle is connected into the nozzle hole in a sleeved mode. The nozzle and the venturi tube are coaxially located at the two ends of the vacuum chamber. The tangential branch tubes are tangent to the side circumference of the vacuum chamber. The two tangential branch tubes are of a central symmetry structure by using the axis of the venturi tube as the center. According to the rotating-in type dual-inlet medium ejector, the two tangential vacuum tubes tangent to the side circumference of the vacuum chamber are arranged, and the function that steam can be sucked by and enter the vacuum chamber in a rotating mode is achieved due to the structure, so that different kinds of steam enter the vacuum chamber through the different branch tubes and are mixed sufficiently inside the vacuum chamber through rotation, and meanwhile the flow direction of flow media is not affected by the two branch tubes of the central symmetry structure.
Description
Technical field
The present invention relates to a kind of medium injection device, relate in particular to the two entrance medium injection devices of a kind of screw-in.
Background technology
Medium injection device be a kind of have vacuumize, the mechanical device of three kinds of available energies such as condensation, draining.It is the nozzle ejection that utilizes the certain gradient of the fluid media (medium) symmetrical uniform one-tenth of circulation of certain pressure, is aggregated in a focus.Because injection stream body medium Flow Velocity is very high, make the indoor generation vacuum of device so form negative pressure around, in addition because indirect steam directly contacts with injection stream body medium, carry out heat exchange, the steam-condensation Cheng Shui of the overwhelming majority, the steam not being condensed on a small quantity and incoagulable gas, also owing to rubbing mutually with the fluid media (medium) of high velocity jet, mix and extruding, be excluded by diffuser pipe, make the higher vacuum of the indoor formation of device.The application of medium injection device is very extensive, be mainly used in vacuum and vapo(u)rization system, carry out that vacuum is drawn water, the technique such as vacuum evaporation, vacuum filtration, vacuum crystallization, dry, deodorization, be the equipment of sugaring, pharmacy, chemical industry, food, salt manufacturing, monosodium glutamate, milk, fermentation and some light industry, defense sector's widespread demand.But at present production medium injection device arm be all vertically to access vacuum chamber, cannot form steam in vacuum chamber rotational flow with well-mixed function.
Summary of the invention
The present invention has overcome the deficiencies in the prior art, provides a kind of screw-in simple in structure two entrance medium injection devices.
For achieving the above object, the technical solution used in the present invention is: the two entrance medium injection devices of a kind of screw-in, comprise: body and the sheathed upper nozzle that is connected to described body, described body comprises vacuum chamber and seals with described vacuum chamber the nozzle bore being communicated with respectively, Venturi tube and two tangential arms, it is characterized in that, described nozzle is sheathed to be connected in described nozzle bore, what described nozzle and described Venturi tube were coaxial is positioned at described vacuum chamber two ends, the side week of described tangential arm and described vacuum chamber is tangent, two described tangential arms are the centrosymmetric structures centered by described Venturi tube axis.
In a preferred embodiment of the present invention, described nozzle is provided with the flat pipe portion that is positioned at described nozzle bore outside and the tip that is positioned at described vacuum chamber, and described tip end is provided with the spout being communicated with described flat pipe portion inner chamber.
In a preferred embodiment of the present invention, described flat pipe portion outside is with external screw thread, and described nozzle bore inwall is with internal thread, and described internal thread mates with described external thread structure.
In a preferred embodiment of the present invention, described Venturi tube is provided with compression section, larynx section and diffuser successively along its axis, the described compression section described vacuum chamber that is tightly connected.
In a preferred embodiment of the present invention, described compression section and described vacuum chamber junction internal diameter are greater than the junction internal diameter of itself and described larynx section, and described expansion segment free end internal diameter is greater than the junction internal diameter of itself and described larynx section.
In a preferred embodiment of the present invention, described nozzle bore free end, described Venturi tube free end, described tangential arm free end and described flat tube section free end are equipped with the edge that is tightly connected of turning up along its circumferential edge.
In a preferred embodiment of the present invention, described vacuum chamber inwall is globoidal structure.
The invention solves the defect existing in background technology, the present invention be provided with two with tangent tangential vacuum tube of vacuum chamber side week, this kind of structure can produce the function that rotates into vacuum chamber after steam is sucked by vacuum chamber, different like this steam enters from different arms, and fully mix by being rotated in vacuum chamber, two arms of centrosymmetric structure can not affect the flow direction of fluid media (medium) simultaneously.
Brief description of the drawings
Below in conjunction with drawings and Examples, the present invention is further described.
Fig. 1 is the two entrance medium injection device structural representations of the screw-in of the preferred embodiments of the present invention;
Fig. 2 is the two entrance medium injection device cross-sectional view of the screw-in of the preferred embodiments of the present invention;
Fig. 3 be in Fig. 1 A-A to cross-sectional view;
In figure: 1, body, 2, nozzle, 3, vacuum chamber, 4, nozzle bore, 5, Venturi tube, 6, tangential arm, 7, flat pipe portion, 8, tip, 9, spout, 10, compression section, 11, larynx section, 12, diffuser, 13, the edge that is tightly connected, 14, crosspoint.
Detailed description of the invention
The present invention is further detailed explanation in conjunction with the accompanying drawings and embodiments now, and these accompanying drawings are the schematic diagram of simplification, and basic structure of the present invention is only described in a schematic way, and therefore it only shows the formation relevant with the present invention.
As Fig. 1, Fig. 2, shown in Fig. 3, the two entrance medium injection devices of screw-in, comprise body 1 and threaded nozzle 2, body 1 is provided with vacuum chamber 3, screwed hole 4, Venturi tube 5 and two two tangential arms 6, wherein the coaxial connection of screwed hole 4 and Venturi tube 5 is at vacuum chamber two ends, nozzle 2 is sheathed to be connected in nozzle bore 4, in 3 side weeks of vacuum chamber, tangential arm 6 is tangent with the side week of vacuum chamber 3, two tangential arms 6 are the centrosymmetric structures centered by Venturi tube 5 axis, then the steam simultaneously entering in vacuum chamber 3 from two tangential arms 6 can mix along vacuum chamber 3 inwall rotations, extend like this residence time of steam at vacuum chamber 3, and two strands of steam of rotation can better mix.
Threaded nozzle 2 is provided with the flat pipe portion 7 that is positioned at screwed hole 4 outsides and the tip 8 that is positioned at vacuum chamber 3, the structural design of tip 8 can ensure the air in vacuum chamber 3, fluid media (medium) and steam etc. flow to Venturi tube 5 smoothly, and can not produce inhibition, tip 8 ends are provided with and the spout 9 of putting down pipe portion 7 inner chambers and being communicated with, the inner diameter of flat pipe portion 7 is far longer than the inner diameter of spout 9, contribute to like this to improve the spouting velocity of fluid media (medium) in threaded nozzle 2, screwed hole 4 internal thread connecting thread nozzles 2, flat pipe portion 7 outsides are with external screw thread, screwed hole 4 inwalls are with internal thread, internal thread mates with external thread structure, threaded nozzle 2 can move at screwed hole 4 inside spins along its axis, rotation threaded nozzle 2, threaded nozzle 2 just can move forward and backward along its axis in screwed hole 4, there is crosspoint 14 with tangential arm 6 axis in threaded nozzle 2 axis, spout 9 be positioned on crosspoint 14 or 14 left and right sides, crosspoint threaded nozzle 2 axis on, when spout 9 positions of the threaded nozzle 2 that can move and the relative position in crosspoint 14 change, the fluid media (medium) of ejection is also different to the vacuum swabbing action in vacuum chamber 3 at a high speed, therefore, by regulating the vacuum of the adjusting vacuum chamber 3 that spout 9 and the relative position in crosspoint 14 just can be relative.
Venturi tube 5 is provided with compression section 10, larynx section 11 and diffuser 12 successively along its axis, compression section 10 vacuum chamber 3 that is tightly connected, compression section 10 and vacuum chamber 3 junction internal diameters are greater than the junction internal diameter of itself and larynx section 11, and expansion segment 12 free end internal diameters are greater than the junction internal diameter of itself and larynx section 11.Fluid media (medium) enters Venturi tube 5 with certain speed from compression section 10, because the compression section 10 cross section radiuses of air stream warp dwindle gradually, the flow velocity of fluid media (medium) increases thereupon, air velocity maximum while arriving larynx section 11, from Bernoulli equation, air velocity is inversely proportional to air pressure herein, it is the air pressure minimum of larynx section 11, the direction top rail section radius that air-flow is flowed through at diffuser 12 becomes large gradually, fluid media (medium) flow velocity diminish gradually slow down and, steam and air that last fluid media (medium) drives flow out Venturi tube 5, Venturi tube 5 has ensured fluid media (medium), steam and air all can not flow backwards as in vacuum chamber 3.
Screwed hole 4 free ends, Venturi tube 5 free ends, two tangential arm 6 free ends and flat tube section 7 free ends are equipped with being tightly connected along 13 of turning up along its circumferential edge, and this kind of structure contributes to its be tightly connected external pipe or equipment.Vacuum chamber 3 inwalls are globoidal structure, contribute to the flowing and mixing in vacuum chamber 3 such as steam or air, also contribute to air-flow, medium etc. to flow out smoothly vacuum chamber 3.
The present invention in use, fluid media (medium) enters at a high speed the inner chamber of threaded nozzle 2 from threaded nozzle 2, and spray with higher flow velocity from the very little spout 9 of internal diameter, flow velocity while entering vacuum chamber 3 due to fluid media (medium) is very high, under the effect of fluid media (medium), air in vacuum chamber 3 can be taken out of and enter Venturi tube 5 by fluid media (medium), in vacuum chamber 3, be now negative pressure, the swabbing action that steam in tangential arm 6 can be produced by the negative pressure of vacuum chamber 3 enters vacuum chamber 3, and can be aspirated and produce with it certain immixture by fluid media (medium), between mixed process fluid media (medium) and steam, can produce friction, heat exchange or even chemical reaction, fluid media (medium), steam and the air mixing flows at a high speed the compression section 10 of Venturi tube 5, along with its internal diameter diminishes gradually, it is large that the flow velocity of mixture becomes gradually, while arriving larynx section 11, it is maximum that its flow velocity reaches, then mixture enters diffuser 12, diffuser 12 internal diameters become large gradually, the flow velocity of mixture diminishes gradually, final mixture leaves Venturi tube 5 and enters in other equipment, the acceleration of Venturi tube 5 to mixture flow and slow down and usedly ensured that mixture can not produce adverse current, and also contribute to the generation of the processes such as the mixing between mixture.
Be enlightenment according to desirable embodiment of the present invention above, by above-mentioned description, related personnel can, not departing from the scope of this invention technological thought, carry out various change and amendment completely.The technical scope of this invention is not limited to the content on description, must determine technical scope according to claim scope.
Claims (7)
1. the two entrance medium injection devices of screw-in, comprise: body and the sheathed upper nozzle that is connected to described body, described body comprises vacuum chamber and seals with described vacuum chamber the nozzle bore, Venturi tube and two the tangential arms that are communicated with respectively, it is characterized in that, described nozzle is sheathed to be connected in described nozzle bore, what described nozzle and described Venturi tube were coaxial is positioned at described vacuum chamber two ends, the side week of described tangential arm and described vacuum chamber is tangent, and two described tangential arms are the centrosymmetric structures centered by described Venturi tube axis.
2. two entrance medium injection devices of screw-in according to claim 1, it is characterized in that: described nozzle is provided with the flat pipe portion that is positioned at described nozzle bore outside and the tip that is positioned at described vacuum chamber, described tip end is provided with the spout being communicated with described flat pipe portion inner chamber.
3. two entrance medium injection devices of screw-in according to claim 2, is characterized in that: described flat pipe portion outside is with external screw thread, and described nozzle bore inwall is with internal thread, and described internal thread mates with described external thread structure.
4. two entrance medium injection devices of screw-in according to claim 1, is characterized in that: described Venturi tube is provided with compression section, larynx section and diffuser successively along its axis, the described compression section described vacuum chamber that is tightly connected.
5. two entrance medium injection devices of screw-in according to claim 4, it is characterized in that: described compression section and described vacuum chamber junction internal diameter are greater than the junction internal diameter of itself and described larynx section, described expansion segment free end internal diameter is greater than the junction internal diameter of itself and described larynx section.
6. two entrance medium injection devices of screw-in according to claim 2, is characterized in that: described nozzle bore free end, described Venturi tube free end, described tangential arm free end and described flat tube section free end are equipped with the edge that is tightly connected of turning up along its circumferential edge.
7. two entrance medium injection devices of screw-in according to claim 1, is characterized in that: described vacuum chamber inwall is globoidal structure.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410262492.1A CN104014442A (en) | 2014-06-13 | 2014-06-13 | Rotating-in type dual-inlet medium ejector |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410262492.1A CN104014442A (en) | 2014-06-13 | 2014-06-13 | Rotating-in type dual-inlet medium ejector |
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| Publication Number | Publication Date |
|---|---|
| CN104014442A true CN104014442A (en) | 2014-09-03 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201410262492.1A Pending CN104014442A (en) | 2014-06-13 | 2014-06-13 | Rotating-in type dual-inlet medium ejector |
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| CN (1) | CN104014442A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105157448A (en) * | 2015-07-30 | 2015-12-16 | 中国海洋石油总公司 | Steam-water mixing heater |
| CN107715719A (en) * | 2017-09-11 | 2018-02-23 | 天津科技大学 | A kind of nozzle of achievable jet pumping system tail pipe secondary jet charging |
Citations (11)
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| GB377864A (en) * | 1931-11-06 | 1932-08-04 | Fisher Longstreth Boyd | Improvements in or relating to a method of and apparatus for producing fire-extinguishing foam |
| GB1514743A (en) * | 1974-05-24 | 1978-06-21 | Occidental Petroleum Corp | Mixing of particulate materials |
| EP0050312A2 (en) * | 1980-10-20 | 1982-04-28 | Hoechst Aktiengesellschaft | Apparatus and process for dispersing and dissolving polymer powders |
| US4447401A (en) * | 1982-02-22 | 1984-05-08 | Phillips Petroleum Company | Carbon black reactor with angled combustion chamber and non-aligned tangential hot gas entries for production of negative tint residual carbon black |
| JPS6245689A (en) * | 1985-08-23 | 1987-02-27 | Babcock Hitachi Kk | Simple gas generator |
| CN1756590A (en) * | 2003-02-28 | 2006-04-05 | 奥多摩工业株式会社 | Mixing device and slurrying device |
| CN2886155Y (en) * | 2006-03-31 | 2007-04-04 | 上海沪冈真空泵制造有限公司 | Anticorrosion water injection vacuum pump |
| CN201124121Y (en) * | 2007-11-21 | 2008-10-01 | 昆明理工大学 | Combined jet micro bubble generator |
| CN202161929U (en) * | 2011-07-18 | 2012-03-14 | 湖北三宁化工股份有限公司 | Combined ejector |
| CN203235546U (en) * | 2013-05-09 | 2013-10-16 | 安徽理工大学 | Coal slurry preprocessor |
| CN203916962U (en) * | 2014-06-13 | 2014-11-05 | 苏州市金翔钛设备有限公司 | The two entrance medium injection devices of screw-in |
-
2014
- 2014-06-13 CN CN201410262492.1A patent/CN104014442A/en active Pending
Patent Citations (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB377864A (en) * | 1931-11-06 | 1932-08-04 | Fisher Longstreth Boyd | Improvements in or relating to a method of and apparatus for producing fire-extinguishing foam |
| GB1514743A (en) * | 1974-05-24 | 1978-06-21 | Occidental Petroleum Corp | Mixing of particulate materials |
| EP0050312A2 (en) * | 1980-10-20 | 1982-04-28 | Hoechst Aktiengesellschaft | Apparatus and process for dispersing and dissolving polymer powders |
| US4447401A (en) * | 1982-02-22 | 1984-05-08 | Phillips Petroleum Company | Carbon black reactor with angled combustion chamber and non-aligned tangential hot gas entries for production of negative tint residual carbon black |
| JPS6245689A (en) * | 1985-08-23 | 1987-02-27 | Babcock Hitachi Kk | Simple gas generator |
| CN1756590A (en) * | 2003-02-28 | 2006-04-05 | 奥多摩工业株式会社 | Mixing device and slurrying device |
| CN2886155Y (en) * | 2006-03-31 | 2007-04-04 | 上海沪冈真空泵制造有限公司 | Anticorrosion water injection vacuum pump |
| CN201124121Y (en) * | 2007-11-21 | 2008-10-01 | 昆明理工大学 | Combined jet micro bubble generator |
| CN202161929U (en) * | 2011-07-18 | 2012-03-14 | 湖北三宁化工股份有限公司 | Combined ejector |
| CN203235546U (en) * | 2013-05-09 | 2013-10-16 | 安徽理工大学 | Coal slurry preprocessor |
| CN203916962U (en) * | 2014-06-13 | 2014-11-05 | 苏州市金翔钛设备有限公司 | The two entrance medium injection devices of screw-in |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105157448A (en) * | 2015-07-30 | 2015-12-16 | 中国海洋石油总公司 | Steam-water mixing heater |
| CN105157448B (en) * | 2015-07-30 | 2017-11-03 | 中国海洋石油总公司 | A kind of steam-water injection |
| CN107715719A (en) * | 2017-09-11 | 2018-02-23 | 天津科技大学 | A kind of nozzle of achievable jet pumping system tail pipe secondary jet charging |
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| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20140903 |
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| RJ01 | Rejection of invention patent application after publication |